1999 - Volume 2 - Journal of Engineered Fibers and Fabrics
1999 - Volume 2 - Journal of Engineered Fibers and Fabrics
1999 - Volume 2 - Journal of Engineered Fibers and Fabrics
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International Nonwovens <strong>Journal</strong> Home Page<br />
A SCIENCE AND TECHNOLOGY PUBLICATION<br />
<strong>Volume</strong> 8 No. 2 Fall, <strong>1999</strong><br />
Air Filters For Ventilating<br />
Systems — Laboratory <strong>and</strong><br />
In Situ Testing<br />
Table <strong>of</strong> Contents<br />
Cover Story<br />
TABLE OF CONTENTS<br />
INJ DEPARTMENTS<br />
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International Nonwovens <strong>Journal</strong> Home Page<br />
Guest Editorial<br />
Director's Corner<br />
Emerging Technology<br />
Rsearcher's Toolbox<br />
St<strong>and</strong>ards Development Forum<br />
Patent Review<br />
PAPERS<br />
Association Focus; TAPPI<br />
The Nonwoven Web<br />
Pira Worldwide Abstracts<br />
Association News<br />
Nonwovens Calendar<br />
Air Filters For Ventilating Systems - Laboratory <strong>and</strong> In Situ Testing<br />
Original Paper by Jan Gustavsson, Camfi<br />
Evaluation <strong>of</strong> the Filtration Performance <strong>of</strong> Biocide Loaded Filter Media<br />
Original Paper by Wayne T. Davis, B. Alan Phillips, Maureen Dever, Thomas Montie <strong>and</strong> Kimberly<br />
Kelly-Wintenberg, The University <strong>of</strong> Tennessee; <strong>and</strong> Sarah Macnaughton, Microbial Insights, Inc<br />
Characterization <strong>of</strong> Melt Blown Web Properties Using Air Flow Technique<br />
Original Paper by Peter Ping-yi Tsai, TANDEC, The University <strong>of</strong> Tennessee<br />
Foamed Latex Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong> To Improve Physical Properties<br />
Original Paper by A. Shahani, Bell Atlantic; D.A. Shiffler <strong>and</strong> S.K. Batra, Nonwovens Cooperative<br />
Research Center, North Carolina State University<br />
Fiberglass Surface And Its Electrokinetic Properties<br />
Original Paper by Daojie Dong, Owens Corning<br />
Applications Of On-Line Monitoring <strong>of</strong> Dynamic Forces Experienced By Needles During Formation<br />
Of Needled <strong>Fabrics</strong><br />
Original Paper by Abdelfattah M. Seyam, Nonwovens Cooperative Research Center, North Carolina<br />
State University<br />
Development <strong>of</strong> Thermal Insulation For Textile Wet Processing Machinery Using Needlepunched<br />
Nonwoven <strong>Fabrics</strong><br />
Original Paper by R<strong>and</strong>eep S. Grewal, Flynt <strong>Fabrics</strong>; <strong>and</strong> Dr. Pamela Banks-Lee, North Carolina<br />
State University<br />
Comparison Of Trends In Latex Emulsions For Nonwovens <strong>and</strong> Textiles:<br />
China <strong>and</strong> the United States<br />
Original Paper by Pamela Wiaczek, Kline & Company<br />
Fiber Renaissance For The Next Millennium<br />
Author's Perspective by Arun Pal Aneja, DuPont<br />
Publisher Ted Wirtz President<br />
INDA,<br />
Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry<br />
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International Nonwovens <strong>Journal</strong> Home Page<br />
Sponsors Wayne Gross Executive Director/COO<br />
TAPPI, Technical Association <strong>of</strong> the Pulp <strong>and</strong> Paper Industry<br />
Teruo Yoshimura<br />
Secretary General<br />
ANIC, Asia Nonwoven <strong>Fabrics</strong> Industry Conference<br />
Editors Rob Johnson 609-256-1040<br />
rjnonwoven@aol.com<br />
D.K. Smith 602-924-0813<br />
nonwoven@aol.com<br />
Association Editor Chuck Allen INDA<br />
D.K. Parikh TAPPI<br />
Teruo Yoshimura ANIC<br />
Production Editor Michael Jacobsen Jacor Publications, Inc.<br />
201-612-6601<br />
mjacobsen@inda.org<br />
Cover Photo provided by AQF Technologies, Charlotte N.C.<br />
The International Nonwovens <strong>Journal</strong> is published by INDA, Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry, P.O. Box<br />
1288, Cary, NC 27512; www.inda.org. Copyright <strong>1999</strong> INDA, Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry. No part <strong>of</strong><br />
this publication may be reproduced or transmitted in any form or by any means, electronic or mechanical, including<br />
photocopying <strong>and</strong> recording, or by any information storage or retrieval system, except as may be expressly permitted in<br />
writing by the copyright owner. The magazine is sent free-<strong>of</strong>-charge to all members <strong>of</strong> INDA <strong>and</strong> TAPPI, P.O. Box<br />
105113, Atlanta, GA 30348; 404-209-727; Fax 404-446-6947; <strong>and</strong> ANNA (Asia Nonwoven <strong>Fabrics</strong> Industry Conference),<br />
Soto k<strong>and</strong>a 6-Chome Bldg. 3Fl, 2-9, Chiyoda-ku, Tokyo, 101, Japan. The International Nonwovens <strong>Journal</strong> can not be<br />
reprinted without permission from INDA. INDA¨ is a registered trademark <strong>of</strong> INDA, Association <strong>of</strong> the Nonwoven<br />
<strong>Fabrics</strong> Industry<br />
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Editor's Corner<br />
To the Future<br />
GUEST EDITORIAL<br />
By Behnam Pourdeyhimi<br />
Ph.D., CText ATI, FTI; Pr<strong>of</strong>essor, <strong>and</strong> Co-Director, Nonwovens Cooperative Research Center, North<br />
Carolina State University, College <strong>of</strong> Textiles<br />
I had the opportunity to attend both INDEX '99 <strong>and</strong> ITMA '99 earlier this year. At both, I listened to<br />
messages about continued growth <strong>of</strong> the nonwovens industry, <strong>and</strong> future prospects for the industry in the<br />
global economy. At these meetings, I met with companies involved in various segments <strong>of</strong> the industry,<br />
including raw material suppliers, roll goods producers, converters <strong>and</strong> fabricators <strong>of</strong> the end use<br />
products, <strong>and</strong> machinery manufacturers.<br />
What was perhaps the most interesting aspect <strong>of</strong> my visits was the fact that most <strong>of</strong> the processes <strong>and</strong><br />
products on display did not exist two or three decades ago; those that did are now referred to as "aging"<br />
technologies. This is not surprising given the new developments exhibited at INDEX <strong>and</strong> ITMA,<br />
although even the "aging" processes have also been improved significantly over the same time period. I<br />
came back from these meeting with the feeling that nonwovens will continue to play a significant role in<br />
the polymer-fiber-textile enterprise for many years to come.<br />
In the near future ANNA/ANIC will be providing members to<br />
the Editorial Advisory Board from their geographic region.<br />
It has been estimated that this industry contributes more than<br />
$30 billion to the U.S. economy, <strong>and</strong> will continue to grow at a<br />
rate <strong>of</strong> at least 5-6% annually. This is indeed great news for the<br />
industry!<br />
As a pr<strong>of</strong>essor <strong>and</strong> educator, however, I have to wonder about<br />
the availability <strong>of</strong> the trained human capital required to help<br />
sustain this industry. Presently, the nonwovens industry<br />
primarily undertakes in-house training <strong>of</strong> individuals with<br />
degrees in engineering or science. This has undoubtedly<br />
contributed to the innovations in the field; however, I am not<br />
certain if this can continue to be a viable option given the<br />
EDITORIAL ADVISORY BOARD<br />
Chuck Allen<br />
INDA<br />
Roy Broughton Auburn University<br />
Robin Dent Albany International<br />
Ed Engle<br />
Fibervisions<br />
Tushar Ghosh North Carolina State<br />
Bhuvenesh<br />
Goswami<br />
Clemson University<br />
Dale Grove<br />
Frank Harris<br />
Albert Hoyle<br />
Owens Corning<br />
Fiberglass<br />
HDK Industries<br />
Hoyle Associates<br />
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Editor's Corner<br />
complexities <strong>of</strong> the materials, processes <strong>and</strong> products available<br />
today.<br />
Gaining, <strong>and</strong> indeed maintaining, leadership in this emerging<br />
field requires substantial investment in human capital as well<br />
as inventing fundamentally new mechanisms for achieving<br />
"versatile" processing; i.e., processing <strong>of</strong> large volume <strong>and</strong><br />
specialized materials with a substantially common production<br />
domain AND environmental compatibility.<br />
In order to maintain the present level <strong>of</strong> innovation, it is<br />
necessary to develop a more structured model for training our<br />
future nonwoven specialists. In academic institutions, our<br />
efforts in this regard should be focused on training these "new"<br />
personnel with sufficient breadth <strong>and</strong> depth in the variety <strong>of</strong><br />
disciplines that impact the nonwovens industry. This<br />
multidisciplinary education will well prepare them for a role<br />
with the new, versatile <strong>and</strong> sustainable technologies that will<br />
require a fundamental, adaptable knowledge <strong>of</strong> process<br />
synthesis, integration <strong>and</strong> subsequent transfer to industrial<br />
production. It is clear that industry <strong>and</strong> academia need to<br />
engage in open debate on the important matter <strong>of</strong> to how to<br />
prepare for the future.<br />
Ed. Note: Dr. Pourdeyhimi has recently joined the faculty at<br />
NCSU as Co-Director <strong>of</strong> the NCRC. Dr. Pourdeyhimi was<br />
most recently on the faculty at Georgia Tech <strong>and</strong> authored an<br />
article in the SPRING, <strong>1999</strong> issue <strong>of</strong> INJ.<br />
Marshall<br />
Hutten<br />
Hyun Lim<br />
Hollingsworth &<br />
Vose<br />
E.I. duPont de<br />
Nemours<br />
Nelson Industries<br />
Joginder Malik<br />
Alan<br />
Meierhoefer<br />
Dexter Nonwovens<br />
Michele<br />
Mlynar<br />
Rohm <strong>and</strong> Haas<br />
Graham Moore<br />
PIRA<br />
D.V. Parikh U.S.D.A.-S.R.R.C.<br />
Behnam<br />
Pourdeyhimi<br />
Georgia Tech<br />
Art Sampson Polymer Group Inc.<br />
Robert<br />
Shambaugh<br />
Univ. <strong>of</strong> Oklahoma<br />
Ed Thomas BBA Nonwovens<br />
Albin Turbak<br />
Retired<br />
Larry<br />
Wadsworth<br />
Univ. <strong>of</strong> Tennessee<br />
In the near future ANNA/ANIC will be<br />
providing members to the Editorial<br />
Advisory Board from their geographic<br />
region.<br />
— INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Directors Corner<br />
THE DIRECTOR’S<br />
CORNER<br />
INJ DEPARTMENTS<br />
A few years ago there was considerable concern about the possibility <strong>of</strong> electromagnetic radiation fields<br />
causing human cancers. The primary concern focused on high power transmission cables that frequently<br />
traverse residential areas. Many people were concerned that living under or around high powered<br />
transmission lines was injurious to health, particularly the health <strong>of</strong> children.<br />
As a result, there was considerable government-sponsored research to determine the reality <strong>of</strong> this<br />
concern <strong>and</strong> to quantify the risks involved. One particular study provided considerable fuel for this<br />
controversy <strong>and</strong> resulted in numerous expensive actions taken as a precautionary measure.<br />
The study was produced by a scientist named Richard Liburdy; in it, he stated that he had proved a link<br />
between high voltage lines <strong>and</strong> cellular changes in the body that could lead to cancer. This resulted in an<br />
acceleration <strong>of</strong> research devoted to the topic, despite the fact that many other studies, particularly those<br />
emanating from Europe indicating that no relationship existed.<br />
Shortly after the<br />
study received wide<br />
circulation, a<br />
whistleblower told<br />
the Federal<br />
Government, which<br />
had funded this<br />
particular research,<br />
that Liburdy had<br />
manipulated his data.<br />
The Office <strong>of</strong><br />
Research Integrity, a<br />
NON-COMPLIANCE CORRELATION<br />
EPA Act<br />
Non-Compliance Events<br />
CAA — Clean Air Act 0%<br />
CERCLA — Comprehensive Environmental Response,<br />
9%<br />
Compensation <strong>and</strong> Liability Act (Superfund)<br />
CWA — Clean Water Act 29%<br />
EPCRA — Emergency Planning <strong>and</strong><br />
Community Right-to-Know Act<br />
7%<br />
RCRA — Resource Conservation & Recovery Act 23%<br />
TSCA — Toxic Substances Control Act 12%<br />
bureau within the U.S. Department <strong>of</strong> Health <strong>and</strong> Human Services that monitors many federally funded<br />
research projects investigated. Further examination revealed that Liburdy had discarded data in preparing<br />
a graph for his publication which did not fall on the line purporting to support the hypothesis. In fact,<br />
further examination revealed that Liburdy had used only 7% <strong>of</strong> the data generated during his studies. As<br />
a result, Liburdy requested <strong>of</strong> the scientific journals that had published his work that three key<br />
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Directors Corner<br />
paragraphs be rescinded. Despite this action Liburdy claimed that he had done nothing wrong. However,<br />
he did leave the Department <strong>of</strong> Energy’s Lawrence Berkeley National Laboratory, where he was<br />
employed, <strong>and</strong> he has lost a portion <strong>of</strong> the $3.3 million grant from The National Institutes <strong>of</strong> Health,<br />
Department <strong>of</strong> Energy <strong>and</strong> Department <strong>of</strong> Defense.<br />
During <strong>and</strong> since these investigations, other studies have been published, all <strong>of</strong> which confirm the fact<br />
that there is no link between the electromagnetic radiation field <strong>and</strong> living organisms. Unfortunately, Mr.<br />
Liburdy’s deception kept the unfortunate myth alive for a period <strong>of</strong> time <strong>and</strong> fostered many actions <strong>of</strong><br />
"prudent avoidance;" the latter term has been concocted to mean that if there is even a hint <strong>of</strong> health<br />
problem, play it safe <strong>and</strong> avoid exposure. As a recent article in the Wall Street <strong>Journal</strong> points out (Wall<br />
Street <strong>Journal</strong>, July 27, <strong>1999</strong>) prudent avoidance "constitutes a rejection <strong>of</strong> science <strong>and</strong> a triumph <strong>of</strong> fear<br />
over reason" <strong>and</strong>, as physicist David Hafemeister <strong>of</strong> California Polytechnics State University notes,<br />
"prudent avoidance is a delight for plaintiff lawyers since it is essentially a conclusion that the danger is<br />
probable."<br />
In this case prudent avoidance resulted in massive expenditures in many different areas <strong>and</strong> conditions.<br />
Unfortunately, researchers seeking additional government funds know that research results which<br />
promote the concept that a growing problem exists can help assure a continuation <strong>of</strong> grants. This has<br />
resulted in what some critics have called "regulatory science." Unfortunately, the Liburdy episode has<br />
not done much to discourage this viewpoint. Although the falsification <strong>of</strong> data by Mr. Liburdy was<br />
exposed in 1995 he remained on the job until this past May. His "punishment" for his unscientific<br />
behavior consisted <strong>of</strong> an agreement that he would not apply for more Federal grants for a period <strong>of</strong> three<br />
years.<br />
Science in the Courtroom<br />
In recent years there has been considerable concern about the impact <strong>of</strong> science in litigation <strong>and</strong> in the<br />
courtroom environment. Unfortunately, many examples exist where testimony <strong>of</strong>fered in court cases<br />
have been labeled as "science," but has failed to meet the st<strong>and</strong>ards normally expected <strong>of</strong> a scientific<br />
discipline. In some cases, the deviation from scientific principles has been appalling.<br />
As Supreme Court Justice Stephen Breyer wrote in an opinion last year: "Society is becoming more<br />
dependent for its well being on scientifically complex technology, so, to an increasing degree, this<br />
technology underlies legal issues <strong>of</strong> importance to all <strong>of</strong> us." Because <strong>of</strong> this increasing importance <strong>of</strong><br />
science in the courtroom, attention has been focused on ways to insure that only the highest st<strong>and</strong>ards are<br />
employed in such contributions.<br />
The Supreme Court <strong>of</strong> the U.S. has made it very clear that the judges themselves are responsible for the<br />
accuracy <strong>and</strong> reliability <strong>of</strong> scientific evidence presented in their courtrooms. There have been several<br />
recent cases adjudicated by The Supreme Court that has stressed the absolute necessity to keep junk<br />
science out <strong>of</strong> technical testimony.<br />
While there can be widespread agreement on the objective, the means to accomplishing this goal can be<br />
difficult delineate.<br />
Some judges have enlisted the use <strong>of</strong> independent experts. The judge in the silicone breast implant case,<br />
for example, appointed a four-member panel <strong>of</strong> independent experts to help him sort through the science.<br />
An encouraging approach to develop a system that insures the highest scientific st<strong>and</strong>ards in the<br />
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Directors Corner<br />
courtroom has been made by the American Association for the Advancement <strong>of</strong> Science (AAAS). This<br />
organization has been working with a group from the American Bar Association to study the problem <strong>of</strong><br />
scientific evidence in the courtroom. Representatives from these two groups have been meeting for the<br />
past few years as the National Conference <strong>of</strong> Lawyers <strong>and</strong> Scientists. In the past few months, the AAAS<br />
has started a five-year demonstration project in which independent scientists with the appropriate<br />
expertise can be identified for judges to consider as scientific resources in determining the truth in<br />
litigation.<br />
Although the mechanism has not been completed, the project is making progress, including establishing<br />
<strong>and</strong> experimenting with the process by which experts are selected. Several subsidiary bodies chosen by<br />
AAAS staff <strong>and</strong> the advisory committee will attempt to develop procedures for both identifying <strong>and</strong><br />
recruiting such experts.<br />
Another committee within the national conference is attempting to develop guidelines to screen experts<br />
for potential conflicts <strong>of</strong> interest. The use <strong>of</strong> anonymity in describing potential experts will likely be<br />
helpful in the selection process.<br />
Other groups within the conference are working on the methods to make expert lists available <strong>and</strong> to alert<br />
the judges <strong>of</strong> the appropriate procedures in utilizing such services. Another activity is directed toward<br />
educating the scientists as to the intricacies <strong>of</strong> the legal process.<br />
While the initial efforts are being focused on Federal courts, it likely the project can be extended to State<br />
courts if the procedure proves successful. This is most desirable, as the State courts are the venue <strong>of</strong> most<br />
tort litigation <strong>and</strong> especially the most outrageous tort litigation.<br />
Hopefully these efforts can prove successful <strong>and</strong> the "legal lottery" can be eliminated along with the<br />
presence <strong>of</strong> junk science in the courtroom.<br />
The Value <strong>of</strong> People<br />
It has <strong>of</strong>ten been said that a company’s most valuable single asset is the people they have. The same can<br />
be said <strong>of</strong> the academic environment; quality <strong>of</strong> the researchers controls the quality <strong>of</strong> the research.<br />
Finding, hiring <strong>and</strong> keeping good people is a never-ending task for the research administrator, whether in<br />
industry, academe, or elsewhere.<br />
One <strong>of</strong> the tools in identifying the best c<strong>and</strong>idates for the job is embodied in a variety <strong>of</strong> pre-employment<br />
assessments. These are generally tests that usually consist <strong>of</strong> questions relating to the skills, behaviors<br />
<strong>and</strong> attitudes that are necessary for a particular job <strong>and</strong> a particular environment. These tests can take<br />
many different forms. The idea behind the test is to identify those applicants with the best chance <strong>of</strong><br />
becoming productive scientists <strong>and</strong> contributors to the industrial or academic research effort.<br />
The desirability <strong>of</strong> picking the right employee is also coupled with the importance <strong>of</strong> retaining the<br />
employee. The average length <strong>of</strong> employment <strong>of</strong> an individual at any pr<strong>of</strong>essional job in the United<br />
States has been declining in recent years <strong>and</strong> is estimated to be somewhere between two <strong>and</strong> four years<br />
by some human resources specialists.<br />
Along with the need to retain good researchers is the growing recognition that everyone needs balance in<br />
their lives. There must be meaning <strong>and</strong> satisfactions in their work, but this needs to be balanced with<br />
their personal, family <strong>and</strong> private aspirations. A recent review <strong>of</strong> this situation by one human resources<br />
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Directors Corner<br />
specialist, Roger E. Herman, gives five reasons why people leave employment <strong>and</strong> what to do about the<br />
situations. His list <strong>of</strong> five reasons for departure include the following:<br />
● "It doesn't feel right around here."<br />
● "They wouldn't miss me if I were gone."<br />
● "I don’t get the support I need to get the job done."<br />
● "There’s a new opportunity for growth somewhere else."<br />
● "I’m not being adequately compensated."<br />
Herman stresses the essential point that each individual needs to feel valued in his/her situation. It is<br />
important to clearly exhibit to the employee how their effort fits in with the overall activity <strong>and</strong> how it<br />
contributes to the success <strong>of</strong> an organization. It has been found that compensation is not the motivator it<br />
once was. However, it is still important to have a competitive benefits package.<br />
Of equal importance are the subtle "perks" that say "I am valued." There is a need for public recognition,<br />
<strong>and</strong> the research director that is innovative in selecting the method <strong>of</strong> such recognition is making a wise<br />
investment.<br />
Incidentally, a book entitled "1001 Ways To Reward Employees" (Workman Publishing Co. Inc; New<br />
York, NY) has been selling very well. Its author, Bob Nelson (Nelson Motivation, Inc.; P.O. Box<br />
500872, San Diego, CA 92150; 619-673-0690; Fax: 619-673-9031; www.nelson-motivation.com) has<br />
written several books on management <strong>and</strong> business skills, <strong>and</strong> is a very popular speaker.<br />
Protecting The Environment <strong>and</strong> Your Staff<br />
Environmental protection, along with employee safety <strong>and</strong> health, are research director's concerns that<br />
seldom actually benefit the bottom line. These responsibilities are viewed by many in the same way that<br />
a lot <strong>of</strong> plant managers view filtration: "Filtering our product doesn’t add any value, it simply adds cost."<br />
However, this attitude relates to an old adage that says: "Do it right the first time <strong>and</strong> you won’t have to<br />
do it the second time."<br />
It is true that the industrial or academic or research director spends more time, effort <strong>and</strong> research<br />
resources on these two factors than the research director <strong>of</strong> a couple generations ago. Every old timer can<br />
relate stories <strong>of</strong> how a critical plant run was made late at night with a "jury rig setup, taking more than a<br />
few risks." However, those times are gone <strong>and</strong> will never return. Today’s reality is that the research<br />
administrator has responsibility for occupational health <strong>and</strong> safety <strong>of</strong> the group, along with an<br />
environmentally sound operation.<br />
In terms <strong>of</strong> industrial plant sites, considerable pressure has been applied by the Environmental Defense<br />
Fund (EDF) <strong>and</strong> the Federal Government’s EPA (Environmental Protection Agency). A few months ago,<br />
these two organizations jointly launched an internet web site designed to pinpoint environmental<br />
problems. No plant manager, or research director for that matter, would like their operation's mistakes,<br />
hazards, accidents <strong>and</strong> just unfortunate incidents broadcast to the entire world. However, this web site<br />
lists plant <strong>and</strong> location emission problems by their Zip Code, making it relatively easy for anyone to<br />
check into the performance <strong>of</strong> their neighbor. It is a little bit like having the contents <strong>of</strong> your closet<br />
exposed, skeletons <strong>and</strong> all.<br />
While many industrial concerns initially expressed dismay at the thought <strong>of</strong> such exposure, the result has<br />
been surprisingly different. This site has not been a p<strong>and</strong>ora's box <strong>of</strong> problems <strong>and</strong> a source <strong>of</strong> major<br />
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Directors Corner<br />
embarrassment. In most cases, the neighbors, the city <strong>of</strong>ficials <strong>and</strong> others have been aware <strong>of</strong> the<br />
situation <strong>and</strong> also aware <strong>of</strong> the company or laboratory efforts to address the problem.<br />
Rather interestingly, some trade associations for the chemical, petroleum <strong>and</strong> other manufacturing<br />
industries have adopted the information site technique to inform <strong>and</strong> educate their neighbors as to their<br />
problems <strong>and</strong> their remedial efforts.<br />
As an example, the Chemical Manufacturers Association (CMA) is launching a web site called<br />
"Chemical Guide." This will be an information site to the plant, the community, the employees <strong>and</strong> the<br />
surrounding neighbors. The CMA has developed templates that member companies can use to report<br />
information ranging from environment, health, <strong>and</strong> safety statistics to financial information, <strong>and</strong> even job<br />
postings. As a CMA spokesman has indicated, "It’s not an attempt to change the public’s perception <strong>of</strong><br />
the industry; it’s meant to personalize our facilities."<br />
In a similar vane, many organizations have "gone public" with respect to injury <strong>and</strong> illness reports. An<br />
example is a new web site that provides online versions <strong>of</strong> environmental, health <strong>and</strong> safety reports; it is<br />
being <strong>of</strong>fered by 111 companies in the U.S. (www.ehsreports.com). This type <strong>of</strong> internet site was rather<br />
strongly tilted to environmental reports when initiated; now, many companies are trying to strike a better<br />
balance in providing health <strong>and</strong> safety information.<br />
Laboratory tours, plant visits <strong>and</strong> similar activities where appropriate, can go a long ways to building<br />
positive relationships with neighbors, employee families <strong>and</strong> other interested parties. Such activities can<br />
also help to boost the esteem <strong>of</strong> employees <strong>and</strong> staff members. In a time <strong>of</strong> electronic information, it is<br />
<strong>of</strong>ten more prudent to exploit than to resist.<br />
Employee Safety Initiatives<br />
In line with the research director’s concern with employee safety, a frequently asked question is: "What<br />
legal rights do employees have to take actions to see that their employer complies with OSHA<br />
St<strong>and</strong>ards?"<br />
This is an interesting <strong>and</strong> rather important question for research directors, plant managers <strong>and</strong><br />
administrators in general. A rather definitive answer to this question was recently provided by Daryl<br />
Brown <strong>of</strong> J.J. Keller & Associates (dbrown2@jjkeller.com). Mr. Brown indicated that The Occupational<br />
Safety <strong>and</strong> Health Act <strong>of</strong> 1970 created by OSHA within the Department <strong>of</strong> Labor was inaugurated to<br />
encouraged employers <strong>and</strong> employees to reduce workplace hazards <strong>and</strong> to implement safety <strong>and</strong> health<br />
programs. This law gives employees many rights <strong>and</strong> responsibilities, including the rights to do the<br />
following:<br />
• Review copies <strong>of</strong> appropriate st<strong>and</strong>ards, rules, regulations <strong>and</strong> requirements that the employer should<br />
have available at the workplace.<br />
• Request information from the employer on safety <strong>and</strong> health hazards in the workplace, precautions that<br />
have been taken <strong>and</strong> procedures that should be followed if the employee is involved in an accident or is<br />
exposed to toxic or hazardous materials.<br />
• Have access to the employee’s exposure to harmful materials, <strong>and</strong> medical records that are relevant to<br />
the situation.<br />
• Request the OSHA area director to conduct an inspection if they believe that hazardous conditions or<br />
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Directors Corner<br />
violations <strong>of</strong> OSHA St<strong>and</strong>ards exist within the workplace.<br />
• Have an authorized employee representative accompany the OSHA compliance <strong>of</strong>ficer during any<br />
inspection tour.<br />
• The right to respond to questions from the OSHA compliance <strong>of</strong>fice, particularly if there is no<br />
authorized employee representative accompanying the compliance <strong>of</strong>ficer doing the inspection tour.<br />
• The right to observe any monitoring or measuring <strong>of</strong> hazardous materials <strong>and</strong> to examine the resulting<br />
records.<br />
• Have an authorized representative or the employee themselves review the OSHA 200 Log at a<br />
reasonable time <strong>and</strong> in a reasonable manner.<br />
• Object to the abatement period set by OSHA for correcting any violation in a citation issued to the<br />
employer; this is done by writing to the OSHA area director within 15 working days from the date the<br />
employer receives the citation.<br />
• The right to be notified by the employer if the employer applies for a variance from a OSHA st<strong>and</strong>ard;<br />
also, the right to testify at the variance hearing <strong>and</strong> to appeal the final decision.<br />
• The employee has the right to have their name withheld from their employer upon their request to<br />
OSHA, if a written <strong>and</strong> signed complaint is filed.<br />
• The right to file a discrimination complaint if the employee is punished for exercising any <strong>of</strong> the above<br />
rights or for refusing to work when faced with an imminent danger <strong>of</strong> death or serious injury <strong>and</strong> there is<br />
insufficient time for OSHA to inspect the situation.<br />
While this listing <strong>of</strong> the employee rights is rather lengthy, a consideration <strong>of</strong> each item rather clearly<br />
establishes the appropriateness <strong>of</strong> each <strong>of</strong> these rights.<br />
Violations <strong>of</strong> Environmental Laws<br />
Anyone who has been involved in a laboratory or plant inspection by EPA (Environmental Protection<br />
Agency) inspectors knows how stressful this situation can be. In many cases, honest efforts have been<br />
made to do an effective job <strong>and</strong> to abide by EPA Regulations. The sheer volume <strong>and</strong> complexity <strong>of</strong> such<br />
regulations, however, <strong>of</strong>ten leaves the whole operation on a rather "chancy" basis.<br />
In a rather unusual exercise, the EPA <strong>and</strong> the Chemical Manufacturers Association (CMA) recently<br />
collaborated on an effort to determine why companies fail to comply with environmental regulations.<br />
The CMA was very willing to participate, as explained by their legal counsel, because "historically the<br />
EPA had been addressing only the symptoms <strong>of</strong> violations, <strong>and</strong> here was the opportunity to find out what<br />
the causes are."<br />
The three-year project was carried out as "Root Cause Analysis Pilot Project." EPA prepared the survey<br />
<strong>and</strong> sent it to 50 member companies who had encountered problems with violations between 1990 <strong>and</strong><br />
1995. These violations were non-criminal, but represented a breach <strong>of</strong> the regulations, nevertheless.<br />
The report on the results <strong>of</strong> the survey (http://www.epa.gov/oeca/ccsmd/rootcause.html) detail six<br />
primary root causes for facility violations. These causes were as follows:<br />
1. Facility unaware <strong>of</strong> the applicability <strong>of</strong> specific regulation.<br />
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Directors Corner<br />
2. Human error in judgment or responsibility.<br />
3. Failure to follow EPA procedures.<br />
4. Faulty equipment design or installation.<br />
5. Problems with compliance by contractors.<br />
6. Various communication difficulties.<br />
From this study, it was determined that certain kinds <strong>of</strong> compliance problems are most regularly<br />
associated with particular laws. Specifically, it was found that the laws relating to two federal acts have<br />
more than one- half the violations involved, primarily because the laws were confusing <strong>and</strong> ambiguous.<br />
These two items were EPCRA (Emergency Planning <strong>and</strong> Community Right-to-Know Act) <strong>and</strong> RCRA<br />
(Resource Conservation & Recovery Act). On the other h<strong>and</strong>, the problems with the Clean Air Act<br />
(CAA) did not involve misunderst<strong>and</strong>ings or permit violations. The violations that did occur regarding<br />
the CAA all involved operational <strong>and</strong> procedure-related problems, such as equipment failure <strong>and</strong> similar.<br />
The report results are summarized in the chart at the top <strong>of</strong> this page.<br />
Again, under the Clean Water Act, most <strong>of</strong> the problems with faulty water discharges had their basis in<br />
the equipment installation or design.<br />
Also, it developed that companies which have environmental audit programs <strong>and</strong> corporate policies,<br />
goals <strong>and</strong> targets for regulatory compliance were the best performers as to compliance. These companies<br />
also reported that when violations were found, their emergency management systems were usually<br />
changed to avoid recurrence <strong>of</strong> the problems.<br />
From this study, a number <strong>of</strong> recommendations for both EPA <strong>and</strong> industry were provided. For EPA, it<br />
was suggested that the agency articulate its regulations more clearly <strong>and</strong> provide immediate compliance<br />
assistance <strong>and</strong> "plain-English" guides for every new rule. Also, it was suggested that EPA could work<br />
more closely with state <strong>and</strong> environmental agencies to insure that regulations are interpreted consistently.<br />
On the part <strong>of</strong> industry, it was suggested that more effort should be devoted to the development <strong>of</strong><br />
comprehensive environmental management systems <strong>and</strong> the promotion <strong>of</strong> a increased level <strong>of</strong> awareness<br />
<strong>of</strong> such systems amongst all employees. Accurate, st<strong>and</strong>ardized operating procedures <strong>and</strong> improved<br />
employee training were also recommended.<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
—INJ<br />
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Emerging Technology<br />
EMERGING<br />
TECHNOLOGY<br />
WATCH<br />
INJ DEPARTMENTS<br />
Sunlight Barrier <strong>Fabrics</strong><br />
Because <strong>of</strong> publicity, there is a heightened awareness <strong>of</strong> the dangers <strong>of</strong> skin cancer due to exposure to the<br />
sun's rays. The risk is not insignificant, as more than a million cases <strong>of</strong> skin cancer are diagnosed in the<br />
United States each year, according to the American Academy <strong>of</strong> Dermatology. About 45,000 <strong>of</strong> these<br />
cases will be the deadly strain <strong>of</strong> skin cancer called melanoma, where the cancerous growth penetrates<br />
the skin layers into the underlying tissue. Melanoma kills over 7,000 people a year in the U.S.<br />
Responding to this hazard, there has been considerable interest in the use <strong>of</strong> clothing to protect against<br />
the deleterious effects <strong>of</strong> the sun's rays. Clothing, <strong>of</strong> course, does not eliminate the need for sun block<br />
creams <strong>and</strong> lotions on exposed areas <strong>of</strong> skin. However, for most <strong>of</strong> the body surface, adequate clothing<br />
can provide a very effective sun block.<br />
The problem is that in the summertime adequate clothing may be discarded in preference for very light,<br />
open fabrics that are more cool, comfortable <strong>and</strong> stylish. As a result, there has been considerable interest<br />
in recent years in developing fabrics specifically designed to block the sun <strong>and</strong> yet provide comfort <strong>and</strong><br />
aesthetics that are normally associated with summertime clothing.<br />
If a fabric is heavy enough, it can effectively block the sun's rays. However, there has been considerable<br />
effort to develop fabric finishes for lightweight fabrics that can still provide adequate protection <strong>and</strong> yet<br />
be lightweight, open, breathable <strong>and</strong> stylish.<br />
This has resulted in a rather sudden growth in fabrics <strong>and</strong> clothing exhibiting good blockage <strong>of</strong> sunlight<br />
<strong>and</strong> thereby give strong protection against the problems associated with sunlight <strong>and</strong> human skin.<br />
Unfortunately, no st<strong>and</strong>ardized techniques have been developed in the United States for measuring how<br />
well a fabric blocks sunlight. Australia does have a st<strong>and</strong>ard method that applies to new, dry materials.<br />
There are efforts underway in the United States to establish a voluntary st<strong>and</strong>ard.<br />
In the meantime, companies that promote special fabrics as a solution to the problem are utilizing a<br />
variety <strong>of</strong> methods to measure the effectiveness. Clothing that is wet or that has been washed repeatedly<br />
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Emerging Technology<br />
can have a very different ability for blocking the harmful effects <strong>of</strong> the sun.<br />
Some apparel companies have focused on this market niche <strong>and</strong> <strong>of</strong>fer a variety <strong>of</strong> clothing claimed to<br />
provide considerable protection. Such apparel generally is quite expensive, however, <strong>and</strong> the consumer is<br />
left to gauge whether the additional expense is worth the claimed protection.<br />
At least one company in Israel has developed a finish technology which it claims provides the perfect<br />
solution to UV protection. As can be expected, the major focus <strong>of</strong> this effort has been on fashionable<br />
apparel fabrics, but there are indications that this technology will be extended to nonwoven structures as<br />
well.<br />
The process developed by Golden Guard Technologies Limited apparently involves the formation <strong>of</strong> a<br />
strong, flexible, breathable <strong>and</strong> translucent polyurethane finish that incorporates UV absorbers <strong>and</strong><br />
attenuators. It is claimed that fabrics that transmit nearly 50% <strong>of</strong> the UV light before treatment, show a<br />
transmission <strong>of</strong> only 2-4% after treatment. The claims also indicate the finish results in a minimal impact<br />
on the moisture-vapor transmission rate <strong>and</strong> on the fabric h<strong>and</strong> <strong>and</strong> drape. This protection is unaffected<br />
by moisture, perspiration <strong>and</strong> machine washing, <strong>and</strong> is durable to abrasion, along with wear <strong>and</strong> tear,<br />
according to the developers (Golden Guard Technologies Ltd, 21 Havaad Haleumi Street, P.O. Box<br />
16120, Jerusalem 91160, Israel; 972-2-675-1123; Fax: 972-2-675-1195;. www.sunprecautions.com <strong>and</strong><br />
www.sunprotection.com.<br />
Reactive Protective Clothing<br />
The category <strong>of</strong> "protective clothing" covers a broad range <strong>of</strong> hazards. As discussed in the item above,<br />
even sunlight can be a focus, <strong>and</strong> an appropriate one, for protective clothing. Anyone who has dealt with<br />
a baby diaper knows that it is also a form <strong>of</strong> protective clothing.<br />
More specialized hazards are being considered, however, <strong>and</strong> some innovative research is being devoted<br />
to such hazards.<br />
A recent development shows a rather dramatic approach to a specific situation, that <strong>of</strong> clothing worn by<br />
agricultural workers, specifically those workers exposed to a significant amount <strong>of</strong> pesticides. In many<br />
such cases the pesticide can pass through the clothing to the skin <strong>of</strong> the worker <strong>and</strong> there constituted a<br />
significant hazard.<br />
The solution worked out by researchers at the University <strong>of</strong> California-Davis involved clothing treated<br />
with chemicals to detoxify such pesticides. These investigators treated cotton fabric used to make shirts<br />
with a cyclic hydantoin compound, which grafted onto the cellulose backbone <strong>of</strong> the cotton fiber. The<br />
fabric is then treated with a bleaching process similar to that normally used in washing clothing.<br />
This process, using sodium hypochlorite solution, converts the hydantoin moiety into a halamine group.<br />
Interaction <strong>of</strong> the halamine group on the surface <strong>of</strong> the shirt fabric with carbamate-type insecticides<br />
results in the carbamate breaking down into small, harmless fragments. In the process, the halamine is<br />
converted back into the hydantoin. Washing the clothing, with a bleach treatment, then regenerates the<br />
halamine, ready to provide the protection.<br />
Thus, the garment is able to go through a cycle: (1) providing protection, (2) washing <strong>and</strong> bleaching, (3)<br />
regeneration <strong>of</strong> active site, ready to again provide the protection.<br />
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Emerging Technology<br />
Chlorine Bleach<br />
R - N - H<br />
...............> R - N - Cl<br />
Emerging Technology<br />
Paperless Society ... The use <strong>of</strong> wireless communications, innovative displays <strong>and</strong> individualized web<br />
publications will help reduce the reliance on paper for many activities. Advanced display systems may<br />
imitate paper in flexibility <strong>and</strong> portability. The researchers suggest that one approach will involve<br />
projecting images directly on the retina <strong>of</strong> the eye. This capability, coupled with a cellular phone, could<br />
provide faxes <strong>and</strong> customized news anywhere. For paper products that continue to be used,<br />
biodegradable inks will be more common.<br />
Molecular Design ... The use <strong>of</strong> molecular design for catalysts can make chemical reactions <strong>and</strong><br />
processes so precise that little or no wastes are produced. It suggests that sensors designed at the<br />
molecular level will monitor material <strong>and</strong> chemical manufacturing processes more precisely. This will<br />
help to halt or correct processes that are sensitive to temperature changes <strong>and</strong> other parameters. This<br />
breakthrough may exp<strong>and</strong> uses <strong>of</strong> nonwovens, but may also have an impact on the production <strong>of</strong><br />
nonwoven products.<br />
Bioprocessing ... This concept utilizes microorganisms <strong>and</strong> plants that will "grow" environmentally<br />
friendly chemicals <strong>and</strong> biological products. Included among these materials may be drugs, proteins <strong>and</strong><br />
enzymes for many uses. Producing chemical feedstocks, fuels <strong>and</strong> pharmaceuticals in this manner will be<br />
cost effective <strong>and</strong> better for the environment. The researchers suggest that microorganisms retrieve from<br />
extremely hot, cold or forbidding environments (extremozymes, such as are recovered at hot holes in the<br />
ocean floor) may exp<strong>and</strong> the range <strong>of</strong> temperatures <strong>and</strong> conditions used in manufacturing biotechnical<br />
products. This may create opportunities for new, environmentally friendly bioprocesses while saving<br />
time <strong>and</strong> energy.<br />
Real-time Environmental Sensors ... By the use <strong>of</strong> yet-to-be-developed sensors, supermarkets could<br />
detect the presence <strong>of</strong> bacteria <strong>and</strong> other dangerous pathogens in food. Workplace air quality could be<br />
monitored to prevent "sick building syndrome." Other benefits that may result from monitoring in the<br />
environment include control <strong>of</strong> airplane <strong>and</strong> other transportation environments, preventing infections in<br />
hospitals <strong>and</strong> in municipal water supplies <strong>and</strong> in guarding against pathogens potentially used in<br />
biological terrorism.<br />
Enviro-manufacturing <strong>and</strong> Recycling ... Greatly enhanced recyclability <strong>of</strong> a whole range <strong>of</strong> products<br />
may change the complexion <strong>of</strong> entire environmental protection in the future. Increased use <strong>of</strong><br />
biodegradable material in such things as plastics, paper, cars <strong>and</strong> computers will have an impact. Dry<br />
cleaning with liquid carbon dioxide will minimize or eliminate this source <strong>of</strong> environmental pollution.<br />
Recycling will become "second nature" to all <strong>of</strong> the citizens <strong>of</strong> the world, <strong>and</strong> recyclates will be a major<br />
resource for future civilizations.<br />
Lightweight Cars ... As the weight <strong>of</strong> automobiles is reduced by the use <strong>of</strong> advanced materials, the<br />
family sedan will get at least 80 miles per gallon <strong>of</strong> gas, generate less pollution <strong>and</strong> use more recycled<br />
materials. Lighter weight cars will be built with less steel <strong>and</strong> more lightweight aluminum, magnesium,<br />
titanium <strong>and</strong> composites. Advanced metal forming techniques will provide precisely the strength needed<br />
at every point. The 150 pounds <strong>of</strong> glass used in today's cars will be cut by a third or more by the use <strong>of</strong> a<br />
composite s<strong>and</strong>wich <strong>of</strong> glass <strong>and</strong> plastic. Today's 100-pound air conditioners will weigh half as much,<br />
particularly as glass is specially coated to reflect or absorb heat radiation.<br />
While some <strong>of</strong> these concepts may sound far fetched, many <strong>of</strong> them already have a running start in<br />
parent technology. Further details on the environmental technology forecast coming from the U.S.<br />
Department <strong>of</strong> Energy can be obtained: Greg Koller at Pacific Northwest National Laboratory;<br />
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Emerging Technology<br />
greg.koller@p&l.gov; 509-372-4864; http://www.pml.bill/news/back/envirbg.htm.<br />
—INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Researchers Toolbox<br />
RESEARCHERS<br />
TOOLBOX<br />
INJ DEPARTMENTS<br />
Good ideas are always welcomed by the effective researcher. Good ideas can help get a difficult job done<br />
easily. Sometimes the right method or tool can get results that would be difficult to do any other way.<br />
Occasionally, the right idea provides a result that simply could not be accomplished otherwise. Hence, a new<br />
trick to put into the collection <strong>of</strong> tricks is always a worthwhile addition. If you have such an item to share,<br />
please let us know so we can include it in a future <strong>of</strong>fering.<br />
Here's hoping that one <strong>of</strong> the current collection will prove useful.<br />
Temperature Indicators<br />
In dealing with thermal processes it is sometimes vital to know the maximum temperature reached by a fabric<br />
or system. It would be very convenient to be able to insert something that would register the maximum<br />
temperature, or would give a signal if a certain temperature is achieved.<br />
A quick, inexpensive <strong>and</strong> easy solution to this need can <strong>of</strong>ten be obtained with the use <strong>of</strong> temperature monitor<br />
product. These can be paper or film label products having a window or small panel that changes color upon<br />
being exposed to a set temperature. Often a label or tape product will carry a series <strong>of</strong> four-to-eight spots that<br />
correspond to a specific temperature. When the product is exposed to that temperature, the spot changes from a<br />
light color to black or some such dark color, so there can be no doubt that the temperature was experienced.<br />
Self-adhesive temperature monitoring labels can be attached to a web undergoing thermal treatment, giving a<br />
positive indication that a certain temperature was achieved within the web. Such monitoring labels can have<br />
spots indicating a temperature <strong>of</strong> 100F between each rating. Other styles have temperature differentials <strong>of</strong> 250<br />
or 500 F between spots. The spots or indicator panels can have a variety <strong>of</strong> shapes <strong>and</strong> configurations,<br />
including circles, micro-dots, buttons, bars, <strong>and</strong> forms <strong>of</strong> bull's eye, clock <strong>and</strong> thermometer configurations.<br />
In general, the temperature range <strong>of</strong> 1000 to 5000 F is available, <strong>and</strong> an accuracy <strong>of</strong> 1% is guaranteed. Such<br />
temperature monitoring systems can also be provided in a pencil or stick version, which allows a mark to be<br />
made on a surface which then changes as that specific temperature is achieved. Also, the products are provided<br />
in paint form so that a cover or machine housing can be converted into a temperature-indicating probe.<br />
The monitoring tape product is <strong>of</strong>ten used with fusing ovens or fusing presses, to confirm the fact that a<br />
temperature adequate for a fabric bonding step has been achieved. This can be done by placing the indicator on<br />
a belt traversing the oven, or between layers <strong>of</strong> fabrics or sheets. This has been particularly useful in<br />
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Researchers Toolbox<br />
applications involving the bonding <strong>of</strong> nonwoven fusible interlinings <strong>and</strong> interfacings to outer face fabrics.<br />
A well-established source for such products is Tempil, Inc. (2901 Hamilton Boulevard, South Plainfield, NJ<br />
07080; 800-757-8301; Fax: 908-757-9273). Their products can also be reviewed at http://www.tempil.com.<br />
Supercritical Fluids in<br />
<strong>Fibers</strong> Research<br />
Considerable interest has been shown in the use <strong>of</strong> supercritical fluids (SCF) in a wide variety <strong>of</strong> experimental<br />
<strong>and</strong> research applications. Where such detailed interests exist, applications almost invariably follow.<br />
The use <strong>of</strong> SCF methods in analytical laboratories has grown substantial over the past few years. This has been<br />
applied especially to extraction <strong>and</strong> chromatographic methods, where the elimination <strong>of</strong> toxic or difficult<br />
solvents has been a boon, along with the accompanying greatly reduced extraction times.<br />
A very interesting application <strong>of</strong> SCF technology in the fibers sector has recently come out <strong>of</strong> research work<br />
done at the Georgia Institute <strong>of</strong> Technology. This has focused on the dyeing <strong>of</strong> fibers, textiles <strong>and</strong> polymers<br />
<strong>and</strong> likely presages further search for suitable applications in the fibers <strong>and</strong> polymer sectors.<br />
One <strong>of</strong> the most popular solvents for using SCF technology is carbon dioxide. This solvent is especially<br />
attractive as it is nonflammable, nontoxic <strong>and</strong> low cost. It is easily separated from other solvents <strong>and</strong><br />
substrates, <strong>and</strong> when so released, it is non-polluting. This solvent is particularly useful with polymeric<br />
materials, as it behaves as a plasticizer <strong>and</strong> can swell many polymers. Because <strong>of</strong> this attribute, its low<br />
viscosity <strong>and</strong> its high solute diffusivity, it can penetrate many polymers with ease. This character also allows<br />
the solvent to carry many materials into polymeric substrates, fostering mass transfer processes.<br />
SCF carbon dioxide is easily absorbed by many polymers. In some cases, the solvent can plasticize glassy<br />
polymers at relatively low temperatures; with rubbery polymers above their glass transition temperatures, the<br />
polymer volume can be substantially increased. These properties can aid in extraction <strong>of</strong> materials from the<br />
polymers, or conversely can aid in the transport <strong>of</strong> materials as additives or impregnants, depending upon<br />
specific conditions employed.<br />
Carbon dioxide is a gas at normal conditions <strong>of</strong> temperature <strong>and</strong> pressure. However, if the temperature is<br />
sufficiently lowered, the gas can be converted into a solid (dry ice). If the pressure is increased sufficiently, the<br />
gaseous carbon dioxide is converted into a solid or a liquid, dependent upon the temperature. At one condition<br />
<strong>of</strong> temperature <strong>and</strong> pressure, all three phases <strong>of</strong> the gas (solid, liquid <strong>and</strong> gas, the triple point) can exist in<br />
equilibrium; for carbon dioxide, the triple point is 310 C <strong>and</strong> 74 bar. pressure. Above this point, the material<br />
can generally be maintained in the liquid state, the preferred state for SCF work. By judicious selection <strong>of</strong> the<br />
pressure <strong>and</strong> temperature, diffusion rates can be controlled for extraction work or for impregnation processes.<br />
The work at Georgia Tech focused on the use <strong>of</strong> SCF carbon dioxide for the dyeing <strong>of</strong> fibers, textiles <strong>and</strong><br />
polymers. Hence, the capability <strong>of</strong> the system for impregnation was particularly studied. These efforts<br />
confirmed the basic capabilities <strong>of</strong> the system, as reported by others. The research was extended by studying<br />
both phases <strong>of</strong> the dyeing process, the solubilization <strong>of</strong> the dyestuff molecule <strong>and</strong> the diffusion into the<br />
polymer matrix.<br />
Rather surprisingly, the Georgia Tech researchers found that the dyestuff could have low solubility in the<br />
solvent <strong>and</strong> still be effective in dyeing. They concluded this result was due to the fact that SCF dyeing can be<br />
effective because <strong>of</strong> the high partition coefficient, the dyestuff molecule preferring the polymer environment to<br />
that <strong>of</strong> the solvent. This property made for high dyeing efficiency <strong>and</strong> minimized dyestuff loses in the disposed<br />
liquor <strong>and</strong> vessel walls.<br />
As might be expected, the treatment did result in the extraction <strong>of</strong> some oligomers <strong>and</strong> surface agents from<br />
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Researchers Toolbox<br />
polyester fibers, for example. Other researchers have shown that such treatment can also affect fiber<br />
morphology, but no more so than the effects <strong>of</strong> heat <strong>and</strong> tension.<br />
Despite the fact that special equipment is required to obtain the temperatures <strong>and</strong> pressures needed, the<br />
interesting results <strong>of</strong> this work, <strong>and</strong> the inherent simplicity <strong>and</strong> cleanliness <strong>of</strong> the process, suggest utility <strong>of</strong><br />
SCF technology in other fiber research <strong>and</strong> applications.<br />
For more information, see: Drews, M. J. <strong>and</strong> Jordan, C., Text. Chem. <strong>and</strong> Color. 30, 13-20 (1998). The work at<br />
Georgia Institute <strong>of</strong> Technology is summarized at: Kazarian, S. G., Noel, H.B., <strong>and</strong> Eckert, C.A., Chemtech,<br />
36-41 (July <strong>1999</strong>).<br />
Microthermal Analysis<br />
Thermal methods <strong>of</strong> chemical <strong>and</strong> physical analysis are well-established techniques for characterizing <strong>and</strong><br />
quantifying the morphology <strong>and</strong> composition <strong>of</strong> polymers <strong>and</strong> fibers. Differential scanning calorimetry (DSC),<br />
thermogravimetric analysis (TGA), thermomechanical analysis (TMA) <strong>and</strong> dynamic mechanical analysis<br />
(DMA) are all useful resources on the palette <strong>of</strong> the fiber <strong>and</strong> polymer scientist.<br />
By adding the option <strong>of</strong> temperature modulation superimposed on the conventional linear heating or cooling<br />
program, further information <strong>and</strong> resolution is possible in many <strong>of</strong> these cases.<br />
Even with such extensions <strong>of</strong> the basic techniques, however, these methods give only an averaged or a<br />
sample-averaged view <strong>of</strong> the condition within a polymer matrix. In order to measure the thermal properties <strong>of</strong><br />
a small domain with the polymer, it is generally necessary to go to a microscopic scale. With some restrictions,<br />
secondary ion mass spectroscopy (SIMS) or X-ray photoelectron spectrometry (XPS) can provide some<br />
focused information, but these techniques have limitations <strong>and</strong> complexities.<br />
The efforts to bring together the capabilities <strong>of</strong> both thermal methods with microscopic techniques have<br />
resulted in the commercialization <strong>of</strong> an instrument called the Micro-Thermal Analyzer, specifically, the TA<br />
2900. The instrument combines the capabilities <strong>of</strong> thermal methods <strong>and</strong> micro visualization. It is achieved by<br />
combining an atomic force microscope (AFM) with a thermal probe.<br />
The TA 2900 is capable <strong>of</strong> providing four images or views <strong>of</strong> the surface <strong>of</strong> a sample:<br />
1. Topography<br />
2. Thermal conductivity<br />
3. Modulated temperature (amplitude)<br />
4. Modulated Temperature (phase)<br />
After these images have been acquired, any specific location on the sample can be further analyzed by what the<br />
instrument producer calls "Micro-Thermomechanical Analysis" <strong>and</strong> "Micro-Modulated Differential Thermal<br />
Analysis." The manufacturer claims these "micro" techniques are comparable with the usual "macro"<br />
counterparts.<br />
By means <strong>of</strong> this micro-thermal methodology, polymer blends can yield useful information. If the blends are<br />
immiscible, a two-phase domain structure results; the thermal properties <strong>of</strong> each individual domain can then be<br />
determined. If a single phase results, indicating miscibility, this becomes apparent from the thermal properties<br />
<strong>of</strong> this main phase.<br />
Similar chemical <strong>and</strong> physical information can be obtained with this equipment <strong>and</strong> technology on<br />
multi-layered films, indicating the thermal composition <strong>and</strong> compatibility <strong>of</strong> the various layers. The thermal<br />
nature, leading to precise characterization, <strong>of</strong> defect areas have also be explored by this technology.<br />
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While the equipment is rather expensive, some consulting physical testing laboratories are acquiring the<br />
equipment <strong>and</strong> <strong>of</strong>fering customized analyses.<br />
Source <strong>of</strong> the equipment: TA Instruments Ltd., Europe House, Bilton Center, Cleeve Road, Leatherhead, KT<br />
227UQ, Surrey, UK; 44+1372/360-363; Fax: 44+1372/360-135; tlever@taeurope.co.uk.<br />
Wetting <strong>of</strong> Nonwoven <strong>Fabrics</strong><br />
The wetting <strong>of</strong> a nonwoven fabric by water <strong>and</strong> other liquids is <strong>of</strong> critical importance in many nonwoven<br />
applications. The most obvious situation, <strong>and</strong> one which has been studied extensively, is the wetting <strong>of</strong><br />
nonwoven topsheet <strong>of</strong> a diaper by urine voided by the wearer. A rapid wetout <strong>and</strong> passage <strong>of</strong> the liquid through<br />
the nonwoven is critical to the performance <strong>of</strong> baby diapers <strong>and</strong> similar absorbent sanitary products.<br />
St<strong>and</strong>ard test methods have been developed <strong>and</strong> carefully studied to measure the property <strong>of</strong> fabric wetting in<br />
this setting. Nonwoven diaper facing typically requires a wet-out or strike-through time <strong>of</strong> only a few seconds<br />
to be acceptable by most converters.<br />
The wetting performance <strong>of</strong> a fabric can be determined quite simply: Place a drop <strong>of</strong> water from an eyedropper<br />
or similar device to give a relatively constant size drop; carefully observe the drop <strong>and</strong> determine the time<br />
required for the drop to be absorbed into the fabric. Once wetting <strong>of</strong> the liquid occurs, absorbency into the<br />
fabric generally occurs very rapidly. If the droplet stays on the surface as an intact sphere for a considerable<br />
period <strong>of</strong> time, the fabric has poor or no wetting performance.<br />
Water (pure or otherwise) can be replaced by saline solution (0.9 weight percent sodium chloride solution),<br />
physiological saline solution (sodium chloride plus other minor constituents), synthetic urine, synthetic<br />
menstrual fluid, synthetic blood or a variety <strong>of</strong> other liquids. The time <strong>of</strong> wetting can be controlled by a variety<br />
<strong>of</strong> methods, <strong>and</strong> can also be automated. The time <strong>of</strong> wetting can usually be determined fairly easily, as the<br />
droplet tends to show a somewhat different visual appearance <strong>and</strong> to spread slightly immediately shortly<br />
before disappearing into the interior <strong>of</strong> the fabric.<br />
For those who want a more precise or quantitative method, variations have been used with some success. For a<br />
pure scientific method, the traditional contact angle <strong>of</strong> the Lucas Washburn equation is <strong>of</strong>ten attempted.<br />
However, upon study it is soon realized that the scientific contact angle is dependent upon having a smooth,<br />
pure, uniform surface where the interface <strong>of</strong> liquid, solid <strong>and</strong> gas can be assessed. Looking at the surface <strong>of</strong> a<br />
nonwoven fabric clearly shows that these requirements are not met.<br />
Much work has been done on single fiber wetting to substitute for the shortcomings <strong>of</strong> a fabric surface<br />
characteristics. This can yield considerable useful information, but it <strong>of</strong>ten departs substantially from the<br />
environment encountered by the drop <strong>of</strong> liquid on a nonwoven fabric surface.<br />
One approach to measuring the contact angle <strong>of</strong> nonwoven fabrics was <strong>of</strong>fered by Cusick <strong>and</strong> Hopkins<br />
(Cusick, G.E. <strong>and</strong> Hopkins, Teresa, INDA <strong>Journal</strong> <strong>of</strong> Nonwoven Research, 1, No. 1, pp. 32-34, 1989). This<br />
method involves an apparatus which holds the test fabric <strong>and</strong> can be rotated until the meniscus formed by the<br />
liquid <strong>and</strong> the fabric "disappears," or the liquid at the fabric surface is level.<br />
Clearly, a controlled technique is needed that approximates the control, precision <strong>and</strong> preciseness <strong>and</strong><br />
versatility <strong>of</strong> the contact angle method, while allowing adaptability to the radically different character <strong>of</strong> a<br />
fabric surface.<br />
A useful adaptation <strong>and</strong> amalgamation <strong>of</strong> these desires is afforded by a method described in a U.S. patent that<br />
was granted a few years ago. The method was originally devised to assess the ability <strong>and</strong> suitability <strong>of</strong> a<br />
nonwoven filter fabric surface to quickly wet out <strong>and</strong> pass whole blood, such as involved in a blood bank<br />
collection operation. With suitable filtration, depletion <strong>of</strong> the leucocytes (white blood cells) in the blood can be<br />
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achieved. These are the cells which have surrounded bacteria, viruses <strong>and</strong> other blood debris; their removal<br />
from the collected blood can greatly improve the quality <strong>of</strong> the blood, <strong>and</strong> rid it <strong>of</strong> the normal risk for a<br />
transfusion patient.<br />
To be practical, an infusion set-up for injecting the blood into a patient must work correctly every time; a<br />
blood filter unit that slows or halts the flow <strong>of</strong> blood from the collection/storage bag into the patient cannot be<br />
tolerated. The pressure driving the blood flow is modest; only that coming from a height <strong>of</strong> several inches.<br />
As a consequence <strong>of</strong> a need for a quick, definitive laboratory test, the inventors <strong>of</strong> this patent fashioned a<br />
modified test method that mimics the utility <strong>of</strong> the contact angle method, applied to the needs <strong>and</strong> surface <strong>of</strong> a<br />
nonwoven filter medium. Their method is called the "Critical Wetting Surface Tension (CWST)."<br />
The method involves a series <strong>of</strong> test solutions having a range <strong>of</strong> surface tensions. A set <strong>of</strong> test solutions is<br />
prepared so that each solution has a surface tension <strong>of</strong> about 3.0 units different than the other solutions. The set<br />
<strong>of</strong> test solutions is prepared so that it covers the range from pure water (73 dynes/cm) to that <strong>of</strong> a fluorocarbon<br />
liquid (25 to 30 dynes/cm range).<br />
The test is carried out by placing 10 st<strong>and</strong>ard-sized drops <strong>of</strong> a test liquid on the surface <strong>of</strong> the nonwoven fabric.<br />
A timer is started at that time, providing for a 10-minute time interval. The test drops are observed for letting<br />
<strong>and</strong> absorption into the fabric at the end <strong>of</strong> that time interval. If at least nine <strong>of</strong> the 10 drops are absorbed<br />
within the 10-minute test period, it is concluded that the test solution wets the fabric. If less than nine <strong>of</strong> the ten<br />
drops are absorbed within the 10-minute time period, it is concluded that the liquid does not wet the fabric.<br />
Tests are run with the solutions from the set <strong>of</strong> st<strong>and</strong>ard surface tension samples until two test solutions with<br />
surface tensions separated by no more than 3.0 dynes/cm are identified, the one test solution wetting the fabric<br />
(giving at least nine out <strong>of</strong> 10 drops that wet the fabric), <strong>and</strong> the other test solution not wetting the fabric (gives<br />
less than nine out <strong>of</strong> 10 drops that wet the fabric). The fabric wetting performance, CWST, is then calculated<br />
as the average surface tension <strong>of</strong> the two identified test solutions.<br />
While the CWST is not exactly identical with the surface character measured by the critical angle test method,<br />
it is a very good empirical substitute, <strong>and</strong> can nicely characterize a nonwoven fabric surface. Such<br />
characterization can be very useful for many situations. There appears to be a relationship with the CWST <strong>of</strong> a<br />
nonwoven fabric <strong>and</strong> the specific surface energy <strong>of</strong> the pure polymer making up the fibers <strong>of</strong> a pure fabric<br />
(non-blended fibers). Also, the CWST correlates well with the specific surface energies <strong>of</strong> the pure polymer<br />
making up fibers in a blended fiber fabric. The presence <strong>of</strong> fiber finish <strong>and</strong> other surface treatments, additives<br />
<strong>and</strong> modifications that affect the fiber surface can be detected. The importance <strong>of</strong> surface tensions <strong>of</strong> the<br />
participating liquids <strong>of</strong> the application can also be delineated.<br />
By using 10 drops <strong>of</strong> the test fluid, a good average is obtained, even taking into account the non-uniformities<br />
<strong>of</strong> a typical fabric surface. The use <strong>of</strong> test solutions with relatively small differences in surface tension, <strong>and</strong> the<br />
averaging <strong>of</strong> data points also helps to even out any abnormalities <strong>and</strong> departures from strict test methodology.<br />
The end result is a versatile, empirical test method that can be very useful in a variety <strong>of</strong> applications.<br />
Source: "Device <strong>and</strong> method for depletion <strong>of</strong> the leukocyte content <strong>of</strong> blood <strong>and</strong> blood components." U.S.<br />
Patent No. 4,925,572 (May 15, 1990). Inventor: David B. Pall. Assignee: Pall Corporation.<br />
Kilobytes versus Kibibytes<br />
A previous issue <strong>of</strong> INJ (Vol. 7, No. 2; Spring, 1995) featured a table in the Researcher's Tool Box that<br />
outlined the prefixes to be used for increasing <strong>and</strong> decreasing orders <strong>of</strong> magnitude. Thus, for an increase <strong>of</strong> 10,<br />
100 or 1,000 times, a simple prefix can be attached to the basic unit to indicate this increase. Similarly, another<br />
set <strong>of</strong> prefixes can be utilized to indicate decreasing orders <strong>of</strong> magnitude. By combining the prefixes with<br />
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scientific units, as specified in the SI System, a considerably simplified <strong>and</strong> consistent notation system results.<br />
This system is outlined in the table below.<br />
10 24 yotta (Y), from Greek <strong>of</strong> Latin octo (eight)<br />
10 21 zetta (Z), from Latin septem (seven)<br />
10 18 exa (F), from Greek hex (six)<br />
10 15 peta (P), from Greek pente (five)<br />
10 12 tera (T), from Greek teras (monster)<br />
10 9 giga (G), from Greek gigas (giant)<br />
10 6 mega (M), from Greek megas (large)<br />
10 3 kilo (k), from Greek chilioi (thous<strong>and</strong>)<br />
10 2 hecto (h), from Greek hekaton (hundred)<br />
10 1 deka or deca (da), from Greek deka (ten)<br />
10 -1 deki (d), from Latin decimus (tenth)<br />
10 -2 centi (c), from Latin centum (hundred)<br />
10 -5 milli (m), from Latin Mille (thous<strong>and</strong>)<br />
10 -6 micro (m), from Latin micro or Greek mikros (small)<br />
10 -9 nano (n), from Latin nanus or Greek nanos (dwarf)<br />
10 -12 pico (p), from Spanish pico (a bit) or Italian piccolo (small)<br />
10 -15 femto (f), from Danish-Norwegian femten (fifteen)<br />
10 -18 atto (a), from Danish-Norwegian atten (eighteen<br />
10 -21 zepto (z), from Latin zeptem (seven)<br />
10 -24 yocco (y), from Greek or Latin octo (eight)<br />
With the advent <strong>of</strong> the computer <strong>and</strong> its accompanying "computerese," these prefixes have been adopted in a<br />
similar manner. Thus, everyone knows that a megabyte is one million bytes. And that a gigabyte is a thous<strong>and</strong><br />
million bytes or one billion bytes. The use <strong>of</strong> this prefix system is so pervasive that the abbreviation system has<br />
been further abbreviated; thus, everybody knows <strong>and</strong> can respond appropriately when told that a computer has<br />
10 "gig" <strong>of</strong> memory.<br />
Unfortunately, this system <strong>of</strong> prefixes applied to the computer situation is not strictly correct. Whereas, the<br />
normal scientific system or metric is based on 10 digits, called a decimal system, in computer work a binary<br />
system based on a two-digit code is employed. Therefore, a "kilo" in the binary computer system is actually<br />
1,024 instead <strong>of</strong> 1,000 (2 to the 10th power).<br />
Consequently, the use <strong>of</strong> the normal metric system prefix is actually incorrect when applied to the computer<br />
binary system.<br />
Thus lacking in exactness, two major organizations have adopted new numerical prefixes for numbers in the<br />
computer binary system. The International Electro-Technical Commission (IEC) is responsible for<br />
international st<strong>and</strong>ards for electronic technologies. With considerable imput from the National Institute <strong>of</strong><br />
St<strong>and</strong>ards <strong>and</strong> Technology (NIST) in the United States, a new system has been adopted for the binary system.<br />
Now, to represent exponentially increasing binary multiples, the IEC has designated kibi (Ki), mebi (MI), gibi<br />
(Gi), tebi (Ti), pebi (Pi) <strong>and</strong> exbi (Ei). Thus a kibibyte is 2 to the 10th power or 1,024 bytes; a mebibyte is 2 to<br />
the 20th power, or 1,048,576 bytes; <strong>and</strong> so forth.<br />
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St<strong>and</strong>ard Development Forum<br />
INJ DEPARTMENTS<br />
STANDARDS DEVELOPMENT<br />
FORUM<br />
By Chuck Allen, INDA Technical Director<br />
Test Method Harmonization<br />
The buzzword in the area <strong>of</strong> st<strong>and</strong>ardized test methods is harmonization (making test methods the same in different parts <strong>of</strong> the<br />
world). As discussed in the last issue <strong>of</strong> the INJ, there are any number <strong>of</strong> st<strong>and</strong>ards setting organizations worldwide. Each<br />
organization has its own process for evaluating <strong>and</strong> adopting test methods.<br />
One can imagine the technical <strong>and</strong> political difficulties that could be associated with identical test methods being adopted by two<br />
or more <strong>of</strong> the organizations. Having to use different test methods on the same product, depending on where the product is being<br />
sold geographically, presents difficulties <strong>and</strong> is costly. Laboratories may need to purchase <strong>and</strong> maintain different pieces <strong>of</strong><br />
equipment or instruments for testing the same properties <strong>of</strong> fabrics or products. To be able to generate reliable <strong>and</strong> reproducible<br />
results, lab personnel must become familiar <strong>and</strong> experienced in conducting the applicable test methods from more than one<br />
st<strong>and</strong>ard setting source.<br />
Almost all the st<strong>and</strong>ard setting organizations recognize there is dem<strong>and</strong> for test method harmonization <strong>and</strong> are investigating ways<br />
<strong>of</strong> cooperating with each other to reach this difficult goal.<br />
Harmonization In Nonwovens: INDA <strong>and</strong> EDANA have made test method harmonization a high priority. INDA publishes its<br />
own St<strong>and</strong>ard Test Method (STM) manual, which contains over 50 test methods for nonwoven fabrics. Test methods from the<br />
STM manual are then moved through the ASTM process, where the goal is to have them all eventually approved as ASTM<br />
methods, <strong>and</strong> in the ASTM format. All the currently adopted ASTM Nonwovens test methods, except for the geotextile methods,<br />
originated as INDA St<strong>and</strong>ard Test Methods.<br />
Likewise, EDANA publishes a test method manual, EDANA Recommen-ded Test Methods (ERT), containing over 40 methods<br />
for testing nonwoven fabrics. EDANA works through CEN (European Committee for St<strong>and</strong>ardization) <strong>and</strong> ISO (International<br />
Organization for St<strong>and</strong>ards) to have their methods recognized as national <strong>and</strong> international st<strong>and</strong>ards.<br />
The STM <strong>and</strong> ERT manuals contain many methods that measure the same properties, but the methods have differences. Due to<br />
recent correlation activities by the two organizations, there are now five methods that have been harmonized <strong>and</strong> are identical as<br />
contained in the INDA STM <strong>and</strong> the EDANA ERT manuals.<br />
Work has begun on the next series <strong>of</strong> five STM <strong>and</strong> ERT methods scheduled for harmonization. INDA, through the Nonwovens<br />
Cooperative Research Center (NCRC) at North Carolina State University, has put together a harmonization document, which is<br />
in its final editing stages; this document lists the differences between INDA STM methods <strong>and</strong> related EDANA, ASTM, TAPPI,<br />
ISO <strong>and</strong> AATCC methods. This document will soon be available through INDA.<br />
Global Harmonization: INDA <strong>and</strong> EDANA are not the only ones involved in test method harmonization. In late 1998, ASTM<br />
<strong>and</strong> ISO had a meeting to discuss how they could work together more productively. As an outcome, ASTM submitted a pilot<br />
program for ISO consideration involving ASTM st<strong>and</strong>ards used in the global market where there are no ISO counterpart<br />
st<strong>and</strong>ards. ASTM would be the developer <strong>and</strong> maintainer <strong>of</strong> the st<strong>and</strong>ards <strong>and</strong> would actively seek input from ISO member<br />
bodies. The resulting st<strong>and</strong>ards would carry an ASTM/ISO designation.<br />
The proposal has met with approval by the ISO leadership task force <strong>and</strong> has been presented to the ISO council for final<br />
approval. At the time <strong>of</strong> this writing, the outcome is not known, but the vote was expected to take place at the ISO meeting in<br />
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July. It is important to note that this new system would be on an<br />
individual test method basis. Any communication <strong>and</strong> cooperation<br />
between ASTM <strong>and</strong> ISO must be considered a step in the right<br />
direction toward harmonization.<br />
In Europe, CEN is st<strong>and</strong>ardizing methods <strong>of</strong> its member<br />
countries, which include Austria, Belgium, Czech Republic,<br />
Denmark, Finl<strong>and</strong>, France, Germany, Greece, Icel<strong>and</strong>, Irel<strong>and</strong>,<br />
Italy, Luxembourg, the Netherl<strong>and</strong>s, Norway, Portugal, Spain,<br />
Sweden, Switzerl<strong>and</strong> <strong>and</strong> the United Kingdom. The national<br />
st<strong>and</strong>ard organizations <strong>of</strong> the member countries are bound to<br />
implement CEN approved European St<strong>and</strong>ards, either by<br />
publication <strong>of</strong> an identical text or by endorsement, <strong>and</strong> conflicting<br />
national st<strong>and</strong>ards will be withdrawn within a given time period.<br />
This will result in harmonizing test methods used within all the<br />
CEN countries.<br />
As can be seen, test method harmonization activities are taking<br />
place around the world <strong>and</strong> are to be applauded. Having global<br />
harmonization <strong>of</strong> test methods is a noble goal that will take lots <strong>of</strong><br />
work <strong>and</strong> even then may not be accomplished in all areas. When<br />
asked, "Is achieving a single st<strong>and</strong>ard practical?" Sergio Mazza,<br />
president <strong>of</strong> ANSI replied, "Sometimes yes, sometimes no. To try<br />
to answer this question out <strong>of</strong> the context <strong>of</strong> a specific application<br />
is completely pointless. In every sector, <strong>and</strong> sometimes in every<br />
instance within a given sector, you're going to get a different<br />
answer. I do believe you can make a general statement <strong>of</strong><br />
principle that you would rather have fewer than more st<strong>and</strong>ards,<br />
that you want to minimize duplication, that you want to minimize<br />
TANDEC Schedules Conference<br />
The ninth annual TANDEC Conference will be held<br />
November 10-12, <strong>1999</strong> at UT Conference Center, The<br />
University <strong>of</strong> Tennessee, Knoxville, Tennessee, USA <strong>and</strong><br />
focus on several exciting areas <strong>of</strong> the nonwovens industry<br />
<strong>and</strong> technology:<br />
● Marketing Analysis <strong>of</strong> Nonwovens<br />
● Innovations in Spunbond <strong>and</strong> Melt Blown Technology<br />
● Nonwoven Composites <strong>and</strong> New Applications<br />
● New Technology Development <strong>and</strong> Opportunities<br />
● Fundamental Studies in Nonwovens<br />
Attendees will receive concise <strong>and</strong> practical information on<br />
new nonwoven products <strong>and</strong> markets, <strong>and</strong> gain a firm<br />
underst<strong>and</strong>ing <strong>of</strong> the latest technological advances in<br />
meltblowing, spunbonding <strong>and</strong> related processes.<br />
TANDEC Conferences feature a broad cross section <strong>of</strong><br />
speakers, who combine the best aspects <strong>of</strong> industry, academia<br />
<strong>and</strong> the consulting sphere. Pr<strong>of</strong>essionals in nonwovens R&D,<br />
marketing, production <strong>and</strong> management will benefit by<br />
attending this conference. For additional conference<br />
information please meet us in cyberspace at:<br />
http://web.utk.edu/tancon. For conference schedule:<br />
http://web.utk.edu/tancon/program.html. For registration<br />
info: http://web.utk.edu/tancon/registra.html.<br />
conflict, but in many circumstances you can't eliminate duplication <strong>and</strong> conflict. You're dealing with different technical<br />
infrastructures, or different regulatory infrastructures, in each sector, <strong>and</strong> in different parts <strong>of</strong> the world. The challenges are<br />
dem<strong>and</strong>ing <strong>and</strong> the goals are worthwhile. Globalization is not a fad. It is here to stay <strong>and</strong> there is a need <strong>and</strong> desire for global test<br />
method harmonization. "<br />
FORMALDEHYDE TEST METHOD EVALUATION FOR NONWOVEN PRODUCTS<br />
Industry Collection Developmement Specific Interference Range Instrument Ease<br />
Time<br />
(ppm)<br />
AATCC Textile Water Nash Yes Yes 10-3500 Spectrom. Easy<br />
Many/day<br />
Japanese Japan Water Nash Yes Yes 10-3500 Spectrom. Easy<br />
Many/day<br />
HPLC ASTM N/A HPLC Yes No >0.05 HPLC Med.<br />
Many/day<br />
Tube Furnace UF/Glass Air/Temp. DNPH/HPLC Yes No >0.05 HPLC Med.<br />
10-15/day<br />
Chamber Wood Air/Temp. ? (Yes) (No) HPLC Med.<br />
Limited<br />
Humidity<br />
Head/Space Chemical Air/Temp GC/MS Yes No >25 GC/MS Med.<br />
8-10/day<br />
GC/MS<br />
Hard<br />
Formaldehyde Measurements<br />
Considerable effort has been focused on formaldehyde, formaldehyde content, formaldehyde analysis <strong>and</strong> related problems over<br />
the past several years. Many concrete <strong>and</strong> expensive steps have been taken by the Nonwovens industry to ensure compliance with<br />
a vast array <strong>of</strong> regulations.<br />
One <strong>of</strong> the most positive <strong>and</strong> helpful activities in this regard has been the TAPPI Binders <strong>and</strong> Additives Committee work directed<br />
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St<strong>and</strong>ard Development Forum<br />
toward the formaldehyde problem. This committee has carried out an<br />
aggressive program focused on developing useful facts <strong>and</strong> technology,<br />
while dispelling myths <strong>and</strong> bias. Status reports <strong>of</strong> this effort were provided<br />
in 1995 <strong>and</strong> the results <strong>of</strong> a Round Robin testing exercise were provided in<br />
1996.<br />
This committee recently completed a major phase <strong>of</strong> their work <strong>and</strong> has<br />
provided a definitive status report on the extensive effort expended. This<br />
report was circulated as a separate paper at the recent TAPPI Technical<br />
Conference (March, <strong>1999</strong>), although it was not presented verbally. This<br />
summary report was prepared by the three leaders <strong>of</strong> the Sub-committee<br />
efforts: Michele Mlynar (Rohm <strong>and</strong> Haas Company); Tom McNeal (Borden,<br />
Inc.) <strong>and</strong> S.J. Wolfersberger (Owens Corning Fiberglas). However, because<br />
<strong>of</strong> the seminal nature <strong>of</strong> the report, wider circulation is certainly justified.<br />
What follows is an abstract <strong>of</strong> this report, prepared to provide insight into<br />
the essentials <strong>and</strong> conclusions <strong>of</strong> the report.<br />
The objective <strong>of</strong> the "Formaldehyde Testing Task Force" was to review<br />
available methods for the measurement <strong>of</strong> formaldehyde for nonwovens, <strong>and</strong><br />
to agree on industry measurement st<strong>and</strong>ard. The committee identified three<br />
areas for formaldehyde measurements related to the nonwoven<br />
manufacturing process:<br />
Binders: water-based emulsions, phenol-formaldehyde resins,<br />
melamine-formaldehyde resins, <strong>and</strong> urea-formaldehyde resins.<br />
Stack Emissions: ducts, ventilation systems, venting stacks <strong>and</strong> other<br />
process sources.<br />
Nonwoven Products: formaldehyde content, evolution from disposable,<br />
durable <strong>and</strong> industrial nonwoven products.<br />
Each area was assigned to a committee which reviewed different test<br />
methods used by various segment <strong>of</strong> the industry. These various test<br />
methods were evaluated by establishing test criteria <strong>and</strong> comparing the<br />
different methods against these criteria. This report summarizes the<br />
formaldehyde test methods evaluated for these three different industry<br />
segments.<br />
The committee found that a single method cannot be recommended for each<br />
industry segment, but that several methods can <strong>of</strong>ten be considered for each<br />
segment. This report can be summarized as follows:<br />
Binders: For water-based emulsions, the ASTM Method (#PS-94-4/#D<br />
5910-96) <strong>and</strong> the AC Method (#AC-7) were examined. The ASTM method<br />
has been approved by ASTM <strong>and</strong> other groups, performs very well, <strong>and</strong> can<br />
be recommended without further evaluation. It is somewhat more complex<br />
<strong>and</strong> more expensive. The AC Method is limited to low pH emulsions. The<br />
ASTM Method is preferred.<br />
Phenol-Formaldehyde resins were evaluated by three methods (ISO #9397;<br />
#IR-038-05; #M2221.2), all <strong>of</strong> which use the same analysis mechanism. The<br />
methods differ by endpoint pH determination method, inclusion <strong>of</strong><br />
calibration or blank procedures, <strong>and</strong> certification. All three methods are<br />
more or less equivalent in their results. The ISO (International St<strong>and</strong>ards<br />
Organization) Method has industry certification <strong>and</strong> is the basic<br />
recommendation..<br />
Melamine-Formaldehyde resins were only analyzed by the Method<br />
ASSOCIATION FORUM<br />
Oil Spill Cleanup St<strong>and</strong>ards<br />
Like many complex activities, techniques for<br />
h<strong>and</strong>ling oil spills have been spur-<strong>of</strong>-the-moment<br />
<strong>and</strong> highly empirical. The experience <strong>of</strong> the last 10<br />
years has provided some useful guidelines in<br />
dealing with these calamities, but the technology<br />
<strong>and</strong> procedures are far from being well established.<br />
To assist in moving toward a more rational<br />
approach to remediating the oil spills <strong>and</strong> related<br />
incidents, the American Society for Testing<br />
Materials (ASTM) has initiated an effort to<br />
develop oil spill cleanup st<strong>and</strong>ards. To that end,<br />
ASTM is requesting assistance in developing new<br />
st<strong>and</strong>ards for shoreline oil spill cleanup <strong>and</strong><br />
restoration.<br />
Members <strong>of</strong> oil spill cleanup cooperatives,<br />
response teams, oil spill removal organizations, oil<br />
companies <strong>and</strong> others are invited to provide input<br />
for develop <strong>of</strong> these guidelines. This project is<br />
under the chairmanship <strong>of</strong> Dr. Dick Lessard, who<br />
is Oil Spill Technology Coordinator for Exxon<br />
Research <strong>and</strong> Engineering.<br />
Additional st<strong>and</strong>ards are also being prepared for<br />
subcommittee review, including the selection <strong>of</strong><br />
the appropriate shoreline cleaning techniques <strong>and</strong><br />
the classification <strong>of</strong> shoreline types, along with<br />
definition <strong>and</strong> delineation <strong>of</strong> cleanup materials.<br />
Comments in regards to these <strong>and</strong> other shoreline<br />
cleanup st<strong>and</strong>ards are also invited.<br />
In view <strong>of</strong> the fact that meltblown oil sorbants<br />
constitute one <strong>of</strong> the major resources for this<br />
activity, a significant contribution from this<br />
segment <strong>of</strong> the nonwovens industry is expected.<br />
For further information or to participate in the<br />
preparation <strong>of</strong> these st<strong>and</strong>ards, the ASTM contact<br />
is Robyn Zelmo, 610-832-9717; Fax:<br />
610-832-9666; rzelmo@astm.org.<br />
Cellulose Aging Study<br />
An interesting research project has been initiated<br />
by The American Society for Testing <strong>and</strong><br />
Materials (ASTM). This will involve a<br />
century-long study <strong>of</strong> the effects <strong>of</strong> natural aging<br />
on printing <strong>and</strong> writing papers. A total <strong>of</strong> 15<br />
experimental paper types will be stored in volume<br />
form by 10 North America universities <strong>and</strong><br />
government agencies. Normal storage conditions<br />
as encountered in a typical library stack will be<br />
involved. Samples will be withdrawn from the<br />
specimens at various time intervals to follow the<br />
changes with time. A century may seem like a long<br />
time to wait for results, but it was decided that<br />
accelerated aging studies need to be cross-checked<br />
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St<strong>and</strong>ard Development Forum<br />
(#ADCH-0188). This method was selected as the resin has a high pH <strong>and</strong><br />
requires initial neutralization, which is provided for in the method. This<br />
method is very similar to the urea-formaldehyde method, after the<br />
neutralization step. It is considered to be quite comparable to the UF<br />
methods. It provides satisfactory results.<br />
with actual experience. However, the researchers<br />
who are initiating the project will not be waiting<br />
around for the results<br />
Urea-Formaldehyde resins were subjected to four test methods (#ADCH-0184; #M2221.1; #ACDH-0185; A.P.#32), all <strong>of</strong> which<br />
were based on the same chemistry. Because <strong>of</strong> the possibility <strong>of</strong> unwanted hydrolysis <strong>of</strong> the resin, the methods are rather<br />
sensitive to operator technique. All four variations are considered valid <strong>and</strong> are quite comparable.<br />
Recommendations for using the methods studied are provided. Suggestions on calibrating the analysis, potential sources <strong>of</strong> error<br />
<strong>and</strong> variation, an indication <strong>of</strong> precision, etc. are <strong>of</strong>fered for some <strong>of</strong> the methods.<br />
Stack Emissions: In this category, five test methods were reviewed, but no recommendations were made, as no Round Robin<br />
tests have been conducted so far.<br />
The analytical methods considered included the following:<br />
Chromotrophic Acid: Samples are collected in impingers, usually with aqueous 1% sodium bisulfite as the impinger collection<br />
solution. Normally, an EPA Method 5 train is used with a heated filter <strong>and</strong> probe ahead <strong>of</strong> the impinger sampling train. Impinger<br />
samples are analyzed by the chromotropic acid method, forming a purple color proportional to formaldehyde concentration,<br />
which is measured in a spectrophotometer at a wavelength <strong>of</strong> 580 nm.<br />
Dinitrophenylhydrazine Method: Samples are collected in impingers, usually using saturated 2,4,DNPH (dinitrophenylhydrazine)<br />
in aqueous 2 NHCl as the impinger collection solution. Normally, an EPA Method 5 train is used with a heated filter <strong>and</strong> probe<br />
ahead <strong>of</strong> the impinger sampling train. Impinger samples are extracted with methylene chloride, <strong>and</strong> the extracts are analyzed by<br />
liquid chromatography. The chromatographic separation is usually optimized so that a variety <strong>of</strong> aldehydes <strong>and</strong> ketones can be<br />
determined in a single analysis.<br />
Pararosaniline: Samples are collected in impingers, using high-purity water as the impinger collection solution. Normally, an<br />
EPA Method 5 train is used (without a filter) <strong>and</strong> probe ahead <strong>of</strong> the impinger sampling train. Impinger samples are analyzed by<br />
the pararosaniline method, forming a purple color proportional to formaldehyde concentration, which is measured in a<br />
spectrophotometer at a wavelength <strong>of</strong> 570 nm.<br />
Fourier-Transform Infrared Spectro-scopy: Measurements are made directly on the stack gas, by passing an infrared beam across<br />
the stack (in-situ), or by extracting a portion <strong>of</strong> the gas into a cell. High-resolution infrared spectra are obtained, <strong>and</strong> interfering<br />
spectral features (from compounds such as water, carbon dioxide, etc.) are subtracted from the spectra. The amount <strong>of</strong><br />
formaldehyde can then be calculated by comparison to a stored reference spectrum <strong>of</strong> a formaldehyde st<strong>and</strong>ard.<br />
Acetylacetone: Samples are collected in impingers, using high-purity water or 10% methanol in water as the impinger collection<br />
solution. Normally, an EPA Method 5 train is used with heated filter <strong>and</strong> probe ahead <strong>of</strong> the impinger sampling train. Impinger<br />
samples are analyzed by the acetylacetone method, forming a yellow color proportional to formaldehyde concentration, which is<br />
measured at a wavelength <strong>of</strong> 412 nm.<br />
It is suggested that Round Robin testing is appropriate in this sector, along with a further study <strong>of</strong> Head Space/Gas<br />
Chromotography/Mass Spectography Detection (GC/MS) Method.<br />
Nonwoven Products: In this industry sector, a total <strong>of</strong> 10 test methods were submitted <strong>and</strong> reviewed, including the following:<br />
AATCC Sealed Jar Test #112-1993: This method is used for nonwovens <strong>and</strong> other textiles employed in the industry. It measures<br />
the free formaldehyde plus some <strong>of</strong> the bound formaldehyde in a fabric.<br />
Tube Furnace Method: This method is specific for urea-formaldehyde <strong>and</strong> glass mat products. With HPLC development properly<br />
carried out, it is very specific for formaldehyde.<br />
Japanese Ministry Ordinance Article #4, Legislation #112, 1973: This method measures the free formaldehyde in a sample, but<br />
under some conditions can generate analyte from bound formaldehyde. The method is required for any imports into Japan. It is<br />
also growing in use as a st<strong>and</strong>ard method for the baby wipe industry.<br />
Chamber Test: This method is used by the wool industry to measure the formaldehyde emission from wool dust particles. It is a<br />
dynamic test that could be adapted for nonwovens, but required further development work.<br />
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Head Space/GC/MS: Further work is required to assess the value <strong>of</strong> this method in comparison to other methods.<br />
LC Pre-Derivatization (High Pressure Liquid Chromatography, HPLC/Nash): This method uses high pressure liquid<br />
chromatography to separate the free formaldehyde from the other components, followed by post column derivatization with Nash<br />
reagent <strong>and</strong> visible absorbence detection. It is a method under development, so is not appropriate at this time for a st<strong>and</strong>ard.<br />
MITI JIS-L1041-1960: This method is the forerunner <strong>of</strong> the present Japanese Law 112-1993 <strong>and</strong> has been replaced by the more<br />
recent method. It is not recommended.<br />
KCN Method: This method was not recommended <strong>and</strong> is not being further studied.<br />
Shirley Institute Test: This test was developed many years ago; it is not recommended <strong>and</strong> will not receive further work.<br />
The first six method were subjected to further evaluation <strong>and</strong> rated for characteristics <strong>and</strong> appropriateness, as summarized above.<br />
It is hoped that individuals who have a definite interest in this report <strong>and</strong> topic will pursue the matter further. For those who<br />
would like to learn more about this project, or make comments on the report <strong>and</strong> the committee's activities, or to study the<br />
material further, a copy <strong>of</strong> the report can be obtained from Michele Mlynar, Specialty Polymers Group Leader, Fiber <strong>and</strong> Textile<br />
Polymers, Rohm <strong>and</strong> Haas, Research Laboratories, 727 Norristown Road, P.O. Box 904, Spring House, PA 19477;<br />
215-641-7107; Fax: 215-619-1622; michele_f_mlynar@rohmhaas.com<br />
Your comments <strong>and</strong> suggestions regarding this department <strong>and</strong> the area <strong>of</strong> st<strong>and</strong>ards development are welcome, please respond<br />
to Chuck Allen, callen@inda.org; INDA, P.O. Box 1288, Cary, N.C. 27513; 919-233-1210, ext. 114, Fax 919-233-1282.<br />
The editors wish to express their appreciation to Mr. Allen for agreeing to develop <strong>and</strong> edit this column.<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
—INJ<br />
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Patent Review<br />
PATENT<br />
REVIEW<br />
INJ DEPARTMENTS<br />
Spunbond <strong>Fabrics</strong> from Nylon <strong>and</strong> Polyethylene<br />
Continuous filament nylon spunbond fabrics are a special category within the spunbond nonwoven<br />
classification. The fabrics are produced by a process in which molten nylon-66 resin is extruded into<br />
continuous filaments, the filaments are attenuated <strong>and</strong> drawn pneumatically, <strong>and</strong> then deposited onto a<br />
collection surface to form a continuous filament web. These filaments are bonded together to produce a<br />
strong, coherent fabric.<br />
Filament bonding in the case <strong>of</strong> nylon can be accomplished either thermally or chemically. Thermal<br />
bonding is accomplished by passing the web <strong>of</strong> filaments through the nip <strong>of</strong> a pair <strong>of</strong> heated calender<br />
rolls; one <strong>of</strong> the rolls carries a pattern <strong>of</strong> elevated points providing discontinuous bond sites resulting<br />
from the heat <strong>and</strong> pressure <strong>of</strong> the calender points.<br />
Chemical or autogenic bonding can also be employed; in this operation, the web <strong>of</strong> filaments is<br />
transported to a chemical bonding station or a "gas house," which exposes the filaments to a mixture <strong>of</strong><br />
hydrogen chloride gas <strong>and</strong> water vapor. The water vapor enhances the penetration <strong>of</strong> the hydrogen<br />
chloride gas into the filaments; the mixture causes the filaments to become tacky <strong>and</strong> thus amenable to<br />
autogenic bonding. Upon leaving the bonding station, the web passes between rolls which compact <strong>and</strong><br />
bond the s<strong>of</strong>tened filaments in the web. Adequate bonding is necessary to minimize fabric fuzzing (that<br />
is, the presence <strong>of</strong> unbonded filaments) <strong>and</strong> to impart good strength properties to the fabric. Autogenic<br />
bonding has been especially used in forming spunbond nylon- 66 industrial fabrics.<br />
Whether bonded by the intermittent thermobond process or autogenic bonding agents, these nonwoven<br />
fabrics tend to be somewhat stiff <strong>and</strong> boardy, as produced. This arises from the fact that even with point<br />
bonded fabrics, it is frequently difficult or even impossible to strictly limit bonding to the desired points.<br />
Filaments that are not compressed by the embossed points are still subject to the heat <strong>of</strong> the calender <strong>and</strong><br />
tend to form weak, secondary or "tack" bonds <strong>of</strong> the filaments outside the desired bond areas. In a similar<br />
manner in autogenic bonding, secondary or tack bonds can form between filaments where the area <strong>of</strong><br />
contact is very limited, giving weak bonds.<br />
In both processes, these weak, secondary bonds promote fabric stiffness, but contribute little to fabric<br />
strength <strong>and</strong> integrity. Consequently, it has been found beneficial to subject such nonwoven fabrics to a<br />
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s<strong>of</strong>tening process. This is generally done by subjecting the fabric to mechanical stress. Such treatments<br />
are believed to effect s<strong>of</strong>tening primarily by breaking the weak, secondary tack bonds, which can be<br />
broken without breaking the primary point bonds or those bonds intentionally created to foster strength.<br />
The mechanical stress methods for s<strong>of</strong>tening may include the process <strong>of</strong> washing the fabric, drawing the<br />
fabric under tension over sharply angled surface such as a knife blade, stretching the fabric, twisting,<br />
crumpling or subjecting the fabric to various combinations <strong>of</strong> such treatments. The fabrics can also be<br />
s<strong>of</strong>tened by impinging the fabric with high pressure fluid jets. While these mechanical stress methods are<br />
relatively effective, they create many problems, especially in view <strong>of</strong> a desire to maintain a direct,<br />
continuous process.<br />
This patent describes a process for obtaining a s<strong>of</strong>t, yet strong nylon spunbond fabric without the<br />
problems associated with the mechanical stress s<strong>of</strong>tening steps. This involves the addition <strong>of</strong> a small<br />
amount <strong>of</strong> polyethylene polymer to the nylon feedstock prior to extrusion. The addition <strong>of</strong> the<br />
polyethylene to the nylon resin enhances specific properties such as s<strong>of</strong>tness. The use <strong>of</strong> polyethylene<br />
also lowers the cost <strong>of</strong> production <strong>and</strong> eases further downstream processing, such as bonding to other<br />
fabrics or to itself.<br />
The improved nylon spunbond fabric is obtained by adding a small amount <strong>of</strong> polyethylene resin,<br />
preferably a linear low density polyethylene resin, in amount <strong>of</strong> about 0.5 weight percent to the nylon<br />
feed material. This amount <strong>of</strong> polyethylene resin does not adversely affect the spinning performance. The<br />
added PE resin actually improves the throughput by approximately 8%, apparently by fostering the<br />
passage <strong>of</strong> the blended resin through the entire spunbonding process.<br />
The filament extrusion step is preferably carried out at a temperature in the range <strong>of</strong> 280° C to about 315°<br />
C. If some nylon-6 resin is added to the feedstock, a somewhat lower extrusion temperature can be<br />
utilized. Other lower melting polyamides can also be used in practicing the patent. The filaments<br />
produced with the modified process can be bonded with the thermal point bond method or by the<br />
chemical autogenic method.<br />
In a typical example, a blend <strong>of</strong> 99.5% nylon <strong>and</strong> 0.5 weight percent linear low density polyethylene can<br />
be converted into a spunbond fabric at one ounce per square yard basis weight, using an extrusion<br />
temperature <strong>of</strong> 300° C. The resulting continuous filament web was bonded at the chemical bonding<br />
station, using hydrogen chloride gas <strong>and</strong> water vapor at a temperature <strong>of</strong> about 39° C. Following<br />
treatment in the gas house, the web was then subjected to a compacting step in which the web was<br />
compacted <strong>and</strong> further bonded.<br />
The quality <strong>of</strong> the fabric produced with the polyethylene additive did not differ appreciably from that<br />
produced without the polyethylene. Furthermore, the process parameters employed in the extruder, filter<br />
packs, etc., did not change significantly. Spinning performance was similar to that encountered in the<br />
routine process. The completed fabric was considerably s<strong>of</strong>ter than the comparable fabric produced from<br />
100% nylon-66 <strong>and</strong> the throughput was increased by approximately 8%.<br />
U.S. 5,913,993 (June 22, <strong>1999</strong>); filed January 10, 1997. "Nonwoven nylon <strong>and</strong> polyethylene fabric."<br />
Assignee: Cerex Advanced <strong>Fabrics</strong>, L.P. Inventors: Ortega, Albert E.; Thomley, R. Wayne.<br />
Electret Meltblown Webs<br />
The meltblown process has been used for several years to prepare nonwoven fibrous webs suitable for<br />
use as filtration media. The webs <strong>of</strong> micr<strong>of</strong>iber resulting from this process are especially effective in the<br />
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filtering <strong>of</strong> particulate contaminates. Consequently, such filter media has been used in face masks,<br />
respirators, panel filters, pocket filters, bag filters <strong>and</strong> other devices for the filtering air <strong>and</strong> liquids.<br />
The aerosol filtration efficiency <strong>of</strong> such nonwoven fibrous webs can be improved by imparting an<br />
electrical charge to the fibers, resulting in the formation <strong>of</strong> an electret fabric. A number <strong>of</strong> methods are<br />
known for forming such electret materials. These methods include, for example, bombarding meltblown<br />
fibers as they issue from the die orifices with electrically charged particles such as electrons or ions (hot<br />
charging), charging fibers by means <strong>of</strong> a corona discharge after fiber formation (cold charging), or<br />
imparting a charge to a fiber mat by means <strong>of</strong> carding <strong>and</strong>/or needle tacking (tribo-charging). Also, the<br />
use <strong>of</strong> jets <strong>of</strong> water impinging on a nonwoven web at a sufficient pressure can provide a filtration<br />
enhancing electret charge to the web (hydro-charging). Other types <strong>of</strong> nonwoven fibrous webs useful for<br />
filtration purposes have been prepared by fibrillating films <strong>of</strong> polyolefin to form a fibrous material. Such<br />
fibrillated materials may be charged as the film followed by corona discharge, for example. Following<br />
fibrillation, the web is collected <strong>and</strong> processed into a filter.<br />
The current process discloses a method <strong>of</strong> making a fibrous electret material particularly suitable for<br />
filtration applications. The process comprises the steps <strong>of</strong> forming a fibrous web via the meltblown<br />
process. A specific chemical agent is added to the thermoplastic polymer prior to conversion into<br />
micr<strong>of</strong>ibers by the meltblown process. Following collection <strong>of</strong> the web, it is subjected to impinging jets<br />
<strong>of</strong> water at a pressure sufficient to provide the web with an electret charge. The resulting web is a<br />
superior filter medium.<br />
Thermoplastic resins suitable for use in the process are nonconductive polymers; polypropylene,<br />
poly-4-methyl-1-pentene resins, blends <strong>of</strong> these two resins or copolymers formed from propylene <strong>and</strong><br />
4-methyl-1-pentene are preferred as the fiber forming material. The resin should be substantially free<br />
from materials such as anti-static agents, which could increase the electrical conductivity or otherwise<br />
interfere with the ability <strong>of</strong> the fibers to accept an hold electrostatic charges.<br />
The chemical additive used in the process enhances the electret-forming propensity <strong>of</strong> the patented<br />
micr<strong>of</strong>iber web. Two different classes <strong>of</strong> suitable additive materials are disclosed <strong>and</strong> the process is<br />
based on using one or other <strong>of</strong> the two additives or a combination <strong>of</strong> the two.<br />
The one class <strong>of</strong> suitable additive is based on a perfluorinated moiety having a flourine content <strong>of</strong> at least<br />
18% by weight. Such compounds include short-chain tetrafluoroethylene telomers. An additive formed<br />
from N-(perfluorooctylsulfonyl)-piperazine, triethylamine <strong>and</strong> phthaloyl dichloride is particularly useful.<br />
The second class <strong>of</strong> electret enhancing additive comprises a thermally stable organic triazine compound<br />
or oligomer containing at least one nitrogen atom in addition to those in the triazine group. Such a<br />
material can be prepared from N,N -di-(cyclohexyl)-hexamethylene-diamine <strong>and</strong><br />
2-(tert-octylamino)-4,6-dichloro-3,5-triazine.<br />
The fluorochemical additive or the triazine-based additive is preferably used in the amount <strong>of</strong> about 0.5<br />
to 2 weight percent. A blend <strong>of</strong> the thermoplastic resin <strong>and</strong> the additive can be prepared by pre-blending<br />
<strong>and</strong> pelletizing. Alternately, the additive can be blended with the resin in the extruder <strong>and</strong> melt extruded<br />
directly. Extrusion conditions are generally those which are suitable for extruding the resin without the<br />
additive.<br />
Micr<strong>of</strong>iber webs from the additive/polymer blend are prepared with effective fiber diameter in the range<br />
<strong>of</strong> 7 to 15 microns. Webs having a basis weight in the range <strong>of</strong> about 10 to 100 gsm are suitable. The<br />
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thickness <strong>of</strong> the filter media is preferably about 0.5 to 2 mm. The electret filter medium <strong>and</strong> the resin<br />
from which it is produced should not be subjected to any unnecessary treatment which might increase its<br />
electrical conductivity, e.g., exposure to gamma rays, ultraviolet radiation, pyrolysis, oxidation, etc.<br />
Hydrocharging <strong>of</strong> the web is carried out by impinging fine jets <strong>of</strong> water onto the web at a pressure<br />
sufficient to provide the web with a filtration enhancing electric charge. The pressure necessary to<br />
achieve optimum results will vary depending on the type <strong>of</strong> jet used , the type <strong>of</strong> polymer, the type <strong>and</strong><br />
concentration <strong>of</strong> additives, the thickness <strong>and</strong> density <strong>of</strong> the web <strong>and</strong> whether pre-treatment such as<br />
corona surface treatment, is carried out prior to hydrocharging. Generally, pressures in the range <strong>of</strong> about<br />
10 to 500 psi (69 to 3450 kPa) are suitable. An apparatus suitable for hydraulically entangling fibers is<br />
generally useful in the method <strong>of</strong> hydrocharging the nonwoven web, although the operation is carried out<br />
at lower pressures in hydrocharging than generally used in hydroentangling.<br />
The inventors suggest the technique <strong>of</strong> measuring the filtration performance <strong>of</strong> the web before <strong>and</strong> after<br />
hydrocharging as the method to determine the effectiveness <strong>of</strong> electret formation. An increase in the<br />
filtration performance is indicative <strong>of</strong> the trapped charge. This can be confirmed by subjecting the treated<br />
web to a charge destroying procedure, such as exposure to x-ray radiation, alcohol treatment<br />
(isopropanol) or heat treatment at a temperature about 30 0 C. below the melting point to near the melting<br />
point <strong>and</strong> again measuring the filtration performance.<br />
The inventors point out that staple fibers can also be introduced into the web. Further, sorbent particulate<br />
material, such as activated carbon or aluminum, may also be incorporated.<br />
The enhanced performance <strong>of</strong> the filter media can <strong>of</strong>ten be further improved by annealing, i.e., heating<br />
for a sufficient time at a sufficient temperature to cause the additive to bloom to the surface <strong>of</strong> the fibers.<br />
Generally, about one 1 to 10 minutes at about 140 0 C is sufficient for a polypropylene filter medium.<br />
U.S. 5,908,598 (June 1, <strong>1999</strong>); filed August 14, 1995. Assignee: Minnesota Mining <strong>and</strong> Manufacturing<br />
Company. Inventors: Alan D. Rousseau, Marvin E. Jones, Seyed A. Angadjiv<strong>and</strong>.<br />
Lotion Wipe with Inverse Emulsion<br />
This patent is directed toward a special type <strong>of</strong> disposable wipe, containing a lotion used to soothe the<br />
skin. Such a wipe can be a special type <strong>of</strong> facial tissue or more substantial nonwoven wipe intended for<br />
multiple uses. Some aspects <strong>of</strong> the patent disclosure are directed toward personal wipes, such as<br />
wet-wipes used to cleanse the perianal area, premoistened baby wipes, adult incontinence wipes or as a<br />
form <strong>of</strong> premoistened bathroom tissue.<br />
The performance <strong>of</strong> such wiping products is enhanced if the wipe releases a significant quantity <strong>of</strong> water<br />
during use for comfort <strong>and</strong> more effective cleansing. Such a wipe is even more effective when a<br />
controlled amount <strong>of</strong> a lotion or emollient ingredient is deposited. In the case <strong>of</strong> both liquids, however,<br />
the quantities involved must be controlled, as an excess <strong>of</strong> either the water or oil is unacceptable.<br />
This patent discloses the use <strong>of</strong> a high internal phase inverse emulsion applied to a nonwoven substrate to<br />
give a superior wiping product. This type <strong>of</strong> an emulsion is referred to a regular emulsion, since the<br />
system consists <strong>of</strong> a discontinuous water phase dispersed in an emulsion <strong>of</strong> a continuous oleophilic<br />
phase. Emulsions that are normally encountered consist <strong>of</strong> the water phase being the major <strong>and</strong><br />
continuous component, with a small amount <strong>of</strong> the oil or lipid phase dispersed as emulsified particles<br />
within the water phase. Such an inverse emulsion can have much <strong>of</strong> the physical character <strong>of</strong> the major<br />
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lipid component.<br />
The inventors disclose that the lipid phase <strong>of</strong> an appropriate inverse emulsion employed in the disclosed<br />
wipes is sufficiently brittle so as to be easily disrupted by low shear contact or compression, such as<br />
would occur during the wiping <strong>of</strong> skin. When the lipid phase is thus disrupted, the inverse emulsion<br />
readily releases the internal water phase. During the rigors <strong>of</strong> processing the dure manufacture, the lipid<br />
phase is sufficiently tough at elevated temperatures as to avoid premature release <strong>of</strong> the water phase<br />
during such processing. The continuous lipid phase is also sufficiently stable during storage so as to<br />
prevent significant evaporation <strong>of</strong> the internal water phase.<br />
The normal tensile strength <strong>and</strong> flushability properties <strong>of</strong> these wipes are not adversely affected when<br />
treated with the high internal phase inverse emulsion. As a result, users <strong>of</strong> these wipes get a comfortable,<br />
efficient, moist cleansing action without having to change their normal cleaning habits. Consequently,<br />
this technology is readily useful for other purposes such as cleaning hard surfaces, etc.<br />
The inventors disclose that they unexpectedly found that a continuous coating <strong>of</strong> the emulsion on a<br />
substrate does not provide the most efficacious cleaning, particularly when it is desired to clean human<br />
skin. A discontinuous pattern <strong>of</strong> the emulsion on the substrate provides a cleaning mechanism not found<br />
in the prior art. The optimum discontinuous pattern <strong>of</strong> emulsion is a pattern having regions <strong>of</strong> the<br />
substrate free <strong>of</strong> the emulsion adjacent to zones <strong>of</strong> the substrate upon which the emulsion is disposed.<br />
The inventors further discovered that during cleaning, water is released from the emulsion to remove dirt<br />
from the skin. The area <strong>of</strong> the skin wetted by the water <strong>and</strong> from which dirt is removed is then wiped dry<br />
with the adjacent regions <strong>of</strong> the nonwoven wiping substrate that are free <strong>of</strong> the emulsion. Thus, the wipe<br />
consists <strong>of</strong> treated zones which release the cleansing water <strong>and</strong> a small amount <strong>of</strong> oil, followed by the<br />
untreated zone <strong>of</strong> the wipe which picks up the excess water, leaving the skin in an ideal condition.<br />
The mechanism to release water from the emulsion to the surface to be cleaned involves several steps.<br />
First, the water is released or expressed from the emulsion due to the pressure imparted by user. The<br />
pressure ruptures the emulsion, freeing the water. The water then saturates the nonwoven substrate. Upon<br />
saturation, the water penetrates the nonwoven substrate in the Z direction. Excess water, which is that<br />
water in excess <strong>of</strong> the local absorbent capacity <strong>of</strong> the substrate, is then transferred from the wipe to the<br />
surface. As the surface is contacted by the untreated zone <strong>of</strong> the wipe, the cleansing water is removed.<br />
The inventors claim that similar benefits occur when the wipe is used to clean other surfaces, such as<br />
window glass, counter tops, sinks, porcelain <strong>and</strong> metal fixtures, walls, <strong>and</strong> the like, as well as from other<br />
surfaces, such as carpeting or furniture.<br />
The patent discloses that a preferred embodiment <strong>of</strong> the invention involves a nonwoven substrate<br />
comprising high <strong>and</strong> low basis weight regions. The emulsion is positioned in the low basis weight<br />
regions. This provides a further differentiation <strong>of</strong> the dispensing zone <strong>of</strong> the wipe followed by the higher<br />
density absorbing zone, providing a multi-functional wiping substrate with a superior performance.<br />
The emulsion comprises: (1) a continuous solidified lipid phase; (2) an emulsifier that forms the<br />
emulsion when the lipid phase is fluid; <strong>and</strong> (3) an internal polar phase dispersed in the liquid phase. This<br />
emulsion ruptures when subjected to low shear during use, for example, wiping <strong>of</strong> the skin or other<br />
surface so as to release the internal polar phase. Preferably, the lipid phase will comprise from about 6 to<br />
15% <strong>of</strong> the emulsion. The major constituent <strong>of</strong> this continuous liquid phase is a waxy lipid material with<br />
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a melting point in the range <strong>of</strong> about 50 to 70 0 C. Although this waxy lipid material is solid at ambient<br />
temperatures, it also needs to be fluid or plastic at those temperatures at which the high internal phase<br />
inverse emulsion is applied to the substrate. The major component <strong>of</strong> the high internal phase inverse<br />
emulsion is the dispersed internal polar phase which consists <strong>of</strong> water, comprising about 85 to 94% by<br />
weight.<br />
The inventors point out that a wide variety <strong>of</strong> materials can be combined with the ingredients <strong>of</strong> the<br />
inverse emulsion, such as emollients, medicaments, bleach, surfactant, solvents, disinfectants, chelating<br />
agents <strong>and</strong> others.<br />
Suitable substrates to be with this wipe can be <strong>of</strong> various types. Nonwoven fabrics, particularly those<br />
with regions <strong>of</strong> low <strong>and</strong> high density are particularly useful. Also, the nonwoven fabric can be apertured<br />
to provide an extreme case <strong>of</strong> density differentiation. Airlaid pulp webs <strong>and</strong> wetform webs can be<br />
employed, along with various types <strong>of</strong> tissue products.<br />
A variety <strong>of</strong> patterns for application <strong>of</strong> the inverse phase emulsions are suggested by the inventors. The<br />
emulsion can be employed in stripes, which affords coated regions adjacent to non-coated regions in the<br />
final wiping product. Also, a variety <strong>of</strong> other patterns can be employed, including patterns which involve<br />
topic designs suitable for aesthetic enhancement.<br />
U.S. 5,914,177 (June 22, <strong>1999</strong>); filed August 11, 1997. "Wipes having a substrate with a discontinuous<br />
pattern <strong>of</strong> a high internal phase inverse emulsion disposed thereon <strong>and</strong> process <strong>of</strong> making." Assignee:<br />
The Procter & Gamble Company. Inventors: Charles Zell Smith, III, Steven Lee Barnholtz, David<br />
William Cabell.<br />
Superfine Micr<strong>of</strong>iber Nonwoven Web<br />
Micr<strong>of</strong>iber webs, such as meltblown fiber webs are well known <strong>and</strong> have found application in a wide<br />
variety <strong>of</strong> industrial, consumer <strong>and</strong> medical products. Despite the use <strong>and</strong> utility <strong>of</strong> these webs, there is a<br />
continuing quest for fiber webs containing even finer micr<strong>of</strong>iber. For many applications, the finer the<br />
fiber, the greater the performance enhancement.<br />
There have been various attempts to reduce the diameter <strong>of</strong> meltblown fibers by a variety <strong>of</strong> methods.<br />
One such approach is to reduce the polymer through-put to the die head. However, this direct approach<br />
can only be used to reduce the fiber size to a limited extent, since increasing reduction in the resin<br />
through-put eventually interrupts the fiber production altogether.<br />
Another method that has been attempted to produce superfine meltblown webs involves producing<br />
bicomponent conjugate meltblown fibers <strong>of</strong> the isl<strong>and</strong>-in-sea configuration <strong>and</strong> then dissolving the sea<br />
component. This does produce micr<strong>of</strong>ibers, but the dissolving process is a distinct disadvantage;<br />
consequently, this method is uneconomical <strong>and</strong> inefficient, <strong>and</strong> so it is seldom used.<br />
Hydro-needling has been attempted to produce superfine micr<strong>of</strong>ibers. This involves the use <strong>of</strong><br />
pressurized jets <strong>of</strong> water to split multi-component conjugate fibers. While this method is applicable to<br />
some nonwoven processes, it has not been used to produce split meltblown fiber webs, since the<br />
autogenously bonded meltblown fiber webs are quite weak <strong>and</strong> contain a numerous interfiber bonds that<br />
restrict fiber movements; consequently, these webs are very difficult to split with a mechanical splitting<br />
process without substantially destroying the web.<br />
The present invention provides a web containing superfine micr<strong>of</strong>ibers. This web is produced from<br />
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side-by-side bicomponent fibers produced by the meltblown process. The characteristics <strong>of</strong> the<br />
components <strong>of</strong> such bicomponent fibers must be carefully selected in order to produce an effective<br />
superfine micr<strong>of</strong>iber web that can be easily split. The two polymer components must be incompatible, so<br />
they have a fairly substantial propensity to split. One polymer component must be a hydrophobic resin,<br />
whereas, the second polymer component must be a hydrophilic resin.<br />
The hydrophobic resin can be a polyolefin resin such as polypropylene or a processable polyethylene.<br />
Also, polyethylene terepthalate is a suitable hydrophobic resin.<br />
The hydrophilic resin can be one <strong>of</strong> a variety <strong>of</strong> resins. The suitability <strong>of</strong> the hydrophilic polymer<br />
component can best be evaluated by determining the contact angle <strong>of</strong> the polymer. This is done most<br />
conveniently by a st<strong>and</strong>ard test (ASTM D724-89) performed on a film produced by melt-casting the<br />
hydrophilic polymer at the temperature <strong>of</strong> the die head that is used to produce the split micr<strong>of</strong>iber web.<br />
The "initial contact angle" is determined, by measuring the contact angle by the test method within five<br />
seconds after application <strong>of</strong> the water drop to the test film specimen. The film must have an initial<br />
contact angle less than 80 degrees, <strong>and</strong> desirably, will have an initial contact angle less than 50 degrees.<br />
Inherently hydrophilic polymers such as copolymers <strong>of</strong> caprolactam <strong>and</strong> alkylene oxide diamine, as well<br />
as a range <strong>of</strong> copolymers <strong>of</strong> poly(oxyethylene) with various base polymers can be used.<br />
In addition, it is possible to hydrophilically modify polymers <strong>and</strong> convert them into modified polymers<br />
having suitable initial contact angle. Thus, a variety <strong>of</strong> modified copolymers <strong>of</strong> polyolefins, a wide<br />
selection <strong>of</strong> copolymers <strong>and</strong> other variations can be used for the hydrophilic component. This can be<br />
done most conveniently by utilizing a surfactant in a hydrophobic polymer to convert it to a wettable<br />
polymer suitable for use as the hydrophilic component. Fugitive surfactants, that is surfactants that wash<br />
<strong>of</strong>f from the fiber surface, are suitable for some applications. For other applications, more durable<br />
surfactants may be used to convert a hydrophobic polymer into a suitable hydrophilic component. The<br />
amount <strong>of</strong> surfactants required <strong>and</strong> the hydrophilicity <strong>of</strong> the modified fibers will depend upon the type <strong>of</strong><br />
surfactant <strong>and</strong> the type <strong>of</strong> polymer used. Typically, the amount <strong>of</strong> surfactant suitable for the wettability<br />
treatment is in the range <strong>of</strong> from about 0.1% to about 0.5% based on the weight <strong>of</strong> the polymer<br />
composition.<br />
The splitting <strong>of</strong> the bicomponent fiber into superfine micr<strong>of</strong>iber components is carried out by contacting<br />
the fibrous web with a hot, aqueous split-inducing medium. Such split-inducing media include hot water<br />
at temperatures preferably between 65 <strong>and</strong> 100 0 C. Additionally, suitable split-inducing media comprise<br />
steam, <strong>and</strong> mixtures <strong>of</strong> steam <strong>and</strong> air that have a temperature higher than 60 0 C, but lower than the<br />
melting point <strong>of</strong> the lowest melting polymer <strong>of</strong> the conjugate fiber. This prevents inadvertent melting <strong>of</strong><br />
the polymer component during the fiber splitting process.<br />
It is suggested that the aqueous spilt-inducing medium exerts an influence, such as swelling <strong>of</strong> the fiber<br />
surface <strong>of</strong> the hydrophilic component. Such reaction to the aqueous medium, <strong>and</strong> especially surface<br />
swelling, greatly assists in the fiber splitting operation.<br />
A variety <strong>of</strong> particularly desirable pairs <strong>of</strong> incompatible polymers useful for the present conjugate<br />
micr<strong>of</strong>ibers are provided. In each case, the aqueous inducing medium causes the conjugate fiber to spit<br />
into the superfine components. The patent points out that such splitting can be achieved in less than one<br />
second, so that splitting is nearly instantaneous.<br />
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A variety <strong>of</strong> suitable configurations for the conjugate fibers can be employed. This includes side-by-side<br />
configurations, wedge configurations, hollow wedge configurations <strong>and</strong> sectional configurations.<br />
Asymmetric geometry for the cross-section can be used provided that it is not occlusive or interlocking.<br />
U.S. 5,935,883 (August 10, <strong>1999</strong>); filed October 23, 1997. "Superfine micr<strong>of</strong>iber nonwoven web;"<br />
Assignee: Kimberly-Clark Worldwide, Inc. Inventor: Richard Daniel Pike.<br />
This patent review was compiled courtesy <strong>of</strong> Smith, Johnson & Associates, a well-known nonwovens<br />
consulting firm that publishes a monthly patent newsletter, Nonwovens Patent News.<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
—INJ<br />
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Worldwide Abstracts <strong>and</strong> Reviews<br />
INJ DEPARTMENTS<br />
ASSOCIATION FOCUS<br />
TAPPI Playing Growing Role<br />
In Nonwovens Industry<br />
A concerted cooperative effort between the two U.S. associations most involved in the nonwovens<br />
industry - INDA, Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry, <strong>and</strong> TAPPI, the Technical Association<br />
<strong>of</strong> the Pulp <strong>and</strong> Paper Industry — has one goal in mind: increasing the knowledge base <strong>of</strong> the nonwovens<br />
industry.<br />
While INDA, by its very nature, has always focused on nonwovens issues, TAPPI has concentrated on<br />
this specialty business through its Nonwovens Division, one <strong>of</strong> 12 technical divisions that reports to the<br />
association's Technical Operations Council. TAPPI, one <strong>of</strong> the oldest technical associations <strong>of</strong> pulp <strong>and</strong><br />
paper <strong>and</strong> allied industries in the world with more than 30,000 members in 80 countries, sees itself as<br />
playing a very special role <strong>of</strong> bridging the gap in the area <strong>of</strong> technology <strong>and</strong> marketing information<br />
between the paper industry <strong>and</strong> the nonwovens industry, according to Nonwovens Division chairman<br />
T.W. Singh, <strong>of</strong> Evanite.<br />
"There seems to be a synergy in process technology <strong>and</strong> testing methods in the paper industry <strong>and</strong><br />
nonwovens, especially wet laid nonwovens," said Singh. "There has been quite an encouraging level <strong>of</strong><br />
cooperation between TAPPI <strong>and</strong> INDA over the last few years. Changes in leadership, both in the TAPPI<br />
<strong>and</strong> INDA organizations, have helped foster collaborative efforts."<br />
The most obvious result <strong>of</strong> increased cooperation between the two associations is the joint INDA/TAPPI<br />
International Conference scheduled for September, 2000 that is basically a bringing together <strong>of</strong> INDA's<br />
annual INDA-Tec meetings <strong>and</strong> TAPPI's annual Nonwovens Conference. "This joint effort is expected to<br />
<strong>of</strong>fer the best <strong>of</strong> both the organizations to their membership, namely market <strong>and</strong> technical expertise that<br />
no other technical organization in this field can provide," Singh said. "It will surely eliminate redundancy<br />
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<strong>of</strong> activities in the technical <strong>and</strong><br />
marketing fields at a time when cost<br />
consciousness is an increasing<br />
concern."<br />
Six different TAPPI Nonwovens<br />
Technical Committees (see chart on<br />
the next page) undertake tasks ranging<br />
from technical information papers,<br />
such as the report on various fibers<br />
used in nonwovens by the Fiber<br />
Committee, to test methods on fiber<br />
mats. The Building <strong>and</strong> Industrial Mat<br />
TAPPI Staff Contacts<br />
Charles Bohanan<br />
Technical Operations Manager,<br />
770-209-7276;<br />
Fax 770-446-6947;<br />
cbohanan@tappi.org<br />
Carol Mitchell<br />
Technical Operations Assistant, 770-209-7267;<br />
Fax 770-446-6947;<br />
cmitchell@tappi.org<br />
Committee is working with the EPA on defining relevant test methods for measuring volatile organic<br />
compounds, <strong>and</strong> the Binders <strong>and</strong> Additives Committee is conducting research on formaldehyde emission<br />
testing. The TAPPI Nonwovens Division also continually revises current publications <strong>and</strong> writes new<br />
ones like a "Primer" or "Nonwovens" in text format.<br />
Singh <strong>and</strong> others involved with TAPPI Nonwovens see the division's role growing as a result <strong>of</strong> its<br />
collaborative efforts with INDA. "Our long-term plan is to continue to work closely with INDA on<br />
projects <strong>of</strong> common interest, especially those involving new membership in this industry," Singh said.<br />
One area <strong>of</strong> growth is at the membership activity area, where, he added, "we would like to see more<br />
student <strong>and</strong> entry-level personnel participate in our activities."<br />
In the near-term, "Our goals are to include more practical information in the conferences <strong>and</strong> short<br />
courses so that attendees may find it more applicable to their daily lives <strong>and</strong> careers," Singh added. "We<br />
also intend to assist potential new authors <strong>and</strong> presenters to improve the quality <strong>of</strong> their technical<br />
presentations by utilizing new skills <strong>and</strong> state-<strong>of</strong>-the-art audio/video support."<br />
Sounds like the beginning <strong>of</strong> a beautiful friendship.<br />
TAPPI Committee Information<br />
— INJ<br />
Building <strong>and</strong> Industrial Mat Committee: To facilitate the exchange <strong>of</strong> information concerning the<br />
manufacture <strong>and</strong> use <strong>of</strong> wet-laid nonwoven mat, using fiberglass <strong>and</strong> other synthetic fibers for industrial<br />
<strong>and</strong> building products applications. Charles Diller, 419-878-1151; Fax 419-878-1297; dillerc@jm.com<br />
Nonwovens Binders <strong>and</strong> Additives Committee: To facilitate the exchange <strong>of</strong> useful information on the<br />
technology <strong>and</strong> use <strong>of</strong> products that relate to or are based on continuous webs made from cellulose,<br />
synthetic <strong>and</strong> inorganic fibers which have been formed or treated with binders <strong>and</strong> additives that impart<br />
specific properties. James Tanger, 704-587-8250; Fax 704-587-8117; tangerj@basf.com<br />
Nonwovens <strong>Fibers</strong> Committee: To promote the underst<strong>and</strong>ing <strong>and</strong> knowledge <strong>of</strong> the fibers used in the<br />
production <strong>of</strong> nonwovens <strong>and</strong> the materials <strong>and</strong> technologies used in making such fibers. Irwin Hutten,<br />
912-783-3200; Fax 912-783-3292; hutten@hom.net<br />
Nonwovens Filtration Media Committee: To facilitate the exchange <strong>of</strong> information on the technology<br />
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<strong>and</strong> usage <strong>of</strong> nonwovens media in filtration. To develop industry test methods in the area <strong>of</strong> nonwovens<br />
filtration materials. To define <strong>and</strong> disseminate terminology <strong>and</strong> tests with regard to nonwovens<br />
filtration. To encourage <strong>and</strong> educate the industry in wider use <strong>of</strong> nonwovens materials in filtration<br />
applications. Joginder Malik, 608-873-2476; Fax 608-873-2434; jmalik@nelsondiv.com<br />
Nonwovens Process Technology Committee: To facilitate the exchange <strong>of</strong> information on the<br />
processing <strong>and</strong> the equipment used in the production <strong>of</strong> nonwovens. Larry Wadsworth, 423-974-6298;<br />
Fax 423-974-3580; lwadswor@utk.edu<br />
Nonwovens Properties <strong>and</strong> Performance Committee: To facilitate the exchange <strong>of</strong> information on the<br />
equipment, methods, procedures, literature <strong>and</strong> s<strong>of</strong>tware used in the structure, characterization,<br />
computer modeling <strong>and</strong> performance <strong>of</strong> nonwoven products. Michael Nijakowski, 419-878-1550; Fax<br />
419-878-1116; miken@jm.com<br />
TAPPI Nonwovens Division Chairman: T.M. Singh, 541-753-0342; Fax<br />
541-753-0343;tmsingh@evanite.com<br />
Vice Chairman: Peter D. Wallace, 828-584-3800; Fax 828-584-3885; wallacepd@bordenchem.com<br />
Secretary: Norman Lifshutz, 978-448-3311; Fax 978-448-9342; nlifshut@hovo.com<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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The Nonwoven Web<br />
THE<br />
NONWOVEN WEB<br />
ORIGINAL PAPER/PEER REVIEWED<br />
For the nonwoven scientist <strong>and</strong> technologist, the Internet has become a virtually unlimited source <strong>of</strong><br />
information. Imagine having access to the memory <strong>and</strong> storage facilities <strong>of</strong> several million computers all tied<br />
together. While the potential is extraordinary, the process <strong>of</strong> finding a specific piece <strong>of</strong> information can be<br />
difficult, tedious <strong>and</strong> frustrating.<br />
It's a little bit like stepping into the middle <strong>of</strong> a very large library, looking around at the books <strong>and</strong> resource<br />
materials <strong>and</strong> then trying to find the needed information without the help <strong>of</strong> a librarian or a catalog system. As<br />
one specialist has put it, "It can seem like a library catalogued by a madman."<br />
Fortunately, there is some help available. One <strong>of</strong> the most common <strong>and</strong> best known is the "search engine."<br />
These are computer programs <strong>and</strong> systems designed to be given an assignment, <strong>and</strong> then go out throughout the<br />
web <strong>and</strong> retrieve the needed information. Unfortunately, even the most popular search engines can cover only<br />
a fraction <strong>of</strong> the indexable web. One fairly recent study (Lawrence S.; Giles, C. L.; "Searching the worldwide<br />
web," Science, 1998, pp. 280-98) concluded that popular search engines cover less than one-third <strong>of</strong> the<br />
indexable web. Since that study was made in 1998, the web has grown even larger; consequently, that figure is<br />
undoubtedly too optimistic.<br />
So what does the Internet user do to take full advantage <strong>of</strong> the potential? The best approach appears to be to<br />
underst<strong>and</strong> the system <strong>and</strong> the tools, <strong>and</strong> then to select the appropriate tool <strong>and</strong> methodology for the particular<br />
search or query. This can look like a daunting task, but it is manageable. Not everything has to be learned at<br />
once <strong>and</strong> use <strong>of</strong> the facility does provide greater underst<strong>and</strong>ing <strong>and</strong> appreciation <strong>of</strong> what is available <strong>and</strong> a<br />
knowledge <strong>of</strong> the most effective ways to procure the information desired.<br />
Also, as a practicality, it is not necessary to underst<strong>and</strong> <strong>and</strong> gain experience on all aspects <strong>of</strong> the web. By<br />
focusing on those resources that are pertinent to the nonwovens industry, the task becomes more manageable<br />
<strong>and</strong> reasonable in scope.<br />
What follows may be <strong>of</strong> some help.<br />
The Internet is basically a great number <strong>of</strong> computers linked together. These computers are called "servers."<br />
When you ask your computer (called the "client") to go get information from another computer, the client<br />
sends out a request over your modem or net connection to a server. What it finds <strong>and</strong> brings back depends on<br />
what you asked for, what application or system you used to form the request, <strong>and</strong> the search system utilized.<br />
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The Nonwoven Web<br />
INDA'S WEB SITE UPDATED<br />
INDA's web site - www.inda.org - has exp<strong>and</strong>ed to include a Job Mart <strong>and</strong> Classifieds section. The Job Mart<br />
(www.inda.org/class/jobmart.html) provides a listing <strong>of</strong> employment opportunities relevant to the nonwovens<br />
industry. Classified advertisements (www.inda.org/class/) list a service or product a company either needs or<br />
<strong>of</strong>fers.<br />
The Job Mart is broken down into six sections: Management, Marketing, Sales, Technical, "Situations<br />
Wanted" <strong>and</strong> Post a Job. Classified Advertisements are broken down into Partnerships <strong>and</strong> Business<br />
Ventures, Recyclable Materials (Wanted <strong>and</strong> For Sale), Used Machinery <strong>and</strong> Equipment, Miscellaneous <strong>and</strong><br />
Place Your Classified Ad.<br />
Also new to INDA's web site is the industry links page. There are links to other associations, organizations<br />
<strong>and</strong> companies related to the nonwovens area. Members <strong>of</strong> INDA can be linked to the INDA web site free <strong>of</strong><br />
charge. Exhibitors at Filtration '99, Suppliers' Showcase '99 <strong>and</strong> IDEA 2001 can also have their websites<br />
linked to INDA's website.<br />
If a web browser was used to carry out the search, your computer is going to ask a web server to bring back a<br />
piece <strong>of</strong> data in form <strong>of</strong> an HTML (HyperText Markup Language) file. If you used an e-mail application, your<br />
computer connects to an e-mail server <strong>and</strong> brings back e-mail.<br />
The Internet is really made up <strong>of</strong> several different ways <strong>of</strong> communicating with servers. Those methods <strong>of</strong><br />
communication are called a "protocol." The many different potential protocols involved break down to a<br />
selected few, such as the following:<br />
● Web: hypertext transfer protocol (html)<br />
● News Groups: news transfer protocol<br />
● FTP: file transfer protocol<br />
● Gopher: specific protocol<br />
● Telnet: specific protocol<br />
● e-mail: e-mail communications<br />
So, the Internet is really made up <strong>of</strong> these elements; everything else is sort <strong>of</strong> a derivation <strong>of</strong> these basic<br />
components. Consequently, it is apparent that the search engine or browser employed for a search controls to<br />
quite a degree the type <strong>of</strong> computer files that will be searched.<br />
In setting up a web site, the webmaster has the opportunity to insert a variety <strong>of</strong> keywords which identify the<br />
type <strong>of</strong> information that will be stored in the site. Some search engines are designed to go out <strong>and</strong> scan these<br />
keywords for a match with the keywords contained in the query. A well-designed search engine does not start<br />
with an empty plate as the search commences, however. Such a server will store the keywords from previous<br />
searches <strong>and</strong> consequently will have a sizeable database on which to draw, in order to shorten the search.<br />
A LOOK AT VARIOUS SEARCH ENGINE 'HITS'<br />
Search Engine Address (http://www.) Number <strong>of</strong> Hits Remarks<br />
AltaVista altavista.com 5,581<br />
All-purpose engine, but can be good for specific<br />
searches, as it has a large database <strong>and</strong> surveys<br />
large portions <strong>of</strong> web.<br />
America Online aol.com 1,223 Popular, but general purpose.<br />
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The Nonwoven Web<br />
Beaucoup beaucoup.com 240.<br />
DejaNews deja.com Primarily for news items; limited for other uses. .<br />
DogPile dogpile.com 2<br />
Meta-search engine, which uses other engines to<br />
do simultaneous searching. .<br />
Euroseek euroseek.net 1,160 Focus on European portion <strong>of</strong> the net. .<br />
Excite excite.com 1,152 An all-purpose engine. .<br />
Google google.com 2,758.<br />
HotBot hotbot.com 1,080<br />
Can use common language; Can specify results<br />
by date, domain, links to an URL. .<br />
InfoSeek infoseek.com 2,073<br />
A hybrid search engine that combines<br />
staff-reviewed sites with search engine results. .<br />
Jeeves ask.com 44<br />
Fair; is a Meta-search engine; in this search it<br />
used Yahoo, Altavista, Webcrawler, Infoseek <strong>and</strong><br />
Excite. .<br />
Lycos lycos.com 6<br />
Netscape netscape.com 9 Web browser.<br />
NonwovensWeb nonwovensweb.com 1,344 Industry specific; building database.<br />
NorthernLight northernlight.com 20,033<br />
Not very discriminating; has a special collection<br />
<strong>of</strong> 2 million articles from many sources. ;<br />
Pr<strong>of</strong>usion pr<strong>of</strong>usion.com 135 Meta-search engine;<br />
CNet cnet.com 1,260<br />
Snap snap.com 1,200<br />
WebCrawler webcrawler.com Meta-crawler.<br />
Yahoo yahoo.com 62 Good for broad topic search<br />
As a practicality, a search engine can shortly become much more expert <strong>and</strong> efficient in searching broad topics<br />
<strong>of</strong> a similar nature. Consequently, some search engines are more useful in dealing with certain topics than with<br />
other topics.<br />
Other search engines are designed to utilize a different search strategy. In some cases the search engine goes<br />
out <strong>and</strong> utilizes the searching capability <strong>of</strong> half a dozen other search engines, bringing back the results <strong>of</strong> their<br />
searching as an answer to the original query. Naturally, the quality <strong>of</strong> such a search is dependent upon the<br />
specific slave search engines employed.<br />
Also, it should be realized that the nature <strong>of</strong> searching on the Internet generally results in a substantial time<br />
delay. When a new website is established, it takes time to be incorporated into the database memories <strong>of</strong> the<br />
popular search engines. It has been estimated that it takes about six months for a new web site to be so<br />
incorporated <strong>and</strong> to be used in subsequent searches. Consequently, newly constructed sites may be ignored for<br />
several months.<br />
All <strong>of</strong> this points out another fact <strong>of</strong> life that should be recognized in organizing a search. This was highlighted<br />
in a recent study published in the scientific journal, Nature (June <strong>1999</strong>). This study revealed that the amount <strong>of</strong><br />
information being indexed by the commonly used search engines is increasing, but it is not increasing as fast<br />
as the amount <strong>of</strong> information being put on the web. Unfortunately, this means that the explosive rate at which<br />
information is being placed on the web may actually result in more information being lost to easy public view<br />
than is made available.<br />
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This more-recent study found that most <strong>of</strong> the major search engines now index less than 10% <strong>of</strong> the web.<br />
Thus, even by combining all the major search engines, less than one-half <strong>of</strong> the web has been indexed.<br />
Unfortunately, the mushrooming size <strong>of</strong> the web creates a substantial gulf between what is on the web <strong>and</strong><br />
what is retrievable.<br />
The following table reveals how much <strong>of</strong> today's<br />
searchable web content is actually h<strong>and</strong>led by a variety <strong>of</strong><br />
search engines.<br />
NorthernLight 16.0<br />
Snap 15.5<br />
AltaVista 15.5<br />
HotBot 11.3<br />
Micros<strong>of</strong>t 8.5<br />
Infoseek 8.0<br />
Google 7.8<br />
Yahoo! 7.4<br />
Excite 5.6<br />
Lycos 2.5<br />
Euroseek 2.2<br />
Also, the nature <strong>of</strong> searchable sites is changing rather<br />
rapidly. As might be imagined, the commercial home<br />
page sites are growing at a faster rate than other types. At<br />
the present time, commercial sites comprise about 82% <strong>of</strong><br />
the total.<br />
The actual breakdown as revealed by this recent study is<br />
as follows:<br />
Commercial sites 82.1<br />
Science/Education 6.0<br />
Health 2.8<br />
Personal 2.3<br />
Societies 1.9<br />
Pornography 1.5<br />
Community 1.4<br />
Government 1.2<br />
Religion 0.8<br />
In the last issue <strong>of</strong> INJ a report from the UK gave an<br />
indication <strong>of</strong> the number <strong>of</strong> "hits" obtained through the<br />
BOOK REVIEW<br />
New Nonwovens Textbook<br />
"Nonwoven Textiles," Oldrich Jirsak, Technical<br />
University <strong>of</strong> Liberec, Czech Republic, <strong>and</strong> Larry<br />
Wadsworth, TANDEC/University <strong>of</strong><br />
Tennessee-Knoxville, USA, 128 pages<br />
For decades there has been a dem<strong>and</strong> for a<br />
comprehensive, well-structured introductory<br />
textbook covering nonwovens. This new book not<br />
only fills this need for academia, but will also have<br />
strong appeal to many other readers. Those in the<br />
nonwovens industry will find it to be a h<strong>and</strong>y<br />
reference for areas outside <strong>of</strong> their specialty.<br />
Further, the numerous descriptions <strong>and</strong> process<br />
schematics will prove useful as reference materials<br />
for sales pr<strong>of</strong>essionals <strong>and</strong> others who must<br />
explain nonwoven technologies to those outside<br />
the industry.<br />
According to Dr. Wadsworth, the text was<br />
developed based on lecture notes <strong>and</strong> experience<br />
teaching numerous nonwovens courses. The two<br />
major sections <strong>of</strong> the book deal with raw materials<br />
for nonwovens <strong>and</strong> the various production<br />
technologies. The authors have been careful not to<br />
overwhelm the reader, striking an appropriate<br />
balance between breath <strong>and</strong> depth <strong>of</strong> coverage.<br />
Available from: Carolina Academic Press, 700<br />
Kent Street, Durham, NC 27701, USA;<br />
Phone:(919) 489 7486, Fax: (919) 489 5668;<br />
cap@cap-press.com. $39.95 plus $4.50 shipping<br />
<strong>and</strong> h<strong>and</strong>ling in the U.S; international please call<br />
for rates.<br />
use <strong>of</strong> various search engines that had been given the assignment to search on the term "nonwovens." On the<br />
previous page is a similar listing done during the month <strong>of</strong> August, <strong>1999</strong> from a location in the U.S. While the<br />
number <strong>of</strong> hits does provide some basis for quantifying the specific search capabilities, a little experience<br />
shows that this is not completely reliable. Also, this sampling revealed that the most recent additions indexed<br />
by the network were generally the first items gathered by the various search engines.<br />
The existence <strong>of</strong> a search engine reputedly designed specifically for searching items <strong>of</strong> interest to the<br />
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nonwovens industry is encouraging. This site, NonwovensWeb (http://www.nonwovensweb.com), has made a<br />
start in indexing items <strong>of</strong> interest to the industry. Most <strong>of</strong> the sites are <strong>of</strong> a commercial nature, but that is<br />
underst<strong>and</strong>able, in view <strong>of</strong> the predominance <strong>of</strong> commercial sites. As further experience <strong>and</strong> searching time is<br />
logged, this site will hopefully improve <strong>and</strong> provide a very useful resource for the industry.<br />
In considering search resources, other possibilities should not be ignored. There are a vast number <strong>of</strong><br />
dictionaries, encyclopedias, directories <strong>and</strong> similar types <strong>of</strong> databases that are now available online. Also, the<br />
contents <strong>of</strong> published books can be a very useful source <strong>of</strong> information, although this may be more difficult to<br />
dig out for older works. The contents <strong>of</strong> technical journals are finding their way onto the net very rapidly.<br />
Some <strong>of</strong> this can be accessed by the use the index <strong>of</strong> contents <strong>of</strong> these various journals. There is frequently a<br />
charge for obtaining copies <strong>of</strong> the entire paper.<br />
Commercial databases have traditionally been a strong source <strong>of</strong> some types <strong>of</strong> information. Such commercial<br />
databases are particularly strong in the area <strong>of</strong> publications, patents, competitive information <strong>and</strong> market<br />
information.<br />
Trade associations, trade publications <strong>and</strong> similar sites also can be very useful resources for the information<br />
search.<br />
As indicated, skill <strong>and</strong> facility in the search for nonwovens information is greatly benefitted by regular use <strong>of</strong><br />
the net <strong>and</strong> experience gained at the keyboard.<br />
Nonwoven Search Resources<br />
The following websites are suggested as useful resources for an individual seeking information on nonwovens<br />
technology <strong>and</strong> the nonwovens industry. Recognize that some sites are updated regularly, whereas other sites<br />
receive little attention after the original construction.<br />
Also, the INJ editorial staff welcomes suggestions from our readers as to useful <strong>and</strong> innovative websites.<br />
Sharing your experience makes it doubly meaningful.<br />
Useful Sites For<br />
Nonwovens Searching<br />
• American Filtration & Separations Society: Comprehensive site including membership, conferences <strong>and</strong><br />
educational services, AFS publications, corporate members, Distributors <strong>and</strong> manufacturers, AFS <strong>of</strong>ficers, <strong>and</strong><br />
local chapters. http://www.afssociety.org<br />
• American Society for Testing Materials (ASTM): Testing methods <strong>and</strong> st<strong>and</strong>ards for materials. Site has a<br />
directory <strong>of</strong> testing laboratories <strong>and</strong> consulting services according to geography <strong>and</strong> specialty. (Consultant<br />
listing: www.astm.org/consultants/NEW/index.html) ;<br />
http://www.astm.org<br />
• AMTEX: The American Textile Partnership is a collaborative research <strong>and</strong> development program among the<br />
industry, the Department <strong>of</strong> Energy, the DOE laboratories, other federal agencies <strong>and</strong> universities. The site<br />
<strong>of</strong>fers a variety <strong>of</strong> textile items. http://apc.pnl.gov:2080/amtex.html<br />
• Association <strong>of</strong> Operating Room Nurses (AORN):. Pr<strong>of</strong>essional society <strong>of</strong> perioperatiave nurses. Includes a<br />
variety <strong>of</strong> features about association <strong>and</strong> pr<strong>of</strong>essional activities, product <strong>and</strong> services, referral services <strong>and</strong><br />
consultation services. (The association also has a site with links to consumer-oriented information about<br />
surgery: www.aorn.org/patient) www.aorn.org/<br />
• Cotton Incorporated: Home page <strong>of</strong> cotton producers, including importer database, cotton market economic<br />
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letter, agricultural research, fiber processing research, textile research <strong>and</strong> implementation, fiber quality<br />
research, 1995 crop reports, corporate research. Twenty pages devoted to "Cotton For Nonwovens: A<br />
Technical Guide." http://www.cottoninc.com<br />
• EDANA: European Disposables <strong>and</strong> Nonwovens Association. This site comprises an excellent resource.<br />
Coverage includes EDANA organization, membership, st<strong>and</strong>ards development <strong>and</strong> test methods, events, news<br />
<strong>and</strong> publications. A particularly effective description <strong>of</strong> nonwoven processes is provided, with very good<br />
schematics. Although not operative as yet, links to other sites are promised. http://www.edana.org<br />
• Fiber Economics Bureau: The activity <strong>of</strong> the American Fiber Manufacturers Association concerned with<br />
fiber economics. An excellent site, with FTC Fiber Rules, Suppliers Guide, Fiber Tariffs, World Directory,<br />
Fiber History, Polymer Science <strong>and</strong> numerous links to other related sites. Added FiberWorld Classroom, with<br />
educational material, some <strong>of</strong> which is downloadable. Also, a good source <strong>of</strong> news on the fibers industry.<br />
http://www.fibersource.com; http://www.fiberworld.com<br />
• Industrial <strong>Fabrics</strong> Association International: Association <strong>of</strong> international industrial <strong>and</strong> techical fabrics <strong>and</strong><br />
textiles. Site includes membership information, market research, worldwide <strong>of</strong>fices, government affairs,<br />
technical services, etc. http://ifai.org<br />
• INDA, Association <strong>of</strong> the Nonwovens Industry: Items include technical papers, st<strong>and</strong>ard tests, conferences<br />
<strong>and</strong> exhibitions, publications. Newly added is section on Academic Research Facilities Database; Industry<br />
links; International Nonwovens <strong>Journal</strong>, with order form; Job Mart <strong>and</strong> Classified Ads. http://www.inda.org<br />
• Machinery Database: TEXDATA five-language database allows machinery manufacturers to provide<br />
listings on new machinery, replacements <strong>and</strong> plant modernization. Listing <strong>of</strong> many machinery categories. Also<br />
provides for a company search <strong>and</strong> information, product categories <strong>and</strong> searching capability. Includes selection<br />
<strong>of</strong> nonwoven machinery, comprising web forming, auxiliary machinery. Has short list <strong>of</strong> technical papers.<br />
Sponsored by Swiss textile publishing firm, ITS Publishing. http://www.texdata.com<br />
• Pira International: A global knowledge provider. Items include: membership information, conferences <strong>and</strong><br />
training, publications, <strong>and</strong> the Pira Database, including a free trial. http://www.pira.co.uk<br />
• Textile Dictionary: Alphabetical listing <strong>of</strong> textile features <strong>and</strong> uses. Managed by the Centre for Canadian<br />
Fashion & Design. http://www.ntg-inter.com/ntg/textile.htm<br />
• Thomas Register: Extensive database on products <strong>and</strong> services, companies, <strong>and</strong> locations, covering all <strong>of</strong> the<br />
USA. www.thomasregister.com<br />
• U.S. Government: Provides a powerful set <strong>of</strong> search tools that look for information on the <strong>of</strong>ficial<br />
government web sites. Also has information on material in the National Technical Information Service (NTIS).<br />
http://www.usgovsearch.com<br />
—INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Worldwide Abstracts <strong>and</strong> Reviews<br />
INJ DEPARTMENTS<br />
WORLWIDE ABSTRACTS AND REVIEWS<br />
A sampling <strong>of</strong> Nonwovens Abstracts from Pira International:<br />
A unique intelligence service for the nonwovens industry<br />
These pages feature an extract from Nonwovens Abstracts, compiled by Pira International, from<br />
international business journals, newspapers, market research reports <strong>and</strong> conference proceedings,<br />
keeping you up-to-date on the latest business <strong>and</strong> technical developments in the nonwovens industry.<br />
Nonwovens Abstracts provides international coverage on all aspects <strong>of</strong> nonwovens production: fibers,<br />
raw materials, web formation, bonding <strong>and</strong> converting. Information is also provided on all the different<br />
nonwoven products, from composites to cleaning materials <strong>and</strong> the companies <strong>and</strong> markets involved.<br />
A monthly journal is available <strong>and</strong> readers can also access the information from the Paper, Printing <strong>and</strong><br />
Packaging Database on CD-ROM, updated quarterly. The information is available online via the major<br />
hosts <strong>and</strong> from the Pira Database on Pira's website - www.pira.co.uk. The web <strong>and</strong> online databases are<br />
updated weekly. Pira can provide full text copies <strong>of</strong> documents cited in the Pira Database <strong>and</strong> the<br />
associated abstracts journals. The full text will normally be in the language <strong>of</strong> publication.<br />
For a sample journal, a free trial <strong>of</strong> the web database or more information, please contact the<br />
Information Center, Pira International, R<strong>and</strong>alls Road, Leatherhead, Surrey KT22 7RU, UK. Fax: 00 44<br />
(0)1372 802239 or email: infocentre@pira.co.uk<br />
For this particular selection, non-English language publications were reviewed in an effort to provide<br />
coverage <strong>of</strong> relatively less accessible sources to a large portion <strong>of</strong> the INJ audience.<br />
Microbial control finish<br />
Toray Industries <strong>of</strong> Tokyo, Japan, have reported on their "Makspec" fabrics - polyesters with a microbial<br />
control finish. The principal bacteria are methicillin-resistant staphylococcus aureus (MRSA), klebsiella<br />
pneumoniae, staphylococcus aureus, pseudomonas aeruginoza <strong>and</strong> escherichia coli. The fabrics have<br />
been test washed for 15 minutes at 85 o C 100 times <strong>and</strong> antibacterial high performance is maintained. The<br />
outer fibre portions are penetrated by the active agent, a method improving on surface adherence <strong>and</strong><br />
kneading into inside fibres in production. Finishing <strong>and</strong> dyeing methods are the same as for normal<br />
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Worldwide Abstracts <strong>and</strong> Reviews<br />
polyester fabrics. MRSA <strong>and</strong> E. coli 0-157 protection is 3-5 times higher than other products. Toray<br />
plans further healthcare developments <strong>and</strong> anticipates Japanese sales <strong>of</strong> 4.5m metres within three years.<br />
(1 fig).<br />
Author: Anon<br />
Source: New Mater. Jpn<br />
Issue: Jan. <strong>1999</strong>, pp 10-11<br />
Finding your solution<br />
Nonwoven panels, especially needle penetrable panels, sometimes referred to as tapestry, are discussed<br />
in a question <strong>and</strong> answer format. These panels can be based on synthetics, viscose or wool fibres, <strong>and</strong><br />
various surface effects can be obtained, e.g. bright or matt, smooth, fleecy, <strong>and</strong> also hot or cold tones.<br />
With synthetics, luminescent effects can be obtained. Needle penetrable panels are relatively new <strong>and</strong> are<br />
not yet widely used, partly because the machines required for their production are not always available.<br />
Author: Aleks<strong>and</strong>rova M<br />
Source: Text. Ind.<br />
Issue: No. 1, 1998, pp 17-19 (In Russian)<br />
Honshu Kinokurosu - Material supplier for two wipe fields, kitchen paper <strong>and</strong> wet h<strong>and</strong> towels<br />
Honshu Kinokurosu's dry pulp non-woven "Kinokurosu" is mostly used for wipes, in particular kitchen<br />
paper <strong>and</strong> wet h<strong>and</strong> towels. Lion's kitchen paper, made <strong>of</strong> Kinokurosu, has been on the Japanese market<br />
for 30 years, <strong>and</strong> its first-grade quality has taken 25% <strong>of</strong> the market share. Honshu Timely, Honshu<br />
Kinokurosu's associated company, is Japan's top supplier <strong>of</strong> wet h<strong>and</strong> towels <strong>and</strong> <strong>of</strong>fers a wide range <strong>of</strong><br />
products from the luxurious to the economical. The market for wet h<strong>and</strong> towels is considered to be<br />
growing steadily. However, the notion that wet h<strong>and</strong> towels are customarily given out free is quite strong<br />
among Japanese consumers, so common acceptance as a retail item may be slow. (1 fig)<br />
Author: Anon<br />
Source: Nonwovens Rev.<br />
Issue: Vol. 9, No. 4, Dec. 1998, p. 14 (In Japanese)<br />
Uni Charm - Top share holder in cosmetic cut cotton <strong>and</strong> baby wipe fields<br />
Uni Charm (UC) supplies a wide range <strong>of</strong> wipes <strong>and</strong> h<strong>and</strong> towels, <strong>and</strong> leads in the field <strong>of</strong> cosmetic cut<br />
cotton <strong>and</strong> baby wipes in Japan. Cosmetic cut cotton "Silcot" has been on the market for 24 years, <strong>and</strong><br />
has become the top-rank br<strong>and</strong>, with a 30% market share. Recently the product has been improved to<br />
inner cotton sealed-in type which does not leave lint on the skin after use. This revision is expected to<br />
increase their market share by 20%. UC's baby wipes are competing well for top position with Pijon<br />
products, but the postponed launch <strong>of</strong> flushable baby wipes may be disadvantageous for UC. In 1997,<br />
UC launched wet tissues for pet dogs. These are made <strong>of</strong> a thick nonwoven impregnated with<br />
deodorizing <strong>and</strong> anti-bacterial substances. (5 fig)<br />
Author: Anon<br />
Source: Nonwovens Rev.<br />
Issue: vol. 9, no. 4, Dec. 1998, pp 18-19 (In Japanese)<br />
High-strength polypropylene fibre<br />
Despite excellent processability, chemical-resistance <strong>and</strong> lightness, polypropylene fibre has poor fibre<br />
strength compared to other general resin fibres. Ube Nitto Kasei, Japan, has been working on this<br />
problem <strong>and</strong> has recently succeeded in manufacturing a high-strength polypropylene fibre. Ordinary<br />
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isotactic polypropylene is used <strong>and</strong> melt spinning performed within normal spinning temperature range at<br />
speeds above several hundred m/min. Highly magnified roller drawing is possible under a temperature<br />
range higher than the crystallization dispersion temperature. Fibre strength greater than 10g/d can be<br />
achieved with a faster drawing speed than current types. Possible applications are ropes <strong>and</strong> nets<br />
requiring high strength <strong>and</strong> elasticity. Use for liquid filters for acid, alkali <strong>and</strong> paints is also appropriate<br />
due to excellent chemical-resistance. (2 fig, 3 tab)<br />
Author: Oota S<br />
Source: Nonwovens Rev.<br />
Issue: vol. 9, no. 4, Dec. 1998, pp 38-39 (In Japanese)<br />
The development <strong>of</strong> spunbond biodegradable nonwoven<br />
Shinwa, Japan, has recently launched a spunbonded biodegradable nonwoven, which is made from<br />
polylactic acid resin, Lactron, developed by Kanebo Gosen. Confirmed as compatible with the human<br />
body, polylactic acid is very safe as a raw material. When disposed <strong>of</strong> it decomposes into carbonic acid<br />
gas <strong>and</strong> water by a microorganism action in the earth or sea. No hazardous gases are created when<br />
incinerated <strong>and</strong> required calories for combustion are only a third or half <strong>of</strong> polyethylene or<br />
polypropylene. A wide range <strong>of</strong> applications is anticipated, including sanitary <strong>and</strong> household items, <strong>and</strong><br />
agricultural <strong>and</strong> construction materials. Shinwa’s development <strong>of</strong> biodegradable nonwovens has started<br />
with spunbond, but development for thermalbond <strong>and</strong> spunlace types are also underway. (1 tab)<br />
Author: Anon<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 11, 10 Nov. 1998, pp 27-28 (In Japanese)<br />
Development <strong>of</strong> range <strong>of</strong> biodegradable materials<br />
Unichika, Japan, has recently developed “Terramac,” a range <strong>of</strong> biodegradable materials including<br />
sheets, films, fibres <strong>and</strong> spunbond. Unichika has worked on the development <strong>of</strong> naturally recyclable<br />
materials for about 10 years, <strong>and</strong> in collaboration with world-leading polylactic acid manufacturer,<br />
Cargill-Daw Polymers, they have transformed biodegradable raw material <strong>of</strong> polylactic acid into various<br />
product forms using original molding technology. A number <strong>of</strong> characters <strong>and</strong> potential properties <strong>of</strong><br />
polylactic acid were drawn out during processing <strong>and</strong> added to each product <strong>of</strong> Terramac. Uses in<br />
agriculture, horticulture, construction, fishery, food sector <strong>and</strong> sanitary <strong>and</strong> household items are<br />
anticipated. Unichika plans for a 5,000t production scale in 3 years <strong>and</strong> 16,000t in 5 years for its<br />
Terramac products.<br />
Author: Anon<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 11, 10 Nov. 1998, p. 28 (In Japanese)<br />
Surface modification <strong>of</strong> aramid fibers to improve composite adhesion by plasma treatment<br />
P-aramid fibres are suitable as reinforcement fibres for high-performance composites because <strong>of</strong> their<br />
low density, increased elongation at rupture compared with steel wire, <strong>and</strong> high decomposition<br />
temperature. Their molecular structure governs their high chemical <strong>and</strong> mechanical resistance. Low<br />
fibre-matrix adhesion can be improved by treating the aramid fibres with plasma, which causes better<br />
moistening <strong>of</strong> the aramid fibres opposite to the epoxide matrix during composite manufacture. Etching<br />
<strong>and</strong> cleaning plasmas <strong>and</strong> plasma polymerization have been investigated. Optimum composite strength is<br />
achieved when all fibres are completely embedded in the matrix. (Short article)<br />
Author: Bechter D; St Berndt R; Oppermann W<br />
Source: Tech. Text.<br />
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Issue: vol. 42, no. 1, Feb. <strong>1999</strong>, p. E2<br />
Effect <strong>of</strong> loading rate on the mechanical behavior <strong>of</strong> fiber glass mat/epoxy composite<br />
Glass fibre mat/epoxy composites were tested to assess effect <strong>of</strong> loading rates on their performance.<br />
Loading rates were investigated in a range <strong>of</strong> 10, 50 <strong>and</strong> 250mm/min, <strong>and</strong> fracture behaviour <strong>of</strong> the<br />
laminated composites was determined using a fibre/matrix interface. Short beam bend <strong>and</strong> three point<br />
bend tests showed cracks occurring on the composite surfaces during loading, a process which would<br />
most likely be controlled by weak links such as poor fibre/matrix interfacial adhesion. Tensile strength <strong>of</strong><br />
the composites decreased with increase <strong>of</strong> loading rate, probably due to voids in the matrix <strong>and</strong> at the<br />
interfaces. Interfacial shear strength did not display a significant loading rate dependence, while flexural<br />
strength was found to increase with loading rate. (4 tab)<br />
Author: Bayram A; Yaziki M; Korkmaz B<br />
Source: Tech. Text.<br />
Issue: vol. 42, no. 1, Feb. <strong>1999</strong>, pp E3-E5<br />
Polyester staple fibre from Toyobo has high moisture absorption<br />
Osaka-based Toyobo Co Ltd has developed a polyester staple fibre that has a 10% rate <strong>of</strong> moisture<br />
absorption. This is compared to conventional polyester staple, which has a rate <strong>of</strong> absorption <strong>of</strong> only<br />
0.4%, climbing to about 1% with the application <strong>of</strong> special finishes. By using a chemical treatment,<br />
Toyobo has made its polyester even more absorbent than cotton. Further, cotton fibres tend to retain the<br />
moisture they absorb, but Toyobo’s polyester quickly releases it. The fibre’s hollow structure also retains<br />
warmth. Quilt fillings will be the principal application, (1 ref) (Short article)<br />
Author: Anon<br />
Source: New Mater. Jpn<br />
Issue: Apr. <strong>1999</strong>, pp 6-7<br />
Tie-up for superabsorbent fibre products agreed by Kanebo Gohsen<br />
Kanebo Gohsen <strong>of</strong> Osaka will exp<strong>and</strong> production <strong>of</strong> its highly water-absorbent fibre Bell Oasis. Japanese<br />
manufacturers Nippon Felt <strong>and</strong> Hattori Takeshi will develop industrial products, such as filters <strong>and</strong><br />
medical items, <strong>and</strong> full-scale projects have already been initiated. Bell Oasis is a highly water- <strong>and</strong><br />
moisture-absorbent fibre based on a proprietary acrylic polymer. It can absorb up to 80 times its own<br />
weight <strong>of</strong> water, <strong>and</strong> is heat resistant up to 150 deg C. (1 ref) (Short article)<br />
Author: Anon<br />
Source: New Mater. Jpn<br />
Issue: Apr. <strong>1999</strong>, p. 7<br />
Injection molding <strong>of</strong> natural fibre-reinforced polypropylene<br />
Research into the use <strong>of</strong> natural fibres, as a replacement for glass fibres, in the reinforcement <strong>of</strong> injection<br />
molded polypropylene parts is described. Compromises need to be made on heat resistance but flax <strong>and</strong><br />
low-THC hemp strains can <strong>of</strong>fer price advantages over glass in the medium loading range. Fibre-matrix<br />
adhesion, compounding concerns such as hygroscopic properties, rheology, mechanical properties <strong>and</strong><br />
special features are described.<br />
Author: Aurig T; Mennig G<br />
Source: Kunstst. Plast Eur.<br />
Issue: Kunstst. Plast. Eur. vol. 89, no. 3, Mar. <strong>1999</strong>, pp 6-7, 30-32<br />
Low foaming spin finishes<br />
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Low foaming is a new requirement for spin finishes, to aid processes such as hydroentanglement. The<br />
antistat component <strong>of</strong> the finish contributes highly to foaming but is a necessary ingredient, especially in<br />
high speed carding. Work has been directed at a target <strong>of</strong> no foam measurable after one minute, which is<br />
tested by means such as the perforated disc method. Hansa Textilchemie GmbH <strong>of</strong> Oyten, Germany uses<br />
a method where fibres are placed in a beaker <strong>and</strong> covered with distilled water, to determine the foaming<br />
qualities <strong>of</strong> the resulting liquor. St<strong>and</strong>ardized tests are <strong>of</strong> further importance for products intended for<br />
hygiene <strong>and</strong> medical uses, to avoid skin irritation.<br />
Author: Niestegge R<br />
Source: Tech. Text.<br />
Issue: vol. 42, no. 2, Apr. <strong>1999</strong>, pp E22-E23<br />
Outer textile linings for cars: an innovation<br />
The need to improve function, reduce costs <strong>and</strong> consider environmental implications is causing car<br />
manufacturers to change to new materials. Needle <strong>and</strong> pile floor carpets (NFC-PFC) fitted in the outer<br />
linings <strong>of</strong>fer improvements in acoustic effect <strong>and</strong> lower weight, leading to reduced fuel consumption.<br />
Their porous structure minimizes noise from water on the road <strong>and</strong> reduces spray, while giving elastic<br />
protection against stone impact. They display positive characteristics in water absorption, drying<br />
behaviour, mechanical stability <strong>and</strong> strength, resistance to abrasion, tearing <strong>and</strong> weather, cleaning ability,<br />
assembly, endurance <strong>and</strong> recycling. The characteristics <strong>of</strong> a wheel-case lining, which may be adapted for<br />
different car types, are analyzed according to DIN 61210. (2 tab)<br />
Author: Elsele D<br />
Source: Tech. Text.<br />
Issue: vol. 42, no. 2, Apr. <strong>1999</strong>, pp E28-E29<br />
1,000 frames per second: revealing the secrets <strong>of</strong> meltblown nonwovens<br />
Meltblowing is a sophisticated process that produces micr<strong>of</strong>ibres <strong>of</strong> under 10 microns in diameter which<br />
are condensed into a nonwoven web. Research into establishing the process factors affecting quality <strong>and</strong><br />
into controlling the process itself has resulted in the formation <strong>of</strong> blur-free, freeze-frame <strong>and</strong> slow motion<br />
film images during production. Acceleration, velocity, diameter, orientation <strong>and</strong> entanglement <strong>of</strong> fibres<br />
as a function <strong>of</strong> distance from the die orifice can now be measured by newly developed equipment.<br />
High-speed single exposures <strong>and</strong> multiple exposures are achievable with a high-speed LSI 1000 pulsed<br />
laser from Oxford Lasers. The processing variables identified so far are air pressure, die-to-collector<br />
distance between which significant acceleration <strong>and</strong> velocity changes take place, <strong>and</strong> collector surface<br />
speed.<br />
Author: Lennox-Kerr P<br />
Source: Tech. Text.<br />
Issue: vol. 42, no. 2, Apr. <strong>1999</strong>, pp E30-E31<br />
Development <strong>of</strong> nonwovens<br />
Within the nonwoven industry in India great potential exists for Indian companies to exp<strong>and</strong> their<br />
activities into new applications through more research <strong>and</strong> development, greater customer awareness <strong>and</strong><br />
faster production. The nonwoven process <strong>and</strong> web formation are explained <strong>and</strong> properties listed which<br />
can be obtained with the use <strong>of</strong> binders. The thermal, spun <strong>and</strong> self-bonded processes are described <strong>and</strong> a<br />
comprehensive list <strong>of</strong> nonwoven end products supplied. Principal fibres are covered, <strong>and</strong> statistical<br />
background on market growth (1994-2000) globally <strong>and</strong> process technologies used (1993 estimate) is<br />
given. Nonwoven consumption is low in India through lack <strong>of</strong> good quality raw materials <strong>and</strong> a heavy<br />
import duty structure for binders, but there is considerable potential for further development <strong>of</strong> the<br />
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industry. (2 tab, 6 ref)<br />
Author: Shiva Prakesh A V<br />
Source: Indian Text. J.<br />
Issue: vol. 109, no. 4, Jan. <strong>1999</strong>, pp 26-27<br />
Compression porometry for nonwoven fibrous mats<br />
Compression porometry represents an advanced tool for the analysis <strong>of</strong> pore paths in the long, in-plane<br />
dimension <strong>of</strong> fibrous materials as a function <strong>of</strong> compression. The new technique is particularly useful in<br />
the study <strong>of</strong> the effect <strong>of</strong> the incremental flattening <strong>of</strong> a mat on the bubble point pressure <strong>and</strong> <strong>of</strong> the<br />
relative pore diameters at the bubble point for the cases <strong>of</strong> z-direction <strong>and</strong> x,y-direction. The technology<br />
allows small, controlled changes in the mechanical pressure on the sample to obtain high-resolution plots<br />
<strong>of</strong> data at intermediate levels <strong>of</strong> compression. Data obtained by use <strong>of</strong> this new technology can prove<br />
particularly relevant for products whose manufacture <strong>and</strong> development requires information regarding<br />
the wetting characteristics <strong>and</strong> movement <strong>of</strong> air or liquids in an enclosed matrix subjected to differing<br />
levels <strong>of</strong> compression.<br />
Author: Perna V F; Wagner K<br />
Source: Allg. Vliesst<strong>of</strong>f-Rep.<br />
Issue: vol. 27, no. 2, <strong>1999</strong>, pp 27-28; 29-30<br />
R <strong>and</strong> D trends: 1997 science <strong>and</strong> technology spending, Y15,741,500m highest ever showing a<br />
steady increase in the past three years<br />
In Japan 1997 science <strong>and</strong> technology spending was highest ever at Y15,741,500m, a 4.4% (Y662,200m)<br />
increase on 1996. Industry was the most active area (Y10,658,400m, 6.1% increase), followed by<br />
universities (Y3,059,200m, 1.5% increase) <strong>and</strong> public institutes (Y2,023,900m, 0.8% increase). Research<br />
trends were application <strong>and</strong> product development orientated, with basic research being suppressed<br />
slightly (13.8% <strong>of</strong> total research, 0.3% negative growth). For the first time female researchers numbered<br />
over 10% <strong>of</strong> total researchers in 1997. The aims <strong>of</strong> the Technical Licensing Organization (TLO) are also<br />
discussed.<br />
Author: Anon<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 2, Feb. <strong>1999</strong>, p. 27 (In Japanese)<br />
Product introduction: vinylon chopped fibre nonwoven, VM Melt, from Japan Vilene Co Ltd, a<br />
new material as an alternative to glass fibre fabric<br />
Japan Vilene Co Ltd <strong>and</strong> Dainippon Ink KK have developed VM Melt from vinylon chopped str<strong>and</strong><br />
fibre. It has been used as an alternative to glass-based materials for the water tanks <strong>of</strong> the Takehara<br />
Power Station (Hiroshima, Japan) <strong>and</strong> owing to its superb performance including chemical resistance,<br />
water resistance <strong>and</strong> mechanical strength under 5,000V testing, together with its ability to be converted it<br />
is now also being used as a surface protection material for concrete. Unlike the glass-based product, this<br />
product does not generate harmful particles during construction. The target sales in the first year are<br />
Y100m, <strong>and</strong> Y600m in three years. The vinylon mat complex (patent pending), combining the surface<br />
material <strong>and</strong> VM Melt, is also available. (1 fig)<br />
Author: Anon<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 3, Mar. <strong>1999</strong>, p. 20 (In Japanese)<br />
JNR prospects: amorphous carbon fibre nonwoven, dream for its development <strong>and</strong><br />
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commercialization<br />
Amorphous metal has now reached the commercial application stage after 20 years research <strong>and</strong><br />
development. This metal is the essential element for the success <strong>of</strong> the electric vehicle (EV) <strong>and</strong><br />
hybrid-car. Amorphous carbon nano-fibre was first reported in January <strong>1999</strong>, by Kogyo Gijyutsuinn, <strong>and</strong><br />
nonwoven development using this fibre is anticipated. Once this task is achieved, the application <strong>of</strong><br />
amorphous carbon nano-fibre nonwoven to the EV will be welcomed by the car industry, since the<br />
weight reduction <strong>of</strong> the car battery, by replacing amorphous metal with a nonwoven, is significant, <strong>and</strong><br />
this will contribute to improving the practicality <strong>of</strong> the EV.<br />
Author: Shimizu T<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 3, Mar. <strong>1999</strong>, pp 24-25 (In Japanese)<br />
Special edition, liquid filter: current status <strong>and</strong> prospect <strong>of</strong> nonwoven filter for blood treatment<br />
The necessity <strong>of</strong> blood treatment filters for the removal <strong>of</strong> leukocytes is widely recognized to ensure safe<br />
blood transfusion: 95% <strong>of</strong> these filters are polyester nonwoven based products. In addition to the<br />
separation performance determined by fibre diameter, as a medical product these filters have to meet<br />
tight regulations. Blood for urgent surgical needs is mainly used untreated as a new closed type system,<br />
in which a filter is integrated in the bleeding bag, will circumvent this problem. Nonwoven filters for<br />
uses other than leukocyte removal from blood transfusion is currently limited: filters for bone marrow<br />
treatment <strong>and</strong> for in vitro blood circulation treatment are showing potential. (9 fig, 4 tab)<br />
Author: Kaneko M<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 4, Apr. <strong>1999</strong>, pp 9-13<br />
R&D trends: The nonwovens industry <strong>and</strong> SBIR (the Small Business Innovation Research)<br />
support system, positive outcomes expected<br />
The SBIR (Small Business Innovation Research) support program was introduced in Japan in <strong>1999</strong> with<br />
a Y1,600m national budget. SBIR is attracting interest from small <strong>and</strong> middle sized companies. A<br />
questionnaire carried out by Nikkei Newspaper indicated that SBIR is a priority interest for 64% <strong>of</strong> those<br />
companies questioned. The program includes financial support for the research <strong>and</strong> development<br />
projects. It is recommended that to become truly high-tech, the nonwoven industry should utilize this<br />
system.<br />
Author: Anon<br />
Source: Jpn Nonwovens Rep.<br />
Issue: no. 4, Apr. <strong>1999</strong>, p. 17 (In Japanese)<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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INJ DEPARTMENTS<br />
ASSOCIATION NEWS<br />
International Nonwovens Technical Conference 2000 Set For Texas<br />
The 2000 International Technical Nonwovens Conference will be co-sponsored by INDA <strong>and</strong> TAPPI <strong>and</strong><br />
is scheduled for September 25-28, 2000 at the Hotel Inter-Continental, Dallas, TX. INTC 2000 is the<br />
technical forum designed to provide opportunities for industry leaders to review the latest research,<br />
product innovations <strong>and</strong> market applications for all nonwoven technologies. INDA is currently accepting<br />
abstracts related to the following topics chosen by the INTC Conference Committee:<br />
● <strong>Fibers</strong><br />
● Properties & Performance<br />
● Process Technologies<br />
● Filtration<br />
● Mats<br />
● Binders & Adhesives<br />
● Absorbents<br />
● Barriers<br />
● Melt Extrusion<br />
● Hydroentangling<br />
● General<br />
By presenting a paper at the INTC Conference, speakers will reinforce their expertise within the<br />
nonwovens community; gain recognition among peers <strong>and</strong> with potential customers; enhance their<br />
reputation as a leader within the industry; provide their company with invaluable industry visibility; <strong>and</strong><br />
their written paper will be distributed to all conference attendees in the INTC 2000 Book <strong>of</strong> Papers. For<br />
end-users <strong>of</strong> nonwoven products, this conference is a unique opportunity to tell suppliers their needs.<br />
To receive more information about presenting a paper at INTC 2000, please contact Deanna Lovell,<br />
Education Coordinator, INDA, Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry, P.O. Box 1288, Cary, NC<br />
27512-1288; 919-233-1210, ext. 119; Fax 919-233-1282; dlovell@inda.org; www.inda.org.<br />
Needlepunch 2000 Call For Papers<br />
INDA will sponsor Needlepunch 2000 at the Hyatt Regency Downtown, Greenville, SC, from April<br />
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26-28, 2000. Needlepunch 2000 is the nonwovens forum designed to provide opportunities for industry<br />
leaders to review the latest research, product innovations <strong>and</strong> market applications for all needlepunch<br />
technologies. INDA is currently accepting abstracts for the following topics chosen by the Needlepunch<br />
Committee:<br />
●<br />
●<br />
●<br />
●<br />
●<br />
●<br />
Competitive Technologies<br />
End Users Forum<br />
<strong>Fibers</strong><br />
Machinery & Needle Advances<br />
International Trade<br />
Production<br />
To receive more information about presenting a<br />
paper at Needlepunch 2000, please contact Deanna<br />
Lovell, Education Coordinator, INDA, Association<br />
<strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry, P.O. Box 1288,<br />
Cary, NC 27512-1288; 919-233-1210, ext. 119; Fax<br />
919-233-1282; dlovell@inda.org; www.inda.org.<br />
EDANA Names New Officers<br />
EDANA, the Brussels-based Europ-ean Disposables<br />
<strong>and</strong> Nonwovens Association, recently re-elected<br />
Rolf Altdorf, vice president <strong>and</strong> managing director,<br />
PGI Nonwovens Europe, The Netherl<strong>and</strong>s, chairman<br />
<strong>of</strong> EDANA for another one-year term <strong>of</strong> <strong>of</strong>fice.<br />
Aldo Ghira, managing director <strong>of</strong> Tenotex S.p.A.,<br />
Italy, was re-elected as treasurer. Also elected as<br />
vice-chairmen were Ingemar Bengtson, managing<br />
director, Trioplanex International, Sweden, <strong>and</strong><br />
Krzyszt<strong>of</strong> Malowaniec, R&D director, Personal<br />
Care Products, Paul Hartmann, Germany.<br />
Four new governors were elected to EDANA's<br />
16-persons Board<br />
● Gianluigi Fornoni, Fiberweb Neuberger<br />
S.p.A., Italy.<br />
● Anne Mykkänen, Mölnlycke Health Care AB,<br />
Sweden<br />
● Gerd Ries, Johnson & Johnson, Germany<br />
● Georg Werner, Stockhausen, Germany<br />
Pourdeyhimi Joins NCRC<br />
Behnam Pourdeyhimi has joined the Department<br />
<strong>of</strong> Textile & Apparel, Technology & Management<br />
in the College <strong>of</strong> Textiles at North Carolina State<br />
university <strong>and</strong> has been appointed Co-Director <strong>of</strong><br />
the Nonwovens Cooperative Research Center<br />
(NCRC). Pourdeyhimi received his PhD from<br />
Leeds University in 1982. This was followed by a<br />
short stint as a post doc at NCSU <strong>and</strong> then at<br />
Cornell University. His distinguished academic<br />
career has taken him through the University <strong>of</strong><br />
Maryl<strong>and</strong> (Assistant/Associate Pr<strong>of</strong>essor,<br />
1984-1995) <strong>and</strong> Georgia Tech (Pr<strong>of</strong>essor,<br />
1995-<strong>1999</strong>).<br />
Pourdeyhimi has taught textile <strong>and</strong> fiber science,<br />
technology <strong>and</strong> engineering as well as well as the<br />
application <strong>of</strong> microscopy <strong>and</strong> image analysis to<br />
textiles <strong>and</strong> materials problems both at<br />
undergraduate <strong>and</strong> graduate levels. His research<br />
experience covers such areas as image <strong>and</strong><br />
structural analysis <strong>of</strong> nonwoven fibrous webs,<br />
textile applications in sports, bioengineering <strong>and</strong><br />
materials, instrumentation <strong>and</strong> test method<br />
development, among others. His contributions to<br />
fiber/textile science, engineering <strong>and</strong> technology<br />
<strong>and</strong> his contributions to the pr<strong>of</strong>ession have been<br />
well recognized by the Textile Institute <strong>and</strong> the<br />
Fiber Society. He served as the Fiber Society<br />
Lecturer in 1993 <strong>and</strong> as the president <strong>of</strong> the Fiber<br />
Society in 1995.<br />
The other continuing members <strong>of</strong> the 16-member EDANA Board <strong>of</strong> Directors are: Heikki Bergholm,<br />
Lassila & Tikanoja, Finl<strong>and</strong>; Hermann Eidel, Freudenberg, Germany; Patrick Jeambar, Ahlstrom Lystil<br />
SA, France; Franz Junkermann, Colbond Nonwovens, The Netherl<strong>and</strong>s; Frantisek Klaska, Pegas AS,<br />
Czech Republic; Jorma Leskinen, UPM-Kymmene, Walkis<strong>of</strong>t, Finl<strong>and</strong>; Luc Maes, Libeltex, Belgium;<br />
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<strong>and</strong> Reiner Schoene, Procter & Gamble, Germany<br />
EDANA Plans 2000<br />
Nonwovens Symposium<br />
A call for original papers has been issued by EDANA, the European Disposables <strong>and</strong> Nonwovens<br />
Assoc-iation, for the EDANA 2000 International Nonwovens Symposium that will take place in Prague,<br />
the Czech Republic, on June 7-8, 2000.<br />
The symposium will feature new developments in the markets for nonwovens, especially hygiene, as<br />
well as the latest advances in technology, fibers <strong>and</strong> webs, treatment <strong>and</strong> bonding, <strong>and</strong> related issues.<br />
EDANA invites short abstracts <strong>of</strong> proposed papers from companies, research institutes, universities <strong>and</strong><br />
individuals for consideration <strong>of</strong> inclusion in the symposium program. The deadline for such submissions<br />
is November 30, <strong>1999</strong>. They should be submitted to EDANA, 157 avenue Eugène Plasky, Bte 4; 1030<br />
Brussels, Belgium; Tel.: 32+2/734-9310; Fax: 32+2/733-3518; edana@euronet.be.<br />
Jacobs Awarded TAPPI<br />
Nonwovens Division Scholarship<br />
Cari Jacobs has been awarded the <strong>1999</strong>-2000 TAPPI Nonwovens Division scholarship. Jacobs is a<br />
student in chemical engineering at Oregon State University <strong>and</strong> is a member <strong>of</strong> the Oregon State<br />
University TAPPI Student Chapter.<br />
Jacobs plans to graduate in 2001. After graduation she would like the opportunity to work in the<br />
nonwovens industry, ideally taking advantage <strong>of</strong> her skill in chemistry. Jacobs is a member <strong>of</strong> TAPPI,<br />
the American Institute <strong>of</strong> Chemical Engineering, the Society <strong>of</strong> Women Engineers, Phi Theta Kappa<br />
Honors Society, <strong>and</strong> the National Honors Society. She received an Academic Achievement Award in<br />
1996, was on the National Dean's List Award for academic achievement (1995-1996), has been on the<br />
Honor Roll since 1992 in both high school <strong>and</strong> college, <strong>and</strong> was a recipient <strong>of</strong> the Who's Who Among<br />
American High School Students Award (1994-1995).<br />
TAPPI's Nonwovens Division promotes the objectives <strong>of</strong> the association with respect to materials,<br />
equipment <strong>and</strong> processes for the manufacture <strong>and</strong> use <strong>of</strong> nonwovens.<br />
PaperBase <strong>and</strong> TAPPI Deal<br />
An agreement between TAPPI <strong>and</strong> Paperbase International now allows TAPPI members to arrange<br />
special access to the Paperbase International extensive database, called "PaperBase."<br />
Paperbase International is a consortium <strong>of</strong> the four leading pulp <strong>and</strong> paper institutes in Europe - CTP<br />
(France), KCL (Finl<strong>and</strong>), Pira International (UK) <strong>and</strong> STFI (Sweden). The consortium was organized<br />
with the aim <strong>of</strong> combining their various databases in order to provide their memberships with full<br />
coverage <strong>of</strong> the latest technical, research <strong>and</strong> business information for the pulp <strong>and</strong> paper industry.<br />
With this new agreement, TAPPI members can obtain subscription to this database at a 20% discount <strong>of</strong>f<br />
the annual subscription via the Internet. In addition, TAPPI members can subscribe to the PaperBase<br />
CD-ROM with a networking license at the same price as the single-user license - a 30% savings.<br />
An introductory <strong>of</strong>fer includes access to PaperBase on the Web free <strong>of</strong> charge for a limited time. For<br />
more information, visit http://www.paperbase.org or http://www.tappi.org.<br />
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NONWOVENS<br />
CALENDAR<br />
September <strong>1999</strong><br />
INJ DEPARTMENTS<br />
Sept. 21-23. INDA-TEC '99 International Conference & Suppliers' Showcase '99. Renaissance<br />
Waverly Hotel, Atlanta, GA. Marilyn Bellinger, INDA, P.O. Box 1288, Cary, NC 27512-1288;<br />
919-233-1210; Fax: 919-233-1282; www.inda.org<br />
Sept. 21-23. SITEC '99 The 3rd Shanghai International Techtextile Exhibition & Conference.<br />
Shanghai, China. Ellen Dillard, Miller Freeman, 2000 Powers Ferry Center, Suite 450, Marietta, GA<br />
30067; 770-563-0129; Fax: 770-818-9092; edillard@mfi.com<br />
Sept. 21-23. SINCE '99/ENA '99 - Meeting The 21st Century Nonwovens Challenge. Shanghai, China.<br />
Ellen Dillard, Miller Freeman, 2000 Powers Ferry Center, Suite 450, Marietta, GA 30067;<br />
770-563-0129; Fax: 770-818-9092; edillard@mfi.com<br />
Sept. 24-28. IPF - International Plastics Fair '99. Makuhari Messe, Tokyo, Japan. IPF Show<br />
Management Office, Kasumigaseki Bldg., 3-2-5 Kasumigaseki, Chiyoda-Ku, Tokyo 100-6012, Japan;<br />
+81-3-3503-7320; Fax: +81-3-3503-7620.<br />
Sept. 27-29. TAPPI/China Paper Conference <strong>and</strong> Exhibit. China International Exhibition Center,<br />
Beijing, China. TAPPI, P.O. Box 105113, Atlanta, GA 30368-5113; 800-332-8686; 770-446-1400; Fax:<br />
404-446-6947 (U.S.) or 800-446-9431 (Canada) or 770-446-1400 (Outside U.S. & Canada).<br />
Sept. 27-29. TAPPI/CORR Tech Asia. China International Exhibition Center, Beijing, China. TAPPI,<br />
P.O. Box 105113, Atlanta, GA 30368-5113; 800-332-8686; 770-446-1400; Fax: 404-446-6947 (U.S.) or<br />
800-446-9431 (Canada) or 770-446-1400 (Outside U.S. & Canada).<br />
Sept. 27-29. "PPE Systems: Putting it All Together. Personal Protective Equipment Seminar."<br />
Wilmington, DE, USA. Sponsored by 3M <strong>and</strong> DuPont. 800-659-0151, ext. 275.<br />
Sept. 30-Oct. 2, <strong>1999</strong>. Bobbin Americas. Georgia World Trade Congress Center, Atlanta, GA: Bobbin<br />
Group <strong>of</strong> Miller Freeman Inc., P. O. Box 279, Euless, TX 76039; 800/789-2223 or 817-255-8050.<br />
October <strong>1999</strong><br />
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Oct. 3-6. ASTM D-13 Committee Meeting. Fort Lauderdale, FL. Bode Buckley, ASTM, 100 Barr<br />
Harbor Drive, West Conshohocken, PA 19428-2959; 610-832-9740; Fax: 610-832-9555;<br />
bbuckley@astm.org<br />
Oct. 3-7. Interpas '99 Exhibition. National Exhibition Centre, Birmingham, Engl<strong>and</strong>. Reed Exhibition<br />
Companies; 203-840-6227; Fax: 203-840-9227.<br />
Oct. 5-8. Composites 2000: An International Symposium on Composite Materials. Trabant University<br />
Center, University <strong>of</strong> Delaware (Newark Campus), Newark, DE, USA. For more information contact:<br />
Center for Composite Materials, 201 Composites Manufacturing Science Laboratory, University <strong>of</strong><br />
Delaware, Newark, DE. 302-831-8149; Fax: 302-831-8525; info@ccm.udel.edu<br />
Oct. 6. Medal <strong>of</strong> Excellence in Composite Materials. Trabant University Center, University <strong>of</strong> Delaware<br />
(Newark Campus), Newark, DE. Center for Composite Materials, 201 Composites Manufacturing<br />
Science Laboratory, University <strong>of</strong> Delaware, Newark, DE. 302-831-8149; Fax: 302-831-8525;<br />
info@ccm.udel.edu<br />
Oct. 6-7. Short Course - Pile <strong>Fabrics</strong>. Madren Conference Center, Clemson University Campus,<br />
Clemson, SC, USA. Kay James, Clemson University, P. O. Box 912, Clemson, SC 29633-0912;<br />
864-656-2200; Fax: 864-656-3997; dregister@clemson.edu.<br />
Oct. 11-12. Filtration in Transportation - 2nd International Conference. Stuttgart, Germany. Filter<br />
Media Consulting, Inc., P.O. Box 2189, LaGrange, GA 30241; 706-882-3108; Fax: 706-882-3039 or<br />
Lutz Bergmann Consulting, Birkacher Str. 2, D-73760 Ostfildern, Germany; Fax: 011-49-711-456-7753.<br />
Oct. 11-13. PPE Systems: Putting it All Together. Personal Protective Equipment Seminar. Phoenix,<br />
AZ. Sponsored by 3M <strong>and</strong> DuPont. 800-659-0151, ext. 275.<br />
Oct. 12-15. American Association <strong>of</strong> Textile Chemists <strong>and</strong> Colorists, International Conference <strong>and</strong><br />
Exhibition. Charlotte Convention Center, Charlotte, NC. AATCC, Research Triangle Park, NC:<br />
919-549-8141; Fax: 919-49-8933; www.aatcc.org<br />
Oct. 12-14. 27th EUCEPA Conference/52nd Annual ATIP Meeting <strong>and</strong> IP-Exhibition. Grenoble,<br />
France. ATIP, +33- (0)- 1-45-62-11-91; Fax: +33- (0) -1-45-63-53-09.<br />
Oct. 14. INDA New Course for Converters. Wyndham Plaza, Philadelphia, PA. INDA, Association <strong>of</strong><br />
the Nonwoven <strong>Fabrics</strong> Industry, P.O. Box 1288, Cary, NC 27512-1288; Tel: 919-233-1210; Fax:<br />
919-233-1282: www.inda.org<br />
Oct. 14-16. Techtextil Asia. Osaka, Japan. Messe Frankfurt K.K., The 2nd Kiya Bldg. 3F, 4-3-2<br />
Iidabashi, Chiyoda-ku, Tokyo 102-0072 Japan; +81-3-5275-2851; Fax: +81-3-5275-2867.<br />
Oct. 19-21. Textile Supplies & Services Expo. Palmetto Expo Center, Greenville. Harry Buzzerd,<br />
Executive Vice President, ATMA, 703-538-1789; Fax: 703-241-5603 or Textile Supplies & Services<br />
Expo '99, P.O. Box 5823, Greenville, SC 29606-5823; 864-233-2562; Fax: 864-233-0619<br />
Oct. 19-21. EDANA Absorbent Hygiene Products Training Course. Brussels, Belgium. Philip Preest,<br />
EDANA, European Disposables & Nonwovens Association, 157 avenue Eugène Plasky, Bte 4, 1030<br />
Brussels, Belgium; Tel: 011+32+2/734-9310; Fax: +32-2/733-3518; . www.edana.org.<br />
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Oct. 20-21. AFS Topical Conference & Expo - Air Filtration Conference. Hyatt Regency, Minneapolis,<br />
MN. Charlotte Stripling, American Filtration & Separations Society, P. O. Box 1530, Northport, AL<br />
35476; 205-333-6111; Fax: 205-333-6446; afs@dbtech.net; www.afsociety.org.<br />
Oct. 20-22. The Fiber Society, <strong>1999</strong> Annual Conference. Madren Center, Clemson, University,<br />
Clemson, SC. Bhuvenesh Goswami, Clemson University, School <strong>of</strong> Textiles, Fiber <strong>and</strong> Polymer Science,<br />
161 Sirrine Hall, Clemson, SC 29634-1307; 864-656-5957; Fax: 864-656-5983; gbhuven-@clemson.edu<br />
Oct. 25-28. Polyester '99 (PET '99) 4th Annual World Congress - The Global Polyester Chain.<br />
Zurich, Switzerl<strong>and</strong>. Maack Business Services, CH-8804 Au/near Zurich, Switzerl<strong>and</strong>. Tel:<br />
+41-1-7813040; Fax: +41-1-7811569; www.MBSpolymer.com<br />
Oct. 26-29. Fundamentals <strong>of</strong> Textiles. Madren Conference Center, Clemson University Campus,<br />
Clemson, SC. Kay James, Clemson University, P. O. Box 912, Clemson, SC 29633-0912; 864-656-2200;<br />
Fax: 864-656-3997; pdregister@clemson.edu<br />
Oct. 27-29. Polyethylene Tereptha-late Technology (PET). Atlanta, GA. Beth Nielsen-Smith, The<br />
University <strong>of</strong> Toledo at SeaGate Centre, University College, Division <strong>of</strong> Continuing Education, 401<br />
Jefferson Ave., Toledo, OH 43604-1005. 419-321-5139; bnielse@utnet.utoledo.edu;<br />
http://www.utoledo.edu/colleges/ucollege<br />
Oct. 27-30. Composites '99 Convention <strong>and</strong> Expo. McCormick Place East, Chicago, IL. Composites<br />
Fabricators Association; 703-525-0511; Fax: 703-525-0743.<br />
Oct. 28-30. IFAI Expo - Industrial <strong>Fabrics</strong> Association International. San Diego Convention Center,<br />
San Diego, CA. Susan Larson, IFAI, 1801 County Road B W, Roseville, MN 55113-4062;<br />
800-225-4324; Fax: 651-631-9334; www.ifai.com<br />
Oct. 28-30. Industrial <strong>Fabrics</strong> Association International Expo. San Diego, CA. Bob Smith,<br />
800-225-4324; Fax: 612/631-9334; www.ifai.com<br />
Oct. 31-Nov 4. INSIGHT '99. Sheraton San Diego Hotel <strong>and</strong> Marina, San Diego, CA. Marketing<br />
Technology Service, 4100 South 7th Street, Kalamazoo, MI. 616-375-1236; Fax: 616-375-6710<br />
November <strong>1999</strong><br />
Nov. 2-4. FILTRATION '99 International Conference <strong>and</strong> Exposition. Navy Pier, Chicago, IL. INDA,<br />
P.O. Box 1288, Cary, NC 27512-1288; 919-233-1210; Fax: 919-233-1282; www.inda.org<br />
Nov. 9. INDA Needlepunch Production Basics. Greenville, SC. INDA, P.O. Box 1288, Cary, NC<br />
27512-1288; 919-233-1210; Fax: 919-233-1282; www.inda.org<br />
Nov. 9-10. ASTM Courses - Weathering <strong>and</strong> Durability. West Conshohocken, PA. ASTM, Technical &<br />
Pr<strong>of</strong>essional Training Department, 100 Barr Harbor Drive, West Conshohocken, PA 19428-2959;<br />
610-832-9686 or 610-832-9685; Fax: 610-832-9668; smurphy@astm.org;<br />
Nov. 9-11. TECHTEXTIL South America. Sao Paulo, Brazil. Messe Frankfurt, Ludwig-Erhard-Anlage<br />
1, D-60327 Frankfurt am Main; +49-69-7575-6415/6578/6406; Fax: +49-69-7575-6541;<br />
techtextil@messefrankfurt.com<br />
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Nov. 10-12. TANDEC '99 - 9th Annual Nonwovens Conference. The University <strong>of</strong> Tennessee<br />
Conference Center, Knoxville, TN. TANDEC-Textiles <strong>and</strong> Nonwovens Development Center, College <strong>of</strong><br />
Human Ecology, 1321 White Avenue, Knoxville, TN 37996-1950. 423-974-6298; Fax: 423-974-3580.<br />
Nov. 14-16. Private Label 20th Anniversary - Megashow. Rosemont Convention Center, Chicago, IL.<br />
Private Label Manufacturers Association, 369 Lexington Avenue, New York, NY 10017. 212-972-3131;<br />
Fax: 212-983-1382.<br />
Nov. 14-19. American Chemical Society - Eastern Analytical Symposium. Somerset, NJ. Eastern<br />
Analytical Symposium, P.O. Box 633, Montchanin, DE 19710; 302-738-6218; Fax: 302-738-5275;<br />
www.eas.org<br />
Nov. 16-18. Short Course - Advanced Fiber Science. Princeton, NJ. Nicole Pozsonyi, TRI/Princeton,<br />
601 Prospect Avenue, P.O. Box 625, Princeton, NJ 08540; 609-430-4806; Fax: 609-683-7149;<br />
www.triprinceton.org<br />
Nov. 18. INDA Needlepunch Production Basics. Worcester, MA. INDA, P.O. Box 1288, Cary, NC<br />
27512-1288; 919-233-1210; Fax: 919-233-1282; www.inda.org<br />
Nov. 23-25. EDANA Nonwovens Training Course. Brussels, Belgium. Philip Preest, EDANA, 157<br />
avenue Eugène Plasky, Bte 4, 1030 Brussels, Belgium; 011+32+2/734-9310; Fax: +32-2/733-3518;<br />
www.edana.org.<br />
Nov. 24-25. 26th Aachen Textile Conference. Aachen Textile Centre, Aachen, Germany. Brigitte<br />
Küppers; +49-241/44-69-129; Fax: +49-241/44-69-100; contact@dwi.rwth-aachen.de<br />
Nov. 30-Dec. 2. Nonwovens Russia Expo '99. St. Petersburg Sport & Concert Complex, St. Petersburg,<br />
Russia. Steven Douglas, Peter's Town Exhibitions, 10th Krasnoarmeiskaya 19, St. Petersburg, Russia,<br />
198103. Tel: +7 (812) 327-5553; +7 (812) 259-4535; www.peterstown.com<br />
January 2000<br />
Jan. 7-8. Cotton Textile Processing Conference - 2000 Beltwide Cotton Conferences. Marriott<br />
Rivercenter <strong>and</strong> San Antonio Convention Center, San Antonio, TX. Kearny Robert, Cotton Textile<br />
Processing Conference, SRRC, 1100 Robert E. Lee Boulevard, New Orleans, LA 70124; 504-286-4562;<br />
Fax: 504-286-4419; krobert@nola.srrc.usda.gov.<br />
February 2000<br />
Feb. 27-29. Annual Meeting INDA - Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry, Four Seasons<br />
Resort, Aviara, Carlsbad, CA. Peggy Blake, INDA, Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong> Industry, P.O.<br />
Box 1288, Cary, NC 27512-1288; 919-233-1210; Fax: 919-233-1282; www.inda.org<br />
March 2000<br />
Mar. 7-10. AFS - Annual Technical Conference & Expo. Myrtle Beach, SC. Charlotte Stripling, AFS,<br />
P.O. Box 1530, Northport, AL 35476-6530. 205-333-6111; Fax: 205-333-6446.<br />
Mar. 23-25. Techtextil North America. Cobb Galleria Centre, Atlanta, GA. Michael Jänecke, Messe<br />
Frankfurt GmbH, TechtextilTeam, Ludwig-Erhard-Anlage 1, D-60327 Frankfurt am Main;<br />
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+49-69-7575-6415/6578/6406; Fax:<br />
+49-69-7575-6541; techtextil@messefrankfurt.com<br />
or Daniel McKinnon, Messe Frankfurt, Inc., 1600<br />
Parkwood Circle, Suite 515, Atlanta, GA 30339;<br />
770-984-8016 ext. 21;<br />
daniel.mckinnon@usa.messefrankfurt.com<br />
April 2000<br />
Apr. 3-7. World Filtration Congress 8. The<br />
Brighton Centre, Brighton, Engl<strong>and</strong>. The<br />
Secretariat, World Filtration Congress 8, 48<br />
Springfield Road, Horsham RH 12 2PD West<br />
Sussex, Engl<strong>and</strong>. +44 (0) 1403-265005; Fax: +44<br />
(0) 1403-257594.<br />
filtech.exhibitions@btinterent.com;<br />
www.elsevier.nl/locate/wfc8<br />
May 2000<br />
May 17-19. ANEX 2000 Asia Nonwovens<br />
Exhibition <strong>and</strong> Conference. Intex Osaka, Osaka,<br />
Japan. E. J. Krause & Associates Inc., John<br />
Gallagher, 301-493-5500; Fax: 301-493-5705;<br />
gallagher@ejkrause.com<br />
May 24-26. CINTE Tech Textil. The China<br />
International Nonwovens, Techtextiles &<br />
Machinery Exhibition <strong>and</strong> Conference. China<br />
International Exhibition Centre, Beijing, China.<br />
Messe Frankfurt (HK) Ltd., 1808 China Resources<br />
Building, 26 Harbour Road, Wanchai, Hong Kong.<br />
Shirley Yan, 852-2238-9932; Janet Lai,<br />
852-2238-9930; Fax: 852-2511-3466;<br />
mfhkfair@netvigator.com; www.techtextil.de<br />
June 2000<br />
June 7-8. EDANA's 2000 International Nonwovens<br />
Symposium. Prague, the Czech Republic. EDANA,<br />
Philip Preest, Marketing Director; 157, avenue<br />
Eugene Plasky, Bte 4, 1040 Brussels, Belgium;<br />
011+32+2/734-9310; Fax: +32-2/733-3518; E-mail:<br />
edana@euronet.be<br />
July 2000<br />
July 25-26. AFS - Water & Waste Water<br />
INDA Exp<strong>and</strong>ing Publishing Efforts<br />
With the goal <strong>of</strong> greatly exp<strong>and</strong>ing its publishing<br />
efforts within the worldwide nonwovens industry,<br />
INDA, Association <strong>of</strong> the Nonwoven <strong>Fabrics</strong><br />
Industry, has partnered with Jacor Publications,<br />
Inc., Midl<strong>and</strong> Park, NJ, to develop <strong>and</strong> produce<br />
highly targeted print <strong>and</strong> electronic media<br />
projects.<br />
Jacor Publications is headed by Michael<br />
Jacobsen, former editor <strong>of</strong> Nonwovens Industry<br />
magazine <strong>and</strong> <strong>of</strong> the Executive Report <strong>of</strong> the<br />
Nonwovens Industry <strong>and</strong> currently production<br />
editor <strong>of</strong> the INDA International Nonwovens<br />
<strong>Journal</strong>. Jacobsen will serve as Director <strong>of</strong><br />
Publications Development for INDA, with the<br />
responsibility <strong>of</strong> researching <strong>and</strong> implementing<br />
focused publications for both INDA members<br />
<strong>and</strong> non-members.<br />
"INDA has recognized the need to increase its<br />
publications pr<strong>of</strong>ile to further its aim <strong>of</strong><br />
becoming the global resource for<br />
nonwovens-related information," said INDA<br />
president Ted Wirtz in announcing the<br />
partnership. "Our members have been asking us<br />
to continue to provide them with information on<br />
all aspects <strong>of</strong> their businesses, <strong>and</strong> exp<strong>and</strong>ing our<br />
effort through our relationship with Jacor is a<br />
major step in this direction."<br />
Wirtz pointed to specific targeted segments<br />
within the nonwovens industry, such as filtration,<br />
needlepunching <strong>and</strong> market research, as areas<br />
with much potential for INDA publications.<br />
"We are not looking to compete with any existing<br />
magazines or newsletters in the nonwovens<br />
industry, which already do a fine job providing<br />
our industry with information," Wirtz added. "We<br />
are looking simply to increase the amount <strong>of</strong><br />
information that is published for our members."<br />
Jacor Publications, a custom publishing <strong>and</strong><br />
internet services company, was founded in<br />
January, 1998 by Michael Jacobsen, who has<br />
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Conference. Anaheim, CA, USA. Charlotte<br />
Stripling, AFS, P.O. Box 1530, Northport, AL<br />
35476-6530. 205-333-6111; Fax: 205-333-6446.<br />
August 2000<br />
almost 20 years <strong>of</strong> experience in the publishing<br />
industry. In addition to serving as editor-in-chief<br />
<strong>of</strong> Nonwovens Industry from 1985 through 1991,<br />
Jacobsen spent seven years directing the editorial<br />
operations <strong>of</strong> the leading trade magazines in the<br />
sporting goods <strong>and</strong> golf industries.<br />
Aug. 20-24. 220th American Chemical Society<br />
National Meeting. Washington DC, USA. ACS<br />
Meetings, 1155 16th St. N.W. Washington, DC 20036; 202-872-4396; Fax: 202-872-6128;<br />
natlmtgs@acs.org<br />
September 2000<br />
Sept. 26-28. International Nonwovens Technical Conference 2000, Joint INDA <strong>and</strong> TAPPI<br />
Conference. Hotel Inter-Continental, Dallas, TX, USA. TAPPI, Charles Bohanan; 770-209-7276;<br />
cbohanan@tappi.org.<br />
Sept. 28-29. Ninth International Symposium on Flammability <strong>and</strong> Sensitivity <strong>of</strong> Materials in<br />
Oxygen-Enriched Atmospheres. Paris, France. Dorothy Savini, Symposia Operations, ASTM, 100 Barr<br />
Harbor Dr., West Conshohocken, PA 19428-2959; 610-832-9677.<br />
October 2000<br />
Oct. 15-28. American Association <strong>of</strong> Textile Chemists <strong>and</strong> Colorists, International Conference <strong>and</strong><br />
Exhibition, Benton Convention center, Winston-Salem, NC, USA. AATCC, Research Triangle Park,<br />
NC,.<br />
USA; 919-549-8141; Fax: 919/549-8933. www.aatcc.org<br />
Oct. 18-20. Techtextil Asia. INTEX Osaka, Japan. Michael Jänecke/Mrs. Silke Sakouchy, Messe<br />
Frankfurt GmbH, TechtextilTeam, Ludwig-Erhard-Anlage 1, D-60327 Frankfurt am Main; Tel:<br />
+49-69-7575-6415/6578/6406; Fax: +49-69-7575-6541; techtextil@messefrankfurt.com<br />
Oct. 23-27. ATME-1 2000 American Textile Machinery Exhibition-International 2000. Palmetto Expo<br />
Center, Greenville, SC, USA. J. Robert Ellis, ATME, P.O. Box 5823, Greenville, SC 29606.<br />
864-233-2562; Fax: 864-233-0619; E-mail: atmei@textilehall.com<br />
Oct. 29 - Nov. 3, 2000. American Chemical Society - Eastern Analytical Symposium. Atlantic City, NJ,<br />
USA. For more information contact: Eastern Analytical Symposium, P.O. Box 633, Montchanin, DE<br />
19710-0633; Tel: 302/738-6218; Fax: 302/738-5275; Internet: http://www.eas.org<br />
November 2000<br />
Nov. 26 - Dec. 1, 2000. 10th International Wool Textile Research Conference. Aachen, Germany. For<br />
more information contact: Deutsches Wollforschungsinstitut, Veltmanplatz 8, D-52062 Aachen,<br />
Germany; Tel: ++49 (0) 241/44-69-129; Fax: ++49 (0)241/44-69-100; E-mail:<br />
contract@dwi.rwth-aachen.de.<br />
April 2001<br />
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Nonwovens Calendar<br />
Apr. 1-5, 2001. 221th American Chemical Society National Meeting. Washington DC, USA. For more<br />
information contact: ACS Meetings, 1155 - 16th St. N.W. Washington, DC 20036-4899; Tel:<br />
202/872-4396; Fax: 202/872-6128; E-mail: natlmtgs@acs.org<br />
Apr. 23-27, 2001. ATME-1 2001 American Textile Machinery Exhibition. Palmetto Expo Center,<br />
Greenville, SC, USA. For more information contact: J. Robert Ellis, ATME, P.O. Box 5823, Greenville,<br />
SC 29606. Tel: 864/233-2562; Fax: 864/233-0619; E-mail: atmei@textilehall.com<br />
September 2001<br />
Sep. 21-23, <strong>1999</strong>. SINCE '99/ENA '99. Hong Kong, China. For more information contact: Ellen Dillard,<br />
Miller Freeman Inc., 2000 Powers Ferry Center, Suite 450, Marietta, GA 30067, USA. Tel:<br />
770/563-0129; Fax: 770/818-9092; E-mail: edillard@mfi.com<br />
October 2001<br />
Oct. 8-13, 2001. OTEMAS. 7th Osaka International Textile Machinery Show. Intex Osaka, Japan. For<br />
more information contact: Naad International, Tel: +81-6-945-0004; Fax: +81-6-945-0006.<br />
Oct. 21-24, 2001. American Association <strong>of</strong> Textile Chemists <strong>and</strong> Colorists, International Conference<br />
<strong>and</strong> Exhibition, Palmetto Expo Center, Greenville, SC, USA. For more information contact: AATCC,<br />
Research Triangle Park, NC, USA; Tel: 919/549-8141; Fax: 919/549-8933. Internet: www.aatcc.org<br />
September 2002<br />
Sep. 29-Oct 2, 2002. American Association <strong>of</strong> Textile Chemists <strong>and</strong> Colorists, International<br />
Conference <strong>and</strong> Exhibition, Charlotte Convention Center, Charlotte, NC, USA. For more information<br />
contact: AATCC, Research Triangle Park, NC, USA; Tel: 919/549-8141; Fax: 919/549-8933.<br />
Internet:www.aatcc.org<br />
October 2003<br />
Oct. 19-22, 2003. American Association <strong>of</strong> Textile Chemists <strong>and</strong> Colorists, International Conference<br />
<strong>and</strong> Exhibition, Palmetto Expo Center, Greenville, SC, USA. For more information contact: AATCC,<br />
Research Triangle Park, NC, USA; Tel: 919/549-8141; Fax: 919/549-8933. Internet: www.aatcc.org<br />
October 2004<br />
Oct. 24-27, 2004. American Association <strong>of</strong> Textile Chemists <strong>and</strong> Colorists, International Conference<br />
<strong>and</strong> Exhibition, Benton Convention Center, Winston-Salem, NC, USA. For more information contact:<br />
AATCC, Research Triangle Park, NC, USA; Tel: 919/549-8141; Fax: 919/549-8933. Internet:<br />
www.aatcc.org<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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INJ Air Filtration<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Air Filters For Ventilating Systems<br />
— Laboratory <strong>and</strong> In Situ Testing<br />
By Jan Gustavvson, Technical Director, Camfil ab 619 33 Trosa, Sweden<br />
Abstract<br />
Over the past few decades, many laboratory test methods have been developed to measure <strong>and</strong> characterize air<br />
filters using different synthetic dusts. Today, with concern about indoor air quality (IAQ) <strong>and</strong> air pollution on the<br />
rise, new st<strong>and</strong>ards are being developed to test the ability <strong>of</strong> air filters to remove particles in the laboratory as well<br />
as in situ. Still, laboratory tests that use coarse dusts can give very misleading results, <strong>and</strong> the rated efficiency for<br />
a filter can decrease dramatically in real-world applications. For better underst<strong>and</strong>ing <strong>and</strong> prevention <strong>of</strong> IAQ<br />
problems, test methods should be extended to include particle shape, type, <strong>and</strong> properties.<br />
History <strong>of</strong> air filter st<strong>and</strong>ards<br />
There are many test methods for measuring <strong>and</strong> characterizing air filters. In the past, different countries have<br />
tended to develop their own test methods using different measurement principles <strong>and</strong> synthetic test dusts. Today<br />
there is a tendency toward more international or worldwide st<strong>and</strong>ards. ASHRAE St<strong>and</strong>ard 52-68 was adopted for<br />
use in the United States in 1968 for testing fine <strong>and</strong> coarse filters. In 1976 it was replaced by ANSI/ASHRAE<br />
52-76, <strong>and</strong> in 1992 it was replaced by ANSI/ASHRAE 52.1-92 [1] As the name implies, this latest st<strong>and</strong>ard was<br />
approved by the American National St<strong>and</strong>ards Institute (ANSI) as an American national st<strong>and</strong>ard.<br />
Manufacturers <strong>and</strong> authorities in most countries have accepted the old ASHRAE 52-76 test method, which was<br />
also adopted as the Eurovent 4/5 st<strong>and</strong>ard, with minor modifications. Eurovent is the European association for<br />
manufacturers <strong>of</strong> air-h<strong>and</strong>ling equipment. This, in turn, served as a basis for some European national st<strong>and</strong>ards<br />
<strong>and</strong> the new European CEN norm EN 779, which came into force in 1993 [2]. CEN is the European committee<br />
for st<strong>and</strong>ardization.<br />
As a result <strong>of</strong> modern technology <strong>and</strong> modified requirements, Eurovent submitted a recommendation in 1992, for<br />
a new st<strong>and</strong>ard that measures the fractional efficiency <strong>of</strong> filters used in general ventilation, Eurovent 4/9 [3]. The<br />
old Eurovent 4/5 has been replaced by the new Eurovent 4/9 st<strong>and</strong>ard. CEN has also decided to develop a new<br />
test method based on a filter's fractional efficiency. This new st<strong>and</strong>ard will be based in principle on Eurovent 4/9<br />
<strong>and</strong> include a procedure for discharging filters. In the United States, ASHRAE has been thinking along the same<br />
lines as Eurovent <strong>and</strong> has proposed a new st<strong>and</strong>ard - ASHRAE STANDARD 52.2, [4] which was adopted in June<br />
<strong>1999</strong>. The old ASHRAE 52.1 st<strong>and</strong>ard [1] will continue to be used as a test method for low efficiency filters.<br />
Figure 1 graphs the history <strong>of</strong> U.S. <strong>and</strong> European st<strong>and</strong>ards for ventilating filters since 1950.<br />
The growing dem<strong>and</strong> for better control particles <strong>and</strong> filter performance has led to the development <strong>of</strong> an in situ<br />
method <strong>of</strong> measuring the fractional efficiency <strong>of</strong> general ventilation filters, Eurovent 4/10-1996 [5]. Nevertheless,<br />
the need for new <strong>and</strong> improved measurement methods continues to increase with the heightened awareness <strong>of</strong><br />
problems with indoor air quality. Simple particle counts <strong>and</strong> measures <strong>of</strong> filter efficiencies will not be adequate<br />
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INJ Air Filtration<br />
for future needs. Test measurements will need to be<br />
extended to include analysis <strong>of</strong> the particles themselves,<br />
including shape, type, <strong>and</strong> risk factors.<br />
Laboratory Test Dust<br />
In both the old <strong>and</strong> new test methods, filters are loaded with<br />
ASHRAE synthetic dust. Unfortunately, the synthetic dust<br />
gives no indication <strong>of</strong> the filter's actual useful life. Tested<br />
filters can have completely different characteristics when<br />
performing under actual operating conditions.<br />
One advantage <strong>of</strong> the new test methods that measure a<br />
filter's fractional efficiency is that they can use the same<br />
instruments <strong>and</strong> techniques to study filter performance<br />
when loaded with other types <strong>of</strong> dust. Perhaps more<br />
importantly, these tests can be run in the laboratory or<br />
under actual operating conditions.<br />
It is fair to ask whether laboratory tests using synthetic dust<br />
are representative <strong>of</strong> operation under real-world conditions.<br />
For example, filters installed in urban environments are<br />
exposed to exhaust fumes <strong>and</strong> gases from combustion<br />
products, while filters in a rural environment are exposed<br />
more to dust from nature.<br />
Figure 1<br />
U.S AND EUROPEAN STANDARDS FOR<br />
VENTILATING FABRICS SINCE 1950<br />
Consider the results for two different types <strong>of</strong> EU7 (85%<br />
dust spot efficiency filters) tested with different test dusts.<br />
One filter is a conventional glass-fiber filter in which the<br />
collecting mechanism is based on diffusion <strong>and</strong><br />
interception <strong>of</strong> fine fibers. The other filter consists <strong>of</strong> coarse synthetic fibers that are electrostatically charged.<br />
One <strong>of</strong> the test dusts is "Arizona road dust" (AC fine test dust), representing "natural" dust in a rural environment.<br />
The other test dust consists <strong>of</strong> diesel exhaust fumes, representing an urban environment.<br />
AC Fine test dust.<br />
Figure 2 shows the results for a test with road dust. The efficiency <strong>of</strong> dust captured on the glass-fiber filter<br />
increased as the dust load increased. In contrast, the efficiency <strong>of</strong> the electrostatically charged material was<br />
somewhat higher in the beginning but decreased as the captured dust neutralized the charged fibers. Figure 3 is a<br />
high-magnification photo <strong>of</strong> AC fine test dust.<br />
For dust containing fibers or coarse particles, such as the widely used ASHRAE test dust, the efficiency <strong>of</strong>ten<br />
increases as the dust load increases, since a dust cake forms on the filter. Once it is formed, the dust cake does the<br />
actual filtering.<br />
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Figure 3<br />
Figure 2<br />
THE EFFECT OF TEST DUST AC FINE ON TWO<br />
FILTER MATERIALS: ONE WITH<br />
ELECTROSTATICALLY CHARGED MEDIA AND ONE<br />
WITH CONVENTIONAL GLASS-FIBER MEDIA<br />
10 000 MAGNIFICATION OF AC FINE TEST<br />
DUST<br />
Figure 4<br />
THE EFFECT OF DIESEL FUMES ON AN EU7<br />
GLASS FILTER MEDIA<br />
Figure 5<br />
THE EFFECT OF DIESEL FUMES ON<br />
ELECTROSTATICALLY CHARGED EU7 FILTER<br />
MATERIAL<br />
Diesel fumes<br />
In tests with diesel exhaust fumes, the results were markedly different. The efficiency <strong>of</strong> the glass-fiber EU7 filter<br />
remained constant when the filter was loaded with diesel exhaust fumes, as seen in Figure 4. In contrast, the<br />
efficiency <strong>of</strong> the electrostatically charged synthetic-fiber filter fell dramatically from 70% to 10% after being<br />
exposed to only a moderate load <strong>of</strong> diesel fumes as seen in Figure 5. The difference is due to the different<br />
filtering mechanisms for the two filters. The diffusion-<strong>and</strong>-interception collection mechanism for the glass-fiber<br />
filter remains active even when the filter is loaded with contaminants. In contrast, the electrostatic charge on the<br />
synthetic fibers <strong>of</strong> the EU7 filter disappears, <strong>and</strong> the filter takes on the same properties as a coarse filter. Figure 6<br />
is a high magnification photo <strong>of</strong> diesel fumes.<br />
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Figure 6<br />
10 000 MAGNIFICATION OF EXHAUST FUMES IN<br />
A GRARAGE<br />
Figure 7<br />
MAGNIFICATION OF ASHRAE TEST DUST. THE<br />
PARTICLES ARE CLOGGED TOGETHER AND<br />
ARE MUCH BIGGER IN SIZE, COMPARED WITH<br />
ATMOSPHERIC DUST<br />
Lähtimäki [6,7] showed that cigarette smoke <strong>and</strong> diesel fumes can quickly neutralize the electret fibers in a filter.<br />
He also showed that, in certain environments with fibers or coarse dust, neutralization <strong>of</strong> charged fibers can be<br />
counteracted if the filter clogs. This can happen when such filters are tested with ASHRAE test dust, which<br />
contains coarse fibers <strong>and</strong> particles. The presence <strong>of</strong> these coarse fibers in the filter enhances its dust-holding<br />
capacity. So a filter with coarse, electrostatically charged fibers will obtain a relatively flat <strong>and</strong> good efficiency<br />
curve when tested with the ASHRAE test dust. Although the filter may score "high marks" in lab tests, these<br />
results may not apply under actual operating conditions with real-world dust particles.<br />
Table 1<br />
EUROVENT 4/9 TEST OF TWO FILTERS<br />
Glass Synthetic<br />
Filter area(m 2 ) 9.2 7.6<br />
Initial pressure drop (Pa) 81 86<br />
Initial Efficiency, 0.4µm (%) 65.1 59.7<br />
Average Efficiency(%) 86.3 88.7<br />
Dust holding capacity(g) 605 666<br />
ASHRAE test dust<br />
Most <strong>of</strong> the st<strong>and</strong>ards for air filters specify the use <strong>of</strong> ASHRAE 52.1 test dust, which is a mixture <strong>of</strong> fine dust,<br />
cotton liners, <strong>and</strong> carbon black. Figure 7 is a high magnification photo <strong>of</strong> ASHRAE test dust. This test dust has<br />
been in use 30 years, <strong>and</strong> many filters have been developed to meet the test st<strong>and</strong>ards rather than performance in<br />
real life.<br />
With the variety <strong>of</strong> commercially available materials in use today, it is relatively simple to make filters from<br />
different materials <strong>and</strong> obtain the same laboratory test results. Table 1 summarizes the results for a glass fiber<br />
filter <strong>and</strong> a synthetic fiber filter that were both tested according to Eurovent 4/9.<br />
To obtain approximately the same performances, the glass fiber filter was made with 9.3 m 2 filtering area, while<br />
the synthetic filter was made with a filtering area <strong>of</strong> only 7.6 m 2 . The pressure drops, the efficiencies, <strong>and</strong> the<br />
dust-holding capacities are very close to each other. Both filters are classified as EU 7 filters. Despite having 20%<br />
less filter area, the synthetic filter has about 10% more dust-loading capacity. It seems to be a very good filter.<br />
The efficiency for both filters-as measured by the Eurovent 4/9 test-are almost identical, as seen in Figure 8.<br />
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INJ Air Filtration<br />
The same filters were then installed in two parallel installations for about one year. Filtration efficiency in<br />
outdoor air was checked regularly during this period. As seen in Figure 9 the efficiency for the glass fiber filter<br />
remained constant <strong>and</strong> increased slightly, while the efficiency for the filter with synthetic fibers decrease from<br />
about 65% to 25% during the same period.<br />
The explanation for this is that the synthetic filter is<br />
made <strong>of</strong> electrostatically charged, rather coarse<br />
fibers. The coarse fibers give a higher dust-loading<br />
capacity, <strong>and</strong> the coarse ASHRAE test dust forms a<br />
dust cake that improves the filter's efficiency during<br />
laboratory tests. In the real world, atmospheric dust<br />
neutralizes the electrostatic charge, <strong>and</strong> the efficiency<br />
decreases. Moreover, the small dust particles<br />
encountered in the world outside the laboratory do<br />
not form a filtration-enhancing dust cake.<br />
Actual Operating Conditions<br />
The prime task <strong>of</strong> an air filter is to remove impurities<br />
from the ambient air. It is therefore important to<br />
study how filtration efficiency changes under<br />
real-world operating conditions. When a filter<br />
collects dust, the pressure drop normally rises, <strong>and</strong><br />
the dust functions as a filter material <strong>and</strong> improves<br />
the collecting efficiency. As a rule, the efficiency <strong>of</strong> a<br />
conventional filter that removes particles through<br />
diffusion <strong>and</strong> interception is greatest when it is time<br />
to replace the filter. However, in coarse filters, or<br />
filters in the lower range, particles accumulating in<br />
the filter can loosen <strong>and</strong> travel with the air flow<br />
through the filter when the pressure drop increases.<br />
Synthetic filters operating with electrostatically<br />
charged fibers perform differently:<br />
Figure 8<br />
EFFICIENCY VS. DUST FED ACCORDING TO<br />
EUROVENT 4/9 FOR TWO DIFFERENT EU7 FILTERS<br />
Figure 9<br />
LIFE TIME TEST OF TWO EU7 FILTERS<br />
• Fine fibers: When fine fibers receive an extra electrostatic charge, the fibers lose this charge fairly swiftly.<br />
Efficiency declines immediately in the beginning but then remains constant for a long period <strong>of</strong> time during the<br />
filter's operation, increasing towards the end when the pressure drop rises <strong>and</strong> the filter accumulates dust.<br />
• Coarse fibers: The collecting efficiency <strong>of</strong> coarse, electrostatically charged, synthetic filters <strong>of</strong>ten decreases<br />
sharply, on a continuous basis, during the greater part <strong>of</strong> the filter's operating life. The collecting efficiency <strong>of</strong>ten<br />
remains low during the entire useful life <strong>of</strong> the filter.<br />
The result varies with the type <strong>of</strong> dust <strong>and</strong> different operating conditions. The advantage <strong>of</strong> the new Eurovent<br />
4/10 method is that we now have an instrument to measure what happens during operation under real-world<br />
operating conditions.<br />
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INJ Air Filtration<br />
Figure 10<br />
LONG-TERM TEST OF AN EU7 GLASS-FIBER<br />
FILTER AND<br />
AN EU8 SYNTHETIC FILTER. (The test was<br />
conducted in a rural environment where the<br />
concentration <strong>of</strong> atmospheric impurities was low.<br />
The cycle goes much faster in an urban<br />
environment.)<br />
Figure 11<br />
LIFETIME TEST MADE AT SINTEF, NORWAY,<br />
COMPARING DIFFERENT FILTER<br />
QUALITIES.(1995).<br />
(The drop <strong>of</strong> efficiency goes very fast for<br />
electrostatically charged filter material)<br />
Air ventilating system<br />
Figure 10 shows how filter efficiency changes in relation to the operating time <strong>of</strong> a ventilation system. When<br />
new, the synthetic-fiber EU 8 filter has a relatively high efficiency, about 70% for 0.4 µm particles. As the filter<br />
loses its electrical charge, its ability to remove particles deteriorates sharply as its efficiency decreases to about<br />
20%, which is normal for this material when it is not electrostatically charged. In contrast, the efficiency <strong>of</strong> the<br />
glass-fiber EU7 filter remains relatively constant. Note that the test was conducted in a rural environment, where<br />
the concentration <strong>of</strong> atmospheric impurities was low. The cycle goes much faster in an urban environment.<br />
Lifetime tests<br />
Sintef (Trondheim, Norway) made a lifetime test <strong>of</strong> five different EU 7 filters [8]. Three glass-fiber filters <strong>and</strong><br />
two synthetic filters from different filter manufactures were compared. Two filters <strong>of</strong> each type were purchased<br />
on the open market. These 10 filters were tested in parallel for more than one year.<br />
The results in Figure 11 show that the glass fiber filters had a small increase in efficiency during the test. One<br />
synthetic filter with electrostatically charged filter material suffered a steep decline in efficiency for 0.4µm<br />
particles — from 80% to 20%--within a couple <strong>of</strong> weeks. The other synthetic filter had a very low efficiency<br />
during the entire test period even though the pressure drop increased almost up to 400 Pa. The increase in<br />
pressure drop for the other filters was low, about 20 %.<br />
Neutralization<br />
In most applications, electrostatically charged filters will be neutralized <strong>and</strong> lose efficiency. An effective way to<br />
verify the loss <strong>of</strong> efficiency with the loss <strong>of</strong> the electrostatic effect is to compare charged <strong>and</strong> uncharged material.<br />
This can be done using ions, X-rays or dust loading, but the easiest way is to dip the material in isopropanol <strong>and</strong><br />
then dry <strong>and</strong> retest it. This will give a good indication <strong>of</strong> what happens in an installation with atmospheric dust.<br />
Figure 12 shows the results for charged EU7 filters before <strong>and</strong> after neutralization with isopropanol. Clearly, the<br />
effects <strong>of</strong> neutralization can vary considerably. The worst-performing filter shows a drop from 77 to 8% <strong>of</strong> 0.4µm<br />
particles, while the drop for the best-performing filter is from 88 to 48%. These figures have been confirmed by<br />
comparing the filters' actual behavior in real conditions. Performance depends on the fiber size, the composition<br />
<strong>of</strong> the material, <strong>and</strong> the type <strong>of</strong> dust. The rate <strong>of</strong> decrease depends on the type <strong>and</strong> concentration <strong>of</strong> dust.<br />
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The Nord test method UUS117 [9] will test electret<br />
filter material using isopropanol or diesel fume.<br />
The purpose will be to (a) determine whether the<br />
filter material is dependent on the electrostatic<br />
removal mechanism <strong>and</strong> (b) provide quantitative<br />
information about the importance <strong>of</strong> the<br />
electrostatic removal mechanism.<br />
Figure 12<br />
EXAMPLE OF THE EFFECT WHEN<br />
CHARGED EU7 FILTER MATERIALS<br />
ARE NEUTRALIZED WITH ISOPROPANOL<br />
Future<br />
Interest in air quality is exp<strong>and</strong>ing from the general<br />
environment to include indoor air quality, spurred<br />
in part by awareness <strong>of</strong> "sick building syndrome."<br />
This highlights the need for new <strong>and</strong> improved<br />
methods for testing air filters. Particle counts <strong>and</strong><br />
filter efficiencies will remain essential variables,<br />
but analysis should also be extended to consider<br />
the nature <strong>of</strong> the particles themselves, including<br />
shape, type, <strong>and</strong> risk factors.<br />
References<br />
1. ANSI/ASHRAE St<strong>and</strong>ard 52.1-1992.<br />
"Gravimetric <strong>and</strong> Dust Spot Procedures for Testing<br />
Air Cleaning Devices Used in General Ventilation<br />
for Removing Particulate Matter," American<br />
National St<strong>and</strong>ards Institute, New York, 1992.<br />
2. CEN EN 779, "Specifications for Particulate Air<br />
Filters for General Ventilation," European<br />
Committee for St<strong>and</strong>ardization (CEN), Brussels,<br />
Belgium, 1993.<br />
3. Eurovent 4/9-1992, "Method <strong>of</strong> Testing Air Filters Used in General Ventilation for Determination <strong>of</strong> Fractional<br />
Efficiency." Eurovent, Paris, revised 1996.<br />
4. ASHRAE St<strong>and</strong>ard 52.2 "Method <strong>of</strong> Testing General Ventilation Air-Cleaning devices for Removal Efficiency<br />
by Particle Size." American Society <strong>of</strong> Heating, Refrigerating <strong>and</strong> Air-conditioning Engineers, Atlanta, June,<br />
<strong>1999</strong><br />
5. Eurovent 4/10-1996. "Recommendation for in situ Determination <strong>of</strong> Fractional Efficiency <strong>of</strong> General<br />
Ventilation Filters," Eurovent, Paris, 1996.<br />
6. Lähtimäki, M. "Reliability <strong>of</strong> Electret Filters," Indoor Air 93 Conference Proceedings, Helsinki University <strong>of</strong><br />
Technology, Finl<strong>and</strong>, 1993, Vol. 6, p. 463.<br />
7. Lähtimäki, M. "Development <strong>of</strong> Test Methods for Electret Filters." Report 320, Nordtest, Espoo, Finl<strong>and</strong>,<br />
1996.<br />
8. STF 11 A95052, "Long-term Tests <strong>of</strong> Filters in Real Environment," SINTEF, Trondheim, Norway, 1995.<br />
9. Nordtest Method Nt VVS 117, "Electret Filters: Determination <strong>of</strong> the Electrostatic enhancement Factor <strong>of</strong><br />
Filter Media," Nordtest, Espoo, Finl<strong>and</strong>, 1998. — INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
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Eval <strong>of</strong> Filtration Performance<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Evaluation <strong>of</strong> the Filtration<br />
Performance <strong>of</strong> Biocide Loaded Filter Media<br />
By Wayne T. Davis, B. Alan Phillips, Department <strong>of</strong> Civil <strong>and</strong> Environmental Engineering, The University <strong>of</strong> Tennessee,<br />
Knoxville, TN 37996; Maureen Dever, Center for Materials Processing, The University <strong>of</strong> Tennessee; Thomas C. Montie <strong>and</strong><br />
Kimberly Kelly-Wintenberg, Department <strong>of</strong> Microbiology, The University <strong>of</strong> Tennessee; <strong>and</strong> Sarah Macnaughton, Microbial<br />
Insights, Inc., Rockford, TN<br />
Abstract<br />
This paper presents the results <strong>of</strong> a study designed to evaluate the filtration performance <strong>of</strong> nonwoven filtration media which<br />
have been loaded with a variety <strong>of</strong> biocides for use as potential indoor air filters. A test st<strong>and</strong> was constructed based on a<br />
modification <strong>of</strong> the ASTM 1215 St<strong>and</strong>ard to provide testing <strong>of</strong> the bacterial removal efficiency <strong>of</strong> the filtration media.<br />
Biocide-loaded filtration media were first tested on an ASTM 1215 test st<strong>and</strong> using st<strong>and</strong>ard monodispersed latex spheres to<br />
determine the particle removal efficiency as a function <strong>of</strong> particle sizes in the 0.5 to 2.0 micrometer sizes. A multichannel<br />
optical particle counter was used to assess the efficiency. Additional samples <strong>of</strong> the same media were then tested in the<br />
modified ASTM 1215 test st<strong>and</strong>, referred to as the Biocontaminant Indoor Air Quality Test St<strong>and</strong> (BIAQTS) by atomizing<br />
bacteria (Gram positive <strong>and</strong> Gram negative) <strong>and</strong> fungi into the test st<strong>and</strong>. Initial bacterial testing was conducted using<br />
single-stage microbial samplers to determine the efficiency <strong>of</strong> filters for removing Escherichia coli (E. coli) bacteria <strong>and</strong> other<br />
bacteria. In addition to testing the filtration efficiency, additional tests were conducted on samples <strong>of</strong> the filter by placing small<br />
disk samples <strong>of</strong> the unexposed biocide-loaded filters <strong>and</strong> a non-loaded control filter onto microorganism-loaded agar in petri<br />
dishes. Microorganisms studied included four bacteria, a fungus, <strong>and</strong> an opportunistic pathogen. The samples were then<br />
incubated <strong>and</strong> quantitative analyses were conducted to determine the zone <strong>of</strong> inhibited growth <strong>of</strong> the microorganisms around the<br />
disks due to the biocide treatments which were applied to the filters.<br />
The results are presented for two <strong>of</strong> a series <strong>of</strong> biocide-loaded nonwoven filters which were prepared using two different<br />
techniques for loading the biocides: 1) nonwoven filters which were prepared by mixing the biocide with the polypropylene<br />
polymer prior to meltblowing the polymer into a filter - referred to as impregnated biocide, <strong>and</strong> 2) spray application <strong>of</strong> the<br />
biocides as a finish onto the filter media--referred to as post treatment. The effects <strong>of</strong> impregnated versus post treatment<br />
applications on filtration efficiency <strong>and</strong> on the inhibition <strong>of</strong> bacterial growth on the filters are presented.<br />
Introduction<br />
A number <strong>of</strong> studies have been conducted in which concentrations <strong>of</strong> bacteria have been measured in both ambient (outside) air<br />
<strong>and</strong> in the indoor environment. Meyer (1983) provided a summary <strong>of</strong> research efforts involved in measuring the concentration<br />
<strong>of</strong> bacteria. In 1899 measurements in Paris showed concentrations <strong>of</strong> 200 microbes/m 3 in the winter <strong>and</strong> nearly 12,000/m 3 in the<br />
summer. Lighthart <strong>and</strong> Shaffer reported in 1995 that concentrations <strong>of</strong> airborne bacteria had a maximum concentration <strong>of</strong> 1,368<br />
colony forming units (CFU) per m 3 with a 24 hour mean <strong>of</strong> 121 CFU/m 3 when measured above a grass seed field in Oregon.<br />
Walsh et al. (1984) reported that a concentration <strong>of</strong> 4000 CFU/m 3 was found in an outdoor environment. Walsh further reported<br />
that concentrations were found to be 7.6 to 14.25 times greater in the indoor environment than in the outdoor environment.<br />
Reports <strong>of</strong> bacteria concentrations as high as 10 5 to 10 6 have been observed in factories involved with the processing <strong>of</strong> cotton,<br />
<strong>and</strong> in factories processing vegetables <strong>and</strong> mushrooms. Based on the above broad ranges, it is reasonable to expect that values<br />
<strong>of</strong> at least 300-500 CFU/m 3 should be present at the very minimum in a typical indoor environment, with concentrations<br />
reaching much higher values at times.<br />
Heating, ventilation <strong>and</strong> air conditioning (HVAC) filters can be used to reduce the concentration <strong>of</strong> particles in the indoor air<br />
environment. These are particularly effective when there is a relatively large recirculation rate within the indoor volume such<br />
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that the air makes multiple passes through the filters (Wadden <strong>and</strong> Sheff, 1983). In a series <strong>of</strong> tests on 10 different commercially<br />
available indoor air filters, Davis et al. (1994) showed that filter efficiencies ranged from 2 to 30% on 0.6 mm particles up to 35<br />
to 90% on 4 mm particles, dependent on the filter <strong>and</strong> the air velocity through the filters. While the filters can effectively<br />
remove a significant portion <strong>of</strong> the particles in the air, including bacteria <strong>and</strong> other organisms, the filters can also provide sites<br />
for growth <strong>of</strong> microorganisms, particularly in humid air streams.<br />
The objectives <strong>of</strong> this study were to evaluate the effectiveness <strong>of</strong> biocide-loaded filters in 1) removing bacteria from the air<br />
stream, 2) preventing the growth <strong>of</strong> bacteria which were collected on the surfaces <strong>of</strong> the filter, <strong>and</strong> 3) to determine if the filters<br />
actually affected the potential growth <strong>of</strong> bacteria which passed through the media uncollected. To accomplish these objectives,<br />
filters were manufactured which 1) contained selected biocides within the polypropylene mix which was used to manufacture<br />
the fibers, referred to as impregnated biocide, <strong>and</strong> 2) in which the biocide was applied as a topical coating onto the fibers <strong>of</strong> the<br />
filter.<br />
Description <strong>of</strong> Test St<strong>and</strong>s<br />
The filters developed in this study were tested on two different filtration efficiency test st<strong>and</strong>s. The first test st<strong>and</strong> was an<br />
ASTM 1215 test st<strong>and</strong> housed in the Indoor Air Quality Laboratory housed in the Department <strong>of</strong> Civil <strong>and</strong> Environmental<br />
Engineering at the University <strong>of</strong> Tennessee <strong>and</strong> constructed by the authors. The test st<strong>and</strong> allows for the evaluation <strong>of</strong> the<br />
filtration efficiency <strong>of</strong> flat filter media at velocities <strong>of</strong> 1 to 300 cm/s for monodispersed polystyrene latex (PSL) spheres with<br />
particle sizes <strong>of</strong> 0.5 to 3 µm. The ASTM 1215 Method <strong>and</strong> test st<strong>and</strong> are described in detail by ASTM 1215 (1989), <strong>and</strong> Davis<br />
(1994). The test st<strong>and</strong> was similar to that shown in Figure 1, except that it was only used for testing <strong>of</strong> PSL spheres <strong>and</strong> di-octyl<br />
phthalate (DOP).<br />
Figure 1<br />
BIOCONTAMINANT INDOOR AIR QUALITY (BIAQ) TEST CHAMBER<br />
The second test st<strong>and</strong>, referred to as a<br />
Biocontaminant Indoor Air Quality Test St<strong>and</strong><br />
(BIAQTS) was designed <strong>and</strong> constructed by the<br />
authors <strong>and</strong> installed at Microbial Insights, Inc.<br />
The test st<strong>and</strong>, shown schematically in Figure 1,<br />
provides the ability to expose a filter to a<br />
constant air flowrate (<strong>and</strong> filtration velocity)<br />
which contains a constant concentration <strong>of</strong> a<br />
biocontaminant (bacteria or fungal spores), <strong>and</strong><br />
to test the efficiency <strong>of</strong> the filter for removal <strong>of</strong><br />
the biocontaminant by isokinetically sampling<br />
upstream <strong>and</strong> downstream <strong>of</strong> the media. Air is<br />
pulled into the test st<strong>and</strong> from the laboratory<br />
through two 99.9% HEPA filters in series to<br />
provide an air stream with a near zero particle<br />
concentration. A TSI Model 3076 Constant<br />
Output atomizer is used to atomize water<br />
droplets containing a relatively constant<br />
concentration <strong>of</strong> bacteria, fungal spores, or PSL<br />
latex spheres. The droplets are then dried in the<br />
upper portion <strong>of</strong> the vertical test st<strong>and</strong> as they<br />
mix with the larger volume <strong>of</strong> drier air from the HEPA filters. The air flow containing the concentration <strong>of</strong> biocontaminant then<br />
passes down through the test st<strong>and</strong>, through the filter, <strong>and</strong> out through a final HEPA filter <strong>and</strong> regenerative pump <strong>and</strong> is vented<br />
into a laboratory exhaust hood. The vertical filter holder is enclosed in a cabinet which is equipped with a glove box entry as an<br />
additional precaution.<br />
The test st<strong>and</strong> is equipped with three different techniques for quantifying the upstream <strong>and</strong> downstream concentrations <strong>of</strong><br />
particulate contaminants. Two sets <strong>of</strong> upstream/downstream sampling probes are positioned in the test st<strong>and</strong> to allow isokinetic<br />
sampling <strong>of</strong> the air flow. One set <strong>of</strong> probes can be used to isokinetically sample into an optical particle counter for sampling <strong>of</strong><br />
PSL latex spheres or DOP in cases where no bacteria are present. It was not possible to sample bacterial concentrations with the<br />
OPC for several reasons. First, the OPC cannot distinguish between viable <strong>and</strong> non-viable bacteria. Second, a 0.1 molar<br />
phosphate buffer solution was required to achieve a sustained bacterial survival over the course <strong>of</strong> the inoculation period for the<br />
bacteria. The buffer solution containing the bacteria was then atomized to create a relatively stable, viable concentration <strong>of</strong><br />
bacteria in the air stream. Unfortunately, the presence <strong>of</strong> the buffer produced very high concentration <strong>of</strong> particles which were<br />
not bacteria to which the OPC responded. The concentration <strong>of</strong> bacteria was in the range <strong>of</strong> 100 CFU per cubic foot <strong>of</strong> air flow,<br />
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whereas buffer itself created several orders <strong>of</strong> magnitude higher concentrations <strong>of</strong> particles <strong>of</strong> a non-bacterial origin.<br />
The second set <strong>of</strong> probes was used to simultaneously sample isokinetically into two Andersen single stage microbial samplers<br />
or into two all-glass liquid impingers (AGLIs) in order to evaluate the bacterial removal efficiency <strong>of</strong> the filters. Isokinetic<br />
sampling at a constant flow rate is important for accurate <strong>and</strong> quantitative data collection from the BIAQTS airstream. The<br />
sampling probes used to extract samples from the BIAQTS into the Andersen <strong>and</strong> AGLI samplers were sized to provide one<br />
cubic foot per minute (1 CFM) isokinetic samples from the test st<strong>and</strong> when the st<strong>and</strong> was operated at 15 CFM. The BIAQTS<br />
was calibrated using the upstream Anderson microbial air sampler to capture <strong>and</strong> quantify viable bacteria introduced into the<br />
system. Using live biomass (Escherichia coli; ATCC strain #8739) aerosolized <strong>and</strong> introduced into the BIAQTS at a flow rate<br />
<strong>of</strong> 15 CFM, samples were collected using the microbial samplers for various time periods ranging from 6 seconds to 10 minutes<br />
to ensure that the viable counts collected in the microbial samplers increased linearly with increasing sampling time.<br />
Bacteria are extracted from the test st<strong>and</strong> into the sampling probe, pass<br />
into the microbial sampler through a plate with a uniform array <strong>of</strong> holes<br />
<strong>and</strong> then impact into a petri dish as the air flow direction changes.<br />
Bacteria passing through each hole in the plate impact directly into the<br />
petri dish. Viable colony forming unit (CFU) counts were linearly<br />
correlated with increased sampling time (r 2 = 0.99; Figure 2), indicating<br />
that the BIAQTS was running at a constant rate <strong>and</strong> that the response <strong>of</strong><br />
the sampler was linear within the sampling times that were to be used.<br />
Certain overall project objectives required the need to collect<br />
substantially greater numbers <strong>of</strong> bacteria than could reliably be measured<br />
with the Anderson microbial samplers due to the finite number <strong>of</strong> holes<br />
in the impactor plate. For example, it was necessary to sample using the<br />
AGLI samplers to acquire sufficient numbers <strong>of</strong> bacteria to be used to<br />
conduct signature lipid biomarker (SLB) analyses on the bacteria. The<br />
Figure 2<br />
CORRELATION BETWEEN TIME (MIN)<br />
AND COLONY FORMING UNITS (CFU)<br />
biomass density per unit volume required for the lipid biomarker analysis at 10 6 total organisms was significantly higher than<br />
the upper limit which could be measured with the Andersen air sampler at 10 3 total organisms. The AGLI samplers were<br />
actually calibrated for this purpose by placing the Andersen samplers upstream <strong>and</strong> downstream <strong>of</strong> the AGLI <strong>and</strong> evaluating its<br />
collection efficiency at the 1 CFM flowrate. The efficiency <strong>of</strong> the AGLI sampler was determined to be 79 ± 7%. The AGLI<br />
samplers are used to quantify bacterial numbers when there is a need to sample high concentrations (>10 4 ) <strong>of</strong> bacteria such as<br />
for lipid biomarker analysis.<br />
Description <strong>of</strong> Indoor Air Filters<br />
Nonwoven polypropylene filters containing known biocides were generated at the University <strong>of</strong> Tennessee (UT) Textiles <strong>and</strong><br />
Nonwovens Development Center (TANDEC). Of the biocides chosen for testing, only one was a solid powder <strong>and</strong> compatible<br />
for combination with the polypropylene prior to the melt-blown process by which the filters were produced. All other biocides<br />
(liquids or suspensions) were topically applied to the filters using a spray chamber. The presence <strong>of</strong> topically applied biocides<br />
was confirmed by zone <strong>of</strong> inhibition testing on a bacterial lawn. The presence <strong>of</strong> the powder-based biocide was confirmed using<br />
a scanning electron microscope equipped with an energy-dispersive x-ray spectrometer (SEM-EDX). In the SEM mode with a<br />
high depth <strong>of</strong> resolution, it is possible to see the individual fibers <strong>of</strong> the air filter<br />
(Figure 3). Use <strong>of</strong> the EDX in combination with the SEM provided a<br />
quantitative determination <strong>of</strong> the presence <strong>of</strong> elements with atomic<br />
numbers six <strong>and</strong> greater. Photographs from the SEM <strong>of</strong> filters<br />
containing the polymer-based biocide showed fibers with "light specks"<br />
on the surface <strong>and</strong> analysis by EDX has shown these to be the biocide.<br />
Analysis by EDX also showed that the trend in the amount <strong>of</strong><br />
polymer-based biocide present within the filters did not correlate well<br />
with the relative concentration <strong>of</strong> biocide which had been added to the<br />
polypropylene prior to filter production. This indicated that there was<br />
some nonuniformity in the ability to mix the biocide with the<br />
polypropylene prior to being meltblown.<br />
The meltblown polypropylene filters used in this study had a<br />
permeability <strong>of</strong> approximately 300 to 450 CFM/ft 2 at 1.3 cm( 0.5")<br />
H 2 O. The BIAQTS <strong>and</strong> the ASTM 1215 test st<strong>and</strong>s were operated at 15<br />
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CFM <strong>and</strong> the diameters <strong>of</strong> the filter holders in each system were 10.2<br />
cm (4 inches). At 15 CFM, the filtration velocity through the filters was<br />
172 fpm (87 cm/s). At this condition, the control filters had a pressure<br />
drop <strong>of</strong> 0.19-0.28 inches <strong>of</strong> H 2 O. The effective fiber diameters <strong>of</strong> the<br />
control filters were approximately 7 to 8 micrometers in diameter. The<br />
pressure drop <strong>of</strong> the polymer-based biocide-loaded filters <strong>and</strong> the<br />
effective fiber diameters were the same as for the control filters, since<br />
this biocide was added to the polypropylene <strong>and</strong> did not alter the fiber<br />
structure. However, significant changes occurred in the filters which<br />
were treated with the topically applied biocides. The filters with<br />
topically applied biocides had pressure drops ranging from 2.2 to 4.2<br />
inches <strong>of</strong> H 2 O <strong>and</strong> effective fiber diameters <strong>of</strong> 9 to 15 micrometers.<br />
Additional study is needed to determine a more effective means <strong>of</strong><br />
applying the biocides without significantly affecting the filters' flow<br />
characteristics.<br />
Results: Filtration Efficiency<br />
The first series <strong>of</strong> tests involved an evaluation <strong>of</strong> the effect <strong>of</strong> seven<br />
different biocides on the removal efficiency <strong>of</strong> the filters. Tests were<br />
conducted in the ASTM 1215 test st<strong>and</strong> to determine the efficiency <strong>of</strong><br />
the control filter, the polymer-based biocide-loaded filters, <strong>and</strong> six<br />
topically applied biocides on 1 µm PSL spheres. All tests were<br />
conducted at a velocity <strong>of</strong> 172 fpm (15 CFM through the 10.2 cm (4<br />
inch) diameter filters). The results are summarized in Table 1. As<br />
shown in the table, the efficiency <strong>of</strong> the control filters on 1 mm PSL<br />
spheres was 97.7%. The efficiency <strong>of</strong> the polymer-based<br />
biocide-loaded filters ranged from 94.3-96.5% for the 1 µm PSL<br />
spheres, indicating that the effect <strong>of</strong> the biocide on the efficiency was<br />
Figure 3<br />
PHOTOMICROGRAPHS OF THE CONTROL (TOP)<br />
AND BIOCIDE (BOTTOM) FILTER<br />
relatively small. This was expected since the pressure drop <strong>of</strong> the biocide impregnated filters had not changed significantly. The<br />
topically-applied biocide-loaded filters had efficiencies varying from 98.6-99.57% suggesting that the efficiencies had increased<br />
slightly. This was probably a result <strong>of</strong> the higher pressure drops <strong>of</strong> these filters after the biocides were topically applied<br />
resulting from a blockage <strong>of</strong> pores within the filters.<br />
Table 1<br />
SUMMARY OF FILTRATION EFFICIENCY RESULTS<br />
Fiber Diam 1 µm PSL Bacterial<br />
Biocide Counts (µm) P (cm/in.H 2 O) Efficiency,% Efficiency, %<br />
Control 0 7.8 0.71/0.28 97.7 95.4<br />
Polymer-based 697 7.6 0.71/0.28 96.4 99.66<br />
Polymer-based 1,333 7.7 0.56/0.22 95.8 99.60<br />
Polymer-based 1,578 8.0 .71/0.28 96.0 99.87<br />
Polymer-based 2,252 8.5 .48/0.19 95.8 99.5%<br />
Polymer-based 2,255 8.3 0.71/0.28 96.5 99.50<br />
Polymer-based 3,932 8.6 0.71/0.28 94.3 99.41<br />
D NA 15.4 10.7/4.2 98.5 99.93<br />
H NA 11.2 7.6/3.0 98.9 99.61<br />
K NA 11.0 5.6/2.2 97.4 99.99<br />
L NA 14.9 6.9/2.7 97.2 99.98<br />
M NA 13.2 7.4/2.9 98.7 99.86<br />
N NA 9.4 5.8/2.3 97.4 96.0<br />
O NA 13.2 7.6/3.0 97.7 99.79<br />
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Figure 4<br />
PHOTOMICROGRAPHS OF THE CONTROL (TOP)<br />
AND BIOCIDE (BOTTOM) FILTER<br />
Additional samples <strong>of</strong> the same filters were then tested in the BIAQTS<br />
to determine the removal efficiency for E. coli. bacteria. E. coli. were<br />
chosen as test bacteria for their ease in preparation, as well as the fact<br />
that they are commonly occurring bacteria. The E. coli. are rod-shaped<br />
Gram-negative bacteria which have a diameter to length <strong>of</strong><br />
approximately 1.1-1.5 µm to 2-6 µm. Tests on the BIAQTS were<br />
conducted at the same conditions <strong>of</strong> the ASTM 1215 tests <strong>and</strong> are also<br />
summarized in Table 1. Figure 4 shows a graph <strong>of</strong> the penetration <strong>of</strong><br />
the E. coli., as measured by the Andersen microbial samplers upstream<br />
<strong>and</strong> downstream <strong>of</strong> the filter, versus the quantity <strong>of</strong> polymer-based<br />
biocide applied to the filter. The fractional penetration through the filter<br />
is equal determined from Table 1 as Penetration = (1-(Efficiency/100)),<br />
<strong>and</strong> represents the portion <strong>of</strong> the bacteria passing through the filter,<br />
where 1.0 represents 100% passage. The polymer counts (as measured<br />
by x-ray diffraction analysis--XRDA) is directly proportional to the<br />
polymer concentration in the filter. For approximation purposes, the<br />
counts ranged from 0-4000 counts, whereas the polymer-based biocide added to the polypropylene ranged from 0 to 1% by<br />
mass. The penetration <strong>of</strong> E. coli. for the control sample in the BIAQTS was approximately the same as that measured previously<br />
in the ASTM 1215 st<strong>and</strong> (0.046 versus 0.023); the efficiencies were 95.4 versus 97.7%. However, in all cases, the efficiencies<br />
<strong>of</strong> bacterial removal on the biocide loaded filters were substantially greater than the efficiencies <strong>of</strong> PSL sphere removal, as<br />
shown in Figure 4. Efficiencies ranged from 99.5 to 99.87% (penetrations <strong>of</strong> 0.005 to 0.0013).<br />
The actual cause <strong>of</strong> this increased efficiency is not completely understood at this time. It was initially proposed that it might be<br />
an electrostatic effect associated with the atomizer. To address this issue, tests were conducted on PSL spheres in the ASTM<br />
1215 test st<strong>and</strong> with <strong>and</strong> without a charge neutralizer at the test conditions above using the filters. No significant difference was<br />
observed, indicating that electrostatic charging <strong>of</strong> the atomized droplets is not the likely source <strong>of</strong> the change in efficiency. It<br />
was also suggested that the effect might be caused by the Gram-negative nature <strong>of</strong> the E. coli. However, if that were true, the<br />
control sample should have had the same efficiency as the polymer-based biocide-loaded filters. Based on tests to date, it is<br />
proposed that the biocide loaded filters not only remove bacteria, but that there is a strong indication that some portion <strong>of</strong> the<br />
bacteria passing through the filter may become sterilized, thus creating the higher effective collection efficiency <strong>of</strong> the<br />
biocide-loaded filters when compared to the control filter. Based on separate research being conducted by Phillips et al. (1995)<br />
on indoor air quality filters using PSL spheres <strong>and</strong> DOP at the same conditions <strong>of</strong> this study, it has been found that dried<br />
particles are substantially less efficient than DOP (oil droplets) <strong>of</strong> the same diameter, showing that particles at these high<br />
velocities representative <strong>of</strong> indoor air filters exhibit significant particle bouncing as they pass through filters. The dried bacteria<br />
present in the BIAQTS would exhibit a similar behavior, suggesting that they would have come in physical contact with<br />
multiple fibers as they passed through the filters. This contact may have enhanced the efficiency as measured by the microbial<br />
samplers, since the samplers only measure the viable bacteria.<br />
Later tests were also conducted downstream <strong>of</strong> a control filter <strong>and</strong> a polymer-based biocide-loaded filter by sampling into an<br />
AGLI sampler, after which an analysis was conducted to determine an approximation <strong>of</strong> the number ratio <strong>of</strong> total bacterial<br />
counts to viable counts. When direct counts (obtained using acridine orange direct counting (AODC)) were compared to viable<br />
plate counts (CFUs) following exposure to a polymer-based biocide-loaded filter, the ratio <strong>of</strong> direct counts to viable counts was<br />
far higher for the treated filter (956:1) than for the control (475:1). This is further evidence that bacterial death occurred after<br />
flow through the biocide-impregnated filters. Further testing is needed to confirm the source <strong>of</strong> the observed increases in<br />
efficiency.<br />
Efficiency tests were also conducted on six topically-applied biocides in the BIAQTS. These tests showed results which were<br />
similar to that <strong>of</strong> the impregnated filter discussed above, although tests were only conducted at a single loading. As shown in<br />
Table 1, the efficiencies <strong>of</strong> five <strong>of</strong> the topically-applied biocide-loaded filters ranged from 99.6 up to 99.99% <strong>and</strong> were<br />
substantially higher than the efficiency <strong>of</strong> the control filter (95.4%). In this case, however, some portion <strong>of</strong> this increase may<br />
have been attributable to the increased flow resistance <strong>and</strong> plugging <strong>of</strong> the filter pores, as indicated by the higher pressure drops<br />
<strong>of</strong> these filters. One <strong>of</strong> the biocides did not show any substantial increase in efficiency resulting from topical application <strong>of</strong> the<br />
biocide.<br />
Inhibition <strong>of</strong> Bacterial Growth<br />
To enable detection <strong>of</strong> biocidal activity on the filters, attempts were made to extract <strong>and</strong> culture bacteria from the filters after<br />
being left overnight on the filters (polymer-based biocide being a slow acting biocide). The filters were vortexed in 0.1 M<br />
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phosphate buffer containing 0.05% Triton-X 100 (detergent), followed by plating the bacteria onto Nutrient® agar <strong>and</strong><br />
incubated for 24 hours at 37 o C. While 5.14 x 10 4 CFUs were able to be extracted from the control filter, no CFUs were able to<br />
be extracted from any <strong>of</strong> the biocide-impregnated or topically-loaded filters, demonstrating efficient biocidal activity. There was<br />
some concern that this technique may not be an accurate measure <strong>of</strong> the inhibition <strong>of</strong> growth on the filter, since the extraction<br />
process would also expose the bacteria to biocide which may have been washed from the filter.<br />
In an effort to more fully underst<strong>and</strong> the potential for inhibition <strong>of</strong> growth on the filters, tests were conducted in which the<br />
above biocides as well as additional biocides were sprayed onto samples <strong>of</strong> the polypropylene filter used in this study. After the<br />
filters were dried, small disks were punched from the control <strong>and</strong> biocide-loaded filters <strong>and</strong> placed upon tryptic soy agar plates<br />
which had been treated with either bacteria or fungi. Two different series <strong>of</strong> tests were conducted. In the first, 0.1 ml <strong>of</strong> cells<br />
were placed on the agar plates <strong>and</strong> spread with an "L" shaped rod upon the surface <strong>of</strong> the agar. In the second set <strong>of</strong> tests, cells<br />
were placed in the agar by mixing them into the agar prior to pouring the agar into the petri dishes (referred to as the pour-plate<br />
method). The use <strong>of</strong> the two different techniques was an effort to provide optimum growing conditions for cells that might<br />
prefer significant exposure to air as opposed to less exposure to air (the pour-plate method). After placing the filter disks upon<br />
the agar plates, the plates were incubated at either 25 o C or 37 o C for 24 to 36 hours. After incubation, zones <strong>of</strong> inhibition were<br />
determined by measuring the areas <strong>of</strong> no growth around the disks using calipers. All tests were conducted in duplicate, <strong>and</strong> a<br />
control disk (no biocide added) was included on each plate.<br />
The results <strong>of</strong> the inhibition tests are shown in Table 2 for a variety <strong>of</strong> bacteria:<br />
Escherichia coli - Gram-negative, rod shaped bacteria<br />
Staphylococcus aureus - Gram-positive, sphere shaped<br />
Streptococcus pyogenes - Gram-positive, strep throat bacteria<br />
Pseudomonas aeruginosa - Gram-negative, opportunistic, antibiotic resistant<br />
Saccharomyces cerevisiae - yeast, single cell fungal group<br />
C<strong>and</strong>ida albicans - opportunistic pathogen<br />
Table 2<br />
ZONE INHIBITION RESULTS FOR VARIOUS BIOCIDES<br />
C<strong>and</strong>ida<br />
albicans<br />
Escherichia Staphylococcus Streptococcus Pseudomona Saccharomyces<br />
Coli aureus pyogenes aeruginosa cerevisiae<br />
Biocide smear pour smear pour smear pour smear pour smear<br />
smear<br />
C + ++ ++ -- ++ ++ -- -- ++<br />
++<br />
D ++ +++ +++ +++ +++ ++++ +++ ++ ++++<br />
+++<br />
E ++ - ++ ++ +++ ++ + --<br />
++<br />
F ++ + ++ ++ +++ ++ + + +<br />
++<br />
G ++ ++ ++ ++ ++ ++ -- ++<br />
++<br />
H -- -- -- -- -- -- -- -- --<br />
--<br />
I -- -- -- -- -- -- -- -- --<br />
--<br />
J -- -- -- -- -- -- -- -- --<br />
--<br />
K ++ ++ +++ ++ ++ +++ -- -- ++<br />
--<br />
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Eval <strong>of</strong> Filtration Performance<br />
L + -- ++++ + +++ + -- + +++<br />
++++<br />
M + -- + + + m -- -- +<br />
++<br />
N +++ ++ ++ ++ ++ m -- -- --<br />
--<br />
O +++ ++ +++ ++ ++++ ++++ ++++ +++ ++++<br />
++++<br />
P -- + ++ ++ -- m -- + +++<br />
++<br />
Control -- -- -- -- -- -- -- -- --<br />
--<br />
-- no zone; + zone diameter <strong>of</strong> 8-15 mm; ++ zone diameter <strong>of</strong> 15-25 mm; +++ zone<br />
diameter <strong>of</strong> 25-40 mm;<br />
++++ zone diameter > 40 mm; m indicates missing data or inconclusive data.<br />
The control filters showed no zone <strong>of</strong> inhibited growth on any <strong>of</strong> the plates that were tested. The zone <strong>of</strong> inhibition for the<br />
various biocides ranged from no measurable zone <strong>of</strong> inhibition to greater than a 40 mm diameter zone <strong>of</strong> inhibited growth,<br />
depending on the biocide <strong>and</strong> the type <strong>of</strong> microorganism being tested. Biocides D <strong>and</strong> O showed superior inhibition to all<br />
microorganisms that were tested whereas Biocides H, I, <strong>and</strong> J were similar to the control samples with no zone <strong>of</strong> inhibited<br />
growth. There was some evidence that the zone <strong>of</strong> inhibition may have been related to the degree <strong>of</strong> solubility <strong>of</strong> the biocide in<br />
water. While this type <strong>of</strong> test would favor such biocides, it is also true that this type <strong>of</strong> biocide would probably perform better<br />
within a filter which was placed in a humid environment such as occurs in HVAC systems. So the test, although sensitive to the<br />
solubility <strong>of</strong> the biocide is probably a good indicator <strong>of</strong> the performance that might occur in filter applications. A final test was<br />
conducted on samples <strong>of</strong> each <strong>of</strong> the biocide-loaded filters listed in Table 2 to determine the effect, if any, <strong>of</strong> the degradation <strong>of</strong><br />
the biocide when exposed to light for 14 hours. The results <strong>of</strong> these tests showed that there was no effect on any <strong>of</strong> the biocides<br />
due to exposure to light for the period tested. However, the long term stability <strong>of</strong> the biocides was not tested, <strong>and</strong> is an area for<br />
future study. Data collected in which the incubation period was held at 37 o C were not included in this paper since the results<br />
were very similar to those obtained with an incubation period <strong>of</strong> 250C.<br />
Conclusions<br />
A Biocontaminant Indoor Air Quality Test St<strong>and</strong> was successfully designed <strong>and</strong> constructed which provided the ability to<br />
evaluate the removal efficiency <strong>of</strong> filters which had been loaded with biocides. An evaluation <strong>of</strong> the filters showed that effective<br />
biocides were identified which had the ability to effectively remove a variety <strong>of</strong> microorganisms, including bacteria <strong>and</strong> fungi.<br />
In all but one <strong>of</strong> the eight biocides which were tested for bacterial removal efficiency using E. coli, the removal efficiencies<br />
were found to be significantly greater than were achieved with the control which contained no biocide. In the case <strong>of</strong> the<br />
polymer-based biocide, there was some indication that the increased efficiency may have been due, in part, to bacteria which<br />
passed through the filter, but whose ability to form CFUs had been inhibited. In the case <strong>of</strong> the topically applied biocides, the<br />
enhancement in efficiency may have been due to the biocide being applied to the filters, increasing the pressure drop <strong>and</strong><br />
blocking the pores.<br />
Fourteen <strong>of</strong> the biocides-loaded filters were evaluated to determine if the biocides created a zone <strong>of</strong> inhibited growth near the<br />
filters when exposed to a variety <strong>of</strong> microorganisms. Eleven <strong>of</strong> the biocides showed a zone <strong>of</strong> inhibition on at least some <strong>of</strong> the<br />
organisms. Two <strong>of</strong> the biocides showed significant zones <strong>of</strong> inhibition for all <strong>of</strong> the microorganisms tested.<br />
Acknowledgments<br />
The authors wish to express appreciation to a variety <strong>of</strong> sponsors who partially funded this work. The work was funded, in part,<br />
by the National Science Foundation (Grant NSF BES-9411572) which provided specific equipment used in the study, Olin<br />
Chemical Corporation who funded development <strong>of</strong> the filter media, TANDEC <strong>and</strong> Exxon Chemical Company (Baytown, TX)<br />
which provided meltblown filter production facilities, to NASA (Contract NAS9-19302) which provided funds for the bacterial<br />
filtration efficiency testing <strong>of</strong> the filters, <strong>and</strong> to the Center for Indoor Air Research (Contract 95-09) which provided funds to<br />
build the BIAQTS. It was only through the cooperative nature <strong>of</strong> these various sponsors that the multidisciplinary nature <strong>of</strong> this<br />
research could be accomplished.<br />
References<br />
ASTM F1215-89. St<strong>and</strong>ard Test Method for Determining the Initial Efficiency <strong>of</strong> Flatsheet Filter medium in an Airflow Using<br />
Latex Spheres, American Society for Testing <strong>and</strong> Materials, Philadelphia, PA, 1989.<br />
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Eval <strong>of</strong> Filtration Performance<br />
Davis, W.T., C. Cornell, <strong>and</strong> M. Dever, "Theoretical Efficiencies <strong>of</strong> Residential Air Filters," TAPPI <strong>Journal</strong>, Vol. 76, No. 7,<br />
1994.<br />
Davis, W.T., "Air Filtration Efficiency Testing," TAPPI <strong>Journal</strong>, Vol. 77, No. 2, pp. 221-226, Feb. 1994..<br />
Phillips, B.A., W.T. Davis, <strong>and</strong> M. Dever, "Investigation <strong>of</strong> the Particle Collection Efficiency <strong>of</strong> Melt Blown Media at High Air<br />
Velocity," Proceedings <strong>of</strong> the American Filtration <strong>and</strong> Separations Society 1995 Technical Conference, Nashville, TN, April<br />
23-25, 1995.<br />
Lighthart, B., <strong>and</strong> B. T. Shaffer, "Airborne Bacteria in the Atmospheric Surface Layer: Temporal Distribution above a Grass<br />
Seed Field," Applied <strong>and</strong> Environmental Microbiology, Vol. 61, No. 4, pp. 1492-1496, 1995.<br />
Meyer, B., Indoor Air Quality, Addison-Wesley Publishing Company, Inc., Reading, MA, p. 107, 1983.<br />
Wadden, R.A., <strong>and</strong> P.A. Sheff, Indoor Air Pollution, John Wiley & Sons, Inc., 1983, p. 106.<br />
Walsh, P. J., C. S. Dudney, <strong>and</strong> E. D. Copenhaver, Indoor Air Quality, CRC Press, Inc., Boca Raton, FL, pp. 176-178, 1984.<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
- INJ<br />
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Melt Blown Web Properties<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Characterization <strong>of</strong> Melt Blown Web Properties Using Air Flow<br />
Technique<br />
By Peter Ping-yi Tsai, Textiles <strong>and</strong> Nonwovens Development Center (TANDEC), The University <strong>of</strong> Tennessee, Knoxville, TN<br />
Abstract<br />
Fiber size, pore size, <strong>and</strong> air permeability are three important properties in melt blown (MB) webs. Air permeability governs the air<br />
resistance or the pressure drop <strong>of</strong> the air through the web. One <strong>of</strong> the major applications <strong>of</strong> MB webs is for air filters. Fiber size<br />
dominates the web air filtration efficiency. Liquid filtration is another major application <strong>of</strong> MB webs. Pore size <strong>of</strong> the web<br />
determines the rated particle size in liquid filtration. Air permeability can be easily determined by air permeability testers. Fiber size<br />
<strong>and</strong> pore size in MB webs are difficult to measure by optical microscopy or other methods. However, they can be determined in<br />
fibrous products from the air flow rate through the web.<br />
Introduction<br />
Melt blowing is a one step process to make micr<strong>of</strong>iber webs directly from polymer resin. Melt blown webs have been developed for<br />
a large variety <strong>of</strong> applications, such as filters, operation gowns, wipes, oil absorbents, <strong>and</strong> battery separators, etc. All utilize the<br />
advantage <strong>of</strong> the micr<strong>of</strong>ibers which result in a breathable barrier fabric. Fiber size is a very important web property, which<br />
dominantly governs the filtration efficiency <strong>of</strong> the webs. The micr<strong>of</strong>iber size <strong>of</strong> a MB web is difficult to measure using an optical<br />
microscope due to the fact that the fiber size is only slightly larger than the visible wavelength <strong>and</strong> no sharp edge is defined because<br />
<strong>of</strong> the light diffraction. It is time-consuming, tedious, <strong>and</strong> expensive to measure the fiber size by scanning electron microscopy<br />
although it is the most commonly used technique at the present time. Pore size is another important melt blown web property, which<br />
determines the web applications as liquid filters <strong>and</strong> battery separators. It can be determined using a porometer. Again, it is<br />
expensive <strong>and</strong> time-consuming. In this paper, the determination <strong>of</strong> fiber size <strong>and</strong> pore size <strong>of</strong> melt blown webs using air flow<br />
technique is discussed. It is a quick <strong>and</strong> accurate method at least for the nonwovens mentioned.<br />
Background<br />
Several relationships between pore size <strong>and</strong> fiber size in fibrous<br />
materials have been shown by earlier researchers. For metal fibrous<br />
mats, Goeminne [1] showed the relationship between largest pore size<br />
(da) <strong>and</strong> fiber size as<br />
(1)<br />
Figure 1<br />
RELATIONSHIP BETWEEN MEASURED FIBER SIZE<br />
(SEM) AND EFFECTIVE FIBER SIZE AS<br />
ESTIMATED USING DATA FROM THE<br />
TSI FILTER TESTER<br />
where D is the fiber size <strong>and</strong> is the mat porosity. He also showed the<br />
relationship between mean pore size (d m ) <strong>and</strong> fiber size for porosity less<br />
than 0.9 as<br />
(2)<br />
Wrotnowski [2] showed the relationship for felt mat as<br />
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Melt Blown Web Properties<br />
(3)<br />
where DEN is fiber denier, x is felt packing density, <strong>and</strong> y is fiber<br />
density.<br />
Equations 1-3 show that there is a relationship between pore size <strong>and</strong><br />
fiber size by packing density for fibrous mats. One parameter, either<br />
fiber size or pore size, can be determined if the other is determined. Fiber<br />
fineness <strong>and</strong> pore size can be determined by air flow technique. The<br />
fineness <strong>of</strong> cotton fibers determined by the Micronaire test [3] is an<br />
example. This test measures the resistance <strong>of</strong> the air flowing through the<br />
fibers in a bulky form. The air resistance is from the friction <strong>of</strong> the air<br />
with the fiber surface. The air resistance increases as the fiber surface<br />
increases. Finer fibers have larger surface area than coarser fibers for a<br />
given amount <strong>of</strong> mass. Another example is the measurement <strong>of</strong> 1st <strong>and</strong><br />
3rd bubble points reported by Wagner [4] who showed that there was an<br />
excellent agreement <strong>of</strong> bubble points measured by several companies<br />
using different flow methods. This paper will discuss how fiber size <strong>and</strong><br />
pore size <strong>of</strong> melt blown webs can be determined by air flowing through<br />
them.<br />
Theory<br />
The general equation for fluid flow through porous medium was described by Brinkman [5] as<br />
where p = fluid pressure on the medium<br />
µ = air viscosity<br />
k = air permeability<br />
v 0 = air superficial velocity<br />
= air density<br />
(4)<br />
Figure 2<br />
RELATIONSHIP BETWEEN MEASURED FIBER<br />
SIZE (SEM) AND EFFECTIVE FIBER SIZE AS<br />
ESTIMATED USING DATA FROM THE FRAZIER<br />
AIR-PERMEABILITY TESTER<br />
The gravity term ( g) can be discarded because air density is negligible compared to the medium resistance to the air flow. The<br />
turbulent term, the third term on the right side <strong>of</strong> the equation, can be neglected at a low air flow rate. Therefore, Equation 4 is<br />
reduced to Darcy's law for air flowing through porous materials at low air flow rate, which is<br />
(5)<br />
For fibrous webs, a porous material, if the fibers are transverse to the flow direction, the air flowing through the web will obey<br />
Darcy's law <strong>and</strong> the following equation must be obeyed [6]<br />
(6)<br />
where c is web packing density (a ratio <strong>of</strong> the fiber volume to that <strong>of</strong> the web in which the fiber is composed <strong>of</strong>) , A is the web<br />
cross-sectional area subjected to the air flow, R is the average fiber radius, Q is the air flow rate <strong>and</strong> h is the web thickness.<br />
Several forms <strong>of</strong> the function <strong>of</strong> c were given, e.g., Langmuir [7] gave the function <strong>of</strong> c as<br />
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Melt Blown Web Properties<br />
(7)<br />
Davies [6] made an experimental correction in Equation 7 <strong>and</strong> provided the following relation for packing density in the interval <strong>of</strong><br />
0.006 < c < 0.3<br />
(8)<br />
(9)<br />
where d f is the average fiber size<br />
v is the fluid flow velocity.<br />
If the fiber cross-sectional area is irregular rather than circular, the fiber size (d f ) in Equation 9 is called effective fiber size, a<br />
parameter that dominantly determines the air filtration efficiency <strong>of</strong> a fibrous material. Depending on the fiber shape <strong>and</strong> the fiber<br />
size distribution in the web, effective fiber diameter varies from the average <strong>of</strong> the actual fiber size. However, effective fiber size is<br />
always larger than the average <strong>of</strong> the actual fiber size [6].<br />
The effective fiber size can be calculated from Equation 9 if the pressure drop is determined from a laminar flow through the fibrous<br />
medium. The actual fiber size can be obtained from the corresponding curve for the effective fiber size <strong>and</strong> actual fiber size. This<br />
technique will be described in a later section <strong>of</strong> this paper.<br />
We now continue on the theory <strong>of</strong> pore size determination. For the fluid flowing inside a circular pipe, Darcy's law becomes<br />
Hagen-Poisulla's law, which is described by the following equation<br />
(10)<br />
in which the coefficient in laminar flow is 32/D 2 in Darcy's law for fluid flowing through porous materials. The fluid velocity inside<br />
the web is higher than the web superficial velocity <strong>and</strong> should be increased by 1/ , where is the web porosity. Together with the<br />
modification <strong>of</strong> the fluid flow by turtosity factor (T), a term that describes the increase <strong>of</strong> the fluid flowing path through porous<br />
materials, Equation 10 becomes<br />
(11)<br />
where z is the web thickness <strong>and</strong> the other terms were defined before. Equation 11 is ASTM F902 St<strong>and</strong>ard [7] to obtain the average<br />
circular-capillary-equivalent pore size by laminar air flow. By combining Equations 9 <strong>and</strong> 11, another relationship between pore<br />
size <strong>and</strong> fiber size can be obtained, i.e.<br />
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Melt Blown Web Properties<br />
Equation 13 says that average circular-capillary-equivalent pore size is related to effective fiber size by a function <strong>of</strong> web packing<br />
density g(c). This agrees with Equations 1-3 found by the previous researchers for fibrous mats.<br />
Now the air permeability in Darcy's law for air flowing perpendicularly through a flat web, i.e. one-dimensional flow, can be<br />
obtained by combining Equations 5 <strong>and</strong> 9 as<br />
(14)<br />
in which for one-dimensional flow,<br />
Equation 14 says that air permeability is only a function <strong>of</strong> fiber size <strong>and</strong> the function <strong>of</strong> packing density, <strong>and</strong> pore size term is not<br />
apparently involved. However, pore size is an implicit function <strong>of</strong> fiber size <strong>and</strong> packing density function.<br />
Experimental<br />
A TSI Automated Filter Tester was used to measure the web filtration efficiency. It also displayed the pressure drop across the web<br />
at a constant air flow rate, 5.3 cm/s in this study. A Frazier air permeability tester was used to measure the air flow rate at constant<br />
web pressure drop, 12.7 mm <strong>of</strong> water according to ASTM Method D737 (10). Pressure drop <strong>and</strong> air flow rate measured from both<br />
instruments were employed to calculate the effective fiber size by Equation 9. Four MB webs were produced at a large range <strong>of</strong><br />
primary air velocity (60%, 70%, 80% <strong>and</strong> 90% air valve opening) from Accurate Products melt blowing line at the University <strong>of</strong><br />
Tennessee to obtain a broad range <strong>of</strong> fiber size. A curve as shown in Figures 1 <strong>and</strong> 2 that corresponds the effective fiber size to SEM<br />
fiber size can be obtained. This curve is therefore used to find the actual fiber size, i.e. SEM-equivalent fiber size, once the effective<br />
fiber size is obtained. Effective fiber size is not the average <strong>of</strong> actual fiber size as described previously. However, it is an excellent<br />
"yard stick" <strong>of</strong> actual fiber size. Effective fiber size is a function <strong>of</strong> fiber shape <strong>and</strong> fiber size distribution <strong>of</strong> a web. The curve<br />
relating SEM-equivalent fiber size to actual fiber size is not a universal curve for all fibrous webs, i.e. the curve changes when either<br />
the fiber shape or the fiber size distribution changes. However, for typical melt blown webs, they have similar fiber shape <strong>and</strong> fiber<br />
size distribution. Therefore, the relating curve is excellent for all typical melt blown webs.<br />
Three other melt blown webs with a broad range <strong>of</strong> fiber sizes were produced by changing the die temperature <strong>and</strong> primary air<br />
velocity. The actual fiber size <strong>of</strong> this group <strong>of</strong> webs was obtained from the corresponding curves in which the effective fiber size was<br />
calculated from the data obtained using TSI tester <strong>and</strong> Frazier tester. The actual fiber size was compared with those measured using<br />
the scanning electron microscope.<br />
The pressure drops obtained at constant air flow rate for different melt blown webs having different fiber size from TSI tester were<br />
used to calculate average circular-capillary-pore size. The results were compared with the mean flow pore size measured from<br />
Coulter Porometer II based on the equation that describes the capillary flow in a tube [11]<br />
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Melt Blown Web Properties<br />
(15)<br />
where D is the pore size, g is the surface tension <strong>and</strong> q is the contact angle. Contact angle is zero for a wet-out sample by the fluid<br />
used in the porometer. Therefore, Equation 15 becomes<br />
(16)<br />
Surface tension is constant <strong>and</strong> can be determined for the liquid used to wet out the sample. Therefore, pore size is inversely<br />
proportional to the applied air pressure.<br />
Results <strong>and</strong> discussion<br />
Figures 1 <strong>and</strong> 2 are the curves that relate the actual fiber size obtained from the scanning electron microscopy to effective fiber size<br />
derived from the data obtained from TSI <strong>and</strong> Frazier testers, respectively. Theoretically, as long as the air flowing through the webs<br />
is laminar, these two curves should be equal for the fibrous materials such as MB webs having similar cross-sectional shape <strong>and</strong> fiber<br />
size distribution. Actually, some deviation occurs <strong>and</strong> it is explained in the later paragraph.<br />
A typical melt blown web has an average fiber size <strong>of</strong> approximate 2 mm. The Reynolds number at TSI st<strong>and</strong>ard air flow rate, 5.3<br />
cm/s, is<br />
(17)<br />
where D is the fiber size. The Reynolds number for a typical melt blown web (Re = 0.0067) is much lower than the critical Reynolds<br />
number (Re = 1.0) for a turbulent flow through a porous medium. Therefore, the air flow through the fabric is laminar.<br />
The pressure drop sensitivity <strong>of</strong> the instrument at different flow rate presents a reason that the two curves derived from two different<br />
testers did not completely agree. Different curves mean that different air flow rates may provide different effective fiber sizes. The<br />
corresponding actual fiber size obtained from different curves should be equal for the same web. However, the fabric is compressed<br />
by the pressure difference in the upstream <strong>and</strong> downstream <strong>of</strong> the fabric. Therefore, testing at different pressure drops attributed to<br />
the distortion <strong>of</strong> the web presents another deviation on the actual fiber size obtained from effective fiber size from different testers.<br />
The actual fiber size obtained from Figures 1 <strong>and</strong> 2, measured by TSI <strong>and</strong> Frazier, respectively, for a group <strong>of</strong> samples produced at<br />
different process conditions is listed on Tables 1 <strong>and</strong> 2 <strong>and</strong> is also compared with that measured from scanning electron microscopy.<br />
The maximum error from TSI was 10.8% <strong>and</strong> 19.1% from Frazier. This amount <strong>of</strong> error is reasonable <strong>and</strong> acceptable for MB webs<br />
because they have a large range <strong>of</strong> fiber size distribution (CV%=50%) <strong>and</strong> their fiber size is too small to be measured by any other<br />
technique. Melt blown fiber size measured from different instruments, e.g. optical microscope <strong>and</strong> SEM, or by different technicians<br />
usually contribute to an error that is greater than 20%.<br />
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Melt Blown Web Properties<br />
Table 1<br />
COMPARISON OF FIBER SIZE OBTAINED<br />
FROM EFFECTIVE FIBER SIZE BY TSI TESTER<br />
AND SEM FIBER SIZE<br />
Table 2<br />
COMPARISON OF FIBER SIZE OBTAINED<br />
FROM EFFECTIVE FIBER SIZE BY FRAZIER<br />
AND SEM FIBER SIZE<br />
Fiber Size<br />
From<br />
FIBER SIZE<br />
From<br />
Effective Effective SEM<br />
Effective Effective SEM<br />
Fiber Size Fiber Size Fiber Size Error<br />
Fiber Size Fiber Size Fiber Size Error<br />
Sample mm mm mm % Sample mm mm mm %<br />
1 4.84 1.92 1.93 0.5 1 5.65 1.76 1.93 8.7<br />
2 7.82 3.13 2.97 5.3 2 9.09 3.54 2.97 19.1<br />
3 10.13 4.56 5.12 10.8 3 11.38 5.62 5.12 9.9<br />
Figure 3<br />
COMPARISON OF MEASURED PORE SIZE<br />
(MFP =<br />
MEAN FLOW PORE SIZE FROM COULTER<br />
POROMETER II) AND<br />
COMPUTER-CALCULATED<br />
PORE SIZE (ACCP - AVERAGE CIRCULAR<br />
CAPILLARY PORE SIZE FROM TSI DATA) FOR<br />
A<br />
VARIETY OF MELT BLOWN WEBS<br />
(pp = polypropylene, lldpe = linear low density<br />
polyethlyene, pet = polyethylene terephthalate)<br />
Figure 4<br />
COMPARISON OF MEASURED PORE SIZE<br />
(MFP<br />
= MEAN FLOW PORE SIZE FROM<br />
COULTER<br />
POROMETER II) AND<br />
COMPUTER-CALCULATED<br />
PORE SIZE (ACCP = AVERAGE CIRCULAR<br />
CAPILLARY PORE SIZE FROM TSI DATA)<br />
FOR A<br />
GROUP OF 34-G/M 2 MELT BLOWN WEBS<br />
Figure 4 shows the pore size relationship between that measured from Coulter Porometer II <strong>and</strong> that derived from the air flow rate<br />
obtained from the TSI Filter Tester for a group <strong>of</strong> MB webs having different fiber size <strong>and</strong> pore size. They had a good agreement for<br />
the pore size smaller than 50 mm. Pore size from Coulter Porometer II may not be stable for large pore size <strong>and</strong> the low pressure<br />
drop in TSI from the webs <strong>of</strong> large pore size may be out <strong>of</strong> the sensitivity <strong>of</strong> the instrument sensor. Figure 4 shows another plot <strong>of</strong><br />
the pore size measured from Coulter Porometer II <strong>and</strong> calculated using air flow rate from TSI Filter Tester for a set <strong>of</strong> nine typical 34<br />
g/m 2 (1 oz/yd 2 ) melt blown webs produced at different time.<br />
Figure 5 shows the disagreement <strong>of</strong> air permeability measured from the Frazier air permeability tester, TSI filter tester <strong>and</strong> Coulter<br />
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Melt Blown Web Properties<br />
Porometer II at different pressure drops <strong>and</strong> normalized to that <strong>of</strong> Frazier<br />
tester (12.7 mm <strong>of</strong> water). The normalized air permeability will be lower<br />
than that measured from Frazier tester if the pressure drop measured from<br />
other testers was higher than Frazier tester because a higher pressure will<br />
compress more on the web as discussed before. Therefore, a lower air<br />
permeability will be measured. This is true for the normalized air<br />
permeability obtained from the Coulter Porometer II at a higher pressure<br />
drop as shown in the curves in Figure 5. The normalized air permeability<br />
from the TSI tester at a lower pressure than from Frazier tester shows a<br />
lower air permeability as illustrated in the same figure, <strong>and</strong> this reason is<br />
not known. It is observed that air permeability should be measured at the<br />
specified pressure drop rather than to convert the air permeability from<br />
another pressure drop by a theoretical equation, such as Equation 9,<br />
because <strong>of</strong> the different distortion <strong>of</strong> the web compression <strong>and</strong> hence<br />
packing density by different pressure across the web from the applied air<br />
flow rate. The higher the pressure across the web, the more the web<br />
packing density is distorted. Therefore, the normalized air permeability is<br />
reduced.<br />
Figure 5<br />
NORMALIZED AIR PERMEABILITY AS<br />
MEASURED USING FRAZIER, TSI AND COULTER<br />
POROMETER II TESTED FOR A GROUP OF<br />
34-G/M 2 MELT BLOWN WEBS<br />
Conclusions<br />
Air flow techniques provide a quick method to accurately calculate two<br />
important MB properties, fiber size <strong>and</strong> pore size. This method can be done<br />
on any air flow instrument if a laminar air flow through the web is<br />
provided. The Frazier air permeability tester <strong>and</strong> TSI filter tester were two<br />
instruments used in this paper for the determination <strong>of</strong> fiber size by air flow<br />
technique. They both show a good agreement with the fiber size measured<br />
from scanning electron microscopy. Air flow rate <strong>and</strong> pressure drop<br />
measured from the TSI instrument was also used to calculate the MB web pore size. The results had a good agreement with those<br />
measured by the Coulter Porometer II for the pore size less than 50 mm. Air permeability measured from the Frazier tester did not<br />
agree with that measured from other air flow testers <strong>and</strong> normalized to the constant pressure drop (12.7 mm <strong>of</strong> water) used in Frazier<br />
tester according to ASTM Method D737.<br />
Literature cited<br />
1. Goeminne, H., "The Geometrical <strong>and</strong> Filtration Characteristics <strong>of</strong> Metal-Fiber Filters - A Comparative Study," Filtration <strong>and</strong><br />
Separation 1974 (August), pp. 350-355.<br />
2. Wrotnowski, A.C., Felt Filter Media, American Felt Co., Glenville, CT, 1968.<br />
3. Grover, Elliot B. <strong>and</strong> Hamby, D.S., H<strong>and</strong>book <strong>of</strong> Textile Testing <strong>and</strong> Quality Control, Textile Book Publishers, Inc., A Division <strong>of</strong><br />
Interscience Publishers, Inc., New York, 1960, pp. 212-220.<br />
4. Wagner, J. Robert, "The relationship <strong>of</strong> filter media 1st <strong>and</strong> 3rd bubble point <strong>and</strong> maximum pore size," TAPPI <strong>Journal</strong>, pp. 108,<br />
199-202, vol. 78, No. 4, 1995.<br />
5. Brinkman, H.C., Appl. Sci. Research, A1, 27-34, 81-86 (1947).<br />
6. Davies, C.N., Air Filtration, Academic Press, London, 1976.<br />
7.Langmuir, I., "Report on Smokes <strong>and</strong> Filters," Section I. U.S. Office <strong>of</strong> Scientific Research <strong>and</strong> Development, No. 865, Part IV<br />
(1942).<br />
8. Hinds, William C., Aerosol Technology, John Wiley & Sons, New York, 1982.<br />
9. ASTM F902, "St<strong>and</strong>ard Practice for Calculating the Average Circular-Capillary-Equivalent Pore Diameter in Filter Media from<br />
Measurements <strong>of</strong> Porosity <strong>and</strong> Permeability," American Society for Testing Materials, 1926 Race St. Philadelphia, PA 19103, 1984.<br />
10. ASTM Method D737, "St<strong>and</strong>ard Test Method for Air Permeability <strong>of</strong> Textile <strong>Fabrics</strong>," American Society for Testing Materials,<br />
1926 Race St. Philadelphia, PA 19103, 1984.<br />
11. Adamson, Arthur W., Physical Chemistry <strong>of</strong> Surfaces, Interscience Publishers, a division <strong>of</strong> John & Sons, New York, 1967.<br />
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Melt Blown Web Properties<br />
This paper was originally submitted for publication in the TAPPI <strong>Journal</strong>. The INJ editors <strong>and</strong> publishers wish to express their<br />
appreciation to TAPPI for their support <strong>and</strong> encouragement.<br />
INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
Foamed Latex Bonding <strong>of</strong><br />
Spunlace <strong>Fabrics</strong> To Improve<br />
Physical Properties<br />
ORIGINAL PAPER/PEER REVIEWED<br />
By A. Shahani, S<strong>of</strong>tware Engineer for Bell Atlantic; D. A. Shiffler, Adjunct Associate Pr<strong>of</strong>essor at the Nonwovens<br />
Cooperative Research Center; <strong>and</strong> S. K. Batra, the Charles A. Cannon Pr<strong>of</strong>essor <strong>of</strong> Textiles at North Carolina State<br />
University, <strong>and</strong> Director <strong>of</strong> the Nonwovens Cooperative Research Center.<br />
Abstract<br />
Strength, abrasion resistance, load at 5% strain (modulus), <strong>and</strong> strain recovery <strong>of</strong> dry lay spunlace fabric are improved by the<br />
addition <strong>of</strong> small amounts (
Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
Round Cross Section<br />
Figure 1<br />
TYPICAL MD TENSILE CURVES<br />
FOR POLYESTER FABRICS AT<br />
3600 kJ/kg FOR FOUR ADD-ON<br />
LEVELS (0,1.25, 2.5, 5%)<br />
Figure 2<br />
TYPICAL MD TENSILE CURVE<br />
FOR COTTON FABRICS AT 3600<br />
kJ/kg FOR FOUR ADD-ON LEVELS<br />
(0,1.25, 2.5, 5%)<br />
Figure 3<br />
TYPICAL MD TENSILE CURVE<br />
FOR ACRYLIC FABRICS AT 3600<br />
kJ/kg FOR FOUR ADD-ON LEVELS<br />
(0,1.25, 2.5, 5%)<br />
Figure 4<br />
MAXIMUM LOAD VS. ADD-ON (%)<br />
FOR POLYESTER FABRICS MADE<br />
AT THREE SPECIFIC ENERGIES<br />
(1800, 3600 AND 7100 kJ/kg<br />
Figure 5<br />
MAXIMUM LOAD VS. ADD-ON (%)<br />
FOR COTTON FABRIC MADE AT<br />
THREE SPECIFIC ENERGIES<br />
(1800, 36000 AND 7100 kJ/kg)<br />
Figure 6<br />
MAXIMUM LOAD VS. ADD-ON (%)<br />
FOR ACRYLIC FABRIC MADE AT<br />
TWO SPECIFIC ENERGIES (3550<br />
AND 7100 kJ/kg)<br />
Figure 7<br />
ELONGATION AT MAXIMUM<br />
LOAD VS. ADD-ON (%) FOR<br />
POLYESTER FABRICS MADE AT<br />
THREE SPECIFIC ENERGIES<br />
(1800, 3600, 7100 kJ/kg)<br />
Figure 8<br />
ELONGATION AT MAXIMUM<br />
LOAD VS. % ADD-ON FOR<br />
COTTON FABRICS MADE AT<br />
THREE SPECIFIC ENERGIES<br />
(1800, 3600, 7100 kJ/kg)<br />
Figure 9<br />
ELONGATION AT MAXIMUM<br />
LOAD VS. % ADD-ON FOR<br />
ACRYLIC FABRICS MADE AT<br />
TWO SPECIFIC ENERGIES ( 3550,<br />
7100 kJ/kg)<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
Figure 10<br />
LOAD AT 5% STRAIN VS. %<br />
ADD-ON FOR POLYESTER<br />
FABRICS MADE AT THREE<br />
SPECIFIC ENERGIES (1800, 3600,<br />
7100 kJ/kg)<br />
Figure 11<br />
LOAD AT 5% STRAIN VS. %<br />
ADD-ON FOR COTTON FABRICS<br />
MADE AT THREE SPECIFIC<br />
ENERGIES (1800, 3600, 7100 kJ/kg)<br />
Figure 12<br />
LOAD AT 5% STRAIN VS. %<br />
ADD-ON FOR ACRYLIC FABRICS<br />
MADE AT TWO SPECIFIC<br />
ENERGIES (3600, 7100 kJ/kg)<br />
Figure 13<br />
BENDING RIGIDITY VS. %<br />
ADD-ON FOR POLYESTER<br />
FABRICS MADE AT THREE<br />
SPECIFIC ENERGIES (1800, 36000,<br />
7100 kJ/kg)<br />
Figure 14<br />
BENDING RIGIDITY VS. %<br />
ADD-ON FOR COTTON FABRICS<br />
MADE AT THREE SPECIFIC<br />
ENERGIES (1800, 3600, 7100 kJ/kg)<br />
Figure 15<br />
BENDING RIGIDITY VS. %<br />
ADD-ON FOR ACRYLIC FABRICS<br />
MADE AT TWO SPECIFIC<br />
ENERGIES (3600, 7100 kJ/kg)<br />
Figure 16<br />
CORRELATION TEST PLOT FOR<br />
BENDING RIGIDITY AND LOAD<br />
AT 5% STRAIN<br />
Figure 17<br />
ABRASION RESISTANCE VS. %<br />
ADD-ON FOR POLYESTER<br />
FABRICS MADE AT THREE<br />
SPECIFIC ENERGIES (1800, 3600,<br />
7100 kJ/kg)<br />
Figure 18<br />
ABRASION RESISTANCE VS. %<br />
ADD-ON FOR COTTON FABRICS<br />
MADE AT THREE SPECIFIC<br />
ENERGIES (1800, 3600, 7100 kJ/kg)<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
Figure 19<br />
ABRASION RESISTANCE VS. %<br />
ADD-ON FOR ACRYLIC FABRICS<br />
MADE AT THREE SPECIFIC<br />
ENERGIES (1800, 3600, 7100 kJ/kg)<br />
Figure 20<br />
TYPICAL RECOVERY CURVE<br />
(POLYESTER, 1800 kJ/kg, 2.5%<br />
ADD-ON)<br />
Figure 21<br />
RECOVERY (%) VS %ADD-ON<br />
FOR DRY POLYESTER FABRICS<br />
MADE AT THREE SPECIFIC<br />
ENERGIES (1800, 3600, 7100 kJ/kg)<br />
Figure 22<br />
RECOVERY (%) VS %ADD-ON<br />
FOR DRY ACRYLIC FABRICS<br />
MADE AT TWO SPECIFIC<br />
ENERGIES (3600, 7100 kJ/kg)<br />
Figure 23<br />
RECOVERY (%) VS % ADD-ON<br />
FOR DRY COTTON FABRICS<br />
MADE AT THREE SPECIFIC<br />
ENERGIES (1800, 3600, 7100 kJ/kg)<br />
Figure 24<br />
EFFECT OF FABRIC WETTING ON<br />
RECOVERY FOR 7100 kJ/kg<br />
COTTON FABRIC<br />
<strong>Fibers</strong> were carded using a roller top card, cross-lapped on a jigger lattice cross lapper to achieve a final web basis weight <strong>of</strong><br />
50 g/m 2 . Webs <strong>of</strong> each fiber type were then hydroentangled (Honeycomb unit) in a second step at three energy levels (1800,<br />
3600 <strong>and</strong> 7100 KJ/kg) <strong>and</strong> dried. Next we used a Gaston County Foaming System in conjunction with a horizontal applicator<br />
<strong>and</strong> roll mechanism [8] to apply foam binder. Foam was generated <strong>and</strong> applied through a pressure applicator. A driven<br />
presser roll was used to force the foam to penetrate the substrate resulting in quantitative application.<br />
The foam mix consisted <strong>of</strong> water, acrylic latex binder <strong>and</strong> foaming agent. There were two critical requirements for a foam<br />
with adequate stability to achieve both uniform surface coating <strong>and</strong> adequate fabric penetration: 1) a foam half life in air <strong>of</strong> 4<br />
to 5 minutes achieved by controlling foaming agent concentration at 0.5 % bwt, <strong>and</strong> 2) a 10:1 blow ratio <strong>of</strong> air to liquid in the<br />
generator.<br />
Table 2<br />
EXPERIMENTAL DESIGN<br />
Specific<br />
Energy<br />
Fiber (kJ/kg.) % Add-on Binder Type<br />
Acrylic, Cotton, Polyester 1800 0, 1.25, 2.5, 5.0 Rhoplex(r) NW-1715<br />
Acrylic, Cotton, Polyester 3600 0, 1.25, 2.5, 5.0 Rhoplex(r) NW-1715<br />
Acrylic, Cotton, Polyester 3600 0, 1.25, 2.5, 5.0 Rhoplex(r) NW-1845<br />
Acrylic, Cotton, Polyester 7100 0, 1.25, 2.5, 5.0 Rhoplex(r) NW-1715<br />
Table 2 summarizes the experimental design. Because mechanism changes fiber to fiber were anticipated, a full statistical<br />
matrix was not used. To provide statistical significance, <strong>and</strong> to measure the degree <strong>of</strong> repeatability, a replicate set <strong>of</strong> samples<br />
was made at the 1.25, 2.5 <strong>and</strong> 5.0% add-on levels. A total <strong>of</strong> 36 replicate samples were made.<br />
Fabric breaking load, % elongation at maximum load, <strong>and</strong> the load at 5% strain were measured on an Instron 4400R using the<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
ASTM D-1682 strip tensile test method [9]. Each sample tested was <strong>of</strong> size 2.54 cm x 20.32 cm., speed <strong>of</strong> testing was 30.48<br />
cm/min, <strong>and</strong> gage length was fixed at 7.62 cm. Bending rigidity was measured by the Cantilever principle using ASTM<br />
D-1388-64 cantilever bending test [10]. The samples used were 2.54 cm x 20.32 cm. Abrasion resistance was measured on a<br />
Taber Abrasion Tester using ASTM D-3884-92 [11] st<strong>and</strong>ard abrasion test method. Four fabric samples, each 12.7 cm x 12.7<br />
cm dimensions, were tested. Two CS-10 abraders attached to 500 gm weight were used to abrade the samples. The vacuum<br />
level was kept constant at 100 mm <strong>of</strong> Hg for all samples. The abrasion resistance was measured as the number <strong>of</strong> cycles <strong>of</strong><br />
abrasion the fabric withstood until its surface was completely abraded.<br />
Wet <strong>and</strong> dry recovery tests were performed on the Instron. Sample size was 2.54 cm x 20.32 cm, the gage length was fixed at<br />
7.62 cm, <strong>and</strong> the strain rate was 400% per minute. Five samples <strong>of</strong> each fabric in the machine direction were stretched to 5%<br />
strain <strong>and</strong> were then relaxed at a rate <strong>of</strong> 400% per minute. Load vs. Strain (%) curves were then plotted for each fabric <strong>and</strong><br />
the recovery (%) was then calculated from the graph for each specimen by<br />
R= (R s /I s ) x 100 (1)<br />
Where:<br />
R = % Recovery<br />
R s = Recovered strain, %<br />
I s = Initial applied strain, %<br />
The ratio <strong>of</strong> machine direction (MD) <strong>and</strong> cross direction (CD) values for dependent variables which are direction sensitive<br />
(for example break strength <strong>and</strong> elongation) was nearly constant, <strong>and</strong> their response to the independent variables was<br />
consistent, so MD <strong>and</strong> CD values for these variables were averaged to simplify the analysis. Results from the two replicate<br />
data sets were statistically indistinguishable at the 5% level in the t-test so replicate <strong>and</strong> initial sets were further averaged to<br />
better display property trends.<br />
Results<br />
A. Stress / Strain Curves<br />
Figures 1-3 present the effect <strong>of</strong> binder addition on fabric MD stress strain curves for the intermediate level <strong>of</strong><br />
hydroentanglement energy for all three fibers. The effects illustrated were typical <strong>of</strong> all fabrics tested <strong>and</strong> exhibit:<br />
● increasing break strength with increasing binder level<br />
● decreasing break elongation with increasing binder level<br />
● a more erect strain curve with higher initial modulus at higher binder levels.<br />
These observations are all consistent with improved fiber bonding.<br />
B. Maximum Break Load<br />
<strong>Fibers</strong> differ in their ability to convert water jet energy into entangled fiber bonds <strong>and</strong> so binder free maximum break load<br />
differs greatly. For example, when 3600 kJ/kg is applied to polyester, cotton <strong>and</strong> acrylic fibers break loads for the fabrics<br />
were 48, 14 <strong>and</strong> 4N/2.54cm width respectively. Webs <strong>of</strong> acrylic fiber hydroentangled at 1800 kJ/kg acted more like<br />
unbonded bats than fabric, <strong>and</strong> were excluded from further analysis. Figures 4, 5 <strong>and</strong> 6 illustrate the effect <strong>of</strong> adding foam<br />
binder to the system. In general, the poorer the binder free hydroentanglement, the greater the relative improvement realized<br />
with foam bonding.<br />
Elongation at Maximum Load<br />
Elongation at maximum load in nonwovens is, in general, inversely related to maximum load carrying capacity. As indicated<br />
in Figures 7, 8 <strong>and</strong> 9 the change in elongation when low levels <strong>of</strong> binder are added is greatest for those fibers which are<br />
poorly bonded by hydroentangling.<br />
Load at 5% Strain<br />
The stress/strain curves <strong>of</strong> nonwovens are highly non-linear (Figures 1, 2 <strong>and</strong> 3) so the modulus is difficult to define. In this<br />
study, nearly all the fabrics had linear curves up to 5% strain, so comparison <strong>of</strong> load at this strain level should provide insight<br />
into fabric response to strains encountered in converting to the final commercial article.<br />
As indicated in Figures 10, 11 <strong>and</strong> 12 addition <strong>of</strong> extremely small levels <strong>of</strong> binder dramatically increases fabric initial<br />
modulus no matter how efficiently the fabric is hydroentangled in terms <strong>of</strong> break strength <strong>and</strong> elongation. This improvement,<br />
which ranges between 2 to 6X, has potential for improving fabric processability during the converting process.<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
E. Fabric Bending Rigidity<br />
Bending rigidity was used as a rough measure <strong>of</strong> fabric h<strong>and</strong>. Rigidity increased roughly proportionally with binder loading<br />
for all three fibers (Figures 13, 14 <strong>and</strong> 15). Therefore one expects that fabric h<strong>and</strong> will <strong>of</strong> necessity need to be traded for the<br />
beneficial improvements in tensile properties <strong>and</strong> abrasion resistance.<br />
Bending rigidity can also be estimated from tensile behavior using the classical equation:<br />
M = E I (2)<br />
Where M is the bending rigidity, E is the fabric Young's modulus, <strong>and</strong> I is the fabric moment <strong>of</strong> inertia, in this case a<br />
constant.<br />
Assuming that Young's modulus is proportional to load at 5% strain (L 5% ) we have:<br />
E =k 1 ( L 5% ) (3)<br />
where k 1 is a constant.<br />
So, the bending rigidity becomes:<br />
M = k 1 (L 5% ) (4)<br />
Figure 16, which contains plots all data points for all three fibers at all binder levels, confirms these assumptions. We<br />
believe, therefore, that a simple determination <strong>of</strong> load at 5% strain can be used to characterize bending rigidity, possibly with<br />
greater accuracy than the rather error prone direct measurement itself. Multiple R=0.95, R-square=0.90<br />
Fabric Abrasion Resistance<br />
Fabric abrasion effects are dominated by the presence <strong>of</strong> poorly bonded surface fibers which become entrapped in the<br />
abrading material, increase the intensity <strong>of</strong> the abrading surface, <strong>and</strong> lead to early fabric failure. Addition <strong>of</strong> extremely small<br />
amounts <strong>of</strong> binder provide a 1.8 to 2X improvement in fabric performance for all three fiber systems at all energy levels<br />
(Figures 17, 18 <strong>and</strong> 19). The mechanism appears to be one <strong>of</strong> reducing the number <strong>and</strong> length <strong>of</strong> poorly bonded surface<br />
fibers.<br />
Fabric Recovery from Small Strains<br />
In the course <strong>of</strong> processing from roll goods to finished article, nonwoven fabrics are subjected to small strains in machines<br />
which are much stronger than the fabric. To preserve dimensional stability it is desirable that all strain is recovered by the<br />
fabric. In fact, this is rarely the case. We studied this by straining our fabrics 5% <strong>and</strong> determining the amount <strong>of</strong> strain<br />
recovered as the load is reduced to zero. Figure 20 is a typical stress strain curve for such a trial.<br />
The addition <strong>of</strong> small amounts <strong>of</strong> binder to both polyester <strong>and</strong> acrylic fabrics significantly increased recovery (Figures 21<br />
<strong>and</strong> 22). In the case <strong>of</strong> polyester 2.5% binder increased recovered strain from about 60 to 85%. For acrylic fabrics the<br />
improvement was from 55 to 80%. Dimensional stability <strong>of</strong> both fabrics should therefore improve.<br />
The curious increase in load as strain is decreased from its maximum is a commonly observed effect having to do with a lag<br />
between the response time <strong>of</strong> the instrument force <strong>and</strong> strain measurements. This could be eliminated with slower strain rates<br />
or s<strong>of</strong>tware modifications taking into account the force measurement response time.<br />
The behavior <strong>of</strong> cotton was different. As indicated in Figure 23, strain recovery for binder-free cotton fabric was relatively<br />
good, particularly at the higher energy levels. Addition <strong>of</strong> binder did not provide the dramatic improvement encountered with<br />
the synthetic fibers.<br />
There is some evidence that this is a hydrogen bonding effect. First, raw cotton was used, <strong>and</strong> the recovery improved<br />
significantly between the two lowest energy levels suggesting that washing <strong>of</strong>f the natural finish oils caused the effect.<br />
Secondly, adding water, which breaks hydrogen bonds, reduced recovery from 80 to 70%, but insufficient trials were carried<br />
out to eliminate lubrication <strong>and</strong> water/binder interaction effects.<br />
The picture suggested is that bond sites are composed <strong>of</strong> three types <strong>of</strong> bonding:<br />
● frictional<br />
● chemical, from the resin<br />
● hydrogen, from the cotton.<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
Additional work aimed at elucidating this mechanism, as well as using small amounts <strong>of</strong> cotton, or other cellulosics in<br />
hydroentangled fabrics to enhance strain recovery, appears justified.<br />
Binder T g<br />
A two sample t-test with unequal variance was used to compare two binders, Rhoplex® NW-1715 <strong>and</strong> Rhoplex® NW 1845,<br />
at the intermediate 3600 kJ/kg hydroentanglement energy level. The t tests showed that the two binders were not statistically<br />
distinguishable for any <strong>of</strong> the dependent variables tested. We suspect that at these low binder levels, the modulus <strong>of</strong> the<br />
binder itself is less important than in saturation bonding at the 10 to 20% binder level.<br />
Discussion <strong>of</strong> Results<br />
Addition <strong>of</strong> small amounts <strong>of</strong> binder in foam form involves trading one physical property <strong>of</strong>f against another. In general,<br />
adding binder increases break strength, modulus, abrasion resistance <strong>and</strong> strain recovery at the expense <strong>of</strong> fabric stiffness <strong>and</strong><br />
elongation.<br />
Table 3<br />
SOME PROPERTY BALANCE CHOICES FOR HYDROENTANGLED POLYESTER NONWOVEN FABRICS<br />
Tensile Properties<br />
Break<br />
Abrasion<br />
Resistance<br />
Bending<br />
Specific Energy,<br />
Break Load Elongation Load at 5% Cycles To % Strain<br />
Rigidity<br />
kJ/kg % Binder N/2.54 cm (%) N/2.54 cm Failure Recovery<br />
mg-cm<br />
7100 0 48 82 0.4 77 78<br />
35<br />
1800 1.25 40 63 1.3 62 73<br />
79<br />
7100 1.25 61 74 3.0 140 77<br />
90<br />
7100 5.00 64 68 6.2 190 86<br />
290<br />
The trade<strong>of</strong>fs appear particularly interesting for the polyester fabric. Some typical property balances are presented in Table 3.<br />
In this case, hydroentaglement energy can be decreased by a factor <strong>of</strong> 4 <strong>and</strong> a satisfactory fabric obtained by adding as little<br />
as 1.25% binder. Further improved properties can be obtained at the expense <strong>of</strong> fabric rigidity by increasing either binder or<br />
energy.<br />
Table 4<br />
SOME PROPERTY BALANCE CHOICES FOR HYDROENTANGLED COTTON NONWOVEN FABRICS<br />
Tensile Properties<br />
Break<br />
Abrasion<br />
Resistance<br />
Bending<br />
Specific Energy,<br />
Break Load Elongation Load at 5% Cycles To % Strain<br />
Rigidity<br />
kJ/kg % Binder N/2.54 cm (%) N/2.54 cm Failure Recovery<br />
mg-cm<br />
7100 23 55 1.8 82 80<br />
82<br />
1800 1.25 7 67 0.5 20 71<br />
71<br />
7100 1.25 25 55 2.4 65 76<br />
120<br />
7100 5.0 28 51 5.0 120 78<br />
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170<br />
Table 5<br />
SOME PROPERTY BALANCE CHOICES FOR HYDROENTANGLED ACRYLIC NONWOVEN FABRICS<br />
Tensile Properties<br />
Break<br />
Abrasion<br />
Resistance<br />
Bending<br />
Specific Energy,<br />
Break Load Elongation Load at 5% Cycles To % Strain<br />
Rigidity<br />
kJ/kg % Binder N/2.54 cm (%) N/2.54 cm Failure Recovery<br />
mg-cm<br />
7100 0 34 76 0.4 35 56<br />
33<br />
3600 1.25 15 69 1.1 39 80<br />
75<br />
7100 1.25 45 64 1.9 67 --<br />
75<br />
7100 5.00 49 57 6.4 98 89<br />
300<br />
Similar property balance choices for cotton <strong>and</strong> acrylic are presented in Tables 4 <strong>and</strong> 5. Cotton is quite interesting in that low<br />
levels <strong>of</strong> binder provide less improvement than with the synthetic fibers. We suspect this is caused by hydrogen bonding.<br />
Summary <strong>and</strong> Conclusions<br />
The addition <strong>of</strong> binder to hydroentangled fabrics <strong>of</strong> polyester, cotton <strong>and</strong> acrylic significantly increases the break strength,<br />
load at 5% strain, abrasion resistance, <strong>and</strong> strain recovery, but the bending rigidity <strong>of</strong> the fabric increases. A synergistic effect<br />
<strong>of</strong> the two bonding mechanisms is greatest in fabrics that are poorly hydroentangled <strong>and</strong> have no possibility <strong>of</strong> hydrogen<br />
bonding. The effect <strong>of</strong> binder add-on tends to even out with well hydroentangled <strong>and</strong> hydrogen bonded fabrics. Fiber<br />
properties <strong>and</strong> type also play a significant role in the hydroentangling process; polyester hydroentangles very well while<br />
cotton <strong>and</strong> acrylic do not. The effect <strong>of</strong> binder choice on the properties was found not to be significant factor at these low<br />
add-on levels. A nonwoven manufacturer can use this experimental data to optimize end-use properties for his products by<br />
balancing the trade <strong>of</strong>fs between the several physical properties.<br />
References<br />
1. Sontara Spunlaced Fabric Finishing, Research Disclosure, No. 138, Oct., 1975 by Dupont.<br />
2. Properties <strong>and</strong> Processing: Sontara® Spunlaced <strong>Fabrics</strong> <strong>of</strong> 100% Polyester Fiber, DuPont Technical Information,<br />
Sontara® Spunlaced Fabric Bulletin SN-1, June 1979.<br />
3. Johns, M. M., <strong>and</strong> Auspos L. A., "The measurement <strong>of</strong> the Resistance to Disentanglement <strong>of</strong> Spunlaced <strong>Fabrics</strong>," INDA<br />
Technical Symposium, 158-173 (1979).<br />
4. Guenther, H. W., Barnes C. G., May R. E., <strong>and</strong> Riggins P. H., "Nexus® Spunlaced Formed <strong>Fabrics</strong>," Modern Textiles,<br />
40-48, (Dec. 1973).<br />
5. Brooks, B. A., Kennette J. W., <strong>and</strong> Buy<strong>of</strong>sky C. C., Lightly Entangled <strong>and</strong> Dry Printed Non Woven <strong>Fabrics</strong> <strong>and</strong> Methods<br />
for Producing the Same, U.S. Patent 4,623,575 issued to Chicopee, Nov. 18, 1986.<br />
6. Viazmensky, H., Richard C. E., <strong>and</strong> Williamson, J. E., Water Entanglement Process <strong>and</strong> Product, U.S. Patent 5,009747,<br />
issued to C.H. Dexter, April 23, 1991.<br />
7. Schortmann, W. E., Microsized Fabric, U.S. Patent 4,449,139, issued to The Kendall Company, February. 12, 1985.<br />
8. The CFS Foam Application, Patents Issued or Pending, (Personal Communication Gaston County Dyeing Machine<br />
Company), (1995).<br />
9. ASTM D 1682, Test Method for Breaking Load <strong>and</strong> Elongation <strong>of</strong> Textile <strong>Fabrics</strong>.<br />
10. ASTM D 1388-64, Test Methods for Stiffness <strong>of</strong> <strong>Fabrics</strong>.<br />
11. ASTM D 3884-92, St<strong>and</strong>ard Test Method for Abrasion <strong>of</strong> Textile <strong>Fabrics</strong> (Rotary Platform , Double Head Method)<br />
- INJ<br />
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Bonding <strong>of</strong> Spunlace <strong>Fabrics</strong><br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Fiberglass Surface<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Fiberglass Surface <strong>and</strong> Its Electrokinetic Properties<br />
By Daojie Dong, PhD, Senior Scientist,<br />
Owens Corning Science & Technology Center, Granville, Ohio<br />
Abstract<br />
The surface charge <strong>of</strong> fiberglass is an important variable for fiber dispersion <strong>and</strong> web formation in a wet-laid process. This<br />
paper presents an overview <strong>of</strong> the glass surface electrokinetic properties as well as their applications for improving the<br />
quality <strong>of</strong> wet-laid nonwovens through good fiber dispersion <strong>and</strong> uniform web formation. The paper addresses the basic<br />
concepts used in electrokinetic characterization <strong>of</strong> glass surface <strong>and</strong> briefly discusses the available techniques for zeta<br />
potential measurement.<br />
Introduction<br />
Wet-laid glass nonwovens, or wet-formed glass mat (WFGM), began appearing in the 1960s in small amounts. Rapid growth<br />
in the production <strong>of</strong> WFGM has occurred since ~1980 when it was introduced into glass-based ro<strong>of</strong>ing shingles. It is<br />
predicted that a moderate growth <strong>of</strong> the WFGM production will continue in the foreseeable future.<br />
The WFGM process primarily deals with the dispersion <strong>of</strong> fiberglass in white water <strong>and</strong> the subsequent formation <strong>of</strong> a glass<br />
web on a forming fabric while being de-watered. The electrokinetic properties (the term "electrokinetic" means the combined<br />
effect <strong>of</strong> motion <strong>and</strong> electrical phenomena) <strong>of</strong> a glass surface play an important role in fiber dispersion/web formation <strong>and</strong><br />
may directly contribute to the quality <strong>of</strong> WFGM.<br />
This paper presents an overview <strong>of</strong> the electrokinetic properties <strong>of</strong> glass surface <strong>and</strong> their applications for improving WFGM<br />
quality through good fiber dispersion <strong>and</strong> uniform web formation. The paper consists <strong>of</strong> two parts: part one discusses<br />
fundamentals <strong>of</strong> fiberglass surface <strong>and</strong> its electrokinetic properties as well as their effect on a colloidal system that contains<br />
fiberglass; <strong>and</strong> part two introduces available techniques for the measurement <strong>of</strong> zeta potential. Helpful references have been<br />
listed at the end <strong>of</strong> this article [1-7].<br />
Part I: ELECTROKINETIC PROPERTIES OF FIBERGLASS SURFACES<br />
Fiberglass/Water Interface <strong>and</strong> Electrical Double layer<br />
Bulk glass does not exhibit electrostatic charges. When brought into contact with water (in liquid or in air), however, glass<br />
surface generally exhibits net negative charge. The negative charges may originate from surface ionization <strong>and</strong> surface ion<br />
adsorption, etc.<br />
The net charges on a fiberglass surface influences the distribution <strong>of</strong> nearby ions in a polar medium: ions <strong>of</strong> opposite charge<br />
(called counter-ions) are attracted to the surface <strong>and</strong> ions <strong>of</strong> like-charge (called co-ions) are repelled away from the surface.<br />
Thermal motion is another factor that affects the distribution <strong>of</strong> charged species in the fiberglass/water interface region, <strong>and</strong><br />
tends to distribute charged species in a diffused manner. The overall effect <strong>of</strong> the electrostatic interaction <strong>and</strong> thermal motion<br />
results in an equilibrium distribution (Figure 1) <strong>of</strong> charged species in the interface region <strong>and</strong> forms a so-called electrical<br />
double layer (EDL).<br />
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Fiberglass Surface<br />
Figure 1<br />
ELECTRIC DOUBLE LAYER CONSISTS OF A<br />
CHARGED SURFACE AND A LAYER OF EXCESS<br />
COUNTER-IONS DISTRIBUTED<br />
IN A POLAR MEDIUM<br />
Figure 2<br />
STERN MODEL TREATS AN EDL AS A CHARGED<br />
SURFACE, A COMPACT LAYER (STERN LAYER) OF<br />
COUNTER-IONS HELD TIGHTLY TO THE SURFACE,<br />
AND A DIFFUSE LAYER OF IONS<br />
Figure 3<br />
pH EFFECT ON THE ZETA POTENTIAL OF BARE<br />
AND SIZED FIBERGLASS SURFACE. (ISOELECTRIC<br />
POINT IS THE pH AT WHICH ZETA POTENTIAL<br />
EQUALS TO ZERO.)<br />
In Figure 1 each "-" sign represents either a negative charge on the fiberglass surface or an anionic ion in the fluid phase, <strong>and</strong><br />
a "+" sign st<strong>and</strong>s for a positive charge on the surface or a cationic ion in the fluid phase. The "-" signs are predominant on the<br />
surface, indicating fiberglass surface is negatively charged. The bulk fluid far away from the surface will not "feel" the<br />
influence <strong>of</strong> surface charges, so it is electronically balanced. In between the negatively charged glass surface <strong>and</strong> the neutral<br />
bulk phase, there exists a layer <strong>of</strong> fluid that contains excess cationic ions (i.e. more cationic ions than anionic ions). Figure 1<br />
schematically shows that an electrical double layer consists <strong>of</strong> a charged surface <strong>and</strong> a layer <strong>of</strong> excess counter-ions<br />
distributed in a polar medium.<br />
There are several models that deal with the distribution <strong>of</strong> ions in an EDL <strong>and</strong> the magnitude <strong>of</strong> electrical potential near a<br />
charged surface. Helmholtz model [2] treats the EDL as "two sheets <strong>of</strong> charges:" a charged surface <strong>and</strong> a layer <strong>of</strong><br />
counter-ions that is held fixed to the surface. Gouy-Chapman model [8-10], as shown in Figure 1, treats the EDL as a<br />
charged surface plus a diffused layer (Gouy layer) <strong>of</strong> counter-ions. Stern-Graham model [11] is a combination <strong>of</strong> the two<br />
above <strong>and</strong> is widely accepted as the representation <strong>of</strong> the EDL structure.<br />
Figure 2 illustrates the Stern-Graham model: an EDL consists <strong>of</strong> a charged surface, a Stern layer (a compact layer <strong>of</strong><br />
counter-ions held tightly to the surface) <strong>and</strong> a diffuse layer <strong>of</strong> ions in a polar medium. While the thickness <strong>of</strong> the diffuse layer<br />
may vary widely, the Stern layer is typically very thin (approximately a monolayer).<br />
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Fiberglass Surface<br />
Surface Potential <strong>and</strong> Zeta Potential<br />
Figure 2 also introduces a concept <strong>of</strong> "shearing surface," which is similar to the term <strong>of</strong> "boundary layer" used in<br />
fluidynamics. For example, when a charged glass surface is moving in a medium (e.g. white water), a layer <strong>of</strong> medium<br />
(boundary layer) will attach to it <strong>and</strong> move with it. So this motion creates a shearing surface relative to the stagnant fluid<br />
phase (see schematic illustration in Figure 8 in Part II).<br />
Surface potential <strong>and</strong> zeta potential are two different concepts. In practice, however, zeta potential is <strong>of</strong>ten used as a<br />
"synonym" <strong>of</strong> surface potential. As shown in Figure 2, unequal distribution <strong>of</strong> electrical charges gives rise to an electrical<br />
potential across the interface region. The magnitude <strong>of</strong> electrical potential varies <strong>and</strong> depends on where it is measured.<br />
Surface potential is the electrical potential measured at the fiberglass surface, <strong>and</strong> the electrical potential determined at the<br />
shearing surface is termed as zeta potential.<br />
As the distance away from the charged surface increases, the electrical potential (magnitudeNote) decreases. The electrical<br />
potential decreases linearly across the Stern layer <strong>and</strong> gradually in the diffused layer. As shown in Figure 2, it is obvious that<br />
the magnitude <strong>of</strong> zeta potential is generally smaller than that <strong>of</strong> surface potential. In practice it is very difficult to directly<br />
measure the surface potential, while the zeta potential can be easily determined (see Part II). For the sake <strong>of</strong> convenience,<br />
people tend to use zeta potential as a "synonym" <strong>of</strong> surface charges, although they are different concepts.<br />
pH Effect <strong>and</strong> Isoelectric Point (IEP)<br />
Figure 3 shows the typical electrokinetic behavior <strong>of</strong> a bare glass surface <strong>and</strong> a sized glass surface. The zeta potential <strong>of</strong> glass<br />
surface is strongly affected by pH. The pH at which the zeta potential equals zero is termed "isoelectric point" (IEP). At the<br />
IEP, the shearing surface is neutralized, so the repulsion between fibers is minimized.<br />
Note: Fiberglass has a negatively charged surface <strong>and</strong> a negative electrical potential. For the matter <strong>of</strong> convenience, in this<br />
article, an "increase" (or "decrease") <strong>of</strong> electrical (zeta) potential means an "increase" (or "decrease") in the MAGNITUDE<br />
<strong>of</strong> electrical (zeta) potential, unless otherwise specified.<br />
Bare glass surface (Figure 3) has an IEP <strong>of</strong> ~2. Variation in glass composition may change it slightly. At pHs above 2, bare<br />
fiberglass has a negatively charged surface <strong>and</strong> its zeta potential is always negative. As pH is increased, the magnitude <strong>of</strong><br />
zeta potential <strong>of</strong> bare fiberglass increases.<br />
Practically, the zeta potential <strong>of</strong> fiberglass is <strong>of</strong> importance to its dispersability <strong>and</strong> to the stability <strong>of</strong> a colloidal system that<br />
contains glass fibers. For example, a zero or low (magnitude) zeta potential is needed in order (1) to efficiently pack wet<br />
glass fibers in a box for shipment or (2) to have a uniform web formation in the WFGM process. Bare glass has an IEP <strong>of</strong> ~2.<br />
At a low pH near 2, a strong acid condition, the fiber-fiber interactions can be minimized. However, there are lots <strong>of</strong><br />
disadvantages to operate the WFGM process at low pHs.<br />
Owens Corning uses <strong>and</strong> supplies sized fiberglass that has an IEP around neutral pHs to facilitate fiberglass h<strong>and</strong>ling <strong>and</strong><br />
glass web formation. Depending on the requirement for a particular process or the properties <strong>of</strong> a particular product, various<br />
sizing chemicals can be used to modify the electrokinetic properties <strong>of</strong> fiberglass.<br />
Interparticle Forces <strong>and</strong> Interparticle Potentials<br />
The electrokinetic behavior <strong>of</strong> fiberglass is <strong>of</strong> critical importance to the WFGM process. In general, there are four types <strong>of</strong><br />
interparticle forces that affect fiber-fiber <strong>and</strong> fiber-white water interactions: electrostatic, van der Waals, hard sphere, <strong>and</strong><br />
steric forces. The repulsive hard-sphere interactions become significant only when the two particles are getting very close to<br />
each other, therefore, are typically negligible in the case <strong>of</strong> WFGM process. The steric interactions certainly play a role due<br />
to the use <strong>of</strong> polymeric substances (in size formulation <strong>and</strong> in white water, e.g. polymeric viscosity modifier), but are also<br />
insignificant due to the relative large dimension <strong>of</strong> fiberglass (the diameter <strong>of</strong> fiberglass is much bigger than sub-micron<br />
colloidal particles). So, in the WFGM process, the fiber-fiber interactions are mainly determined by the overall balance <strong>of</strong> the<br />
van der Waals attraction <strong>and</strong> the electrostatic repulsion. Figure 4 schematically shows the potential energy versus the<br />
distance between two particles. Curve 1 is the electrostatic repulsion potential, Vr (Equation 1), curve 2 is the van der Waals<br />
attraction potential, Va (Equation 2) , <strong>and</strong> curve 3 is the net (total) potential energy, V (Equation 3). Since the van der Waals<br />
attractive potential (Equation 2) is predetermined for a given system, the electrostatic repulsion is the only factor that can be<br />
manipulated to vary the net potential energy between two fibers.<br />
Vr = f(s, S, D, 0, , b) [1]<br />
Va = f(s, S, D) [2]<br />
V = Va + Vr [3]<br />
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Fiberglass Surface<br />
where,<br />
s = particle size<br />
S = particle shape<br />
D = distance between two particles<br />
0 = surface potential<br />
= dielectric constant <strong>of</strong> the dispersing liquid<br />
b = thickness <strong>of</strong> EDL = 1/<br />
= Debye parameter<br />
For the purpose <strong>of</strong> simplicity, the repulsive potential (force) between<br />
glass fibers is directly affected by the value <strong>of</strong> zeta potential. The<br />
higher the magnitude <strong>of</strong> zeta potential, the more repulsive the fibers<br />
are. As a result, the glass fibers will be more repulsive to each other.<br />
This helps fiber dispersion, but hurts the web formation in the WFGM<br />
process. On the other h<strong>and</strong>, the lower the magnitude <strong>of</strong> zeta potential,<br />
the less repulsive the fibers are. As a result, the glass fibers tend to get<br />
closer to each other.<br />
WFGM Process: A Special Case<br />
As indicated in Equation 1, the electrostatic repulsive potential energy<br />
is a function <strong>of</strong> particle size, shape, surface potential, the effective<br />
thickness <strong>of</strong> EDL, the distance between two particles, <strong>and</strong> the<br />
dielectric constant <strong>of</strong> a dispersing liquid. In many cases there might be<br />
Figure 4<br />
no solutions at all. Fortunately, the input glass fibers for the WFGM<br />
INTERPARTICLE POTENTIALS<br />
process are relatively large (large fiber diameter compared to sub-micron colloidal particles) with a relatively thin EDL. By<br />
approximation, the electrostatic repulsion between glass fibers can be estimated by Equation 4. The van der Waals attractive<br />
potential energy (Equation 2) is a simple function <strong>of</strong> the size <strong>and</strong> shape <strong>of</strong> two particles <strong>and</strong> the distance between them. With<br />
a spherical approximation, the attraction potential energy can be simply calculated by Equation 5. Therefore, the net (total)<br />
potential energy ((Equation 6) between two glass fibers is the sum <strong>of</strong> Equations 4 <strong>and</strong> 5.<br />
Vr = 1/2 ( r 0 2 /D) ln (1+e -(D-r) k ) (4)<br />
Va = -Ar/12(D-r) (5)<br />
V= Vr + Va (6)<br />
where,<br />
A = Hamaker (van der Waals ) constant<br />
r = glass fiber radius<br />
D = distance between two fibers<br />
0 = surface potential<br />
= dielectric constant<br />
= Debye parameter = [8 e 2 N a I/1000 kT] 1/2<br />
e = 4.0803 x 10 -10 esu<br />
Na = 6.02 x 10 23 moles-1<br />
k = 1.38 x 10 -16 ergs/ o k<br />
T = temperature in o k<br />
I = ionic strength = 1/2 Z 2 i C i<br />
Z i = valence <strong>of</strong> ion i<br />
C i = molar concentration <strong>of</strong> ion i<br />
For a given fiber diameter, the attractive energy (Equation 5) is fixed. By varying the zeta potential (surface potential) <strong>of</strong><br />
fiberglass or the ionic strength <strong>of</strong> medium (e.g. white water), the repulsive energy (Equation 4) can be changed. As a result,<br />
the net potential (Equation 6), as schematically illustrated in Figure 5, can be changed.<br />
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Fiberglass Surface<br />
Conflict: Web Formation vs. Dispersion<br />
In the WFGM process, the dispersion <strong>of</strong> glass fibers in white water <strong>and</strong> the formation <strong>of</strong> a glass web in the forming zone are<br />
two conflicting concepts. To achieve good fiber dispersion, the fiber-fiber repulsion needs to be maximized. On the other<br />
h<strong>and</strong>, the fiber-fiber interactions need to be minimized in order to form a uniform glass web. Usually the solution is a<br />
compromise between the two.<br />
Generally, the author believes that the effect <strong>of</strong> electrokinetic properties on web formation is more critical than on fiber<br />
dispersion, <strong>and</strong> a good fiber dispersion can usually be achieved by the assistance <strong>of</strong> vigorous mechanical agitation <strong>and</strong><br />
hydrodynamic means. As shown in Figure 5, we believe that the WFGM process typically deals with the secondary<br />
minimum on the net potential energy curve. For instance, in order to achieve a good web formation for improving mat<br />
quality, we compress the EDL <strong>and</strong> reduce the zeta potential <strong>of</strong> fiberglass by applying sizing chemicals on the surface <strong>of</strong> input<br />
glass fibers <strong>and</strong> by using chemicals in white water. As a result, the repulsion barrier is reduced <strong>and</strong> the glass fibers can come<br />
closer to each other (trapped in the secondary minimum, a potential well). To disperse fibers in white water, mechanical<br />
agitation, in addition to sizing <strong>and</strong> white water chemistry, plays an important role to "pull" the fibers out <strong>of</strong> the relative<br />
shallow "potential well. "<br />
Figure 5<br />
NET (TOTAL) INTERFACE POTENTIAL AS A FUNCTION OF<br />
THE DISTANCE BETWEEN TWO FIBERS<br />
Figure 6<br />
FIBERGLASS ZETA POTENTIAL AS A<br />
FUNCTION OF pH<br />
(Non-specific adsorption <strong>of</strong> sizing chemicals<br />
reduces the magnitude <strong>of</strong> zeta potential. The<br />
isoelectric point stays the same.)<br />
Manipulating <strong>of</strong> Zeta Potential: Specific <strong>and</strong> Non-specific Adsorptions<br />
The aforementioned principles clearly indicate that the electrokinetic property <strong>of</strong> fiberglass is very important to a WFGM<br />
process. Logically, the next question is how to manipulate it for the ease <strong>of</strong> process <strong>and</strong> the quality <strong>of</strong> products. Although<br />
what additives to use <strong>and</strong> how much to use are kept secret by the fiberglass suppliers (sizing chemistry) <strong>and</strong> the WFGM<br />
producers (white water chemistry), it is generally understood that the addition <strong>of</strong> ionic surfactants (either low molecular<br />
weigh substances or polymers) is an effective mean to manipulate the zeta potential <strong>of</strong> fiberglass. To answer the question, in<br />
general, there are several means that can be used to vary the electrokinetic behavior <strong>of</strong> fiberglass, such as, (1) variation in pH,<br />
(2) non-specific adsorption <strong>and</strong> (3) specific adsorption <strong>of</strong> charged chemicals on the fiberglass surface, etc.<br />
In non-specific adsorption, charged species are "physically" attracted to a charged fiberglass surface, but not chemically<br />
bonded to it. In specific adsorption, the charged species are attracted <strong>and</strong> chemically bonded to the fiberglass surface. As a<br />
rule <strong>of</strong> thumb, (1) variation in pH <strong>and</strong> (2) non-specific adsorption (Figure 6) can change only the magnitude <strong>of</strong> zeta potential,<br />
the IEP <strong>of</strong> the fiberglass surface will stay the same. On the other h<strong>and</strong>, (3) specific adsorption (Figure 7) <strong>of</strong> charged species<br />
on the fiberglass surface may change not only the magnitude <strong>of</strong> its zeta potential, but also its sign (from negative to positive<br />
or from positive to negative) <strong>and</strong> IEP (usually moving to a higher pH).<br />
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Fiberglass Surface<br />
Figure 7<br />
FIBERGLASS ZETA POTENTIAL AS A FUNCTION OF<br />
pH<br />
(Specific adsorption <strong>of</strong> chemicals can change the magnitude<br />
<strong>and</strong> sign <strong>of</strong> zeta potential. It also effectively changes the<br />
IEP.)<br />
Figure 8<br />
THE PRINCIPLE OF ZETA POTENTIAL<br />
MEASUREMENT TECHNIQUES IS BASED ON A<br />
RELATIVE MOTION AT THE SHEARING SURFACE<br />
Adsorption (specific or non-specific) <strong>of</strong> various charged substances on a fiberglass surface is an effective mean to vary its<br />
electrokinetic properties, <strong>and</strong> specific adsorption is usually more effective than non-specific adsorption. The effect <strong>of</strong><br />
non-specific adsorption <strong>of</strong> charged chemicals is to "compress" the EDL, therefore, reducing the magnitude <strong>of</strong> zeta potential.<br />
As the concentration <strong>of</strong> charged species in a medium (sizing solution or white water) increases, the magnitude <strong>of</strong> fiberglass<br />
zeta potential will decrease (Figure 6). To obtain a very low magnitude <strong>of</strong> zeta potential at a given pH by non-specific<br />
adsorption, however, may have fundamental limits or may be very costly (a high concentration <strong>of</strong> charged species is needed).<br />
Also, as a general rule, the magnitude <strong>of</strong> zeta potential may approach zero, but non-specific adsorption does not change the<br />
IEP <strong>of</strong> fiberglass surface, nor the sign <strong>of</strong> its zeta potential.<br />
As shown in Figure 7, specific adsorption is very effective a mean to vary the electrokinetic properties <strong>of</strong> fiberglass surface.<br />
In specific adsorption, charged species (counter-ions) are chemically bonded to the fiberglass surface. When higher valence<br />
ions or a polymer that carries multiple charges are adsorbed on a fiberglass surface, it not only changes the fiberglass surface<br />
zeta potential, but also reverse the sign <strong>of</strong> its zeta potential <strong>and</strong> the value <strong>of</strong> its IEP (Figure 7). Therefore, specific adsorption<br />
is more effective <strong>and</strong> more flexible. By selecting proper charged chemical species <strong>and</strong> by controlling adsorption conditions,<br />
both the IEP <strong>and</strong> the magnitude <strong>of</strong> the zeta potential <strong>of</strong> a glass surface can be tailored for a good WFGM process. The<br />
mechanism that affects the rate <strong>of</strong> adsorption <strong>and</strong> the factors that affect <strong>of</strong> adsorption equilibrium are out <strong>of</strong> the scope <strong>of</strong> this<br />
article.<br />
The "variation in pH" alone plays a very limited role in terms <strong>of</strong> manipulating the WFGM process. Figure 3 (see the curve <strong>of</strong><br />
bare glass) does show that pH strongly affects the zeta potential <strong>of</strong> (bare) fiberglass. Without using any chemical additives,<br />
however, a low zeta potential can be achieved only at a low pH near 2. On the other h<strong>and</strong>, pH is an important control variable<br />
when sized glass fibers are used. In order to achieve a good web formation, for example, we want to operate the WFGM<br />
process at a pH near the IEP <strong>of</strong> sized fiberglass (usually a neutral pH, see Figure 7 or Figure 3 for the sized glass curve).<br />
Part II: ZETA POTENTIAL MEASUREMENT<br />
There are four types <strong>of</strong> techniques that can be used to measure zeta potential: microelectrophoresis, streaming potential,<br />
electro-osmosis, <strong>and</strong> sedimentation potential. Although the experimental setup, driving force, <strong>and</strong> calculation methods may<br />
vary widely, these four methods are all based on a same principle: a relative motion (Figure 8) between the charged surface<br />
<strong>and</strong> the part <strong>of</strong> electrical double layer that is sheared <strong>of</strong>f from the charged surface. A brief description about each method is<br />
given as follows <strong>and</strong> is also summarized in Table 1.<br />
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Fiberglass Surface<br />
Table 1<br />
METHODS FOR ZETA POTENTIAL MEASUREMENT<br />
Driving<br />
Stationary Moving Sample<br />
Methods Force Potential Phase Phase Preparation<br />
Microelectrophoresis electrical field applied liquid solid dispersed<br />
particles<br />
Electro-Osmosis electrical field applied solid liquid porous plug<br />
Streaming Potential pressure induced solid liquid porous plug<br />
Sedimentation Potential gravity induced liquid solid dispersed<br />
particles<br />
1. Microelectrophoresis - An applied electrical potential causes charged particles to move through a continuous liquid phase.<br />
Mobility (migration velocity) <strong>of</strong> the charged particles is measured <strong>and</strong> zeta potential is calculated based on its relation to the<br />
mobility.<br />
2. Streaming Potential - An applied pressure head forces a continuous liquid phase to flow past a charged solid phase<br />
(porous plug) <strong>and</strong> a streaming potential is created due to the motion <strong>of</strong> liquid phase in relation to the charged solid. Streaming<br />
potential is measured <strong>and</strong> zeta potential is calculated based on its relation to the streaming potential.<br />
3. Electro-osmosis - An applied electrical potential causes a continuous liquid phase to flow past a charged solid phase<br />
(porous plug). The volumetric flow rate is measured <strong>and</strong> zeta potential is calculated based on its relation to the capillary flow<br />
rate.<br />
4. Sedimentation Potential - Gravitational force causes charged particles to settle <strong>and</strong> a sedimentation potential is created<br />
due to the motion <strong>of</strong> charged particles in relation to the stationary liquid phase. The sedimentation potential is measured <strong>and</strong><br />
zeta potential is calculated based on its relation to the sedimentation potential.<br />
Lab Zeta Potential Measurement<br />
Both microelectrophoresis <strong>and</strong> streaming potential methods have been successfully used in lab zeta potential measurement,<br />
<strong>and</strong> each has some advantages <strong>and</strong> disadvantages. Microelectrophoresis measures charged particles, which are first<br />
suspended in a liquid, then filled into a flat rectangular measuring cell. A pair <strong>of</strong> electrodes are connected to the opposite<br />
ends <strong>of</strong> the sample cell. Under the influence <strong>of</strong> an applied electrical field, the suspended particles will move toward an<br />
appropriate electrode. The particle mobility (migration velocity) is measured, then, the zeta potential can be calculated<br />
(Equation 7).<br />
The method is reliable because the fundamentals are well understood <strong>and</strong> theoretical calculation is well developed.<br />
Practically, it is a very good method for the characterization <strong>of</strong> particle/powder materials. However, it is not convenient for<br />
characterization <strong>of</strong> fiber or fabric materials. For example, glass fibers have to be grounded or crushed before it can be<br />
measured. When sized fibers are grounded to particles, the exposed new surface (bare surface) may be quite different from<br />
the sized surface.<br />
= U / E [7]<br />
= 4 E s + 2 s /R)/ P [8]<br />
where<br />
= zeta potential<br />
U = mobility (migration velocity)<br />
= kinematics viscosity <strong>of</strong> the fluid<br />
E = applied electrical field strength<br />
= dielectric constant <strong>of</strong> the fluid<br />
P = pressure head<br />
E s = streaming potential<br />
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Fiberglass Surface<br />
= specific conductivity <strong>of</strong> the fluid<br />
s = specific conductivity <strong>of</strong> the surface<br />
R = radius <strong>of</strong> capillary<br />
Streaming potential method directly measures fiber (or fabric) surface, which are packed into a cylindrical tube. A pump<br />
(pressure head) forces an electrolyte solution to flow through the fiberglass pack (porous plug). Consequently, the flow<br />
induces a streaming potential across the sample pack. The streaming potential is measured with a pair <strong>of</strong> electrodes placed at<br />
the opposite ends <strong>of</strong> fiberglass pack, recorded with a potentiometer, <strong>and</strong> used to calculate the zeta potential (Equation 8). It is<br />
certainly an advantage that the zeta potential <strong>of</strong> fiber surface (bare or sized) can be directly measured. Streaming potential<br />
method, however, also has some disadvantages. For instance, the reproducibility <strong>of</strong> fiberglass pack is a concern, <strong>and</strong> a more<br />
vigorous theoretical correction for the effect <strong>of</strong> surface conductivity is needed to improve the accuracy <strong>of</strong> streaming potential<br />
method.<br />
In-Line Zeta Potential Measurement<br />
In general, there is no in-line version instrument available for the WFGM process at this time. Recently a couple <strong>of</strong> in-line<br />
zeta potential measurement instruments have been developed for paper mills. But, they are not applicable for the WFGM<br />
process, due to their limits either in measurable slurry consistencies or in manageable fiber lengths, etc.<br />
References<br />
1. Dong, D., et al, Tappi 79(7), 191(1996).<br />
2. Rosen M. J., "Surfactants <strong>and</strong> Interfacial Phenomena," 2nd edition, John Wiley & Son, New York, 1989.<br />
3. Adamson, A. W., "Physical Chemistry <strong>of</strong> Surface (4th edition)," Wiley-Interscience, New York, 1982.<br />
4. Hiemenz P. C., "Principle <strong>of</strong> Colloid <strong>and</strong> Surface Chemistry," Marcel Dekker, New York, 1986.<br />
5. Shaw D. J., "Introduction to Colloid <strong>and</strong> Surface Science (3rd edition)," Butterworths, London, 1980.<br />
6. Matijevic, E. Et al, J. Physical Chemistry, 65, 826 (1961).<br />
7. James R. O. <strong>and</strong> Healy T. W., J. Colloid <strong>and</strong> Interface Science, 40(1), 53 (1972).<br />
8. Chapman D. L., Philos. Mag., 25, 475 (1913).<br />
9. Gouy G. J., J. Phys, 9, 457(1910).<br />
10. Gouy G. J., Ann. Phys., 7, 129 (1917).<br />
11. Stern O. Z., Electrochemistry, 30, 508 (1924).<br />
Acknowledgments<br />
The author would like to thank Dr. Kathryn Br<strong>and</strong>enburg, leader <strong>of</strong> the Composites <strong>Engineered</strong> Fiber Structures COE at the<br />
Owens Corning Science <strong>and</strong> Technology Center, Granville, OH, for supporting the preparation <strong>and</strong> publication <strong>of</strong> this work.<br />
—INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Monitoring Of Dynamic Forces<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Applications Of On-Line Monitoring Of Dynamic Forces<br />
Experienced By Needles During Formation Of Needled<br />
<strong>Fabrics</strong><br />
By Abdelfattah M. Seyam, Nonwovens Cooperative Research Center, College <strong>of</strong> Textiles, North Carolina<br />
State University, Raleigh, North Carolina, USA<br />
Abstract<br />
The significance <strong>of</strong> a recently developed system that measures dynamic forces experienced by individual<br />
needles during formation <strong>of</strong> needlepunched fabrics is demonstrated. The system design, coupled with a<br />
new signal analysis technique allows measurement <strong>of</strong> peak penetration <strong>and</strong> stripping forces as well as the<br />
penetration <strong>and</strong> stripping energies due to needle/fiberweb interaction. Systematic experimental<br />
investigations were conducted to determine the critical locations in the needle board where needles<br />
experience the highest forces, <strong>and</strong> correlate needle force parameters to fabric performance.<br />
The research results, supported by statistical analysis, show there is a strong relationship between needle<br />
penetration energy <strong>and</strong> fabric properties. Additionally, the needling density significantly impacts the<br />
location <strong>of</strong> maximum penetration forces.<br />
Introduction<br />
The needlepunching industry was once considered a "waste products" industry, but has now successfully<br />
established itself in numerous first quality markets. Recently, Smith [10] listed eighteen markets <strong>of</strong><br />
needlepunched products. These include: automotive (headliner, door trim, etc.), filtration, furniture <strong>and</strong><br />
bedding, geotextiles, ro<strong>of</strong>ing, aerospace (shuttle tiles, brake pads, etc.), agriculture, advanced composites,<br />
industrial (belting, roller linings, etc.), insulators, marine, medical (blood filters, b<strong>and</strong>ages, etc.), paper<br />
making felts, protective clothing, sports felts (floor covering, tennis ball covers, etc.), synthetic<br />
leather/shoes, wall coverings, <strong>and</strong> miscellaneous (carpet underlay, car wash brushes, oil sorbents, <strong>of</strong>fice<br />
products, etc.).<br />
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The success <strong>of</strong> the industry can be attributed to low manufacturing cost <strong>and</strong> the flexibility <strong>of</strong> the<br />
needlepunching technology to tailor products to meet a variety <strong>of</strong> end use requirements. The increasing<br />
dem<strong>and</strong> for needled fabrics prompted machine manufacturers to construct high-speed/high performance<br />
needle looms. Today's needle looms are capable <strong>of</strong> running at speeds <strong>of</strong> up to 3,000 strokes/min. with<br />
working width <strong>of</strong> up to 15 meters. A parallel effort has been pursued by needle manufacturers to produce<br />
high performance needles. Needles are engineered with numerous design parameters in attempts to<br />
obtain needled fabrics with desired properties to meet end use requirements. These parameters include:<br />
number <strong>of</strong> barbs, barb spacing, needle gauge, kick-up size <strong>and</strong> needle shape.<br />
Historically, William Bywater <strong>of</strong> Leeds, Engl<strong>and</strong> [1] manufactured the first commercial needle machine<br />
in the late 1800's; however, scientific research was not published until the 1960's. The published research<br />
has targeted three areas:<br />
●<br />
●<br />
●<br />
Experimental work to study the influence <strong>of</strong> processing <strong>and</strong> fiber parameters on needled fabrics<br />
properties,<br />
Approaches to model the tensile behavior <strong>of</strong> needled fabrics, <strong>and</strong><br />
Developing devices to measure forces acting on needles.<br />
Recently Sarin, Meng <strong>and</strong> Seyam [6] published a review <strong>of</strong> previous work on needle force<br />
measurements. They found that the previous work was either performed statically using multiple needles<br />
or dynamically at low speed using both single <strong>and</strong> multiple needles. These techniques are incapable <strong>of</strong><br />
providing the accurate information important to needle manufacturers, machine producers <strong>and</strong> fabric<br />
producers. Dem<strong>and</strong> exists for a system capable <strong>of</strong> measuring needle forces during high-speed needling.<br />
Seyam, Meng <strong>and</strong> Mohamed have developed recently such system [7] that is briefly described later in<br />
this paper.<br />
While the previous studies provided basic underst<strong>and</strong>ing, the results <strong>and</strong> conclusions <strong>of</strong> such studies are<br />
valid only for the experimental range used. Moreover, the studies were conducted using small machines<br />
producing narrow fabrics at low needling speed. The applicability <strong>of</strong> such findings to an industry that<br />
uses today's high-speed needle looms producing wide fabrics is questionable. Additionally, in a research<br />
environment, an experiment is <strong>of</strong>ten run for extremely short time. In industry, however, the continuous<br />
processing <strong>of</strong> fabrics causes needle wear <strong>and</strong>, as a result, fabric properties may be significantly deviate<br />
from the desired levels.<br />
There is relatively limited literature regarding the modeling <strong>of</strong> fabric performance; only two publications<br />
have been identified. The first was published by Hearle <strong>and</strong> Sultan [2] showing an approach to<br />
theoretical underst<strong>and</strong>ing <strong>of</strong> tensile behavior <strong>of</strong> needled fabrics. The other publication, by Ji [3],<br />
developed a model to predict the entire load-extension behavior <strong>of</strong> needled fabrics. While his work is an<br />
improvement, the theoretical model <strong>and</strong> experimental results did not significantly agree. This is due to<br />
the assumptions used to develop the model in order to facilitate the prediction. Needled fabrics are<br />
complex structures that are very difficult to model. It would be extremely beneficial to the industry to<br />
develop an on-line technique that is capable <strong>of</strong> monitoring <strong>and</strong> controlling <strong>of</strong> fabric properties while the<br />
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fabrics are being produced. Our research team at the Nonwoven Cooperative Research Center undertook<br />
research efforts to accomplish this goal, developing a new system that measures dynamic forces<br />
experienced by individual needles during formation <strong>of</strong> needlepunched fabrics.<br />
Needle Force Measurement System<br />
Figure 1 shows the components <strong>of</strong> the needle force measurement system developed by Seyam, Meng <strong>and</strong><br />
Mohamed [7]. The force data could be collected from nine different instrumented needles located in the<br />
machine <strong>and</strong> cross machine directions (Figure 2).<br />
The NCRC needle force measurement system consists <strong>of</strong> force transducers in washer form, signal<br />
conditioner, data acquisition hardware <strong>and</strong> s<strong>of</strong>tware, <strong>and</strong> data analysis s<strong>of</strong>tware. These, along with<br />
possible applications <strong>of</strong> the system are fully explained in previous publications [5-9].<br />
Figure 1<br />
FORCE MEASUREMENT SYSTEM<br />
Figure 2<br />
LOCATIONS OF THE FIVE-INSTRUMENTED<br />
NEEDLES IN THE NEEDLE BOARD<br />
Signal Analysis<br />
Using signal analysis, we developed a technique to extract useful information from force data collected<br />
on-line [8]. The signal analysis procedure involves data filtration using low frequency pass filter in order<br />
to filter out vibration. Then the filtered data is processed to subtract the forces exerted on the needles due<br />
to inertia. The remaining forces are those due to needle/fiberweb interactions. From this data, needle<br />
penetration <strong>and</strong> stripping forces as well as energies can be deduced. Figure 3 shows the superimposition<br />
<strong>of</strong> the filtered data for total forces (solid line) <strong>and</strong> the inertia forces (dotted line) for several needling<br />
cycles. The solid line ABCDEF represents the total force experienced by an instrumented needle, while<br />
the dotted line ABCD'F represents the inertia forces. The solid portion CD represents the data <strong>of</strong> the<br />
penetrating forces experienced by the needle during the downward movement <strong>of</strong> the needle board. Point<br />
D is the peak penetration force corresponding to the highest pressure the needle experiences from the<br />
fiberweb. During the portion DE, the pressure on the needle is reduced due to the upward movement <strong>of</strong><br />
the needle board. The pressure reaches zero at the point where DE intercepts the dotted line. Beyond the<br />
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interception point, the needle is subjected to stripping forces as a result <strong>of</strong> its withdrawal from the<br />
fiberweb.<br />
Figure 3<br />
SUPERIMPOSITION OF TOTAL AND<br />
INERTIA FORCES IN TIME DOMAIN<br />
Figure 4<br />
NET NEEDLE FORCES DUE TO FIBERWEB<br />
RESISTANCE<br />
From Figure 3 one can notice that the total forces (solid line) <strong>and</strong> the inertia forces (dotted line) are<br />
identical during half cycle or at least during quarter cycle AB. This feature allows modeling <strong>of</strong> the whole<br />
inertia cycle ABC'D'F as a sinusoidal function. Subtraction <strong>of</strong> inertia forces from total forces gives the<br />
net forces that the needle experienced due to penetration <strong>of</strong> <strong>and</strong> withdrawal from the fiberweb (Figure 4).<br />
From the net force data <strong>of</strong> Figure 4 <strong>and</strong> the time-displacement data <strong>of</strong> the needle board, penetration <strong>and</strong><br />
stripping energies can be determined.<br />
Applications <strong>of</strong> the Needle Force Measurement System<br />
In this section, the experimental procedures <strong>and</strong> results are given for two applications <strong>of</strong> the system:<br />
Determination <strong>of</strong> the critical locations in the needle board at which needles experience the highest forces,<br />
<strong>and</strong> correlation <strong>of</strong> needle force parameters with fabric performance. For both applications, the force data<br />
were acquired from five instrumented needles (marked 1 through 5, Figure 2). The data was recorded<br />
simultaneously for each needle at a rate <strong>of</strong> 1,000 observations/sec.<br />
Correlation Between Force Parameters <strong>and</strong> Fabric Performance<br />
Experimental<br />
For this part <strong>of</strong> the study a total <strong>of</strong> sixteen needled fabrics were produced representing a full experimental<br />
design (4 levels <strong>of</strong> weight x 4 levels <strong>of</strong> needling density). For each fabric, three sets (replicates) <strong>of</strong> force<br />
data were collected at different times. For each set, force data <strong>of</strong> 150 needling cycles per instrumented<br />
needle were collected by the force measurement system. The fabrics were comprised <strong>of</strong> polypropylene<br />
fibers produced at 76.2 mm fiber length <strong>and</strong> 10 denier/filament. <strong>Fabrics</strong> were produced using carding <strong>and</strong><br />
cross-lapping prior to needling. More details are published elsewhere by Kim <strong>and</strong> Seyam [4]. The<br />
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properties (responses) selected for this study are tensile <strong>and</strong> tear resistance. Statistical Analysis System<br />
(SAS) was used to develop regression equations correlating needle penetration energy to needled fabric<br />
performance.<br />
Calculation <strong>of</strong> Penetration Energy<br />
The penetration energy (J/cm 2 ) was obtained by integrating the area under the curve <strong>of</strong> net needle force<br />
due to fiberweb resistance (Figure 4) combined with needle board displacement <strong>and</strong> the needling density.<br />
For each fabric the data was averaged over 2,250 needling cycles (3 replicates x 5 needles x 150 cycles)<br />
<strong>and</strong> used as an estimate for the energy expended to bond the fabric.<br />
Figure 5<br />
BREAKING ENERGY VS. PENETRATION<br />
ENERGY<br />
Figure 6<br />
PREDICTED TEAR STRENGTH VS.<br />
PENETRATION ENERGY<br />
Results <strong>and</strong> Discussion<br />
For each <strong>of</strong> the experimental run, the force data was fed into a computer, which calculated the<br />
penetration energy. Figures 5 <strong>and</strong> 6 show the predicted relationships between needling energies <strong>and</strong><br />
needled fabric performance as well as the correlation for each with the experimental data. The symbols<br />
<strong>of</strong> the predictive equations shown in Figures 5 <strong>and</strong> 6 are defined as follows:<br />
BE = Tensile Breaking Energy, J<br />
PE = Needling Penetration Energy, J/cm 2<br />
TS = Tear Resistance, N<br />
W = Needled Fabric Basis Weight, g/m 2<br />
Figure 5 depicts the relationship between needling energy <strong>and</strong> the energy required breaking the fabrics in<br />
tensile mode. The experimental data <strong>and</strong> the predictive equation <strong>of</strong> Figure 5 indicate that the relationship<br />
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between penetration energy <strong>and</strong> breaking energy is linear with high correlation coefficient (R2=0.9018).<br />
Figure 6 shows the predictive equation <strong>of</strong> the needling energy <strong>and</strong> the tear resistance <strong>of</strong> the needled<br />
fabrics. Unlike the breaking energy, tear resistance is impacted significantly by fabric basis weight. For a<br />
given weight, increasing the penetration energy (needling density) reduces the tear resistance. This can<br />
be explained by the decrease in the degree <strong>of</strong> fiber mobility with the increase in the penetration energy<br />
(due to increase in fiber interlocking with needling density). The high degree <strong>of</strong> fiber interlocking hinders<br />
the fiber movement to the delta zone during tear tests. Consequently, fewer fibers move to delta zone to<br />
share the load from the tear stresses. The high correlation coefficients (R2 = 0.9754) <strong>of</strong> the predictive<br />
equation <strong>of</strong> Figure 6 indicates that the needling energies <strong>and</strong> fabric weight are highly correlated to<br />
needled fabric tear resistance. It must be noted that this strong linear correlation should only be applied in<br />
the range over which the data was measured. Significant non-linearity is expected at very low needle<br />
densities.<br />
Figure 7<br />
PEAK PENETRATION FORCE IN TERMS OF<br />
NEEDLE LOCATION AND NEEDLING<br />
DENSITY. FABRIC WEIGHT = 260 G/M 2 ,<br />
NUMBER OF BARBS = 9<br />
Figure 8<br />
PEAK PENETRATION FORCE IN TERMS<br />
OF NEEDLE LOCATION AND NEEDLING<br />
DENSITY. FABRIC WEIGHT= 650 G/M 2 ,<br />
NUMBER OF BARBS = 9<br />
Significance<br />
The high correlation between fabric properties <strong>and</strong> penetration energies means that this technique can be<br />
used to predict <strong>and</strong> control the fabric properties while the fabrics are being produced. A computer<br />
algorithm can be developed for these on-line estimates through the predictive equations.<br />
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Determination <strong>of</strong> the Critical Locations In The Needle<br />
Board At Which Needles Experience The Highest<br />
Force<br />
Experimental<br />
To determine the locations where needles experience the<br />
highest penetration forces, a series <strong>of</strong> runs were performed<br />
on 60 cm wide Dilo loom using carded <strong>and</strong> cross-lapped<br />
fiberwebs. The fiber webs were produced from<br />
polypropylene fibers with 76.2 mm fiber length <strong>and</strong> 10<br />
denier/filament. A full experimental design (4 levels <strong>of</strong><br />
weight x 4 levels <strong>of</strong> needling density x 5 levels <strong>of</strong> needle<br />
location) was conducted. Each run was replicated three<br />
times. For each run, force data <strong>of</strong> 150 needling cycles per<br />
Figure 9<br />
LOCUS OF THE MAXIMUM PEAK<br />
PENETRATION FORCE<br />
instrumented needle were collected by the force measurement system. The key parameter <strong>of</strong> interest here<br />
is the peak penetration force due to fiberweb resistance that is developed after a certain number <strong>of</strong><br />
strokes (cycles <strong>of</strong> Figure 4). Again, SAS was used to develop regression equations relating peak needle<br />
penetration force to needle location, fabric weight <strong>and</strong> needling density.<br />
Results <strong>and</strong> Discussion<br />
Figures 7 <strong>and</strong> 8 show the predicted peak penetration forces as influenced by needling density, needle<br />
location <strong>and</strong> fabric weight. In these figures, the needle location represents the distance from the first row<br />
in the needle board at the feed side. Therefore, location = 0 cm indicates the first needle row where the<br />
fiberweb starts to receive needling. At location = 18 cm, the fiberweb received the target needling density<br />
(last needle row).<br />
It can be noticed from Figures 7 <strong>and</strong> 8 that the peak force increases with location up to a certain<br />
maximum value after which the peak penetration force decreases. Additionally, the maximum peak<br />
penetration force is dependent on the level <strong>of</strong> needling density. The location <strong>of</strong> the maximum moves<br />
toward the feed side as the needling density increases <strong>and</strong> toward the delivery side as the needling<br />
density decreases. The results indicate there may be several phenomena at play; their relative force<br />
contributions being dependent on the level <strong>of</strong> fiberweb integrity. Details <strong>of</strong> these force contributions are<br />
not yet understood but are postulated to include the following effects:<br />
●<br />
●<br />
●<br />
At locations near the feed side the fiberweb is bulky, which leads to frictional forces for the<br />
needles penetrating due to long contact length between fiberweb <strong>and</strong> needles. Additionally, the<br />
number <strong>of</strong> fibers caught by needle barbs at the feed side is higher compared to the delivery side.<br />
As bonding progresses, fibers become more entangled <strong>and</strong> the fiberweb is more consolidated.<br />
Thus, the fibers are more trapped in the fiberweb, resulting in an increased force contribution <strong>of</strong> a<br />
fiber caught by a needle.<br />
As the web advances to the delivery side, it receives more punches that cause fiber breakage.<br />
Consequently, the broken fibers contribute less to the needle forces.<br />
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●<br />
Additionally, as the web advances to the delivery side <strong>and</strong> the web is more consolidated, each<br />
needle tends to engage fewer fibers.<br />
Additional results similar to these <strong>of</strong> Figures 7 <strong>and</strong> 8 using other types <strong>of</strong> needles are published<br />
elsewhere [5].<br />
Figure 9 shows a generalized version <strong>of</strong> the needling density distribution that the web receives at<br />
different locations <strong>of</strong> the needle board. The four straight lines represent the needling density distribution<br />
<strong>of</strong> different target needling densities (50, 70, 90 <strong>and</strong> 110 punches/cm 2 ). Based on the above discussion on<br />
the effect <strong>of</strong> the needling density on the location <strong>of</strong> the maximum peak force, one would assume that the<br />
maximum would take place at a certain critical needling density. This means that a line as shown in<br />
Figure 9 can represent the locus <strong>of</strong> the maximum. The intercepts <strong>of</strong> this line with the four lines<br />
representing the needling density distribution determine the location <strong>of</strong> the maximum peak penetration<br />
force. Our results show however, that this locus is not necessarily a straight line, in fact the locus could<br />
assume a general line or curve. Irrespective <strong>of</strong> the exact shape <strong>of</strong> the critical line, the reason why the<br />
location <strong>of</strong> the maximum peak force varies with needling density is clear. The maximum peak force is<br />
strongly dependent on the total number <strong>of</strong> punches encountered by the web as it progresses through the<br />
needle loom.<br />
Significance <strong>of</strong> Locating The Position Of Maximum Peak Force<br />
Needle Rotation Technique<br />
To maximize needle utilization, fabric producers developed methods to rotate the needles in the needle<br />
board after a given number <strong>of</strong> needling cycles. This is done since the needles are subjected to different<br />
forces, <strong>and</strong> hence different wear levels, depending on their location in the needle board. The rotation<br />
supposes to equalize the needle wear. Each needled fabric producer developed different techniques <strong>of</strong><br />
needle rotation based on experience. Thus, the needle rotation is considered as an art rather than science.<br />
To base this on science, needles should be rotated based on the force distribution <strong>of</strong> Figures 7 <strong>and</strong> 8.<br />
Needles in the rows where the force is high should be moved to locations <strong>of</strong> low forces.<br />
The force measurement system, therefore, could rationalize the needle rotation process.<br />
Needle Design<br />
Another significant benefit <strong>of</strong> the determination <strong>of</strong> the needle force distribution is needle design. Needle<br />
manufacturers can make use <strong>of</strong> the results to design needles to withst<strong>and</strong> the high stress positions <strong>and</strong><br />
thereby avoid excessive needle breakage during fabric formation. Alternatively, this underst<strong>and</strong>ing may<br />
allow the strongest (<strong>and</strong> presumably most expensive) needles to be mounted in positions <strong>of</strong> highest<br />
stress.<br />
The industry benefit would be production <strong>of</strong> high quality needled fabrics at high efficiency.<br />
Conclusion<br />
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Our research findings showed that the force measurement device coupled with signal analysis have<br />
significant benefits to needled fabric producers as well as needle manufacturers. The high correlation<br />
found between needle force parameters <strong>and</strong> fabric properties can be used to on-line monitor the needled<br />
fabric properties to ensure the produced fabrics are within the specified requirements. The location <strong>of</strong> the<br />
maximum needle forces is essential for fabric producers to rationalize the needle rotation technique in<br />
order to maximize the needle utilization. Additionally, needle producers can make use <strong>of</strong> the information<br />
in designing high performance needles.<br />
Acknowledgment<br />
This work was supported by the Nonwovens Cooperative Research Center, which is funded by the<br />
National Science Foundation, the State <strong>of</strong> North Carolina, <strong>and</strong> Industry Members.<br />
Reference<br />
1. Foster, J.H., "Needlepunching - Past, Present <strong>and</strong> Future," INDA-TEC '88 209 (1988)<br />
2. Hearle, J.W.S., <strong>and</strong> Sultan, M.A.I., "Study <strong>of</strong> Needled <strong>Fabrics</strong>, Part V: The approach to theoretical<br />
underst<strong>and</strong>ing," J. Text. Inst., 59, 183 (1968).<br />
3. Ji, Y., Tensile Properties <strong>of</strong> Needlepunched Nonwoven <strong>Fabrics</strong>, Ph. D. Thesis, North Carolina State<br />
University, 1992.<br />
4. Kim, H. <strong>and</strong> Seyam, A.M., Needle Force Parameters/Needled Fabric Performance Relationships,<br />
Proceedings <strong>of</strong> the INDA International Needlepunch Conference, Charlotte, NC, October, 1998.<br />
5. Kim, H., Study <strong>of</strong> Needlepunching Process <strong>and</strong> Products, Ph. D. Thesis, North Carolina State<br />
University, 1998.<br />
6. Sarin, S., Meng, J., <strong>and</strong> Seyam, A. M., "Mechanics <strong>of</strong> Needlepunching Process <strong>and</strong> Products, Part I:<br />
Critical Review <strong>of</strong> Previous Work on Forces Experienced by Needles during Needling <strong>of</strong> Nonwoven<br />
<strong>Fabrics</strong>," International Nonwovens J., 6, 32 (1994).<br />
7. Seyam, A.M., Meng, J., <strong>and</strong> Mohamed, A., "Mechanics <strong>of</strong> Needlepunching Process <strong>and</strong> Products, Part<br />
II: An On-Line Device to Measure the Punching Forces Experienced by Individual Needles,"<br />
International Nonwovens J., 7, 31 (1995).<br />
8. Seyam, A.M., Mohamed, A.S., <strong>and</strong> Kim, H., "Signal Analysis <strong>of</strong> Dynamic Forces Experienced by<br />
Individual Needles at High Speed Needlepunching," Text. Res. J., 68, 296 (1998).<br />
9. Seyam, A.M., <strong>and</strong> Sarin, S., "Effect <strong>of</strong> Needle Position <strong>and</strong> Orientation on Forces Experienced by<br />
Individual Needle during Needle Punching," Text. Res. J., 67, 772 (1997)<br />
10. Smith, W.C., Markets for Technical Needled <strong>Fabrics</strong>, Proceedings <strong>of</strong> the INDA's International<br />
Needlepunch Conference, Charlotte, NC, October, 1998. - INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
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Monitoring Of Dynamic Forces<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Applications Of On-Line Monitoring Of Dynamic Forces<br />
Experienced By Needles During Formation Of Needled<br />
<strong>Fabrics</strong><br />
By Abdelfattah M. Seyam, Nonwovens Cooperative Research Center, College <strong>of</strong> Textiles, North Carolina<br />
State University, Raleigh, North Carolina, USA<br />
Abstract<br />
The significance <strong>of</strong> a recently developed system that measures dynamic forces experienced by individual<br />
needles during formation <strong>of</strong> needlepunched fabrics is demonstrated. The system design, coupled with a<br />
new signal analysis technique allows measurement <strong>of</strong> peak penetration <strong>and</strong> stripping forces as well as the<br />
penetration <strong>and</strong> stripping energies due to needle/fiberweb interaction. Systematic experimental<br />
investigations were conducted to determine the critical locations in the needle board where needles<br />
experience the highest forces, <strong>and</strong> correlate needle force parameters to fabric performance.<br />
The research results, supported by statistical analysis, show there is a strong relationship between needle<br />
penetration energy <strong>and</strong> fabric properties. Additionally, the needling density significantly impacts the<br />
location <strong>of</strong> maximum penetration forces.<br />
Introduction<br />
The needlepunching industry was once considered a "waste products" industry, but has now successfully<br />
established itself in numerous first quality markets. Recently, Smith [10] listed eighteen markets <strong>of</strong><br />
needlepunched products. These include: automotive (headliner, door trim, etc.), filtration, furniture <strong>and</strong><br />
bedding, geotextiles, ro<strong>of</strong>ing, aerospace (shuttle tiles, brake pads, etc.), agriculture, advanced composites,<br />
industrial (belting, roller linings, etc.), insulators, marine, medical (blood filters, b<strong>and</strong>ages, etc.), paper<br />
making felts, protective clothing, sports felts (floor covering, tennis ball covers, etc.), synthetic<br />
leather/shoes, wall coverings, <strong>and</strong> miscellaneous (carpet underlay, car wash brushes, oil sorbents, <strong>of</strong>fice<br />
products, etc.).<br />
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The success <strong>of</strong> the industry can be attributed to low manufacturing cost <strong>and</strong> the flexibility <strong>of</strong> the<br />
needlepunching technology to tailor products to meet a variety <strong>of</strong> end use requirements. The increasing<br />
dem<strong>and</strong> for needled fabrics prompted machine manufacturers to construct high-speed/high performance<br />
needle looms. Today's needle looms are capable <strong>of</strong> running at speeds <strong>of</strong> up to 3,000 strokes/min. with<br />
working width <strong>of</strong> up to 15 meters. A parallel effort has been pursued by needle manufacturers to produce<br />
high performance needles. Needles are engineered with numerous design parameters in attempts to<br />
obtain needled fabrics with desired properties to meet end use requirements. These parameters include:<br />
number <strong>of</strong> barbs, barb spacing, needle gauge, kick-up size <strong>and</strong> needle shape.<br />
Historically, William Bywater <strong>of</strong> Leeds, Engl<strong>and</strong> [1] manufactured the first commercial needle machine<br />
in the late 1800's; however, scientific research was not published until the 1960's. The published research<br />
has targeted three areas:<br />
●<br />
●<br />
●<br />
Experimental work to study the influence <strong>of</strong> processing <strong>and</strong> fiber parameters on needled fabrics<br />
properties,<br />
Approaches to model the tensile behavior <strong>of</strong> needled fabrics, <strong>and</strong><br />
Developing devices to measure forces acting on needles.<br />
Recently Sarin, Meng <strong>and</strong> Seyam [6] published a review <strong>of</strong> previous work on needle force<br />
measurements. They found that the previous work was either performed statically using multiple needles<br />
or dynamically at low speed using both single <strong>and</strong> multiple needles. These techniques are incapable <strong>of</strong><br />
providing the accurate information important to needle manufacturers, machine producers <strong>and</strong> fabric<br />
producers. Dem<strong>and</strong> exists for a system capable <strong>of</strong> measuring needle forces during high-speed needling.<br />
Seyam, Meng <strong>and</strong> Mohamed have developed recently such system [7] that is briefly described later in<br />
this paper.<br />
While the previous studies provided basic underst<strong>and</strong>ing, the results <strong>and</strong> conclusions <strong>of</strong> such studies are<br />
valid only for the experimental range used. Moreover, the studies were conducted using small machines<br />
producing narrow fabrics at low needling speed. The applicability <strong>of</strong> such findings to an industry that<br />
uses today's high-speed needle looms producing wide fabrics is questionable. Additionally, in a research<br />
environment, an experiment is <strong>of</strong>ten run for extremely short time. In industry, however, the continuous<br />
processing <strong>of</strong> fabrics causes needle wear <strong>and</strong>, as a result, fabric properties may be significantly deviate<br />
from the desired levels.<br />
There is relatively limited literature regarding the modeling <strong>of</strong> fabric performance; only two publications<br />
have been identified. The first was published by Hearle <strong>and</strong> Sultan [2] showing an approach to<br />
theoretical underst<strong>and</strong>ing <strong>of</strong> tensile behavior <strong>of</strong> needled fabrics. The other publication, by Ji [3],<br />
developed a model to predict the entire load-extension behavior <strong>of</strong> needled fabrics. While his work is an<br />
improvement, the theoretical model <strong>and</strong> experimental results did not significantly agree. This is due to<br />
the assumptions used to develop the model in order to facilitate the prediction. Needled fabrics are<br />
complex structures that are very difficult to model. It would be extremely beneficial to the industry to<br />
develop an on-line technique that is capable <strong>of</strong> monitoring <strong>and</strong> controlling <strong>of</strong> fabric properties while the<br />
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fabrics are being produced. Our research team at the Nonwoven Cooperative Research Center undertook<br />
research efforts to accomplish this goal, developing a new system that measures dynamic forces<br />
experienced by individual needles during formation <strong>of</strong> needlepunched fabrics.<br />
Needle Force Measurement System<br />
Figure 1 shows the components <strong>of</strong> the needle force measurement system developed by Seyam, Meng <strong>and</strong><br />
Mohamed [7]. The force data could be collected from nine different instrumented needles located in the<br />
machine <strong>and</strong> cross machine directions (Figure 2).<br />
The NCRC needle force measurement system consists <strong>of</strong> force transducers in washer form, signal<br />
conditioner, data acquisition hardware <strong>and</strong> s<strong>of</strong>tware, <strong>and</strong> data analysis s<strong>of</strong>tware. These, along with<br />
possible applications <strong>of</strong> the system are fully explained in previous publications [5-9].<br />
Figure 1<br />
FORCE MEASUREMENT SYSTEM<br />
Figure 2<br />
LOCATIONS OF THE FIVE-INSTRUMENTED<br />
NEEDLES IN THE NEEDLE BOARD<br />
Signal Analysis<br />
Using signal analysis, we developed a technique to extract useful information from force data collected<br />
on-line [8]. The signal analysis procedure involves data filtration using low frequency pass filter in order<br />
to filter out vibration. Then the filtered data is processed to subtract the forces exerted on the needles due<br />
to inertia. The remaining forces are those due to needle/fiberweb interactions. From this data, needle<br />
penetration <strong>and</strong> stripping forces as well as energies can be deduced. Figure 3 shows the superimposition<br />
<strong>of</strong> the filtered data for total forces (solid line) <strong>and</strong> the inertia forces (dotted line) for several needling<br />
cycles. The solid line ABCDEF represents the total force experienced by an instrumented needle, while<br />
the dotted line ABCD'F represents the inertia forces. The solid portion CD represents the data <strong>of</strong> the<br />
penetrating forces experienced by the needle during the downward movement <strong>of</strong> the needle board. Point<br />
D is the peak penetration force corresponding to the highest pressure the needle experiences from the<br />
fiberweb. During the portion DE, the pressure on the needle is reduced due to the upward movement <strong>of</strong><br />
the needle board. The pressure reaches zero at the point where DE intercepts the dotted line. Beyond the<br />
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interception point, the needle is subjected to stripping forces as a result <strong>of</strong> its withdrawal from the<br />
fiberweb.<br />
Figure 3<br />
SUPERIMPOSITION OF TOTAL AND<br />
INERTIA FORCES IN TIME DOMAIN<br />
Figure 4<br />
NET NEEDLE FORCES DUE TO FIBERWEB<br />
RESISTANCE<br />
From Figure 3 one can notice that the total forces (solid line) <strong>and</strong> the inertia forces (dotted line) are<br />
identical during half cycle or at least during quarter cycle AB. This feature allows modeling <strong>of</strong> the whole<br />
inertia cycle ABC'D'F as a sinusoidal function. Subtraction <strong>of</strong> inertia forces from total forces gives the<br />
net forces that the needle experienced due to penetration <strong>of</strong> <strong>and</strong> withdrawal from the fiberweb (Figure 4).<br />
From the net force data <strong>of</strong> Figure 4 <strong>and</strong> the time-displacement data <strong>of</strong> the needle board, penetration <strong>and</strong><br />
stripping energies can be determined.<br />
Applications <strong>of</strong> the Needle Force Measurement System<br />
In this section, the experimental procedures <strong>and</strong> results are given for two applications <strong>of</strong> the system:<br />
Determination <strong>of</strong> the critical locations in the needle board at which needles experience the highest forces,<br />
<strong>and</strong> correlation <strong>of</strong> needle force parameters with fabric performance. For both applications, the force data<br />
were acquired from five instrumented needles (marked 1 through 5, Figure 2). The data was recorded<br />
simultaneously for each needle at a rate <strong>of</strong> 1,000 observations/sec.<br />
Correlation Between Force Parameters <strong>and</strong> Fabric Performance<br />
Experimental<br />
For this part <strong>of</strong> the study a total <strong>of</strong> sixteen needled fabrics were produced representing a full experimental<br />
design (4 levels <strong>of</strong> weight x 4 levels <strong>of</strong> needling density). For each fabric, three sets (replicates) <strong>of</strong> force<br />
data were collected at different times. For each set, force data <strong>of</strong> 150 needling cycles per instrumented<br />
needle were collected by the force measurement system. The fabrics were comprised <strong>of</strong> polypropylene<br />
fibers produced at 76.2 mm fiber length <strong>and</strong> 10 denier/filament. <strong>Fabrics</strong> were produced using carding <strong>and</strong><br />
cross-lapping prior to needling. More details are published elsewhere by Kim <strong>and</strong> Seyam [4]. The<br />
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properties (responses) selected for this study are tensile <strong>and</strong> tear resistance. Statistical Analysis System<br />
(SAS) was used to develop regression equations correlating needle penetration energy to needled fabric<br />
performance.<br />
Calculation <strong>of</strong> Penetration Energy<br />
The penetration energy (J/cm 2 ) was obtained by integrating the area under the curve <strong>of</strong> net needle force<br />
due to fiberweb resistance (Figure 4) combined with needle board displacement <strong>and</strong> the needling density.<br />
For each fabric the data was averaged over 2,250 needling cycles (3 replicates x 5 needles x 150 cycles)<br />
<strong>and</strong> used as an estimate for the energy expended to bond the fabric.<br />
Figure 5<br />
BREAKING ENERGY VS. PENETRATION<br />
ENERGY<br />
Figure 6<br />
PREDICTED TEAR STRENGTH VS.<br />
PENETRATION ENERGY<br />
Results <strong>and</strong> Discussion<br />
For each <strong>of</strong> the experimental run, the force data was fed into a computer, which calculated the<br />
penetration energy. Figures 5 <strong>and</strong> 6 show the predicted relationships between needling energies <strong>and</strong><br />
needled fabric performance as well as the correlation for each with the experimental data. The symbols<br />
<strong>of</strong> the predictive equations shown in Figures 5 <strong>and</strong> 6 are defined as follows:<br />
BE = Tensile Breaking Energy, J<br />
PE = Needling Penetration Energy, J/cm 2<br />
TS = Tear Resistance, N<br />
W = Needled Fabric Basis Weight, g/m 2<br />
Figure 5 depicts the relationship between needling energy <strong>and</strong> the energy required breaking the fabrics in<br />
tensile mode. The experimental data <strong>and</strong> the predictive equation <strong>of</strong> Figure 5 indicate that the relationship<br />
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between penetration energy <strong>and</strong> breaking energy is linear with high correlation coefficient (R2=0.9018).<br />
Figure 6 shows the predictive equation <strong>of</strong> the needling energy <strong>and</strong> the tear resistance <strong>of</strong> the needled<br />
fabrics. Unlike the breaking energy, tear resistance is impacted significantly by fabric basis weight. For a<br />
given weight, increasing the penetration energy (needling density) reduces the tear resistance. This can<br />
be explained by the decrease in the degree <strong>of</strong> fiber mobility with the increase in the penetration energy<br />
(due to increase in fiber interlocking with needling density). The high degree <strong>of</strong> fiber interlocking hinders<br />
the fiber movement to the delta zone during tear tests. Consequently, fewer fibers move to delta zone to<br />
share the load from the tear stresses. The high correlation coefficients (R2 = 0.9754) <strong>of</strong> the predictive<br />
equation <strong>of</strong> Figure 6 indicates that the needling energies <strong>and</strong> fabric weight are highly correlated to<br />
needled fabric tear resistance. It must be noted that this strong linear correlation should only be applied in<br />
the range over which the data was measured. Significant non-linearity is expected at very low needle<br />
densities.<br />
Figure 7<br />
PEAK PENETRATION FORCE IN TERMS OF<br />
NEEDLE LOCATION AND NEEDLING<br />
DENSITY. FABRIC WEIGHT = 260 G/M 2 ,<br />
NUMBER OF BARBS = 9<br />
Figure 8<br />
PEAK PENETRATION FORCE IN TERMS<br />
OF NEEDLE LOCATION AND NEEDLING<br />
DENSITY. FABRIC WEIGHT= 650 G/M 2 ,<br />
NUMBER OF BARBS = 9<br />
Significance<br />
The high correlation between fabric properties <strong>and</strong> penetration energies means that this technique can be<br />
used to predict <strong>and</strong> control the fabric properties while the fabrics are being produced. A computer<br />
algorithm can be developed for these on-line estimates through the predictive equations.<br />
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Determination <strong>of</strong> the Critical Locations In The Needle<br />
Board At Which Needles Experience The Highest<br />
Force<br />
Experimental<br />
To determine the locations where needles experience the<br />
highest penetration forces, a series <strong>of</strong> runs were performed<br />
on 60 cm wide Dilo loom using carded <strong>and</strong> cross-lapped<br />
fiberwebs. The fiber webs were produced from<br />
polypropylene fibers with 76.2 mm fiber length <strong>and</strong> 10<br />
denier/filament. A full experimental design (4 levels <strong>of</strong><br />
weight x 4 levels <strong>of</strong> needling density x 5 levels <strong>of</strong> needle<br />
location) was conducted. Each run was replicated three<br />
times. For each run, force data <strong>of</strong> 150 needling cycles per<br />
Figure 9<br />
LOCUS OF THE MAXIMUM PEAK<br />
PENETRATION FORCE<br />
instrumented needle were collected by the force measurement system. The key parameter <strong>of</strong> interest here<br />
is the peak penetration force due to fiberweb resistance that is developed after a certain number <strong>of</strong><br />
strokes (cycles <strong>of</strong> Figure 4). Again, SAS was used to develop regression equations relating peak needle<br />
penetration force to needle location, fabric weight <strong>and</strong> needling density.<br />
Results <strong>and</strong> Discussion<br />
Figures 7 <strong>and</strong> 8 show the predicted peak penetration forces as influenced by needling density, needle<br />
location <strong>and</strong> fabric weight. In these figures, the needle location represents the distance from the first row<br />
in the needle board at the feed side. Therefore, location = 0 cm indicates the first needle row where the<br />
fiberweb starts to receive needling. At location = 18 cm, the fiberweb received the target needling density<br />
(last needle row).<br />
It can be noticed from Figures 7 <strong>and</strong> 8 that the peak force increases with location up to a certain<br />
maximum value after which the peak penetration force decreases. Additionally, the maximum peak<br />
penetration force is dependent on the level <strong>of</strong> needling density. The location <strong>of</strong> the maximum moves<br />
toward the feed side as the needling density increases <strong>and</strong> toward the delivery side as the needling<br />
density decreases. The results indicate there may be several phenomena at play; their relative force<br />
contributions being dependent on the level <strong>of</strong> fiberweb integrity. Details <strong>of</strong> these force contributions are<br />
not yet understood but are postulated to include the following effects:<br />
●<br />
●<br />
●<br />
At locations near the feed side the fiberweb is bulky, which leads to frictional forces for the<br />
needles penetrating due to long contact length between fiberweb <strong>and</strong> needles. Additionally, the<br />
number <strong>of</strong> fibers caught by needle barbs at the feed side is higher compared to the delivery side.<br />
As bonding progresses, fibers become more entangled <strong>and</strong> the fiberweb is more consolidated.<br />
Thus, the fibers are more trapped in the fiberweb, resulting in an increased force contribution <strong>of</strong> a<br />
fiber caught by a needle.<br />
As the web advances to the delivery side, it receives more punches that cause fiber breakage.<br />
Consequently, the broken fibers contribute less to the needle forces.<br />
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●<br />
Additionally, as the web advances to the delivery side <strong>and</strong> the web is more consolidated, each<br />
needle tends to engage fewer fibers.<br />
Additional results similar to these <strong>of</strong> Figures 7 <strong>and</strong> 8 using other types <strong>of</strong> needles are published<br />
elsewhere [5].<br />
Figure 9 shows a generalized version <strong>of</strong> the needling density distribution that the web receives at<br />
different locations <strong>of</strong> the needle board. The four straight lines represent the needling density distribution<br />
<strong>of</strong> different target needling densities (50, 70, 90 <strong>and</strong> 110 punches/cm 2 ). Based on the above discussion on<br />
the effect <strong>of</strong> the needling density on the location <strong>of</strong> the maximum peak force, one would assume that the<br />
maximum would take place at a certain critical needling density. This means that a line as shown in<br />
Figure 9 can represent the locus <strong>of</strong> the maximum. The intercepts <strong>of</strong> this line with the four lines<br />
representing the needling density distribution determine the location <strong>of</strong> the maximum peak penetration<br />
force. Our results show however, that this locus is not necessarily a straight line, in fact the locus could<br />
assume a general line or curve. Irrespective <strong>of</strong> the exact shape <strong>of</strong> the critical line, the reason why the<br />
location <strong>of</strong> the maximum peak force varies with needling density is clear. The maximum peak force is<br />
strongly dependent on the total number <strong>of</strong> punches encountered by the web as it progresses through the<br />
needle loom.<br />
Significance <strong>of</strong> Locating The Position Of Maximum Peak Force<br />
Needle Rotation Technique<br />
To maximize needle utilization, fabric producers developed methods to rotate the needles in the needle<br />
board after a given number <strong>of</strong> needling cycles. This is done since the needles are subjected to different<br />
forces, <strong>and</strong> hence different wear levels, depending on their location in the needle board. The rotation<br />
supposes to equalize the needle wear. Each needled fabric producer developed different techniques <strong>of</strong><br />
needle rotation based on experience. Thus, the needle rotation is considered as an art rather than science.<br />
To base this on science, needles should be rotated based on the force distribution <strong>of</strong> Figures 7 <strong>and</strong> 8.<br />
Needles in the rows where the force is high should be moved to locations <strong>of</strong> low forces.<br />
The force measurement system, therefore, could rationalize the needle rotation process.<br />
Needle Design<br />
Another significant benefit <strong>of</strong> the determination <strong>of</strong> the needle force distribution is needle design. Needle<br />
manufacturers can make use <strong>of</strong> the results to design needles to withst<strong>and</strong> the high stress positions <strong>and</strong><br />
thereby avoid excessive needle breakage during fabric formation. Alternatively, this underst<strong>and</strong>ing may<br />
allow the strongest (<strong>and</strong> presumably most expensive) needles to be mounted in positions <strong>of</strong> highest<br />
stress.<br />
The industry benefit would be production <strong>of</strong> high quality needled fabrics at high efficiency.<br />
Conclusion<br />
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Monitoring Of Dynamic Forces<br />
Our research findings showed that the force measurement device coupled with signal analysis have<br />
significant benefits to needled fabric producers as well as needle manufacturers. The high correlation<br />
found between needle force parameters <strong>and</strong> fabric properties can be used to on-line monitor the needled<br />
fabric properties to ensure the produced fabrics are within the specified requirements. The location <strong>of</strong> the<br />
maximum needle forces is essential for fabric producers to rationalize the needle rotation technique in<br />
order to maximize the needle utilization. Additionally, needle producers can make use <strong>of</strong> the information<br />
in designing high performance needles.<br />
Acknowledgment<br />
This work was supported by the Nonwovens Cooperative Research Center, which is funded by the<br />
National Science Foundation, the State <strong>of</strong> North Carolina, <strong>and</strong> Industry Members.<br />
Reference<br />
1. Foster, J.H., "Needlepunching - Past, Present <strong>and</strong> Future," INDA-TEC '88 209 (1988)<br />
2. Hearle, J.W.S., <strong>and</strong> Sultan, M.A.I., "Study <strong>of</strong> Needled <strong>Fabrics</strong>, Part V: The approach to theoretical<br />
underst<strong>and</strong>ing," J. Text. Inst., 59, 183 (1968).<br />
3. Ji, Y., Tensile Properties <strong>of</strong> Needlepunched Nonwoven <strong>Fabrics</strong>, Ph. D. Thesis, North Carolina State<br />
University, 1992.<br />
4. Kim, H. <strong>and</strong> Seyam, A.M., Needle Force Parameters/Needled Fabric Performance Relationships,<br />
Proceedings <strong>of</strong> the INDA International Needlepunch Conference, Charlotte, NC, October, 1998.<br />
5. Kim, H., Study <strong>of</strong> Needlepunching Process <strong>and</strong> Products, Ph. D. Thesis, North Carolina State<br />
University, 1998.<br />
6. Sarin, S., Meng, J., <strong>and</strong> Seyam, A. M., "Mechanics <strong>of</strong> Needlepunching Process <strong>and</strong> Products, Part I:<br />
Critical Review <strong>of</strong> Previous Work on Forces Experienced by Needles during Needling <strong>of</strong> Nonwoven<br />
<strong>Fabrics</strong>," International Nonwovens J., 6, 32 (1994).<br />
7. Seyam, A.M., Meng, J., <strong>and</strong> Mohamed, A., "Mechanics <strong>of</strong> Needlepunching Process <strong>and</strong> Products, Part<br />
II: An On-Line Device to Measure the Punching Forces Experienced by Individual Needles,"<br />
International Nonwovens J., 7, 31 (1995).<br />
8. Seyam, A.M., Mohamed, A.S., <strong>and</strong> Kim, H., "Signal Analysis <strong>of</strong> Dynamic Forces Experienced by<br />
Individual Needles at High Speed Needlepunching," Text. Res. J., 68, 296 (1998).<br />
9. Seyam, A.M., <strong>and</strong> Sarin, S., "Effect <strong>of</strong> Needle Position <strong>and</strong> Orientation on Forces Experienced by<br />
Individual Needle during Needle Punching," Text. Res. J., 67, 772 (1997)<br />
10. Smith, W.C., Markets for Technical Needled <strong>Fabrics</strong>, Proceedings <strong>of</strong> the INDA's International<br />
Needlepunch Conference, Charlotte, NC, October, 1998. - INJ<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Development <strong>of</strong> Thermal Insulation<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Development <strong>of</strong> Thermal<br />
Insulation for Textile Wet<br />
Processing Machinery<br />
Using Needlepunched Nonwoven <strong>Fabrics</strong><br />
By R<strong>and</strong>eep S. Grewal, Flynt <strong>Fabrics</strong>, Inc., <strong>and</strong> Dr. Pamela Banks-Lee, North Carolina State University<br />
Abstract<br />
In textile manufacturing, many fiber manufacturing, dyeing <strong>and</strong> finishing processes require temperatures in<br />
the range <strong>of</strong> 100 o C to 200 o C. A substantial amount <strong>of</strong> energy is needed to produce the desired temperature,<br />
<strong>and</strong> part <strong>of</strong> this energy is wasted when heat from the process escapes to the environment. Many <strong>of</strong> the<br />
processes are batch processes requiring frequent reheating <strong>and</strong> restarting. Most process equipment is<br />
constructed from stainless steel, which is a good conductor <strong>of</strong> heat. In addition to this, because <strong>of</strong> the cost<br />
involved in installation <strong>and</strong> regular maintenance <strong>of</strong> insulation, many manufacturers do not insulate their<br />
process equipment.<br />
The heat <strong>and</strong> moisture loss to the environment makes the manufacturing facilities environmentally<br />
uncomfortable for employees. This reduces their productivity <strong>and</strong> is a health risk. Due to the energy wasted in<br />
the textile wet processing industry, there is a need to develop suitable insulating materials specifically for<br />
these applications. For commercial applications, both the cost <strong>of</strong> the insulating material as well as its<br />
effectiveness, ease <strong>of</strong> installation <strong>and</strong> durability are important.<br />
Needlepunched fabrics have the potential to meet these dem<strong>and</strong>s [1]. Since low density needled felts with<br />
good heat blocking capacity can be made from durable fibers, they are ideal for heat insulation applications<br />
[1,2]. This research focuses on identifying suitable fibers <strong>and</strong> the manufacturing technology which will yield<br />
the desired results. After testing <strong>of</strong> prepared samples, the data was analyzed to determine the fabric <strong>and</strong> fiber<br />
parameters which influence heat transfer. An economic analysis was also conducted to optimize both cost <strong>and</strong><br />
effectiveness.<br />
The important factors contributing to the transfer <strong>of</strong> heat through needlepunched nonwoven fabrics were<br />
found to be the bulk density <strong>of</strong> the batt <strong>and</strong> the surface area <strong>of</strong> the fibers. Incorporation <strong>of</strong> low denier fibers<br />
(meltblown web) in the needlepunched structure led to a significant decrease in the apparent thermal<br />
conductivity <strong>of</strong> the batt. A cost analysis <strong>of</strong> this insulation (incorporating the meltblown web) determined the<br />
optimum thickness <strong>of</strong> such an insulation to be 10.1 mm.<br />
Introduction<br />
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Development <strong>of</strong> Thermal Insulation<br />
Heat insulators are defined as those materials or combination <strong>of</strong> materials with air or evacuated spaces that<br />
will retard the transfer <strong>of</strong> heat with reasonable effectiveness under ordinary conditions [3]. Thermal insulation<br />
is used not only to conserve energy, but also to provide year-round comfort for living <strong>and</strong> working spaces.<br />
Needled felts, due to their bulk <strong>and</strong> internal voids, are inherently good insulators <strong>and</strong> are widely used for<br />
insulation purposes [4]. Although a wide array <strong>of</strong> nonwoven insulation is commercially available for<br />
wide-ranging applications, their commercial feasibility for application to the textile wet processing industry<br />
has never been seriously investigated. The textile wet processing industry consumes a large quantity <strong>of</strong><br />
energy for heating water <strong>and</strong> making steam, which is used in almost all <strong>of</strong> its processes such as scouring,<br />
bleaching, dyeing <strong>and</strong> finishing. The temperature range is approximately 100 o C to 200 o C. As energy costs<br />
<strong>and</strong> environmental concerns escalate, this industry has specific needs which must be studied in order to<br />
develop an appropriate insulation.<br />
Modes <strong>of</strong> Heat Transfer in Fibrous Insulations<br />
When energy is transferred from one body to another by virtue <strong>of</strong> a temperature difference existing between<br />
them, it is said that heat is transferred. There are three modes <strong>of</strong> heat transfer: conduction, radiation <strong>and</strong><br />
convection [3,4].<br />
Conduction<br />
Heat will flow from a high temperature region to a lower temperature region by conduction. In general, the<br />
particles <strong>of</strong> matter (molecules, atoms <strong>and</strong> electrons) in the high-temperature region, being at higher energy<br />
levels, will transmit some <strong>of</strong> their energy to the adjacent lower-temperature regions through particle<br />
interaction. Conduction can be either through gases, liquids or solids. In the case <strong>of</strong> conduction in gases, the<br />
interchange <strong>of</strong> kinetic energy by molecules colliding is the predominant mechanism. In non-metallic solids,<br />
the primary mechanism is by lattice-vibration wave propagation. Higher temperatures are associated with<br />
higher molecular energies, <strong>and</strong> when neighboring molecules collide, as they are constantly doing, a transfer<br />
<strong>of</strong> energy from the more energetic to the less energetic molecules occurs [4,5].<br />
The heat transfer rate per unit area is proportional to the normal temperature gradient. That is,<br />
(1.1)<br />
where q is the heat transfer rate <strong>and</strong> dT/dx is the temperature gradient in the direction <strong>of</strong> the heat flow. The<br />
positive constant k is the thermal conductivity <strong>of</strong> the material, <strong>and</strong> the minus sign is inserted so that the<br />
second principle <strong>of</strong> thermodynamics will be satisfied, i.e., heat must flow from a body at a higher temperature<br />
to a body at a lower temperature [6].<br />
Convection<br />
Convective heat transfer may be categorized according to the nature <strong>of</strong> the flow. It is called forced convection<br />
when the flow is caused by some external means, such as by a fan, a pump or atmospheric winds. In contrast,<br />
for free (or natural) convection, the flow is induced by buoyancy in the fluid. These forces arise from density<br />
variations caused by temperature variations in the fluid. A circulation pattern exists in which the warm fluid<br />
moves up from the hot surface <strong>and</strong> cooler fluid moves downwards [7]. Regardless <strong>of</strong> the particular nature <strong>of</strong><br />
the convective heat transfer mode, the appropriate heat transfer equation is <strong>of</strong> the form:<br />
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Development <strong>of</strong> Thermal Insulation<br />
q=h(T s - T o ) (1.2)<br />
where,<br />
q : the convective heat flux<br />
T s : surface temperature, <strong>and</strong><br />
T o : gas temperature.<br />
h : proportionality constant or convection heat transfer coefficient [7].<br />
This expression is known as Newton’s Law <strong>of</strong> Cooling. This formula encompasses all the effects that<br />
influence the convection mode. It depends on the conditions in the boundary layer, which are influenced by<br />
surface geometry, the nature <strong>of</strong> the fluid motion, <strong>and</strong> the fluid thermodynamic <strong>and</strong> transport properties [7,8].<br />
Radiation<br />
In contrast to the mechanisms <strong>of</strong> conduction <strong>and</strong> convection, where energy transfer through a material<br />
medium is involved, heat may also be transferred through regions where a perfect vacuum exists. The<br />
mechanism in this case is electromagnetic radiation or propagation <strong>of</strong> a collection <strong>of</strong> particles termed photons<br />
or quanta. This is called thermal radiation. Radiation is a surface phenomenon. For radiation propagation in a<br />
particular medium, its frequency <strong>and</strong> wavelength l are related by:<br />
(1.3)<br />
where c: velocity <strong>of</strong> light in the medium [4,9].<br />
Definition <strong>and</strong> Basic Equation <strong>of</strong> Apparent Thermal Conductivity<br />
Apparent thermal conductivity <strong>of</strong> a porous material is the overall (sum <strong>of</strong> all individual conductivity terms)<br />
conductivity <strong>of</strong> the material. This value takes into account the conduction due to the solid <strong>and</strong> gas terms,<br />
including all the conduction, convection, <strong>and</strong> radiation values. The apparent thermal conductivity <strong>of</strong> a<br />
material can thus be referred to as the conductivity <strong>of</strong> the material as a whole.<br />
k app = k g + k cv + k f + k rc + k i (1.4)<br />
where,<br />
k g = conduction <strong>of</strong> air x (1 - f ), where f is volume fraction <strong>of</strong> fiber<br />
k cv = conduction by convection<br />
k f = conduction through fibers<br />
k rc = conduction by radiation<br />
k i = interaction between air <strong>and</strong> fiber. [10]<br />
Methodology<br />
To study the effect <strong>of</strong> fiber types <strong>and</strong> fiber parameters on thermal insulating properties, needlepunched<br />
nonwoven fabrics were produced from fibers listed in Table 1.<br />
The fibers were carded, crosslapped <strong>and</strong> needlepunched using four different needling densities (93, 140, 186<br />
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Development <strong>of</strong> Thermal Insulation<br />
<strong>and</strong> 248 pen./cm 2 ) <strong>and</strong> two<br />
different needle penetration<br />
depths (7mm <strong>and</strong> 12mm). In<br />
addition, meltblown PBT<br />
(poly(butylene<br />
terephthalate)) web, 40<br />
grams per square meter,<br />
supplied by TANDEC,<br />
University <strong>of</strong> Tennessee,<br />
was used. These webs were<br />
incorporated into the<br />
needlepunched nonwoven to<br />
form a barrier for the heat<br />
flux flow.<br />
Table 1<br />
SPECIFICATIONS OF FIBERS USED<br />
Polymer dpf Length Supplier Type<br />
(in)<br />
PET 4.0 3.0 DuPont Solid<br />
PET 6.0 2.5 Hoechst Celanese Solid<br />
PET 6.0 2.0 Hoechst Celanese Hollow<br />
PET 6.0 2.0 Eastman Chemical Deep Grooved<br />
(4DG)<br />
PET 1.0 2.5 Hoechst Celanese Solid<br />
Kevlar(r) 2.25 1.5 DuPont Solid<br />
The data obtained was regressed against bulk density, thickness, air resistance <strong>and</strong> fiber type.<br />
Testing Procedures<br />
The needlepunched nonwoven fabrics were tested for air resistance, thickness, grab tensile strength, basis<br />
weight, <strong>and</strong> apparent thermal conductivity. The procedures <strong>and</strong> equipment used are described in Table 2.<br />
Measurement <strong>of</strong> Apparent Thermal Conductivity (kapp)<br />
For measuring the apparent thermal conductivity <strong>of</strong> the nonwoven samples, the guarded hot plate instrument<br />
was used. The Holometrix model TCFGM guarded hot plate thermal conductance measuring system is used<br />
for determining the thermal performance <strong>of</strong> insulation <strong>and</strong> other materials <strong>of</strong> relatively low thermal<br />
conductance. When such a material, in the form <strong>of</strong> a flat slab, is exposed to different temperatures on the two<br />
opposites faces, heat flows across the slab resulting from a combination <strong>of</strong> conduction, convection, <strong>and</strong><br />
radiation within the material.<br />
The effective thermal conductivity <strong>of</strong> the test samples is determined from measurements <strong>of</strong> the final surface<br />
temperatures, the power input to the main heater, <strong>and</strong> the geometry <strong>of</strong> the test sample, as follows:<br />
(2.1)<br />
where<br />
kapp: apparent thermal conductivity <strong>of</strong> the sample, W/moK<br />
E: main heater voltage, Volts<br />
I: main heater current, Amps<br />
S: main heater surface area, m 2<br />
T 1 , T 2 : temperature gradients through the samples, o C, <strong>and</strong> d 1 , d 2 : sample thickness, m.<br />
Results <strong>and</strong> Discussion<br />
The needlepunched fabrics made were tested for thickness, air resistance, bulk density, grab tensile strength,<br />
<strong>and</strong> apparent thermal conductivity. Two samples at each data point were averaged to obtain the raw data.<br />
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Development <strong>of</strong> Thermal Insulation<br />
Effect <strong>of</strong> Bulk<br />
Density<br />
Bulk density was the<br />
most important factor<br />
affecting the<br />
apparent thermal<br />
conductivity <strong>of</strong> the<br />
needlepunched<br />
samples. Good linear<br />
Table 2<br />
TESTING EQUIPMENT<br />
Equipment<br />
Model number Manufacturer<br />
Air resistance KES-F8-AP1 Kato Tech. Co.<br />
Thickness Ames 282 B.C. Ames<br />
Tensile strength M786 Instron Co.<br />
Thermal Conductivity TCFGM<br />
Holometrix Co.<br />
regression fits were obtained between apparent thermal conductivity <strong>and</strong> bulk density. The statistical analysis<br />
showed that bulk density has a significant effect on apparent thermal conductivity at a significance level <strong>of</strong><br />
99.99%. As can be seen in Figure 1, for the range <strong>of</strong> bulk densities studied, as the bulk density increased, the<br />
apparent thermal conductivity also increased. In the literature, for fibrous insulation, a "U" shaped curve is<br />
usually obtained for the effect <strong>of</strong> bulk density on conductivity [11]. In this research, only a linear relationship<br />
has been established due to the limited range <strong>of</strong> bulk densities investigated. Only fabrics with the highest bulk<br />
densities would have the durability needed in insulating textile wet processing equipment.<br />
<strong>Fibers</strong> with lower deniers have lower apparent thermal<br />
conductivity values due to higher fabric surface areas.<br />
On the other h<strong>and</strong>, 4DG fiber needlepunched fabrics,<br />
due to the unique cross section <strong>of</strong> the fibers have a<br />
higher surface area than lower denier fibers studied.<br />
The 4DG fiber surface also leads to "channeling<br />
effect" <strong>and</strong> traps air to provide better insulation.<br />
Though needlepunched Kevlar® has higher apparent<br />
thermal conductivity than all the other fibers studied,<br />
incorporation <strong>of</strong> meltblown webs into 4dpf polyester<br />
needlepunched structures led to a significant decrease<br />
in apparent thermal conductivity <strong>of</strong> the batt. This is<br />
due to a loss in convection <strong>and</strong> radiative heat transfer.<br />
The very fine denier meltblown web acts as a barrier<br />
for radiative heat transfer <strong>and</strong> at the same time due to<br />
its high surface area traps air to reduce convective<br />
heat transfer. This same reduction in apparent thermal<br />
conductivity was seen when meltblown webs were<br />
incorporated into 4dpf PET webs also. This is a very<br />
significant finding.<br />
Figure 1<br />
EFFECT OF BULK DENSITY ON APPARENT<br />
THERMAL CONDUCTIVITY OF<br />
NEEDLEPUNCHED FABRICS<br />
Effect <strong>of</strong> Air Flow Resistance<br />
In the review <strong>of</strong> literature, air permeability (reciprocal<br />
<strong>of</strong> air flow resistance) <strong>of</strong> the fabric played an important role in the heat transfer properties <strong>of</strong> nonwoven fabric<br />
[1,12]. However, most <strong>of</strong> the nonwoven examples in the literature review were for apparel insulation<br />
purposes, <strong>and</strong> thus had very low bulk densities. In low bulk density materials, air permeability has an very<br />
significant effect on apparent thermal conductivity because the larger air spaces present lead to greater heat<br />
transfer by convection. In the bulk density range investigated, air flow resistance did not have as significant<br />
an effect on effective thermal conductivity <strong>of</strong> the needlepunched fabric as did bulk density. This was<br />
confirmed by the statistical analysis when a significance level <strong>of</strong> 90% was obtained (Figure 2)<br />
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Development <strong>of</strong> Thermal Insulation<br />
Figure 2<br />
EFFECT OF AIR FLOW RESISTANCE ON<br />
APPARENT THERMAL CONDUCTIVITY OF<br />
NEEDLEPUNCHED NONWOVEN FABRICS<br />
Figure 3<br />
EFFECT OF THICKNESS OF NEEDLEPUNCHED<br />
FABRIC ON ITS APPARENT THERMAL<br />
CONDUCTIVITY<br />
.<br />
Effect <strong>of</strong> Thickness<br />
Thickness is one <strong>of</strong> the main factors influencing the effective thermal conductivity <strong>of</strong> the needlepunched test<br />
specimens. Apparent thermal conductivity value has been normalized for thickness, but in the data obtained<br />
there is a distinct difference in the thermal conductivity values <strong>of</strong> nonwovens with higher thickness <strong>and</strong> those<br />
<strong>of</strong> lesser thickness at the same value <strong>of</strong> bulk density. The statistical analysis suggested with 97% confidence<br />
that thickness has a significant effect on apparent thermal conductivity <strong>of</strong> needlepunched nonwoven fabric.<br />
This result is in accordance with previous research on fibrous thermal insulations [13]. An increase in<br />
thickness leads to a lower thermal gradient across individual air spaces, thus leading to a reduction in the<br />
value <strong>of</strong> convective heat transfer. Also, radiative heat transfer is reduced due to more scattering <strong>and</strong><br />
absorption <strong>of</strong> radiation. This effect is not linear <strong>and</strong> is called "shadowing effect" [13]. (Figure 3)<br />
Effect <strong>of</strong> Fiber Type<br />
Four fiber parameters were investigated: denier, surface area, solid or hollow, <strong>and</strong> fiber type. It was found<br />
that lower denier led to a decrease in apparent thermal conductivity. There are more void spaces created by a<br />
thinner fiber, reducing convection, radiation <strong>and</strong> air conduction [14,15].<br />
Fiber surface area also played a role in heat transfer properties <strong>of</strong> the fabric. This can be seen in the case <strong>of</strong> 6<br />
denier 4DG as compared to regular 6 denier fibers. The higher surface area led to more void spaces, <strong>and</strong> in<br />
the case <strong>of</strong> 4DG there is a "channeling effect" <strong>of</strong> the void spaces. This channeling effect is due to very narrow<br />
elongated voids along the fiber surface. Very minute voids are created by the unique structure <strong>of</strong> 4DG fibers<br />
<strong>and</strong> this resulted in the nonwoven having a lower apparent thermal conductivity by reducing radiative <strong>and</strong><br />
convective heat transfer.<br />
Hollow fibers reduced heat conduction compared to solid fibers due to the trapped air in their interior. They<br />
also show some scattering <strong>and</strong> absorption <strong>of</strong> radiation in the hole in their center, reducing radiative heat<br />
transfer. They effectively have higher surface area than solid fibers. This effect has been confirmed in the<br />
literature [16,17].<br />
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Development <strong>of</strong> Thermal Insulation<br />
Conclusion<br />
The c<strong>and</strong>idate fiber<br />
recommended for<br />
insulating textile wet<br />
processing machinery<br />
incorporates meltblown<br />
web in its structure <strong>and</strong> has<br />
Kevlar® on the side that<br />
would be in touch with the<br />
equipment. This will give<br />
the fabric better thermal<br />
stability properties on that<br />
side. Polyester<br />
needlepunched fabrics <strong>and</strong><br />
PBT meltblown webs<br />
combined together had a<br />
lower apparent thermal<br />
conductivity than all single<br />
polyester needlepunched<br />
Determinant<br />
Fabric<br />
Purchase price<br />
Capital for insulation<br />
manufacturing<br />
machinery<br />
Table 3<br />
BASIS FOR ECONOMIC<br />
THICKNESS CALCULATIONS.<br />
Type/Value<br />
PET/Meltblown/ Kevlar®<br />
needlepunched<br />
$4.91/m 2 in.<br />
$1.3 million<br />
Capital for insulation<br />
manufacturing<br />
building $500,000<br />
For use on equipment<br />
Cost <strong>of</strong> heat<br />
Cost <strong>of</strong> labor $22.6/m 2<br />
Project life<br />
5 years<br />
Textile dyeing/drying equipment<br />
$5.74/106Btu<br />
fabrics. Polyester, however, oxidizes over a long period <strong>of</strong> time due to the presence <strong>of</strong> heat, air <strong>and</strong> moisture<br />
at the insulation utilization site due to hydrolysis. Kevlar® on the other h<strong>and</strong> has better resistance to thermal<br />
degradation <strong>and</strong> provides the nonwoven with improved strength as compared to polyester. The tensile<br />
properties <strong>of</strong> the needlepunched nonwovens in the bulk density range studied are well above those required<br />
for a durable thermal insulation.<br />
Cost Analysis<br />
Determination <strong>of</strong> Economic Thickness <strong>of</strong> Insulation<br />
Calculations for the economic thickness <strong>of</strong> a thermal insulation are based on recommendations made by the<br />
U.S. Department <strong>of</strong> Energy, Office <strong>of</strong> Industrial Programs [18].<br />
There are two methods widely used for determining the optimal economic thickness <strong>of</strong> an industrial<br />
insulation: the minimum total cost method <strong>and</strong> the incremental cost method. For the minimum total cost<br />
method, actual calculations for the cost <strong>of</strong> insulation <strong>and</strong> the cost <strong>of</strong> lost energy are determined at each<br />
insulation thickness. The thickness producing the lowest total cost is the optimal economic solution. Due to a<br />
large number <strong>of</strong> tedious calculations involved, this method is not very practical. On the other h<strong>and</strong>, the<br />
incremental (or marginal cost) method is much simpler for determining the optimal thickness. With this<br />
method, the optimum thickness is determined to be the point where the last dollar invested in insulation<br />
results in exactly one dollar in energy cost savings. At a thickness greater than that point, a dollar invested<br />
will result in less than one dollar in energy cost savings. For a given situation both methods will yield the<br />
same optimum thickness solution.<br />
Economic Thickness Determination<br />
The economic thickness was determined using the incremental cost method. It used the cost <strong>of</strong> heat <strong>and</strong> the<br />
cost <strong>of</strong> insulation to obtain the optimum thickness based on the life <strong>of</strong> the insulation project. Using the graphs<br />
<strong>and</strong> the worksheets [18] prepared by the U.S. Department <strong>of</strong> Energy, Office <strong>of</strong> Industrial Programs, the<br />
economic thickness is determined to be less than one inch, but the specific thickness cannot be determined.<br />
To determine the exact thickness mathematical calculations are found to be more suitable than using<br />
pre-determined graphs [18]. Table 3 lists the basis for economic thickness calculations.<br />
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Development <strong>of</strong> Thermal Insulation<br />
Using certain assumptions <strong>and</strong> cost, the optimum economic thickness was determined by the incremental cost<br />
method. The most economic thickness is determined to be 10.1 mm (0.4 in.) based on an apparent thermal<br />
conductivity value <strong>of</strong> 0.089 watts/mK.<br />
Conclusion<br />
The objective <strong>of</strong> this investigation was to develop <strong>and</strong> evaluate needlepunched nonwovens as thermal<br />
insulation for textile wet processing machinery. This purpose has been fulfilled within the limitations <strong>of</strong> the<br />
experimental setup. A novel needlepunched insulation has been developed by s<strong>and</strong>wiching a PBT meltblown<br />
web between two carded webs <strong>of</strong> PET. One side <strong>of</strong> this insulation (which is to be in contact with the textile<br />
wet processing machinery) is then layered with a carded Kevlar® web. The purpose <strong>of</strong> the Kevlar® is to<br />
prevent oxidation <strong>and</strong> degradation <strong>of</strong> the PET fibers since Kevlar® has superior thermal stability. The<br />
thermal insulation thus developed showed lower apparent thermal conductivity than a variety <strong>of</strong> other<br />
needlepunched structures studied. A cost analysis <strong>of</strong> this insulation (based on a five-year project life return <strong>of</strong><br />
investment) determined the optimum thickness <strong>of</strong> such an insulation to be less than half an inch (10.1 mm),<br />
which is well below the industry norm. This means that the last dollar invested in the insulation project would<br />
be recovered by savings in energy bills after five years. The optimum thickness for a specific textile plant will<br />
depend upon the cost <strong>of</strong> energy, local labor rates <strong>and</strong> prevailing material costs. The tensile properties were<br />
also found to be adequate for commercial applications. The implementation <strong>of</strong> such an insulation project by a<br />
textile wet processing industry would however depend upon the competition, insulation cost, capital<br />
available, etc.<br />
The investigation into the effect <strong>of</strong> various fabric parameters such as bulk density, air permeability, etc.,<br />
which was intended for this investigation has also been completed. For needlepunched nonwovens the bulk<br />
density is found to be the most significant factor determining its heat blocking properties. At higher bulk<br />
densities, the fabrics have higher apparent thermal conductivities, i.e. in the range <strong>of</strong> bulk densities<br />
investigated, lower bulk densities represent better thermal insulation. This must be balanced, <strong>of</strong> course, with<br />
the structural integrity requirements <strong>of</strong> the application.<br />
Thermal conductivity properties do not correlate with air resistance values. The thickness <strong>of</strong> the web<br />
however, affects the apparent thermal conductivity. At higher thicknesses, the apparent thermal conductivity<br />
is reduced as compared to thinner webs. This is due to a decrease in convective <strong>and</strong> radiative heat transfer<br />
through the web at higher thicknesses. The effect <strong>of</strong> thickness on apparent thermal conductivity <strong>of</strong> the<br />
needlepunched insulation was not taken into account when calculating the economic thickness <strong>of</strong> the<br />
insulation. Incorporation <strong>of</strong> the meltblown PBT web in the structure <strong>of</strong> the needlepunched web significantly<br />
reduced the apparent thermal conductivity <strong>of</strong> the nonwoven batt. This is the most significant finding <strong>of</strong> this<br />
investigation. Utilizing this finding can lead to superior insulation at lower cost.<br />
Bibliography<br />
1. Morris, G.J., "Thermal Properties <strong>of</strong> Textile materials," <strong>Journal</strong> <strong>of</strong> the Textile Institute, pp. T449-475, May<br />
1953.<br />
2. Wijeysundersa, N.E., <strong>and</strong> Hawlader, M.N.A, "Effects Of Condensation And Liquid Transport On The<br />
Thermal Performance Of Fibrous Insulations," International, J. <strong>of</strong> Heat <strong>and</strong> Mass Transfer 35, pp.<br />
2605-2616, Oct.1992.<br />
3. Bales E., "Research for Thermal Insulation," J. <strong>of</strong> Heat Transfer 90, pp. 44-45, March 1968.<br />
4. Bankvall, C., "Heat Transfer In Fibrous Material," J. <strong>of</strong> Testing <strong>and</strong> Evaluation, pp. 235-243, May 1973.<br />
5. Bomberg, M., <strong>and</strong> Klarsfeld, S., "Semi-Empirical Model <strong>of</strong> Heat Transfer in Dry Mineral Fiber<br />
Insulations," J. <strong>of</strong> Thermal Insulation 6, pp. 157-173, Jan 1983.<br />
6. Fricke, J., <strong>and</strong> Caps, R., "Heat Transfer In Thermal Insulations - Recent Progress And Analysis,"<br />
International <strong>Journal</strong> <strong>of</strong> Thermophysics 9, pp. 885-893, May 1988.<br />
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Development <strong>of</strong> Thermal Insulation<br />
7. Degen, K.G., Rossetto, S., <strong>and</strong> Reinchenauer, T., "Investigation Of Heat Transfer In Evacuated Foil Spacer<br />
Multilayer Insulation," J. Thermal Insulation 16, pp. 140-152, Oct, 1992.<br />
8. Horton, C.W., <strong>and</strong> Rogers, F.T., "Convection Currents in a Porous Medium," J. Applied Physics 16, pp.<br />
367-370, June 1945.<br />
9. Kowalski, G. J., Mitchell, J.W., "An Evaluation And Experimental Investigation Of The Heat Transfer<br />
Mechanism Within Fibrous Media," ASME publication 79-WA/HT-40.<br />
10. Pelanne, C.M., "Heat Flow Principles In Thermal Insulations," J. Thermal Insulation, pp. 50-81, July<br />
1977.<br />
11. Wang, K.Y., <strong>and</strong> Tein, C.L., "Thermal Insulation In Flow Systems: Combined Radiation And<br />
Convection Through A Porous Segment," J. Heat Transfer 106, pp. 453-459, May 1984.<br />
12. Pierce, F.T., <strong>and</strong> Rees, W.H., "The Transmission Of Heat Through Textile <strong>Fabrics</strong>-Part II," <strong>Journal</strong> <strong>of</strong> the<br />
Textile Institute, pp. T181-T202, Sept. 1946.<br />
13. Speakman, J.B., <strong>and</strong> Chamberlain, N.H., "The Thermal Conductivity Of Textile Materials And <strong>Fabrics</strong>,"<br />
<strong>Journal</strong> <strong>of</strong> the Textile Institute 29, pp. T29-T53, 1929.<br />
14. Rees, W.H., "The Transmission Of Heat Through Textile <strong>Fabrics</strong>," <strong>Journal</strong> <strong>of</strong> the Textile Institute 32, pp.<br />
T149-T165, Aug. 1941.<br />
15. Caps, R., Umbach, K.H., "Optimizing Polyester Nonwoven Fabric Thermal Insulation," Mell<strong>and</strong> English,<br />
pp. E 201, May 1990.<br />
16. Martin, J.R., <strong>and</strong> Lamb, G.E.R., "Measurement Of Thermal Conductivity Of Nonwovens Using A<br />
Dynamic Method," Textile Research <strong>Journal</strong>, pp. 721-727, Dec 1987.<br />
17. Lee, Y.M., <strong>and</strong> Barker, R., "Thermal Protective Performance Of Heat-Resistant <strong>Fabrics</strong> In Various High<br />
Intensity Heat Exposures," Textile Research <strong>Journal</strong>, pp. 123-132, March 1987.<br />
18. "Economic Thickness for Industrial Insulation U.S. Department <strong>of</strong> Energy," U.S. Office <strong>of</strong> Industrial<br />
Programs, Fairmont Press Inc., Atlanta, GA, 1983.<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
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Trends In Latex Emulsions<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Comparison Of Trends In Latex<br />
Emulsions For Nonwovens <strong>and</strong> Textiles: China <strong>and</strong> the<br />
United States<br />
By Pamela Wiaczek, Project Manager, Polymers <strong>and</strong> Materials,<br />
Kline & Company, Inc., Little Falls, New Jersey, USA<br />
Abstract<br />
The U.S. <strong>and</strong> Chinese markets for synthetic latex polymers in the nonwoven <strong>and</strong> textile markets reached<br />
337,000 dry tons (or 744 million dry pounds) in 1996. Overall, the dem<strong>and</strong> for latex polymers in these<br />
two market segments will grow to 377,000 dry tons (or 831 million dry pounds) in 2001. Latex usage in<br />
nonwovens in these two regions will reach an estimated 202,000 dry tons (or 445 million dry pounds) in<br />
2001, representing average annual growth <strong>of</strong> 2.2% a year. Likewise, dem<strong>and</strong> in the textile market will<br />
grow to 175,000 dry tons (or 386 million dry pounds) in 2001. It is critical to underst<strong>and</strong> that the dem<strong>and</strong><br />
for latex polymer in both markets in the United States will follow that <strong>of</strong> a more mature market, growing<br />
at approximately 2% a year. Dem<strong>and</strong> in China, however, will grow by an estimated 6% a year, but from<br />
a very small base.<br />
Future dem<strong>and</strong> for latex polymers in the nonwovens market will be driven by such factors as:<br />
● Consumer discretionary income <strong>and</strong> preference<br />
● The continued development <strong>of</strong> specialty niche applications<br />
● Capacity changes in nonwoven products<br />
Introduction<br />
"Synthetic latex polymers" are defined as aqueous emulsions that are sometimes referred to as "colloidal<br />
dispersions." They are applied primarily as film formers <strong>and</strong> binding agents throughout a broad range <strong>of</strong><br />
end uses.<br />
Discussion<br />
Nonwovens are described as flat, flexible, porous sheet or web structures produced by binding <strong>and</strong><br />
interlocking fibers, yarns, or filaments by mechanical, thermal, chemical, or solvent means. Synthetic<br />
latex polymers act as binders in the chemical bonding process.<br />
Textile materials are produced from natural <strong>and</strong> synthetic fibers having a finite length or filaments <strong>of</strong><br />
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continuous length. These fibers are processed in three stages:<br />
● yarn manufacturing<br />
● fabric production, <strong>and</strong><br />
● finishing.<br />
Latex polymers may be utilized in the fabric construction stage, however, the majority is consumed in<br />
textile dyeing <strong>and</strong> finishing. They serve as backcoats, h<strong>and</strong> builders, pigment binders, <strong>and</strong> flocking<br />
adhesives in textiles.<br />
Market Size<br />
The nonwovens markets in the United States <strong>and</strong> China are very different in both size <strong>and</strong> process<br />
technology. The worldwide production <strong>of</strong> nonwovens is estimated at 2.2 million tons to 2.5 million tons<br />
(or 4.8 billion pounds to 5.5 billion pounds) in 1994. The United States represented 43% <strong>of</strong> the<br />
nonwoven production, while Asia represented 27% [1]. Of the 15% <strong>of</strong> the total nonwovens market<br />
categorized as "other" regions <strong>of</strong> the world, Kline's estimates place the total production <strong>of</strong> nonwoven<br />
products in China at 160,000 tons in 1995. Nonwoven producers in China number more than 400<br />
companies with approximately 800 production lines [2].<br />
In the United States, nonwovens production is estimated at approximately 2.3 million tons (or 5 billion<br />
pounds). U.S. Department <strong>of</strong> Commerce data indicates that the value <strong>of</strong> nonwoven product shipments is<br />
$4.3 billion in 1996. Approximately 170 nonwovens manufacturing establishments exists in the United<br />
States [4].<br />
Historically, the U.S. nonwovens market first developed around the drylaid process technology. Over the<br />
last half-century, other process technologies have been successfully developed with spunbonding now<br />
representing about one-third <strong>of</strong> the U.S. market. In China, the market is geared more evenly toward<br />
spunbonding, needlepunching, <strong>and</strong> carding.<br />
The textile market in the United States <strong>and</strong> China is also very different in scale <strong>and</strong> structure. The value<br />
<strong>of</strong> U.S. textile product shipments is cited at $79.1 billion in 1995 [5]. Approximately 5,900<br />
establishments in the United States participate in the textile market [6]. In China, textile production in<br />
1995 totaled 24,576 million meters. State-owned textile mills represent an estimated 75% <strong>of</strong> the total<br />
production in China, however, the number <strong>of</strong> local, country-owned enterprises is growing. This is<br />
particularly true in the textile dyeing <strong>and</strong> printing industries in China.<br />
Types <strong>of</strong> Emulsions Consumed<br />
The types <strong>of</strong> emulsions utilized in nonwoven <strong>and</strong> textile applications in both the United States <strong>and</strong> China<br />
are similar, however, the degree to which the products are utilized in each country varies. Pure acrylics<br />
are among the major products in both countries. Likewise, styrene-acrylics are second tier latexes for<br />
nonwoven applications in both countries.<br />
Several dissimilar characteristics also exist between the two countries, as follows:<br />
• Scale: Emulsion consumption in the U.S. nonwovens market totals 164 thous<strong>and</strong> tons (or 362 million<br />
dry pounds) versus the Chinese market at 17 thous<strong>and</strong> dry tons (or 37 million dry pounds), so the United<br />
States is approximately 10 times larger than China.<br />
• Vinyl-acrylics, polyvinyl acetate (PVAc), <strong>and</strong> styrene-butadiene (SBR) are major products for<br />
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nonwovens in the United States, but only minor products in China.<br />
• Vinyl acetate-ethylene (VAE) latexes are major products for nonwovens in the United States, yet are<br />
not consumed in China. In addition, the more specialty products such as polyvinyl chloride (PVC),<br />
polyurethane (PUR), acrylonitrile-butadiene, <strong>and</strong> ethylene-vinyl chloride (EVCL) are only seen in the<br />
United States.<br />
• Scale: Emulsion consumption in the U.S. textile market totals 140 thous<strong>and</strong> tons (or 310 million dry<br />
pounds) versus the Chinese market a 16 thous<strong>and</strong> dry tons (or 35 million dry pounds), so the United<br />
States is approximately nine times larger than China<br />
• PVAc latex is a major product for textiles in the United States, but only a minor product in China<br />
• SBR latex is a major product for textiles in the United States, yet not consumed in China. In addition,<br />
the more specialty products such as PVC, PUR, <strong>and</strong> polyolefins are only seen in the United States<br />
Emulsion Pricing<br />
In general, market prices <strong>of</strong> latex polymers in China are higher than those in the United States. The<br />
average price for the nonwovens market in China was about 10% higher than the United States in 1996.<br />
In the textile market, average prices in China are approximately 33% higher than in the United States.<br />
The higher prices in China can be attributed to several factors including:<br />
• The higher quality level <strong>of</strong> emulsions locally produced by the multinational companies in China versus<br />
the local producers, <strong>and</strong> the resulting gap in prices.<br />
• The smaller sizes, typically in the range <strong>of</strong> 30 kg to 200 kg in China, versus truckloads in the United<br />
States.<br />
• Different terms <strong>of</strong> credit coupled with the fact that many purchases in China are made on a spot basis to<br />
serve short-term needs<br />
Function <strong>of</strong> the Latex Polymer in Nonwovens<br />
As previously noted, latex polymers are the primary binding agent in nonwovens. As such, they are <strong>of</strong>ten<br />
referred to as "chemical binders." One <strong>of</strong> the important attributes <strong>of</strong>fered by latex polymers in nonwoven<br />
applications is the h<strong>and</strong> <strong>of</strong> the finished product. Latexes <strong>of</strong>fer the ability to modify the s<strong>of</strong>tness or<br />
stiffness <strong>of</strong> the nonwoven. The range <strong>of</strong> h<strong>and</strong> characteristics <strong>of</strong> the nonwoven is impacted by the<br />
selection <strong>of</strong> the latex type. Generally speaking, acrylics <strong>of</strong>fer a wide range in h<strong>and</strong> from s<strong>of</strong>t to stiff.<br />
PVAc latex possesses inherent stiffness. Other latexes such as VAE, SBR, <strong>and</strong> vinyl-acrylics impart h<strong>and</strong><br />
qualities that range between the two extremes.<br />
Latex polymers are largely responsible for the tensile strength <strong>of</strong> the nonwoven product. In addition,<br />
latexes also impact other properties such as tear, grab, burst, <strong>and</strong> seam strength. As a rule <strong>of</strong> thumb, the<br />
latex polymers that are not self-cross-linking yield good dry strength but redisperse on exposure to water.<br />
Likewise, the emulsions that are self-cross-linking <strong>of</strong>fer good wet strength.<br />
Color fastness <strong>of</strong> the nonwoven is also largely impacted by the selection <strong>of</strong> the latex polymer. Acrylic<br />
latexes <strong>of</strong>fer the best results in terms <strong>of</strong> color fastness. At the other extreme, both PVAc <strong>and</strong> SBR latex<br />
polymers have poor color fastness. PVAc experiences issues with fading after washing, while SBR tends<br />
to yellow upon exposure to heat <strong>and</strong> light.<br />
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Mechanical properties such as flexibility, stretch <strong>and</strong> crease recovery, <strong>and</strong> abrasion resistance, among<br />
others, are important attributes in nonwovens. Acrylic <strong>and</strong> SBR latex polymers typically are known for<br />
their good flexibility, while PVAc is viewed as more brittle.<br />
Other important attributes impacted by the choice <strong>of</strong> latex polymer include absorbency, flammability,<br />
<strong>and</strong> permeability.<br />
Function <strong>of</strong> the Latex Polymer in Textiles<br />
The function <strong>of</strong> latex polymers in the textile industry is generally categorized as coatings/backcoatings,<br />
h<strong>and</strong> builders, pigment binders, or flocking adhesives. In coatings, the latex polymer enhances fabric<br />
tensile strength, surface abrasion resistance, <strong>and</strong> stiffness. In backcoating applications, the latex provides<br />
strength, durability, <strong>and</strong> wear resistance.<br />
The selection <strong>of</strong> the latex type impacts the h<strong>and</strong>-or manner in which the textile fabric feels-by s<strong>of</strong>tening,<br />
stiffening, or adding body to the product. PVAc latex polymers typically stiffen <strong>and</strong> add body to textiles,<br />
while polyethylene (PE) latexes s<strong>of</strong>ten the products. Acrylics can be manufactured to <strong>of</strong>fer a wide range<br />
<strong>of</strong> h<strong>and</strong> characteristics, depending upon the application.<br />
In pigment processes, latex polymers such as acrylics are combined with the dyes <strong>and</strong> other additives <strong>and</strong><br />
then applied to the fabric surface. The latex serves to hold the color into the fabric for processes such as<br />
screen <strong>and</strong> engraved roll printing.<br />
Finally, latex polymers serve as a binder or "flocking adhesive" to adhere fibers to a cheesecloth in the<br />
production <strong>of</strong> imitation velour fabrics. This process is typically seen in such market segments as<br />
upholstery <strong>and</strong> ribbons.<br />
Latex Consumption<br />
Overall, China is an emerging market for latex emulsions. The consumption <strong>of</strong> latex emulsions in<br />
nonwovens <strong>and</strong> textiles in the United States is approximately 10 times larger than in China. However, as<br />
previously noted, the types <strong>of</strong> emulsions utilized in nonwoven <strong>and</strong> textile applications in both the United<br />
States <strong>and</strong> China are somewhat similar. Pure acrylics are the major products in both countries. In fact, the<br />
dominance <strong>of</strong> acrylic latexes in China compared to that in the United States is striking. In addition, the<br />
percentage <strong>of</strong> the total dem<strong>and</strong> in each region represented by vinyl-acrylic emulsions is almost identical.<br />
As previously noted, VAE dem<strong>and</strong> in the United States is significant while it is not seen at all in China,<br />
Finally, specialty emulsion products are consumed in the United States but not in China.<br />
Channels <strong>of</strong> Distribution<br />
The channels <strong>of</strong> distribution for supply <strong>of</strong> latex emulsions differ in the United States <strong>and</strong> China. In the<br />
United States, the level <strong>of</strong> captive production <strong>and</strong> imports <strong>of</strong> emulsion polymers to serve the nonwoven<br />
<strong>and</strong> textile markets is very minor, if it exists. In China imports are significant, representing 22% <strong>of</strong> the<br />
total Chinese dem<strong>and</strong> in these two markets.<br />
Leading Suppliers<br />
One <strong>of</strong> the largest suppliers <strong>of</strong> latex emulsions to the nonwoven <strong>and</strong> textile markets in the United States<br />
<strong>and</strong> China is Rohm <strong>and</strong> Haas. In addition to Rohm <strong>and</strong> Haas, the United States is also served by three<br />
other significant suppliers <strong>and</strong> a host <strong>of</strong> other minor producers <strong>of</strong> latex polymers. Other leading suppliers<br />
<strong>of</strong> latexes in China include Union Carbide <strong>and</strong> Lan Zhou Petrochemical.<br />
Major Trends in the United States<br />
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Several processing changes have impacted the U.S. nonwovens market in the past, <strong>of</strong> which some<br />
continue today. Among them:<br />
Thermal bonding: Beginning in the 1980s, the U.S. nonwovens industry saw a change from drylaid<br />
processing <strong>of</strong> polyethylene terephthlate (PET) to thermal bonding <strong>of</strong> polypropylene (PP) in the diaper<br />
coverstock segment. This negatively impacted the dem<strong>and</strong> for latex polymers in this market segment in<br />
the 1980s <strong>and</strong> early 1990s. In addition, in the recent two to three years, the apparel interlinings <strong>and</strong><br />
automotive markets have also shifted to thermal bonding, resulting in a decline <strong>of</strong> latex dem<strong>and</strong> for these<br />
applications.<br />
Spunbonding: Overcapacity in the spunbonding segment <strong>of</strong> the U.S. nonwovens market, combined with<br />
the economics <strong>of</strong> this process, has also negatively impacted latex dem<strong>and</strong> in recent years. The<br />
spunbonding process <strong>of</strong>fers advantages in that the latex cost is cut entirely, while the fiber cost can be<br />
reduced by approximately one-half due to the product form.<br />
Spunlace: In some segments <strong>of</strong> the towels <strong>and</strong> wipes market, spunlace products are beginning to see<br />
acceptance. However, the major br<strong>and</strong>s such as H<strong>and</strong>i Wipes <strong>and</strong> Chicks had remained with<br />
latex-bonded technology as <strong>of</strong> late 1996.<br />
Despite the negative impact <strong>of</strong> some <strong>of</strong> these changes, several niche applications exist which are viewed<br />
as <strong>of</strong>fering a brighter potential for latex polymers in the U.S. nonwovens market. Among these is the<br />
baby wipe market, which is a strong consumer <strong>of</strong> VAE latexes in airlaid processes <strong>and</strong> is one <strong>of</strong> the faster<br />
growing segments <strong>of</strong> the nonwovens market. On the positive side, acrylic latex dem<strong>and</strong> has been<br />
impacted by a strengthening in the market for latex-bonded acquisition layers for diapers which replaced<br />
tissue paper. However, even this segment is thought to be at risk for a potential shift to thermal bonding<br />
technology in the future. In addition, the imitation leather sector <strong>of</strong>fers opportunities for PVC <strong>and</strong> PUR<br />
specialty latex polymers. Finally, the ro<strong>of</strong>ing membrane market <strong>of</strong>fers opportunities for SBR <strong>and</strong> acrylic<br />
based latexes.<br />
Opportunities also exist in niche segments <strong>of</strong> the U.S. textile market. As a result, much <strong>of</strong> the new<br />
product <strong>and</strong> application development by latex producers centers around these new opportunities. For<br />
example, Para-Chem has developed a new acrylic copolymer that improves strength yet <strong>of</strong>fers s<strong>of</strong>tness<br />
for backcoating applications. Para-Chem is also promoting a new acrylic copolymer with flame-retardant<br />
properties for both nonwovens <strong>and</strong> textiles. Likewise, Scott Bader is promoting a blend <strong>of</strong> acrylic <strong>and</strong><br />
acrylonitrile polymers for better color values in pigment dyeing. Finally, VAE latex has found success in<br />
flocking <strong>of</strong> polyolefin ribbons.<br />
Consolidation has occurred in the nonwovens industry as a means <strong>of</strong> addressing changing market<br />
conditions <strong>and</strong> growing share. Examples include the merger <strong>of</strong> Kimberly-Clark <strong>and</strong> Scott Paper Co. in<br />
diapers, Proctor & Gamble's acquisitions in Europe <strong>and</strong> South America in diapers <strong>and</strong> feminine products,<br />
<strong>and</strong> Tyco's acquisition <strong>of</strong> medical products manufacturer Kendall, among others.<br />
Major Trends in China<br />
Similar to the United States, some process changes are occurring in both the nonwoven <strong>and</strong> textile<br />
markets in China that will impact the dem<strong>and</strong> for latex polymers. Among them:<br />
• In nonwovens, a shift in processing from drylaid technologies has occurred in the last 10 to 12 years.<br />
The result is that the percentage <strong>of</strong> nonwovens production represented by needlepunched drylaid<br />
products has declined significantly <strong>and</strong> chemical-bonded drylaid products have marginally declined<br />
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Trends In Latex Emulsions<br />
while spunlaid <strong>and</strong> melt blow processing has increased [7]. The primary impact <strong>of</strong> these technologies<br />
upon latex polymer dem<strong>and</strong> has been that such newer technologies do not always utilize latexes.<br />
• In the textile industry, China is being severely impacted by loss <strong>of</strong> business to other regions, including<br />
Indochina, the Indian subcontinent, <strong>and</strong> the Middle East. Part <strong>of</strong> the shift is attributed to subst<strong>and</strong>ard<br />
product quality from textile materials manufactured in China. The technology employed in a number <strong>of</strong><br />
textile processes is not as well developed in China as in other regions <strong>of</strong> the world. Investments in new,<br />
higher quality processing technologies have not been sufficient to stem the tide <strong>of</strong> competition.<br />
The outlook for the nonwoven <strong>and</strong> textile industries in China is varied. In the nonwovens market,<br />
opportunities for spunlaid technologies are viewed as greater than that for traditional products. However,<br />
the overall Chinese market for chemically bonded nonwovens is still viewed as a high growth potential<br />
from its current base. Thus, latex polymer dem<strong>and</strong> for existing <strong>and</strong> new chemically bonded products will<br />
be strong. On the other h<strong>and</strong>, the textile market in China is not expected to grow a great deal over the<br />
coming five years <strong>and</strong> the potential exists for continued declines in some segments. The longer-term<br />
prospects will be more promising if state-owned textile mills are able to invest in new technologies to<br />
make themselves more competitive. In terms <strong>of</strong> segments <strong>of</strong> the market where latex polymers are<br />
consumed, some growth in pigment binding is anticipated.<br />
Opportunities for more specialized product developments exist in China. In the nonwovens market, some<br />
technical development has been directed at formulating products with a suitable cost versus performance<br />
balance for applications in the domestic market where dry cleaning practices are not as common or<br />
severe. In another nonwoven application, low formaldehyde products are being used in certain clothing<br />
types such as baby wear <strong>and</strong> undergarments.<br />
Conclusions<br />
What does all <strong>of</strong> this mean for latex emulsions? In general, the nonwoven <strong>and</strong> textile markets will<br />
continue to be important to dem<strong>and</strong> for latex polymers. Opportunities for growth exist in both the United<br />
States <strong>and</strong> China. Overall, the dem<strong>and</strong> for latex polymers in these two market segments will grow to 377<br />
thous<strong>and</strong> dry tons (or 831 million dry pounds) in 2001. Latex usage in nonwovens in these two regions<br />
will reach an estimated 202 thous<strong>and</strong> dry tons (or 445 million dry pounds) in 2001, representing an<br />
average annual growth <strong>of</strong> 2.2% a year. Likewise, dem<strong>and</strong> in the textile market will grow to 175 thous<strong>and</strong><br />
dry tons (or 386 million dry pounds) in 2001.<br />
So, growth will occur in both market segments, albeit at different paces for the two countries.<br />
Consumption <strong>of</strong> synthetic latex polymers in the U.S. nonwoven <strong>and</strong> textile markets will reach 333<br />
thous<strong>and</strong> dry tons (or 734 million dry pounds) in 2001. This represents average growth <strong>of</strong> 1.8% a year in<br />
the coming five years in the United States, typical <strong>of</strong> a more mature market.<br />
Dem<strong>and</strong> for latex polymers in the Chinese nonwoven <strong>and</strong> textile market will increase from 33 thous<strong>and</strong><br />
dry tons (or 72 million dry pounds) in 1996 to 44 thous<strong>and</strong> dry tons (or 97 million dry pounds) in 2001.<br />
This is representative <strong>of</strong> a 6.1% a year growth rate for China, but from a very small base.<br />
References:<br />
1. Smith, T., <strong>and</strong> Smith, D., Nonwoven Markets 1996 International Factbook <strong>and</strong> Directory, Miller<br />
Freeman, Inc., San Francisco, 1996, p. 7.<br />
2. China Nonwoven Association<br />
3. 1995 Annual Survey <strong>of</strong> Manufacturers, U.S. Department <strong>of</strong> Commerce, Washington, DC, January<br />
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1997, p. 2-11.<br />
4. 1992 Census <strong>of</strong> Manufacturers, U.S. Department <strong>of</strong> Commerce, Washington, DC, May 1995 p.<br />
22E-10.<br />
5. 1995 Annual Survey <strong>of</strong> Manufacturers, U.S. Department <strong>of</strong> Commerce, Washington, DC, January<br />
1997, p. 2-10 <strong>and</strong> 2-11.<br />
6. 1992 Census <strong>of</strong> Manufacturers, U.S. Department <strong>of</strong> Commerce, Washington, DC, March <strong>and</strong> May<br />
1995, p. 22A-9, 10; 22B-12, 13, 14; 22C-9, 10, 11; 22D-9; 22E-9, 10, 11.<br />
7. China Nonwoven Association<br />
This paper was originally submitted for publication in the TAPPI_<strong>Journal</strong>. The INJ_editors <strong>and</strong><br />
publishers wish to express their appreciation to TAPPI_for their support <strong>and</strong> encouragement.<br />
Return to International Nonwovens <strong>Journal</strong><br />
Home Page & Table <strong>of</strong> Contents<br />
- INJ<br />
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Fiberglass Surface<br />
ORIGINAL PAPER/PEER REVIEWED<br />
Fiber Renaissance For<br />
The Next Millennium<br />
By Arun Pal Aneja, Dacron® Research Laboratory, DuPont Company, Kinston, NC<br />
Abstract<br />
As we enter 21st century, technical advances are dramatically influencing the world <strong>of</strong> fibers, fabrics <strong>and</strong><br />
textiles. Today, technology can provide us with fabrics that imitate <strong>and</strong> actually improve upon nature's best<br />
fibers. In the next millennium, textiles will not just be an extension or simple alternatives to natural or<br />
synthetic fibers, but will provide superior functionality in broad <strong>and</strong> emerging sectors <strong>of</strong> the economy from<br />
space to super conductivity <strong>and</strong> agriculture to geotextile. This will be accomplished through modern business<br />
strategies for enhanced stakeholder value <strong>and</strong> highly efficient production schemes with no adverse impact on<br />
the environment <strong>and</strong> development <strong>of</strong> precisely specified molecules for new textile platforms.<br />
Introduction<br />
We are living in a world in which technology is advancing at such an astonishing rate that most <strong>of</strong> us have<br />
difficulty comprehending the overall impact it has, <strong>and</strong> will continue to have, on our lives. Cloning <strong>of</strong> adult<br />
mammals, World Wide Web, smart materials, high-speed processors <strong>and</strong> wonder drugs continue to dazzle us<br />
almost on a daily basis. The textile industry has kept pace <strong>and</strong> technology today can provide fabrics that go<br />
well beyond the best that nature has to <strong>of</strong>fer. It is, indeed, a narrow view to think <strong>of</strong> textiles as a fixed<br />
discipline <strong>of</strong> making "strings." It is much more diverse than that <strong>and</strong> most importantly, it is in a state <strong>of</strong> flux<br />
in response to changing needs <strong>of</strong> society <strong>and</strong> new innovations. The inherent characteristics <strong>of</strong> new textiles<br />
underpin the functional <strong>and</strong> aesthetic qualities <strong>of</strong> these many <strong>and</strong> varied applications from the world <strong>of</strong><br />
fashion to agriculture, medical, aerospace, reinforced composites <strong>and</strong> architecture. There has been rapid<br />
growth in polymer, material, information <strong>and</strong> biological sciences. The advance, in these adjacent sciences<br />
<strong>and</strong> their inevitable interface, will catalyze the reconceptualization <strong>of</strong> tomorrow's textiles. This concept <strong>of</strong><br />
interdisciplinary research, development <strong>and</strong> product innovations will lead to new textile platforms for the<br />
next millennium.<br />
Looking back on the history <strong>of</strong> fibers, you will find that most natural fibers originated in Asia. Cotton <strong>and</strong><br />
silk are native to China <strong>and</strong> India, while wool was first put to practical use in Central Asia. It is widely<br />
known that the Silk Road was opened by the strong desire <strong>of</strong> Western peoples to acquire silk products<br />
originating in China<br />
Meanwhile, the history <strong>of</strong> man-made fibers began with the invention <strong>of</strong> rayon in the late 19th century.<br />
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Figure 1<br />
GLOBAL GROWTH OF MAN-MADE FIBERS<br />
OVER THIS CENTURY<br />
Following the invention <strong>of</strong> nylon in 1935 by Wallace<br />
Hume Carothers at DuPont, acrylic <strong>and</strong> polyester<br />
fibers were developed [1], leading to increased<br />
research activities for a variety <strong>of</strong> new materials<br />
comprised mainly <strong>of</strong> these three major synthetic<br />
fibers. New fiber-making technologies suitable for the<br />
new materials were invented. New high-performance<br />
fibers including, among others, carbon <strong>and</strong> aramid<br />
fibers, are also beginning to mature. Thirty-five years<br />
after the invention <strong>of</strong> nylon, world-wide synthetic<br />
fibers surpassed man-made cellulose. Today,<br />
synthetic fibers have surpassed natural fiber<br />
production (Figure 1).<br />
Trends <strong>and</strong> Current Concerns<br />
Over the last 60 years the textile business has enjoyed<br />
rapid growth in synthetic fibers, fueled largely by<br />
seminal discoveries in polymer <strong>and</strong> fiber science. Fiber <strong>and</strong> textile manufacturing facilities also have<br />
undergone enormous improvements in automation <strong>and</strong> simplification where large volume fiber production<br />
facilities today may require only tens (instead <strong>of</strong> hundreds) <strong>of</strong> personnel for their operation.<br />
<strong>Fibers</strong> that have ease <strong>of</strong> care <strong>and</strong> natural-like<br />
aesthetics have been major themes in recent decades,<br />
with high performance <strong>and</strong> specialty fibers taking on<br />
particular significance. Fiber <strong>and</strong> fabric tests, critical<br />
to product quality have relied largely on destructive,<br />
<strong>of</strong>f-line methods. Advances in testing <strong>and</strong> quality<br />
control promise to have a major impact on first pass<br />
product yields <strong>and</strong> product quality.<br />
Figure 2<br />
DISCOVERY OF TEXTILE FIBERS<br />
(The fibers discovered by DuPont or in collaboration<br />
with DuPont are to the right <strong>of</strong> the worldwide<br />
synthetic fiber growth curve. The fibers discovered<br />
by the rest <strong>of</strong> the world are to the left <strong>of</strong> the curve)<br />
DuPont pioneered the fiber revolution <strong>of</strong> the 20th<br />
century (Figure 2). Looking to the next millennium,<br />
the textile industry st<strong>and</strong>s in stark contrast to its<br />
preeminent position <strong>of</strong> just 20 years ago. Many <strong>of</strong> the<br />
synthetic fiber products that once fueled the rapid<br />
growth <strong>of</strong> the industry have become mature<br />
commodity products now characterized by low<br />
growth <strong>and</strong> lower pr<strong>of</strong>it margins. Intense global cost<br />
pressures, higher consumer expectations, a highly<br />
diverse customer base <strong>and</strong> reduced R&D spending<br />
have all contributed to the current state <strong>of</strong> affairs. The<br />
challenge for the future is to revitalize the industry - a<br />
fiber renaissance - through technological innovations<br />
in products <strong>and</strong> manufacturing <strong>and</strong> to reevaluate business practices in a global context.<br />
Ecological Factors<br />
The delicate balance that exists in the planet's ecosystem is well understood around the world <strong>and</strong> grassroots<br />
organizations exist in most countries for its preservation. There is also increased awareness <strong>of</strong> the harmful<br />
environmental effects <strong>of</strong> most manufacturing processes. If textile industry is to survive, it too must take a<br />
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leading role in "environmentalism." Indeed, companies researching new textiles are making ecology a<br />
primary concern. Some, in fact, will not develop new products unless they can be made safely <strong>and</strong> without<br />
deleterious impact to the environment. The companies are fully aware <strong>of</strong> the fact that world's resources will<br />
soon be depleted unless major changes are implemented in manufacturing systems. These are:<br />
● Waste elimination<br />
❍ Reduce<br />
❍ Reuse<br />
❍ Redesign<br />
● Energy conservation<br />
● Reclamation<br />
● Recycle<br />
All steps <strong>of</strong> the textile processing value chain from raw material conversion to fabric disposal must be<br />
environmentally friendly. We must close the recycling loop (polymer, fiber, product to l<strong>and</strong>fill) for all<br />
polymers with no material ever entering the l<strong>and</strong>fill.<br />
Processes <strong>of</strong> the Future<br />
Commodity fibers technology is generally mature <strong>and</strong> broadly available to investors. Hence, competitive<br />
advantages in process technology around the world are shrinking fast. The progress in process technology for<br />
the future will mainly be driven by the following factors:<br />
● Knowledge intensity<br />
● Highly competitive market with resultant ultra-high quality products <strong>and</strong> productivity<br />
● Fiber production by a few large companies with availability <strong>of</strong> diverse fibers<br />
● Strong business alliance for ease <strong>of</strong> market access<br />
● Capacity rationalization <strong>and</strong> decentralized business structures for shareholder value<br />
● Strategic shifts for competitiveness <strong>and</strong> reduced risk<br />
● Collapsed value chain with control moving downstream<br />
● Consistent global pricing<br />
● Rapid information exchange<br />
The last decade in the textile sector has seen major reduction in cost <strong>and</strong> productivity improvement. This is<br />
due to innovations in processing technologies <strong>of</strong> automation, increased spinning speed, production capacity<br />
<strong>and</strong> process simplification. The production cost variance <strong>of</strong> fiber manufacturers is governed by two factors:<br />
(1) investment cost per ton <strong>of</strong> fiber dictated by economy <strong>of</strong> scale <strong>and</strong> (2) price advantage <strong>of</strong> basic feedstock.<br />
The investment cost for new plants are determined by raw material conversion cost (size <strong>of</strong> reactor),<br />
operating speeds <strong>of</strong> spinning, drawing <strong>and</strong> texturing, <strong>and</strong> quench technology to obtain the desired fiber<br />
morphology.<br />
Future fiber manufacturing technology must also accommodate mass customization in the market place.<br />
Hence, a system <strong>of</strong> specialized product variants for small-lot production will provide high value-added<br />
products to the consumer. The challenge for the future will be the development <strong>of</strong> efficient small-scale<br />
production technology for such products.<br />
Biotechnology<br />
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The route to new polymer platforms will most likely emerge from biological synthesis <strong>of</strong> polymeric<br />
materials for the precise synthesis <strong>of</strong> modular building blocks for polymeric materials. The need for exquisite<br />
tailoring <strong>and</strong> uniformity <strong>of</strong> macromolar structure has never been greater. Macromolecular synthesis <strong>of</strong><br />
polymers by biological route will take on increasing importance <strong>and</strong> traditional chemicals will be made<br />
through biotechnology. It is no longer necessary to start with a barrel <strong>of</strong> oil to produce chemicals. Corn,<br />
beets, rice - even potatoes - make great feedstocks. Yeast, grain <strong>and</strong> water can be used to make a fine quality<br />
ale, or for that matter, other molecules. Comfortable, easy-care apparel may soon be made with fibers spun<br />
from chemicals that have been fermented from sugar. [2]<br />
DuPont is building a pilot plant that uses genetically altered microorganisms to produce basic chemicals that<br />
are not made from petroleum. Biotechnology will ferment glucose <strong>and</strong> produce intermediates that can then<br />
be used to make nylon <strong>and</strong> polyester. The process is less expensive <strong>and</strong> kinder to the environment than<br />
traditional chemical methods. Our progress is far exceeding our expectations. If the pilot goes well, the<br />
process could be commercialized in the near future.<br />
Figure 3<br />
PRECICELY SPECIFIED MOLECULES —<br />
BIOSYNTHETIC SCHEMATIC<br />
The transformation <strong>of</strong> sugars into alcohol by<br />
microscopic organisms has been known for 4000<br />
years. With the advent <strong>of</strong> genetic engineering, we can<br />
now harness the sophistication <strong>of</strong> biological systems<br />
to create molecules that are difficult to synthesize by<br />
traditional methods.<br />
For example, the polymer polytrimethylene<br />
terephthalate (3GT) has enhanced properties as<br />
compared to traditional polyester (2GT). Yet the<br />
commercialization has been slow because <strong>of</strong> the high<br />
cost to make one <strong>of</strong> 3GT's intermediates. Through<br />
recombinant DNA technology, DuPont <strong>and</strong> Genecor<br />
Figure 4<br />
UNIQUE STRESS-STRAIN PROPERTIES<br />
OF SPIDER SILK<br />
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have created a single microorganism with all the<br />
enzymes to convert cornstarch to sugar into this<br />
intermediate. This breakthrough is opening the door<br />
to low-cost, environmentally sound, large-scale<br />
Figure 5<br />
MATERIALS REVOLUTION OF THE 21ST<br />
CENTURY<br />
production <strong>of</strong> this enhanced polyester that will eventually approach the cost <strong>of</strong> traditional polyester. With<br />
two decades <strong>of</strong> research, DuPont is making an ambitious push in biotechnology that may transform DuPont<br />
<strong>and</strong> the textile industry. Today, we have two classes <strong>of</strong> materials in man-made fibers: man-made cellulosics<br />
made from natural sources such as pulped wood, cotton or vegetable materials; <strong>and</strong> true synthetics made<br />
from products <strong>of</strong> the petrochemicals <strong>and</strong> natural gas industries. Tomorrow, we will have a new class <strong>of</strong> fibers<br />
- natural synthetics made from agricultural crops - <strong>and</strong> new polymer <strong>and</strong> fibers that we have not even<br />
conceived.<br />
The success <strong>of</strong> our initial demonstrations in creating synthetic spider silk illustrates the new materials<br />
revolution that will be ushered into the 21st century. By using recombinant DNA <strong>and</strong> learning exactly how a<br />
spider makes its silk, DuPont scientists have created synthetic spider silk as a model for a new generation <strong>of</strong><br />
advanced materials. For spider silk, we use advanced computer simulation techniques that design a<br />
molecular model to integrate all the information available to date about the structure <strong>of</strong> this amazingly strong<br />
<strong>and</strong> elastic fiber. Synthetic genes are then designed to encode gene matching the silk proteins (Figure 3).<br />
These genes are inserted into yeast <strong>and</strong> bacteria to produce the silk proteins. The protein is dissolved <strong>and</strong><br />
then spun into biosilk fibers.<br />
Spider silk is the most dramatic example <strong>of</strong> a sizable family <strong>of</strong> biopolymers possessing a combination <strong>of</strong><br />
properties that synthetic materials cannot yet approach. With its lightweight, tough <strong>and</strong> elastic properties, our<br />
learnings from biosilk may improve the properties <strong>of</strong> our existing products such as Lycra® <strong>and</strong> nylon.<br />
Synthetic spider silk may help create super-performing garments <strong>of</strong> the future (Figure 4). More importantly,<br />
the new generation <strong>of</strong> advanced materials from spider silk <strong>and</strong> biotechnology research have the potential to<br />
transform our lives in countless ways we can scarcely imagine.<br />
<strong>Engineered</strong>/Smart Performance <strong>Fibers</strong><br />
The degree to which it is possible to engineer textiles today is truly astonishing. There is an increasing need<br />
for fabrics that can combine strength, functionality, fabric h<strong>and</strong>le/tactility <strong>and</strong> enhanced mill value; all <strong>of</strong> this<br />
at competitive cost. Natural fibers, which dominated textile commerce until a few years ago, can be<br />
identified as the first generation (Figure 5). Synthetic fibers such as nylon, polyester <strong>and</strong> polypropylene,<br />
which were in response to improvements in natural fibers <strong>and</strong> currently dominate, are the second generation.<br />
The third generation textiles <strong>and</strong> beyond are not simply alternatives to natural or synthetic fibers but must<br />
provide superior functionality in broad emerging sectors <strong>of</strong> the economy from space to super conductivity<br />
<strong>and</strong> agriculture to geotextiles.<br />
Table 1<br />
PRODUCT TRENDS - 'SUPER' FIBERS<br />
Modulus gpd/(Gpa/gm/cm 3 ) Strength gpd/(Gpa/gm/cm 3 )<br />
Theoretical Observed Theoretical Observed<br />
PET 1023/1.12 160/0.18 232/0.25 9.5/0.01<br />
Nylon 6 1406/1.53 50/0.06 316/0.35 9.5/0.01<br />
PAN 833/0.91 85/0.09 196/0.21 5/0.006<br />
As the interface between polymer science <strong>and</strong> biotechnology merges, textiles will evolve to adaptive<br />
technology-textiles that adapt to the environment around you. [3,4] Today's clothing is essentially passive.<br />
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Table 2<br />
PRODUCT TRENDS - FUNCTIONAL FIBERS<br />
Textile Functions Application<br />
Thermal<br />
High Temperature Insulation<br />
Electrical<br />
Grounding, Signal Transmission<br />
Optical<br />
UV Protector, Light Refraction,<br />
Communication<br />
Acoustic<br />
Sound Absorbing<br />
Magnetic<br />
Magnetic Filaments<br />
Separation/Absorption Gas/Water Purification,<br />
Medical Applications<br />
Adhesion<br />
Hot Melt Adhesion, Concrete<br />
Reinforcement<br />
Materials<br />
Anti-Bacteria<br />
Barrier Properties<br />
Stretch<br />
Pillows, Geriatric/Baby Clothing<br />
Waterpro<strong>of</strong>, Water-Perishable<br />
Comfort, Fit<br />
you cooler. This places a whole new meaning to smart, intelligent garments.<br />
Your clothing reacts only<br />
after your body does<br />
something. With Lycra®,<br />
your clothing stretches <strong>and</strong><br />
moves as you move. With<br />
Coolmax®, your clothing<br />
wicks moisture away after<br />
your perspire. The<br />
clothing <strong>of</strong> the 21st<br />
century will be active.<br />
Your clothing will<br />
recognize the environment<br />
surrounding you <strong>and</strong> adapt<br />
to that environment.<br />
Instead <strong>of</strong> waiting for you<br />
to become hot <strong>and</strong><br />
perspire, your clothing<br />
will sense that it is hot<br />
outside <strong>and</strong> adapt to make<br />
With the advent <strong>of</strong> high-strength fibers, we can now aspire to approach the theoretical limit in a whole host<br />
<strong>of</strong> functionalities. The strength <strong>of</strong> existing synthetic fibers can be increased many times (Table 1). Fiber<br />
functionality will be improved (Table 2) to yield novel applications in the future.<br />
Conclusion - The Emerging Paradigm<br />
The essence <strong>of</strong> new product development in fiber<br />
science during the 20th century has followed a<br />
relatively narrow <strong>and</strong> perhaps limited route <strong>of</strong><br />
development. <strong>Fibers</strong> are made from either<br />
condensation or addition-type polymer platforms. The<br />
fiber may have polymer modifications, contain<br />
additives or be altered on the surface. This has<br />
resulted in textiles from nylon <strong>and</strong> Dacron® which<br />
may be cationic dyeable, flame retardant <strong>and</strong> with<br />
whitener/delusterant features available in a variety <strong>of</strong><br />
cross section <strong>and</strong> surface treatments.<br />
The next century, however, will demonstrate the<br />
seemingly unlimited power <strong>of</strong> the synergy <strong>of</strong> diverse<br />
disciplines as borders between material science,<br />
Figure 6<br />
EMERGING PARADIGM FOR<br />
TEXTILE FIBER SCIENCE<br />
biological science <strong>and</strong> information science blur <strong>and</strong> erode (Figure 6). Today the breadth <strong>of</strong> complementary<br />
technologies is far greater. In the future fiber molecules will be designed, engineered <strong>and</strong> produced more<br />
efficiently than ever before due to advances in combinatorial chemistry, robotics, nanotechnology,<br />
bioinformatics, spectroscopy, <strong>and</strong> high-throughput screening.<br />
We will continuously seek to express a desired property in a molecule or a material, whatever be the<br />
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composition <strong>and</strong> the structure, <strong>and</strong> develop strategies towards building precise molecules with desired<br />
properties <strong>and</strong> functions [5,6]. This will finally result in smart textile materials with attributes <strong>of</strong> selectivity,<br />
sensitivity, shapability, self recovery, self repair, self diagnosis, self tuning <strong>and</strong> switchability.<br />
References<br />
1. Hiratzuka, S. 1996. "Present Situation <strong>and</strong> Future Outlook for Technological Developments in Man-Made<br />
<strong>Fibers</strong>," JTN, July, 1996, pp. 56-76.<br />
2. Siegel, D&S. Birk 1998. "Fiber Development in 21st Century," Mark & Spence Lingerie Conf., UK.<br />
3. Aneja, A. P. 1994. "Wear No One Has Made Before," Chemtech, August, 1994, pp. 48-52.<br />
4. Aneja, A. P. <strong>and</strong> Popper, P. 1997. "Trends in U.S. Fiber Technology," Proceedings <strong>of</strong> the International<br />
Conference on Advances in Fiber <strong>and</strong> Textile Science <strong>and</strong> Technology, Mulhouse, France, April, 1997.<br />
5. Aneja, A.P. <strong>and</strong> J.P. O'Brien. <strong>1999</strong>, "21st Century <strong>Fibers</strong>." Int. Fiber J., August <strong>1999</strong>.<br />
6. O'Brien, J.P., <strong>and</strong> Aneja, A.P., <strong>1999</strong>. "<strong>Fibers</strong> for the Next Millennium." J. <strong>of</strong> Soc. <strong>of</strong> Dyers <strong>and</strong> Colourists,<br />
U.K. Accepted for publication.<br />
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