Annual Meeting Preliminary Program - Full Brochure (PDF) - SME
Annual Meeting Preliminary Program - Full Brochure (PDF) - SME
Annual Meeting Preliminary Program - Full Brochure (PDF) - SME
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TECHNICAL PROGRAM<br />
wall face approached and entered into the western edge of the sandstone channel.<br />
The longwall face mined through the center axis of the sandstone channel in mid-<br />
January 2012 and advanced outby the eastern edge of the sandstone channel in<br />
early February 2012. Results from daily underground observations and production<br />
delay analysis confirmed the effectiveness of the hydraulic fracturing program<br />
and the validity of the LVA Software.<br />
chair:<br />
9:00 AM<br />
Introductions<br />
environmental:<br />
Mine Water treatment II<br />
9:00 AM • Wednesday, February 27<br />
M. Mierzejewski, CH2MHill, Richmond, VA<br />
9:05 AM<br />
Antiscalants for Gold Processing Applications<br />
W. Dickinson; R&D, Kemira Chemical, Atlanta, GA<br />
Mineral scale adversely affects the performance of activated carbon circuits used<br />
in gold extraction. The performance of ten antiscalants spanning a range of<br />
chemistries was evaluated for control of calcium carbonate scale in simulated carbon<br />
circuit process water. Three preferred chemistries were identified which provided<br />
greater than 75 percent CaCO3 inhibition under static test conditions. The<br />
three products were further tested using a model carbon extraction circuit developed<br />
for this application. The test circuit enabled direct measurement of calcium<br />
carbonate formed on the carbon from a supersaturated solution under dynamic<br />
conditions. The antiscalants improved calcium transport through the circuit by as<br />
much as 60% while reducing CaCO3 buildup on the columns by 30 40 percent.<br />
On-site testing at a gold processing facility where severe CaCO3 scale was restricting<br />
flow and plugging pipelines demonstrated that the preferred product was<br />
able to reduce CaCO3 formation in thickener overflow water by greater than<br />
70%. Impact of the antiscalants on the rate and extent of gold loading onto carbon<br />
absorbent was also established.<br />
9:25 AM<br />
High Recovery Sulfate Removal Process for Chemically Efficient<br />
Removal of Sulfate From Acid Mine Drainage<br />
S. Karrs and J. Ceklosky; Siemens, Warrendale, PA<br />
Siemens Industry, Inc., a Water Technologies Business Unit, has developed a<br />
High Recovery Sulfate Removal (HRSR) process aimed at the removal of high<br />
levels of sulfate from lime neutralized Acid Mine Drainage (AMD) with minimal<br />
chemical costs. The HRSR process involves treating an influent stream containing<br />
calcium sulfate concentrations at 0.7 to 2 times saturation. This stream is then<br />
conditioned with an antiscalant prior to a Reverse Osmosis (RO) system producing<br />
a purified permeate stream and a reject stream containing the rejected ions at<br />
2 to 7 times saturation and organic matter. The reject stream is further treated to<br />
remove dissolved and suspended species through a desaturation/clarification<br />
process. The preferred desaturation process occurs via a Constant Stirred Tank<br />
Reactor (CSTR) wherein a coprecipitation/antiscalant poisoning/seeding agent<br />
is added followed by clarification. The clarifier overflow is recycled back to the influent<br />
stream whereas the clarifier underflow is disposed of in a manner consistent<br />
with applicable regulations. Additional details of Siemens piloting experience<br />
will be presented in this document.<br />
9:45 AM<br />
Important Characteristics of Membranes for Reliable Performance<br />
in Mine Wastewater Treatment Systems<br />
T. Lilley; Pall Corporation, Portsmouth, United Kingdom<br />
The use of membranes in wastewater systems has increased rapidly in recent<br />
years. Microporous or semipermeable barriers augment conventional chemical or<br />
microbial processes to meet stringent treatment targets. These developments enable<br />
elegant solutions to waste discharge challenges and extend the scope of<br />
water recycle redressing the overall water balance and operational economics<br />
Wastewater treatment processes are discussed by reference to the spectrum of waterborne<br />
contaminants and the respective membrane separation capabilities. The<br />
role chemical pretreatment to enable physical separation of metals with microfiltartion<br />
(MF) is described and how integration of MF with diffusional reverse osmosis<br />
(RO) is used to control a broader range of dissolved contaminants<br />
Membrane configuartions are considered apropos function, operational economics<br />
and sustainability. These features are exemplified with case studies. Firstly,<br />
MF alone following chemical precipitation for the removal of heavy metals, then<br />
MF onto two stages RO of different configurations for TDS reduction and waste<br />
volume minimisation and finally an open channel RO alone for the reduction of<br />
inorganic COD.<br />
10:05 AM<br />
ARD Remediation with Slag: An Application to Berkeley<br />
Pitlake Water<br />
C. Young; Met & Mat Eng, MT Tech, Butte, MT<br />
Treating waste water, particularly acid rock drainage (ARD) from both active and<br />
inactive mines, is critical worldwide for many reasons but usually for environmental<br />
purposes. Being part of a superfund site, the Berkeley Pitlake (BPL) in Butte<br />
MT may be the most famous ARD site in the world. Currently, its treatment consists<br />
of a two-stage lime precipitation. Research has shown that another waste<br />
product can be substituted for lime either wholly or in part. Three slags from<br />
closed MT smelters were investigated: Rhone Poulenc from Ramsay; ARCO slag<br />
from Anaconda; and ASARCO slag from East Helena. Each slag differed in iron,<br />
silica and calcium content and therefore reacted differently to remediate BPL<br />
water. Results were analyzed and modeled using StatEase statistical software and<br />
are presented in regards to pH and metal concentration as a function of amount<br />
added and particle size. Results indicate that slags can be used to either supplement<br />
or replace lime, depending on the application. Conceivably, the process<br />
could also be done in-situ. Aside from remediating ARD, an added socio-benefit,<br />
often referred to as dual ecosystem enhancement, is the removal of the slag piles.<br />
10:25 AM<br />
Progress in Passive Biological Treatment of Selenium in Mine and<br />
Industrial Wastewaters<br />
J. Bays; CH2MHILL, Tampa, FL<br />
Industries are challenged to meet increasingly stringent regulations for selenium<br />
and metals. Cost-effective treatment is required. Biological treatment of selenium<br />
uses passive biochemical reactor cells comprised of mixed organic media<br />
such as wood chips, sawdust, hay, composted manure, peat and other components<br />
that create a microenvironment supportive of anaerobic biological reduction.<br />
Biochemical reactors can be combined with constructed wetlands for effluent<br />
polishing and flow equalization. Passive treatment reduces capital cost and<br />
operational effort compared to more expensive and complex conventional treatment.<br />
The coal mining industry of southern Appalachia offers pertinent examples.<br />
One coal company implemented passive treatment at four discharge outlets<br />
(flows = 60-1,500 gpm; Se = 8-25 ug/L) using biochemical reactors integrated<br />
into treatment wetlands ranging from 0.4 to 1.8 acres in area. Other companies<br />
and agencies have conducted pilot studies and are implementing similar bioreactor<br />
wetland systems. These and other case histories of passive selenium treatment<br />
will be summarized and conceptual configurations and applicable constraints<br />
will be described.<br />
environmental:<br />
resource recovery<br />
9:00 AM • Wednesday, February 27<br />
chairs: L. Figueroa, Colorado School of Mines, Golden, CO<br />
P. Hoeferlin, Veolia Water, Vandalia, OH<br />
9:00 AM<br />
Introductions<br />
9:05 AM<br />
Water Impact Index – Water Reuse<br />
P. Hoeferlin 1 and C. Dupont 2 ; 1 Veolia Water, Paris, France and<br />
2<br />
Veolia Water, Vandalia, OH<br />
Veolia Water recently unveiled the Water Impact Index, the first indicator enabling<br />
a comprehensive assessment of the impact of human activity on water resources.<br />
It is a tool that can help cities and companies plan long-term projects<br />
and better understand sustainable approaches to ensure long-term water supplies<br />
and healthy water ecosystems. In states as far flung as Georgia and Nevada, communities<br />
are experiencing service inconveniences or stating serious concerns over<br />
their long-term water supplies. Other states have halted industrial projects or<br />
commercial developments as water resources are strained. Business and governance<br />
as usual will not suffice as competing demands for water escalate. Cities,<br />
industries and citizens need data, smart-planning tools, better approaches and<br />
more cost-effective best practices to ensure a successful, sustainable future that<br />
takes into account our new realities.<br />
This is the Technical <strong>Program</strong> as of September 1, 2012. IT IS SUBJECT TO CHANGE.<br />
Please see the Onsite <strong>Program</strong> for final details.<br />
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