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Modern Plastics Worldwide - July/August 2009 - dae uptlax

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PROCESSING<br />

TECHNOLOGY<br />

Traditionally, highly filled<br />

polyolefin compounds have been<br />

produced by repeated loading via<br />

several feed positions on the compounding<br />

extruder, followed by<br />

mixing up to three or more times.<br />

This, says Eitel, is done because<br />

CaCO 3 , with a bulk density of<br />

600-800 kg/m 3 , tends to be sticky<br />

and build bridges, often creating<br />

headaches for an operator. To<br />

overcome such problems, agitators<br />

are often used, hoppers are<br />

designed with special geometry to<br />

improve material drop, or flexible<br />

walls can be incorporated that<br />

can shake up the filler to break up<br />

bridging.<br />

Coperion says experience has shown,<br />

in its latest line design for such applications,<br />

that, during refilling of loss-inweight<br />

feeders using slide, butterfly, or<br />

rotary valves, the valve itself needs to<br />

be installed closer to the feeder hopper<br />

so that it can react quickly in shutting<br />

PROCESSING TRENDS<br />

Specific energy input drops, and pressure increases,<br />

as filler content increases: that has been Coperion’s<br />

experience with its new line for highly filled compounds.<br />

off. This is necessary to avoid overfilling.<br />

The company developed a new layout<br />

for its ZSK compounder by mounting<br />

the CaCO 3 feeder directly above the<br />

unit’s co-rotating twin-screw side feeder,<br />

ZSB. This setup, says Eitel, results in the<br />

need for only two feeders and two refill<br />

hoppers for the CaCO 3 . It also provides<br />

Bioplastic barrier fi lm matches EVOH, PA<br />

By Matt Defosse<br />

Blown- and cast-fi lm extrusion<br />

line manufacturer Colines (with<br />

manufacturing sites in Novara and<br />

Varese, Italy) says recent testing<br />

proves that PLA/PVOH fi lms extruded<br />

on the company’s cast- and<br />

blown-fi lm lines with structures of<br />

up to 7 layers and with thicknesses<br />

from 50 to 90 μm offer sufficient<br />

oxygen barrier properties, while<br />

also maintaining top optical<br />

performance, as shown by the<br />

values of haze and gloss and the<br />

fi lm’s printability.<br />

Colines officials say the lines have been<br />

modified so as to render the same performance<br />

as lines running barrier films<br />

containing polyamide or ethylene vinyl<br />

alcohol (EVOH) barrier materials, with<br />

no loss in line productivity.<br />

The combined structure of polylactic<br />

acid (PLA), based on plant starches,<br />

and polyvinyl alcohol (PVOH, a biodegradable,<br />

water-soluble polymer) in<br />

these barrier films offers sufficient gas<br />

barrier performance to prove them<br />

suitable for use in applications such<br />

as packaging of meat and fish, and, in<br />

particular, fruit and vegetables.<br />

The company invited interested processors<br />

to its open house from <strong>July</strong><br />

27-31, <strong>2009</strong>, and requested email preregistration<br />

at marketing@colines.it.<br />

Also during that open house the company<br />

planned to run a line extruding<br />

breathable film with an in-line double<br />

mono-orienting unit (MDO). The line,<br />

which can extrude breathable film in<br />

PE and in PP, has a useful width of<br />

2200 mm and the double-MDO unit<br />

offers orientation of up to 600% (2 x<br />

300%). It will feature post-stretching<br />

embossing and comes outfitted with a<br />

thickness control before and after the<br />

a longer mixing section for the<br />

filler, better dispersion, and higher<br />

output. With the increase by percentage<br />

of the compound/weight<br />

of filler, the discharge pressure in<br />

bar is increased while the specific<br />

energy input measured in kWh/kg<br />

is reduced.<br />

Farrel takes a different approach<br />

to compounding highly filled concentrates.<br />

Its FCM (Farrel Continuous<br />

Mixer) operates on the principle<br />

that the material is exposed<br />

to a variable mixing intensity in<br />

the form of shear stress and strain<br />

developed between the rotor tips<br />

and chamber wall, as well as melt<br />

blending by the kneading action between<br />

the rotors. “The measure of dispersion<br />

through either visual examination or<br />

filter pressure values are as good or better<br />

than those achieved with twin-screw<br />

extruders,” says Broadhead. “Besides<br />

that, we get the added benefit of lower<br />

energy costs.”<br />

stretching, with automatic adjustment<br />

according to the set target. Trim is<br />

recovered directly and pelletized.<br />

It also includes the firm’s Fast<br />

AdJUST (Elav) system for micrometric<br />

adjustments of the stretching parameters<br />

of the line. Colines reports it<br />

has worked with this system and is<br />

able to offer processors the option<br />

of live monitoring of the data relative<br />

to the extrusion lines. The report<br />

system lets a user track consumption<br />

data (energy and raw material), various<br />

trends (throughout and machine data),<br />

recipes, management of the production<br />

orders, ordinary and preventive maintenance,<br />

and diagnostics. The acquisition<br />

and processing of the data are<br />

incorporated directly in the automation<br />

system, with the data then able to<br />

be sent to computers on the other side<br />

of a facility or even further afield.<br />

18 JULY/AUGUST <strong>2009</strong> • MODERN PLASTICS WORLDWIDE mpw.plasticstoday.com

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