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The Recycling of Thermoset Materials into Thermoplastic Composites Abstract
Thermoset process scrap costs companies millions of dollars annually. Specific
thermoplastics could benefit from the addition of recycled thermoset material.
The incorporation of thermoset regrind into thermoplastic material would provide
a viable alternative for the thermoset scrap that is currently sent to the
landfills. Theory and Background When a thermoset part has been cross-linked,
that material either has to be used in the application it was intended for, or
thrown out. In process scrap, generally shear sand/saw grindings and other
waste, is shipped to the landfill for disposal. The lack of recycling in the
thermoset industry results in higher final prices for the consumer. Developing a
practical method to recycle thermoset materials would create a commercially
feasible composite material. The addition of the regrind would reduce the
requirement for expensive virgin material, decreasing the composite material’s
price. This would provide the thermoset and thermoplastic industries with
substantial savings. Thermoset regrind, from Haysite Re-Inforced plastics,
polypropylene co-polymer from ExxonMobil, and Silane Q1-6106 from Dow Corning
were used to create the new composite. At Haysite, the regrind is a by-product
of the sanding of large laminate sheets of fiberglass-reinforced polyester. Each
sheet is sanded to final size, with the waste dust being sent to the landfill.
The dust used in this study was taken from Haysite's EMD product line.
This
regrind consists of approximately 30% glass fibers, 31.5% calcium carbonate
filler, 20% polyester resins, and the final 18.5% of the mixture is comprised of
organic catalysts, pigments, and trace amounts of highly concentrated chemicals.
The silane acts as a coupling agent between the polypropylene and the regrind on
a molecular level. The silicon and oxygen molecules, present in the silane, form
strong ionic bonds between the glass particles in the regrind. This part of the
silane-coupling agent also forms secondary force bonds with the chains of the
propylene polymer. Van der wal forces may create bond strength between the glass
fibers and the polypropylene as well. The polyester resin portion of the
reground material also utilizes van der wal forces. These forces weakly bond the
resin molecules to the virgin propylene. The resin and glass fiber portion of
the regrind is best if bonded to the polypropylene directly. The silane does not
provide any bonding forces between the calcium carbonate and propylene
molecules.
Calcium carbonate is also hygroscopic which may necessitate material
drying if properties are affected by the water absorption. Dow Corning's Silane
Q1-6106 is a high viscosity liquid, and compares best to a waxy gel. The
addition of the silane provide significant wetting between the materials, which
causes clumping. Multiple, less expensive materials can reproduce the wetting
characteristic of the silane, however, the molecular bonding benefits are not
duplicable with these other materials. Experimental Mixing Originally, it was
proposed that the material be compounded through extrusion and palletizing with
subsequent injection molding. A regrind level of 20% and 30% was selected to
ensure the financial benefits would outweigh the costs associated with silane
and the compounding of the composite material. Also, a less expensive
alternative was desirable as the costs of the overall process would rise and
detract from the cost savings provided by the use of the thermoset regrind. When
it became evident that the material could be directly injection molded, this
alternative was selected over the extrusion operation. Overall, the procedure
followed was clean, efficient, and could be used to produce large quantities of
the composite material in a short period of time. Mixing was preformed to the
following guidelines.
A five-gallon bucket was lined with two garbage bags, and
filled with 4.35 kilograms of the virgin polypropylene. Next, the resin was
wetted with 0.17 kilograms of silane. The mixture was then tumbled to avoid
clumping in a specific area and to prevent poor distribution of the silane. The
second wetting also consisted of the 0.17 kg of silane and a second tumbling.
The regrind was then integrated into this mixture by splitting the amount in
half, and adding the regrind in two batches of 0.99 kg each. After each addition
of regrind the material was tumbled. To produce the 20% loaded parts, half of
the 30% regrind loaded parts were reground into normal pellet size and mixed
with virgin polypropylene at a weight ratio that produced a mixture of 20%
regrind to 80% polypropylene and silane. This mix was then molded and tested.
The 30% material contained powder that was not attached to the virgin
polypropylene pellets. The material did not clump together completely, but the
friction created by the silane was enough to curb separation and keep the
mixture homogeneous. Since the material did not separate in the machine hopper
during molding, direct injection molding was the best processing technique
available.
Without the silane acting dually as a wetting agent and a molecular
bonding agent, the regrind would have filtered to the bottom of the hopper and
created a non-uniform loaded part. Processing The parts were molded using an
Arburg Allrounder Injection Molding Machine. The process settings can be seen in
Tables 1-3 in the Appendix. The virgin polypropylene was molded using the
manufacturer’s recommendations. The 20% and 30% mixtures followed the mixing
procedures outlined. The composite materials required higher hold pressures to
pack the mold completely, as the original hold pressure was not adequate. The
back pressure was also increased in order to provide homogeneous mixture of the
composite material. The higher back pressure also caused the temperature of the
melt to be approximately 5o Celsius higher. Testing Procedure Four tests were
run on the molded tensile and flexural bars for all three materials. The first
was the flex test on an Instron machine, following ASTM D-790. The flex bar lies
horizontally on a base and is supported at the ends while a crosshead presses in
the center of the bar, moving at a rate of 50.8 mm/min. The second test as the
tensile test, using ASTM D-638 guidelines, which was performed on the same
machine. The tensile bars were placed vertically in tow crosshead grips, one on
the top, the other at the bottom. The top crosshead is then pulled upward on the
bar at a rate of 50.8 mm/min, stretching the bar until it fails. The third test
was the Notched Izod impact test, according to ASTM D-256 on an Izod testing
machine. First, the flex bar was notched on one wedge, about 2 mm from one edge.
Next, it was placed vertically and clamped on the bottom of the machine. A 2.27
kg hammer was then released and swung over the bar, breaking it.
The impact
strength and type of break was recorded for each sample. The fourth test
conducted was an extended load test. Five flex bars of each material had small
holes drilled into the center of each end. Each bar also had a one inch space
measured out and marked, to be used to measure once the load was applied. Brass
rings were used to connect the five similar bars together, and then they were
hung from a beam and a 26.4 kg load was hung from each chain of bars. The
distance between each reference mark on each bar was measured at the initial
time, 5 minutes, 15 minutes, 90 minutes, 1 day, and 1 week. These results were
than averaged and recorded for each material sample. Results The results of the
testing can be found in the Appendix. Graphs 1-4 compare the three different
sample bases used in this experiment in the tests previously described.
Discussion Improvements to the procedure could be made to this study. First, the
choice to straight injection mold the samples versus extruding the material
mixture and re-pelletizing the composite. This was because the use of the silane
was sufficient to cause the two materials to clump together. Pelletizing the
material would then just be extra time and cost. With using the straight
injection molding technique of processing, although of good quality, the
homogeneousness of the material is still uncertain. This is the reason for
averaging all of the tests’ results according to batch. The levels of thermoset
integrated into the virgin polypropylene samples were decided based on
industry’s use of 20% and 30% filled resin in production. Further testing should
be done on levels under 20% in order to better show the regrinds affects on the
mechanical properties of the polypropylene. This is evident in the Notched Izod
testing (Graph 3 of the Appendix).
The resultant curve between the levels of
regrind may differ a great deal after exploring levels of regrind less than 20%.
Discussion was held on the choice of using Silane over basic vegetable oils in
order to wet the mixture creating clumping. Testing could be done to compare the
use of oil to the current use of silane. Conclusion Until recently there have
been little to no uses found for thermoset scrap. Millions of dollars are spent
annually on handling and disposal of their potentially useful and profitable
materials. The integration of this particular thermoset into polypropylene
applications is only one possibility in the reuse of thermoset materials.
Although on a small scale, the study was effective and simple. If applied on an
industrial level it may prove to be very profitable to both the plastics
industry and the consumer. Future Actions § Performing tests on regrind levels
lower than 20% § Performing filler content burn-off testing to determine the
consistency of regrind material in the samples. This will aid us in determining
the effectiveness of our processing procedure. § Cost comparisons of this
thermoset regrind versus common polypropylene fillers. Acknowledgements We would
like to give our thanks to: § Tim Pfister, Senior Design Engineer, Haysite
Reinforced Plastics for donation of the thermoset scrap dust and information on
the properties of the material. § Dow Corning Chemical for the donation of the
Silane § Exxon Mobil for the donation of polypropylene copolymer to the Penn
State Erie, The Behrend College plastics program § Brian Young, Penn State Erie,
The Behrend College , for his time and assistance with processing and testing. §
Dr. Paul Koch, Advisor, Penn State Erie, The Behrend College, for his guidance
in the projects design.
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