Process for making gray expanded polystyrene
Gray expanded polystyrene achieving target molecular weight, bead size, bead distribution, and cell structure may be reproducibly prepared by suspension polymerization by introducing to the suspension polymerization an additive that is carbon black and/or graphite only after approximately 20 to 60 wt % of the styrene monomer has been converted to polystyrene. Introducing the additive at this point slows the polymerization rate, such as for an optimized period of time to allow for the droplet size to equilibrate to the desired target range. In one nonlimiting embodiment, the styrene polymerization rate has about 35 wt % to about 60 wt % styrene monomer remaining after about 3 hours from the beginning of polymerizing.
1. A method for preparing gray expanded polystyrene (EPS), the method comprising:
polymerizing styrene monomer to polystyrene by suspension polymerization;
after approximately 20 to 60 wt % of the styrene monomer has been converted to polystyrene, introducing to the suspension polymerization an additive selected from the group consisting of carbon black, graphite, and combinations thereof; and after a period of polymerizing to allow droplet size to equilibrate to within a desired size range between about 0.1 mm and about 1.0 mm, then
continuing to polymerize the styrene monomer to polystyrene by suspension polymerization to produce gray EPS having:
a weight average molecular weight between about 50,000 and about 1,000,000 amu;
a bead size between about 50 and about 1500 microns;
a bead distribution where from about 10 to about 90 weight % of the beads are in the range of about 850 to about 1170 microns; and
a cell size between about 4 and about 20 cells per millimeter.
2. The method of claim 1 where the gray EPS has a density from about 5 to about 35 g/l.
3. The method of claim 1 where the additive is introduced by a method selected from the group consisting of:
introducing the additive predispersed as a masterbatch;
introducing the additive as fluff or powder grade; and
combinations thereof.
4. The method of claim 3 , where
when the additive is introduced predispersed as a masterbatch:
a primary free radical initiator is introduced which is activated at about 90° C. in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a secondary free radical initiator is introduced which is activated at about 130° C. in an amount from about 0.1 wt % to about 0.3 wt % based on the styrene monomer;
when the additive is introduced as fluff or powder grade:
a free radical initiator is introduced which is in an initial dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a free radical initiator is introduced which is in an additional dose in an amount from about 0.4 wt % to about 0.6 wt % based on the styrene monomer; and
when the additive is introduced as a combination of predispersed as a masterbatch and as fluff or powder grade:
a free radical initiator is introduced which is in an initial dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a free radical initiator is introduced which is in an additional dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer.
5. The method of claim 1 where the amount of additive introduced ranges from about 0.1 to about 10 wt %, based on the produced gray EPS.
6. A method for preparing gray expanded polystyrene (EPS), the method comprising:
polymerizing styrene monomer to polystyrene by suspension polymerization;
after approximately 20 to 60 wt % of the styrene monomer has been converted to polystyrene, introducing to the suspension polymerization an additive selected from the group consisting of carbon black, graphite, and combinations thereof; and after a period polymerizing to allow droplet size to equilibrate to within a desired size range between about 0.1 mm and about 1.0 mm; and
continuing to polymerize the styrene monomer to polystyrene by suspension polymerization to produce gray EPS having:
a density from about 5 to about 35 g/l;
a cell size between about 4 and about 20 cells per millimeter;
a weight average molecular weight between about 50,000 and about 1,000,000 amu;
a bead size between about 50 and about 1500 microns; and
a bead distribution where from about 10 to about 90 weight % of the beads are in the range of about 850 to about 1170 microns;
where the polymerizing has a polymerization rate, and where the polymerization rate has about 35 wt % to about 60 wt % styrene monomer remaining after about 3 hours from the beginning of polymerizing.
7. The method of claim 6 where the additive is introduced by a method selected from the group consisting of:
introducing the additive predispersed as a masterbatch;
introducing the additive as fluff or powder grade; and
combinations thereof.
8. The method of claim 7 introduced predispersed as a masterbatch:
a primary free radical initiator is introduced which is activated at about 90° C. in an amount from about 0.3wt % to about 0.5 wt % based on the styrene monomer, and
a secondary free radical initiator is introduced which is activated at about 130° C. in an amount from about 0.1 wt % to about 0.3 wt % based on the styrene monomer;
when the additive is introduced as fluff or powder grade:
a free radical initiator is introduced which is in an initial dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a free radical initiator is introduced which is in an additional dose in an amount from about 0.4 wt % to about 0.6 wt % based on the styrene monomer; and
when the additive is introduced as a combination of predispersed as a masterbatch and as fluff or powder grade:
a free radical initiator is introduced which is in an initial dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a free radical initiator is introduced which is in an additional dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer.
9. The method of claim 6 where the amount of additive introduced ranges from about 0.1 to about 10 wt %, based on the produced gray EPS.
10. A method for preparing gray expanded polystyrene (EPS), the method comprising:
polymerizing styrene monomer to polystyrene by suspension polymerization;
after approximately 20 to 60 wt % of the styrene monomer has been converted to polystyrene, introducing to the suspension polymerization an additive selected from the group consisting of carbon black, graphite, and combinations thereof, and after a period polymerizing to allow droplet size to equilibrate to within a desired size range, where the additive is introduced by a method selected from the group consisting of:
introducing the additive predispersed as a masterbatch;
introducing the additive as fluff or powder grade; and
combinations thereof;
when the additive is introduced predispersed as a masterbatch:
a primary free radical initiator is introduced which is activated at about 90° C. in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a secondary free radical initiator is introduced which is activated at about 130° C. in an amount from about 0.1 wt % to about 0.3 wt % based on the styrene monomer;
when the additive is introduced as fluff or powder grade:
a free radical initiator is introduced which is activated at about 90° C. in an initial dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer, and
a free radical initiator is introduced which is activated at about 130° C. in an additional dose in an amount from about 0.4 wt % to about 0.6wt % based on the styrene monomer; and
when the additive is introduced as a combination of predispersed as a masterbatch and as fluff or powder grade:
a free radical initiator is introduced which is activated at about 90° C. in an initial dose in an amount from about 0.3 wt % to about 0.5% wt % based on the styrene monomer, and
a free radical initiator is introduced which is activated at about 130° C. in an additional dose in an amount from about 0.3 wt % to about 0.5 wt % based on the styrene monomer; and
continuing to polymerize the styrene monomer to polystyrene by suspension polymerization to produce gray EPS.
11. The method of claim 10 where the desired droplet size ranges between about 0.1 mm and about 1.0 mm.
12. The method of claim 10 where the gray EPS:
has a weight average molecular weight between about 50,000 and about 1,000,000 amu;
has a bead size between about 50 and about 1500 microns;
has a bead distribution where from about 10 to about 90 weight % of the beads are in the range of about 850 to about 1170 microns; and
has a cell size between about 4 and about 20 cells per millimeter.
13. The method of claim 10 where the gray EPS has a density from about 5 to about 35 g/l.
14. The method of claim 10 where the amount of additive introduced ranges from about 0.1 to about 10 wt %, based on the produced gray EPS.
15. The method of claim 10 where the polymerizing has a polymerization rate, and where the polymerization rate has about 35 wt % to about 60 wt % styrene monomer remaining after about 3 hours from the beginning of polymerizing.