Dry ice assisted polymer processing, methods for making, and articles formed thereof

Patent metadata

Field	Value
Publication number	US-9458296-B2
Application number	US-201213602460-A
Country	US
Kind code	B2
Filing date	Sep 4, 2012
Priority date	Sep 4, 2012
Publication date	Oct 4, 2016
Grant date	Oct 4, 2016

Abstract

In an embodiment, a method of processing a polymer comprises: mixing polymer and solid carbon dioxide; introducing the polymer and solid carbon dioxide mixture to a hopper of a vented extruder; plasticizing the mixture to form a polymer melt with dissolved carbon dioxide; venting carbon dioxide as a gas before the die exit; and extruding the polymer melt through a die. In an embodiment, a method of making an article comprises: introducing a polymer powder to an extruder; introducing solid carbon dioxide powder to the extruder at the hopper; plasticizing and extruding the polymer and solid carbon dioxide mixture; venting the solid carbon dioxide before the die exit; extruding the polymer melt through a die to form pellets; and injection molding the polymer pellets without solid carbon dioxide to form molded articles.

First claim

We claim:

1. A method of processing a polymer, comprising:
mixing polymer and solid carbon dioxide, wherein the polymer comprises polar groups and/or aromatic rings, wherein the polymer includes polyacrylonitrile;
introducing the polymer and solid carbon dioxide mixture to a vented extruder having a die exit;
plasticizing the mixture to form a polymer melt with dissolved carbon dioxide;
venting carbon dioxide as a gas before the die exit; and
extruding the polymer melt through a die; and
at least one of processing the polyacrylonitrile in the extruder at a temperature of 150° C. to 200° C.; and wherein the polymer comprises less than 20% comonomer.

2. The method of claim 1 , wherein the extrusion temperature is lowered less than or equal to 80° C. below the degradation temperature of the polymer.

3. The method of claim 2 wherein, the extrusion temperature is lowered 45° C. to 55° C. below the degradation temperature of the polymer.

4. The method of claim 1 , wherein the polymer further includes polyphenylene ether, polyvinyl chloride, polytetrafluoroethylene, or combinations comprising at least one of the foregoing.

5. The method of claim 1 , wherein the polymer further includes polyphenylene ether-based resin, polyacetal-based resin, polyamide-based resin, polystyrene-based resin, acrylic resin, polyester-based resin, polycarbonate, polyphenylene sulfide, polyetherimide, polyethersulfone, polysulfone, polyether (ether) ketone, poly(tetrafluroethylene), polyvinyl chloride, or combinations comprising at least one of the foregoing.

6. The method of claim 1 , wherein the solid carbon dioxide is in the form of a powder or pellet.

7. A method of making a polymer, comprising:
introducing a pre-mixed polymer and solid carbon dioxide mixture to a vented extruder, wherein the polymer comprises polar groups and/or aromatic rings, wherein the polymer includes polyacrylonitrile;
plasticizing the mixture;
venting gas from the extruder; and
extruding the polymer through a die; and
at least one of
processing the polyacrylonitrile in the extruder at a temperature of 150° C. to 200° C.; and
wherein the polymer comprises less than 20% comonomer.

8. The method of claim 7 , wherein the polymer and solid carbon dioxide are introduced at a throat of the vented extruder.

9. The method of claim 8 , further comprising introducing the polymer and the solid carbon dioxide to a hopper prior to introduction to the throat of the vented extruder.

10. The method of claim 7 , further comprising introducing the polymer and the solid carbon dioxide to the vented extruder separately.

11. The method of claim 7 , further comprising forming an article from the polymer.

12. The method of claim 7 , further comprising forming fibers from the extrudate with a melt spinning spinneret die, wherein the fiber size is less than 100 micrometers in diameter.

13. The method of claim 7 , wherein the polymer further includes polyphenylene ether-based resin, polyacetal-based resin, polyamide-based resin, polystyrene-based resin, acrylic resin, polyester-based resin, polycarbonate, polyphenylene sulfide, polyetherimide, polyethersulfone, polysulfone, polyether (ether) ketone, poly(tetrafluroethylene), polyvinyl chloride, or combinations comprising at least one of the foregoing.

14. The method of claim 7 , wherein the polymer comprises less than 10% comonomer.

15. The method of claim 7 , further comprising forming an article from the polyacrylonitrile.

16. A method of making an extrudate, comprising:
plasticizing a polymer with solid carbon dioxide to form a melt, wherein the polymer comprises polar groups and/or aromatic rings;
venting gaseous carbon dioxide before a die exit;
extruding the melt through a die to form the extrudate; and
recovering the vented gaseous carbon dioxide and converting the gaseous carbon dioxide to solid carbon dioxide in a closed loop without releasing carbon dioxide to the atmosphere.

17. The method of claim 16 , further comprising forming profiles, pellets, filaments, films, sheets, and combinations comprising at least one of the foregoing from the extrudate using a die.

18. The method of claim 17 , wherein the profiles comprise a rod or a tube with a diameter of greater than or equal to 1 millimeter.

19. The method of claim 17 , further comprising extruding the polymer through a strand die to form a strand or multi-strands and pelletizing the strand or multi-strands.

20. The method of claim 19 , wherein the pellets are subsequently re-processed with or without solid carbon dioxide.

21. The method of claim 20 , wherein the re-processing is by a method selected from the group consisting of injection molding, filament spinning, film extrusion, sheet extrusion, pipe extrusion, and profile extrusion.

22. The method of claim 16 , wherein the polymer is selected from the group consisting of polyphenylene ether, polyacrylonitrile, polyvinyl chloride, polytetrafluoroethylene, and combinations comprising at least one of the foregoing.

23. The method of claim 16 , further comprising melt spinning filaments wherein the method comprises applying a threadline tension to draw fibers having a diameter of less than or equal to 100 micrometers.

24. The method of claim 23 , further comprising post drawing the fibers.

25. A method of making an article; comprising:
introducing a polymer powder to an extruder having a hopper and a die exit, wherein the polymer comprises polar groups and/or aromatic rings;
introducing solid carbon dioxide powder to the extruder at the hopper;
plasticizing the polymer and solid carbon dioxide mixture;
venting the solid carbon dioxide before the die exit;
extruding the polymer through a die to form pellets; and
injection molding the pellets without solid carbon dioxide to form molded articles.

26. The method of claim 25 , wherein the polymer is selected from the group consisting of polyphenylene ether, polycarbonate, polyacrylonitrile, polyvinyl chloride, polytetrafluoroethylene, and combinations comprising at least one of the foregoing.

27. The method of claim 26 , wherein the polyphenylene ether consists of less than 15 wt. % of a combined total of another polymer selected from the group consisting of polystyrene, polyester, polyimide, polyamide, polypropylene, and combinations comprising at least one of the foregoing.

Assignees

• Bandyopadhyay Sumanda
• Gopalakrishnan Sadasivam
• Kumar Sathish Ranganathan
• Banik Kaushik
• Bashir Zahir
• Saudi Basic Ind Corp

Inventors

• Bandyopadhyay Sumanda
• Gopalakrishnan Sadasivam
• Kumar Sathish Ranganathan
• Banik Kaushik
• Bashir Zahir

Classifications

• B29C48/395

  using screws surrounded by a cooperating barrel, e.g. single screw extruders · CPC title

• C08J3/203 Primary

  Solid polymers with solid and/or liquid additives · CPC title

• B29C47/38

  Operations & Transport · mapped topic