IP Library Granted Patent US 8,225,937
Granted Patent B2
US 8,225,937 · App. 11/916,479 · Granted Jul 24, 2012

Method for separating differently additivated polymer components and use thereof

Assignee: Fraunhofer-Gesellschaft zur Forderung der angewandten Forschung, e.V.
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Quick Facts
Patent No.
US 8,225,937
App. No.
11/916,479
Granted
Jul 24, 2012
Kind
B2
Abstract

Disclosed is a method for separating differently additivated polymers based on polystyrene, the copolymers and/or blends thereof. This method is used in particular when recycling flame-retardant plastic materials, in particular from old electrical appliances. The method is characterised by a density separation with at least one liquid or gaseous separation medium.

Claims (24)

1. A method for separating flame-protected from flame-retardant-free polymers from a mixture comprising flame-protected and flame-retardant-free polymers based on polystyrene, the copolymers and/or blends thereof, the method comprising:

contacting said mixture comprising flame-protected and flame-retardant free polymers based on polystyrene, the copolymer and/or blends thereof with at least one liquid or gaseous separation medium;

wherein the separation medium is a mixture of water and a solvent miscible with water with a density >1 g/cm 3 or a salt solution and wherein the separation medium has a specific density in the range of 1.06 to 1.14 g/cm 3 so that the polymers in a sink fraction are separated from those in a float fraction, or a separation being effected by means of an air separator, wherein a part of the polymers being entrained more strongly by the air flow of said separator whilst another part of the polymers being deflected less because of their density.

2. The method according to claim 1 , wherein the solvent is glycerine.

3. The method according to claim 1 , wherein the polymers of the float fraction are separated mechanically.

4. The method according to claim 3 , wherein the polymers of the float fraction are separated mechanically by sieving.

5. The method according to claim 1 , wherein the sink fraction is sedimented.

6. The method according to claim 5 , wherein the sedimented sink fraction is separated mechanically.

7. The method according to claim 6 , wherein the sedimented sink fraction is separated mechanically by sieving.

8. The method according to claim 1 , wherein the separation of the polymers is accelerated by a centrifugal field.

9. The method according to claim 1 , wherein the separation effected by means of an air separator is effected with a fluidised bed.

10. The method according to claim 1 , wherein the copolymers and blends of polystyrene are selected from the group consisting of styrene-butadiene (SB), styrene-acrylonitrile (SAN), acrylonitrile-butadiene-styrene (ABS), acrylic ester-styrene-acrylonitrile (ASA) and blends thereof.

11. The method according to claim 10 , wherein the blends of said styrene-butadiene (SB), styrene-acrylonitrile (SAN), acrylonitrile-butadiene-styrene (ABS), and acrylic ester-styrene-acrylonitrile (ASA) are blends with polycarbonate (PC) or polyphenylene oxide (PPO).

12. The method according to claim 1 , wherein the mixture of polymers contains further polymer components and/or non-polymer components.

13. The method according to claim 12 , wherein the further polymer components are selected from the group consisting of polyolefins, polyamides, polyvinyl chlorides, polyurethanes, polycarbonates, polyacrylates, polymethacrylates, polyester resins, epoxy resins, polyoxyalkylenes, polyalkylene terephthalates and polyvinyl butyral and copolymers and blends thereof.

14. The method according to claim 12 , wherein the further polymer components are separated in a preceding step by at least one further density separation.

15. The method according to claim 14 , wherein preceding the further density separation is implemented with a separation medium with a specific density in the range of 0.95 to 1.05 g/cm 3 .

16. The method according to claim 14 , wherein the further density separation is implemented with a separation medium with a specific density in the range of 1.15 to 1.25 g/cm 3 .

17. The method according to claim 12 , wherein the further non-polymer components are separated by a density separation method.

18. The method according to claim 1 , wherein the flame retardants are based on bromine compounds.

19. The method according to claim 18 , wherein the mixture of polymers includes softeners as additives.

20. A method for separating flame-protected from flame-retardant-free polymers from a mixture comprising flame-protected and flame-retardant-free polymers based on polystyrene, the copolymers and/or blends thereof, the method comprising:

contacting said mixture comprising flame-protected and flame-retardant free polymers based on polystyrene, the copolymer and/or blends thereof with at least one liquid or gaseous separation medium;

wherein the separation medium is a mixture of water and a solvent miscible with water with a density >1 g/cm 3 or a salt solution and wherein the separation medium has a specific density in the range of 1.08 to 1.14 g/cm 3 so that the polymers in a sink fraction are separated from those in a float fraction.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 10, 2008
From: SCHLUMMER, MARTIN; MAURER, ANDREAS
To: FRAUNHOFER-GESELLSCHAFT ZUR FORDERUNG DER ANGEWANDTEN FORSCHUNG E.V.
Reel/Frame 020624/0480 →
Priority Claims (1)
DE 10 2005 026 450 · Jun 8, 2005 · national
Continuity (1)
Related Publication 20080190819A1 · Aug 14, 2008