IP Library Granted Patent US 9,193,839
Granted Patent B2
US 9,193,839 · App. 14/211,387 · Granted Nov 24, 2015

Crosslinking control in high impact polystyrene manufacturing process

Inventors: Wei Wang (League City, TX); David Knoeppel (League City, TX); Madison Bluhm (Houston, TX)
Assignee: FINA TECHNOLOGY, INC.
C08J3/24C08J2325/06
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Quick Facts
Patent No.
US 9,193,839
App. No.
14/211,387
Granted
Nov 24, 2015
Kind
B2
Abstract

The method includes providing a high impact polystyrene (HIPS) reaction system, wherein the HIPS reaction system has a devolitalizer downstream of a reactor and injecting a retarding agent into the HIPS reaction system prior to the devolitalizer.

Claims (25)

1. A method comprising:

providing a high impact polystyrene (HIPS) reaction system, wherein the HIPS reaction system has a devolitalizer downstream of a reactor;

injecting a retarding agent into the HIPS reaction system prior to the devolitalizer, wherein the retarding agent comprises a free radical scavenger.

2. The method of claim 1 , wherein the retarding agent further comprises a chain transfer agent.

3. The method of claim 2 , wherein the chain transfer agent is a mercaptan, thiol, or halocarbon.

4. The method of claim 3 , wherein the chain transfer agent is a mercaptan selected from the group consisting of n-octyl mercaptan, t-octyl mercaptan, n-decyl mercaptan, n-dodecyl mercaptan (NDM), t-dodecyl mercaptan, tridecyl mercaptan, tetradecyl mercaptan, n-hexadecyl mercaptan, t-nonyl mercaptan, ethyl mercaptan, isopropyl mercaptan, t butyl mercaptan, cyclohexyl mercaptan, benzyl mercaptan and mixtures thereof.

5. The method of claim 3 , wherein the chain transfer agent is carbon tetrachloride.

6. A method comprising:

providing a high impact polystyrene (HIPS) reaction system, wherein the HIPS reaction system has a devolitalizer downstream of a reactor;

injecting a retarding agent comprising a chain transfer agent into the HIPS reaction system prior to the devolitalizer, wherein the chain transfer agent is ethylbenzene, and wherein a concentration of the retarding agent in a polymer melt prior to the devolitalizer is between 50 ppm and 1000 ppm.

7. The method of claim 1 , wherein the free radical scavenger is a phenolic antioxidant.

8. The method of claim 1 , wherein the retarding agent further comprises a crosslinking coagent.

9. The method of claim 8 , wherein the crosslinking coagent is a polyfunctional (meth)acrylic monomer, allylic compound or metal salt of an unsaturated monocarboxylic acid.

10. A method comprising:

providing a high impact polystyrene (HIPS) reaction system, wherein the HIPS reaction system has a devolitalizer downstream of a reactor;

injecting a retarding agent into the HIPS reaction system prior to the devolitalizer, wherein the retarding agent is a tertiary amine oxide or a tertiary amine.

11. The method of claim 10 , wherein the retarding agent is the tertiary amine oxide, wherein the tertiary amine oxide is N,N,N-trialkylamine oxide, and wherein one N is a methyl group and the other two Ns are C 14 -C 24 saturated aliphatic chains.

12. The method of claim 10 , wherein the retarding agent is the tertiary amine oxide, and wherein the tertiary amine oxide is co-injected with an aliphatic or aromatic solvent.

13. The method of claim 12 , wherein the solvent is a heptane or ethylbenzene.

14. The method of claim 10 , wherein the retarding agent is an aromatic tertiary amine oxide.

15. The method of claim 1 , wherein the retarding agent is the tertiary amine, wherein peroxide and oxygen are present in the reaction system, and wherein the tertiary amine forms a corresponding tertiary amine oxide in the reaction system.

16. The method of claim 15 , wherein the tertiary amine is 2,6-di-tert-butyl-4-(dimethylamino)methylphenol.

17. The method of claim 1 , wherein the swell index of the HIPS 15 to 25 over that when no retardant is used.

18. The method of claim 1 , wherein the concentration of the retarding agent in a polymer melt prior to the devolitalizer is between 1 ppm and 1% (by weight).

19. The method of claim 18 , wherein the concentration of the retarding agent in the polymer melt prior to the devolitalizer is between 50 and 1000 ppm (by weight).

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 7, 2014
From: WANG, WEI; KNOEPPEL, DAVID; BLUHM, MADISON
To: FINA TECHNOLOGY, INC.
Reel/Frame 032619/0674 →
Continuity (1)
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