Process for preparing poly(arylene sulfide) polymers using cyclic arylene sulfide oligomers

• US 5,354,841 A
• Filed: 08/09/1993
• Issued: 10/11/1994
• Est. Priority Date: 06/24/1991
• Status: Expired due to Fees

• Current Assignee: Phillips Petroleum Company (ConocoPhillips)
• Original Assignee: Phillips Petroleum Company (ConocoPhillips)
• Inventors: Ash, Carlton E., Geibel, Jon F.
• Primary Examiner(s): Marquis, Melvyn I.
• Assistant Examiner(s): PEZZUTO, HELEN LEE
• Application Number:
  US08/103,847
• Time in Patent Office: 428 Days
• Field of Search: 528/388, 525/537
• US Class Current: 528/388
• CPC Class Codes: C08G 75/0259 metal hydrogensulfides
• CPC Class Codes: C08J 11/06 without chemical reactions
• CPC Class Codes: C08J 2381/02 Polythioethers; Polythioether-ethers
• CPC Class Codes: Y02W 30/62 Plastics recycling; Rubber recycling

Abstract

A process is provided for producing a poly(arylene sulfide) polymer which employs as a reactant cyclic arylene sulfide oligomers.

Claims

1. A process for preparing a poly(arylene sulfide) polymer which comprises:

contacting reactants consisting essentially of at least one dihaloaromatic compound, a sulfur source, a polar organic compound, water and cyclic oligomers of the formula ##STR4## wherein 4≦

n≦

15, under polymerization conditions sufficient to form said poly(arylene sulfide) polymer.

2. A process according to claim 1 wherein said reactants further consist essentially of at least one molecular weight modifying agent selected from the group consisting of alkali metal carboxylates, and lithium halides.

5. A process according to claim 1 wherein the molar ratio of the amount of said dihaloaromatic compound to said sulfur source is in the range of about 0.8/1 to about 2/1.

6. A process according to claim 1 wherein the molar ratio of the amount of said polar organic compound to said sulfur source is in the range of about 1/1 to about 10/1.

7. A process according to claim 6 wherein said cyclic oligomers and water are contacted with said sulfur source and said polar organic compound under conditions sufficient to remove at least a portion of said water, prior to addition of said dihaloaromatic compound and commencement of said polymerization conditions.

8. A process according to claim 7 wherein said cyclic oligomers and water are contacted with said polymerization mixture after commencement of the polymerization at any point in time after about 40 mole percent conversion of the dihaloaromatic compound.

9. A process according to claim 1 wherein said cyclic oligomers are contacted with said polymerization reaction mixture at any time after commencement of polymerization until termination of said polymerization.

10. A process according to claim 1 wherein said cyclic oligomers are obtained by separating said cyclic oligomers from a desired product in a process to purify a previously prepared poly(arylene sulfide) polymer.

11. A process according to claim 1 wherein said cyclic oligomers are obtained by separating said oligomers from poly(arylene sulfide) polymer during the recovery of said poly(arylene sulfide) polymer.

3. A process according to claim 3 wherein said molecular weight modifying agent is an alkali metal carboxylate.

4. A process according to claim 3 wherein said alkali metal carboxylate is sodium acetate.