IP Library Granted Patent US 7,915,364
Granted Patent B2
US 7,915,364 · App. 12/065,034 · Granted Mar 29, 2011

Method for producing vinyl chloride-vinyl acetate copolymers in the form of their solid resins

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,915,364
App. No.
12/065,034
Granted
Mar 29, 2011
Kind
B2
Abstract

The invention provides a process for preparing vinyl chloride-vinyl acetate copolymers in the form of their solid resins by means of free-radically initiated suspension polymerization in aqueous medium of 70% to 90% by weight of vinyl chloride, 10% to 30% by weight of vinyl acetate and, if desired, further comonomers copolymerizable therewith, characterized in that 0.1% to 5% by weight of a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate is introduced as an initial charge, the amounts in % by weight being based in each case on the total weight of the comonomers.

Claims (20)

1. A process for preparing vinyl chloride-vinyl acetate copolymers in the form of their solid resins by means of free-radically initiated suspension polymerization in aqueous medium, comprising polymerizing in a polymerization reactor 70% to 90% by weight of vinyl chloride, 10% to 30% by weight of vinyl acetate, optionally further comonomers copolymerizable therewith, the amounts in % by weight being based on the total weight of the comonomers being polymerized, wherein 0.1% to 5% based on the weight of the comonomers being polymerized of a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate is introduced into the polymerization reactor as an initial charge.

2. The process of claim 1 , wherein 10% to 20% by weight of vinyl acetate and 80% to 90% by weight of vinyl chloride are copolymerized.

3. The process of claim 1 , wherein additionally 0.1% to 10% by weight of ethylenically unsaturated monocarboxylic or dicarboxylic acids are copolymerized.

4. The process of claim 1 , wherein additionally epoxide-containing monomers are copolymerized.

5. The process of claim 1 , wherein during or after the polymerization, 0.001% to 0.1% by weight of ascorbic acid and/or isoascorbic acid, based on the total weight of the comonomers, is added, and optionally, in addition to the ascorbic acid and/or isoascorbic acid, citric acid is added in an amount of 0.001% to 0.1% by weight, based on the total weight of the comonomers.

6. The process of claim 1 , wherein a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate comprising 15 to 85 weight percent vinyl acetate moieties is employed.

7. The process of claim 2 , wherein additionally 0.1% to 10% by weight of ethylenically unsaturated monocarboxylic or dicarboxylic acids are copolymerized.

8. The process of claim 2 , wherein additionally epoxide-containing monomers are copolymerized.

9. The process of claim 3 , wherein additionally epoxide-containing monomers are copolymerized.

10. The process of claim 2 , wherein during or after the polymerization, 0.001% to 0.1% by weight of ascorbic acid and/or isoascorbic acid, based on the total weight of the comonomers, is added, and optionally, in addition to the ascorbic acid and/or isoascorbic acid, citric acid is added in an amount of 0.001% to 0.1% by weight, based on the total weight of the comonomers.

11. The process of claim 3 , wherein during or after the polymerization, 0.001% to 0.1% by weight of ascorbic acid and/or isoascorbic acid, based on the total weight of the comonomers, is added, and optionally, in addition to the ascorbic acid and/or isoascorbic acid, citric acid is added in an amount of 0.001% to 0.1% by weight, based on the total weight of the comonomers.

12. The process of claim 4 , wherein during or after the polymerization, 0.001% to 0.1% by weight of ascorbic acid and/or isoascorbic acid, based on the total weight of the comonomers, is added, and optionally, in addition to the ascorbic acid and/or isoascorbic acid, citric acid is added in an amount of 0.001% to 0.1% by weight, based on the total weight of the comonomers.

13. The process of claim 2 , wherein a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate comprising 15 to 85 weight percent vinyl acetate moieties is employed.

14. The process of claim 3 , wherein a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate comprising 15 to 85 weight percent vinyl acetate moieties is employed.

15. The process of claim 4 , wherein a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate comprising 15 to 85 weight percent vinyl acetate moieties is employed.

16. The process of claim 5 , wherein a vinyl acetate-vinyl chloride copolymer soluble in ethyl acetate comprising 15 to 85 weight percent vinyl acetate moieties is employed.

17. A vinyl acetate and vinyl chloride copolymer in the form of a spherical particle powder, prepared by the process of claim 1 , and the further process step of isolating polymer particles formed in the suspension polymerization and drying, the particles soluble in ethyl acetate at 20 weight percent solids to form a clear solution.

18. A vinyl acetate and vinyl chloride copolymer in the form of a spherical particle powder, prepared by the process of claim 2 , and the further process step of isolating polymer particles formed in the suspension polymerization and drying, the particles soluble in ethyl acetate at 20 weight percent solids to form a clear solution.

19. A vinyl acetate and vinyl chloride copolymer in the form of a spherical particle powder, prepared by the process of claim 3 , and the further process step of isolating polymer particles formed in the suspension polymerization and drying, the particles soluble in ethyl acetate at 20 weight percent solids to form a clear solution.

20. A vinyl acetate and vinyl chloride copolymer in the form of a spherical particle powder, prepared by the process of claim 5 , and the further process step of isolating polymer particles formed in the suspension polymerization and drying, the particles soluble in ethyl acetate at 20 weight percent solids to form a clear solution.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 1, 2008
From: WACKER POLYMER SYSTEMS GMBH & CO. KG
To: WACKER CHEMIE AG
Reel/Frame 021603/0608 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 27, 2008
From: KAISER, STEPHAN; STROHMEIER, CLAUDIA; ZENK, FRANK
To: WACKER POLYMER SYSTEMS GMBH & CO. KG
Reel/Frame 020569/0993 →