IP Library › Granted Patent US 7,932,328
Granted Patent B2
US 7,932,328 · App. 12/806,352 · Granted Apr 26, 2011

Vinyl alcohol copolymers for use in aqueous dispersions and melt extruded articles

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Quick Facts
Patent No.
US 7,932,328
App. No.
12/806,352
Granted
Apr 26, 2011
Kind
B2
Abstract

A product comprising a cold water soluble film wherein: a) the film comprises a copolymer of vinyl alcohol (VOH) with a minor amount of 2-acrylamido-2-methyl propane sulfonic acid in free acid form or as a salt of the free acid (AMPS); and b) the film has a harsh chemical dissolution time of less than about 80 seconds measured by the harsh chemical dissolution test method after 8 weeks.

Claims (19)

1. A process for the production of a copolymer of vinyl alcohol (VOH) and a comonomer comprising:

a) continuously feeding with agitation, vinyl acetate (VAM) and comonomer, a free radical yielding polymerization initiator, and a solvent to a first reaction zone under polymerization conditions for a residence time sufficient for a major proportion of comonomer fed to said first reaction zone to polymerize;

b) continuously feeding reaction mass from said first reaction zone with an additional supply of comonomer to a second reaction zone, maintaining the reaction mass in the second reaction zone for a residence time sufficient to polymerize a major proportion of the comonomer added to the second reaction zone;

c) continuously withdrawing reaction mass from the second reaction zone;

d) separating copolymer from the reaction mass of step (c); and

e) saponifying by hydrolysis and/or alcoholysis a major proportion of the acetate groups in said copolymer to form a copolymer of VOH.

2. The process of claim 1 , wherein the amount of comonomer continuously fed to both reaction zones is about 1 to about 20 wt. %, based on the total of VAM and comonomer being fed.

3. The process of claim 1 , wherein the amount of comonomer continuously fed to both reaction zones is about 4 to about 15 wt. %, based on the total of VAM and comonomer being fed.

4. The process of claim 1 , wherein the ratio between the amounts of comonomer fed to the first and second reaction zones, respectively, is from about 55:45 to about 80:20.

5. The process of claim 1 , wherein the average residence time in the first reaction zone of the components fed to the first reaction zone is from about 30 to about 120 minutes.

6. The process of claim 1 , wherein the average residence time in the first reaction zone of the components fed to the first reaction zone is from about 45 to about 70 minutes.

7. The process of claim 1 , wherein the reaction temperature in the first reaction zone is from about 55° C. to about 85° C.

8. The process of claim 1 , wherein the reaction temperature in the first reaction zone is from about 60° C. to about 80° C.

9. The process of claim 1 , wherein the average residence time in the second reaction zone of the reaction mass and additional comonomer fed to the second reaction zone is from about 30 to about 120 minutes.

10. The process of claim 1 , wherein the average residence time in the second reaction zone of the reaction mass and additional comonomer fed to the second reaction zone is from about 45 to about 70 minutes.

11. The process of claim 1 , wherein the reaction temperature in the second reaction zone is from about 55° C. to about 85° C.

12. The process of claim 1 , wherein the reaction temperature in the second reaction zone is from about 60° C. to about 80° C.

13. The process of claim 1 , wherein the pressure in each reaction zone is from about 1 to about 30 psi.

14. The process of claim 1 , wherein the pressure in each reaction zone is from about 3 to about 15 psi.