Process to improve performance of wet-strength resins through base activation
Provided is a process for improving the performance of wet-strength resins, such as polyaminopolyamide-epichlorohydrin resins, by treatment with a base to increase molecular weight to provide improved wet strength.
1. A process of making paper having higher wet strength comprising:
providing an aqueous solution of at least 8% solids of an initial water-soluble wet-strength resin having an RSV of less than about 0.25 dL/dry gram selected from the group consisting of polyaminopolyamide-epihalohydrin resins, polyalkylene polyamine-epihalohydrin resins, and mixtures thereof,
treating the aqueous solution with a base to a pH of from about 13.0 to about 11.0, at a temperature of from about 30° C. to about 60° C. for from about 20 minutes to about 4 hours, thereby forming an aqueous solution of a treated resin, wherein the resin has an RSV of greater than about 0.35 dL/g, and wherein at least about 95% of the tertiary aminohalohydrin present in the starting resin is converted to epoxides; and
adding the treated resin to a papermaking furnish.
2. The process of claim 1 , wherein the initial water-soluble wet-strength resin having an RSV of less than about 0.15 dL/dry gram.
3. The process of claim 1 , wherein the initial water-soluble resin is a polyaminopolyamide-epichlorohydrin resin.
4. The process of claim 1 , wherein the wet strength resin comprises from about 10 mole % to about 40 mole % azetidinium ions and from about 60 mole % to about 90 mole % tertiary aminohalohydrin.
5. The process of claim 1 , wherein the starting resin has a 1,3-dichloropropanol level of less than 1000 ppm.
6. The process of claim 1 , wherein treatment of the initial water-soluble wet-strength resin with base is from about 2.0 mmole/dry gram to about 10 mmole/dry gram of initial resin.
7. The process of claim 6 , wherein treatment of the initial water-soluble wet-strength resin with base is from about 3.0 mmole per dry gram to 8 mmole/dry gram of initial resin.
8. The process of claim 1 , wherein the treated resin can be added to the pulp slurry in an amount of from about 0.05 weight percent based on dry weight of the pulp to about 5 weight percent of dry pulp.
9. The process of claim 8 , wherein the treated resin can be added to the pulp slurry in an amount of about 0.1 weight percent of dry weight pulp to about 3 weight percent dry weight pulp.
10. The process of claim 1 , wherein the initial PAE resin has a solids content of greater than 40%.
11. The process of claim 10 , wherein the initial PAE resin has a solids content of greater than 50%.
12. The process of claim 1 , wherein the ratio of ACH:AZE can be about 30:70 to about 75:25.
13. The process of claim 1 , wherein the treated resin is added to the paper furnish process about 1 minute to about 24 hours after completion of the base treatment.
14. The process of claim 1 , wherein the initial water-soluble wet-strength resin has an RSV of less than about 0.25 dL/dry gram.
15. The process of claim 14 , wherein the water-soluble wet-strength resin has an RSV of less than about 0.15 dL/dry gram.
16. The process of claim 1 , wherein the amount of treated resin added to the papermaking furnish is from about 0.25% to about 1.75% dry weight pulp furnish.
17. The process of claim 16 , wherein the amount of treated resin added to the papermaking furnish is from about 0.5% to about 1.5% dry weight pulp furnish.
18. The process of claim 17 , wherein the amount of treated resin added to the papermaking furnish is from about 0.75% to about 1.25% dry weight pulp furnish.
19. The process of claim 1 , wherein the treated resin has at least about 150% to about 200% of the effectiveness of the initial water-soluble wet-strength resin.