ROBUST PROMOTER CATALYST SYSTEM
A modified ion exchange resin catalyst having an attached dimethyl thiazolidine promoter is disclosed. Also disclosed is a process for catalyzing condensation reactions between phenols and ketones, wherein reactants are contacted with a modified ion exchange resin catalyst having an attached dimethyl thiazolidine promoter. Also disclosed is a process for catalyzing condensation reactions between phenols and ketones that does not utilize a bulk promoter.
1 - 14 . (canceled)
15 . An attached promoter catalyst system comprising an ion exchange resin and a dimethyl thiazolidine promoter, wherein the attached promoter catalyst system is more resistant to hydroxyacetone than a conventional bulk promoter system.
16 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system maintains at least about 60% of its initial performance after 200 hours of operation, in terms of the amount of p,p-bisphenol-A produced, in the presence of about 10 ppm hydroxyacetone.
17 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system maintains at least about 75% of its initial performance after 200 hours of operation, in terms of the amount of p,p-bisphenol-A produced, in the presence of about 10 ppm hydroxyacetone.
18 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system is substantially unaffected, during operation, by exposure to up to about 1,000 ppm of alcohol.
19 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system is substantially unaffected, during operation, by exposure to up to about 3,000 ppm of alcohol.
20 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system is substantially unaffected by recycled bisphenol-A impurities.
21 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system, in a condensation reaction, selectively catalyzes the production of p,p-bisphenol-A in a ratio of at least about 25:1 p,p-bisphenol-A to o,p-bisphenol-A.
22 . The attached promoter catalyst system of claim 15 , wherein the attached promoter catalyst system, in a condensation reaction, can selectively catalyze the production of p,p-bisphenol-A in a ratio of at least about 30:1 p,p-bisphenol-A to o,p-bisphenol-A.
23 .- 41 . (canceled)