IP Library Granted Patent US 6,855,795
Granted Patent B2
US 6,855,795 · App. 10/850,249 · Granted Feb 15, 2005

Catalyst removal process

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Quick Facts
Patent No.
US 6,855,795
App. No.
10/850,249
Granted
Feb 15, 2005
Kind
B2
Abstract

The present invention provides a process for producing polycarbonates in the presence of one or more alkali metal or alkaline-earth metal catalysts, and subsequently removing the catalyst residues by chelation, to yield a clear polycarbonate product that is free from catalyst residues, and is thus suitable for use as a binding material in the ceramics industry where residual amounts of catalysts in the binder are burdensome.

Claims (14)

1. A process for producing a polycarbonate having the structure:

in which n is any number between about 5 and 50, R is any C 1 to C 20 alkyl group, whether straight-chain, cyclic, or branched, comprising the steps of:

a) reacting a reaction mixture comprising an aliphatic diol according to the formula: HO—R—OH in which R is any C 1 to C 20 alkyl group, whether straight-chain, cyclic, or branched and a linear organic carbonate having the formula:

in which R 1 and R 2 may independently be alkyl groups ranging from C 1 to C 4 , linear or branched, at a temperature of 60° C. to 180° C. in the presence of a catalyst selected from the group consisting of: one or more alkali or alkaline earth metal alkoxide, hydroxide, carbonate, or carboxylate salts, or mixtures of any of the foregoing;

b) supplying heat to said reaction mixture to cause distillation of alcohol by-product(s) produced from step a) above until said reaction mixture reaches a termination temperature of at least 150° C. to provide a semi-stripped crude product;

c) contacting said semi-stripped crude product from step b) with a chelating agent; to form a slurry; and

d) filtering said slurry from step c) to provide a clear liquid.

2. A process according to claim 1 wherein said semi-stripped crude product is mixed with an alcohol prior to its being contacted with a chelating agent or adsorbent.

3. A process according to claim 1 wherein said chelating agent is a magnesium silicate.

4. A process according to claim 1 wherein said termination temperature is in the range of 150° C. to 200° C.

5. A process according to claim 1 wherein said termination temperature is in the range of 160° C. to 200° C.

6. A process according to claim 1 wherein said termination temperature is in the range of 170° C. to 200° C.

7. A process according to claim 1 wherein said termination temperature is in the range of 180° C. to 200° C.

8. A process according to claim 1 wherein said termination temperature is in the range of 190° C. to 200° C.