Regeneration of polyvalent metal dicarboxylate catalyst for carbon dioxide-epoxide copolymerization

Claim 3

The method of Claim 1 wherein said catalyst is a product formed by reacting zinc oxide and a dicarboxylic acid.

Claim 4

The method of Claim 2 wherein the dicarboxylic acid used to contact the recovered catalyst has the same chemical formula as the dicarboxylic acid used to form said catalyst.

Claim 5

The method of Claim 2 wherein said dicarboxylic acids are selected from aromatic and aliphatic dibasic acids having from 2 to 10 carbon atoms.

Claim 6

The method of Claim 3 wherein said dicarboxylic acids are glutaric or adipic acids.

Claim 7

A process for reactivating spent catalyst from copolymerization of carbon dioxide and epoxide, said catalyst having been formed by reacting dicarboxylic acid and polyvalent metal oxide, hydroxide, alkoxide or organic acid salt, comprising (a) separating said spent catalyst from the reaction mixture of said copolymerization; (b) forming a slurry of said catalyst in a liquid medium contain­ing dicarboxylic acid of the type used in forming the cat­alyst originally; (c) heating and agitating said slurry to obtain thorough contact between said catalyst and said dicarboxylic acid in said liquid medium; (d) removing the contacted catalyst from said slurry; and (e) removing any excess dicarboxylic acid from said catalyst.

Claim 8

A process for reactivating spent catalyst from copolymerization of carbon dioxide and epoxide, said catalyst having been formed by reacting dicarboxylic acid and polyvalent metal oxide, hydroxide, alkoxide or organic acid salt, comprising (a) separating said spent catalyst from the reaction mixture of said copolymerization; (b) forming a slurry of said catalyst in a liquid medium contain­ing dicarboxylic acid of the type used in forming the cat­alyst originally; (c) heating and agitating said slurry to obtain thorough contact between said catalyst and said dicarboxylic acid in said liquid medium; (d) removing the contacted catalyst from said slurry; and (e) removing any excess dicarboxylic acid from said catalyst.

Claim 9

The process of Claim 6 wherein said slurry contains 1 to 50 weight percent catalyst solids.

Claim 10

The process of Claim 6 wherein said liquid medium contains at least one weight percent dicarboxylic acid.

Claim 11

The process of Claim 6 wherein said slurry contains 5 to 15 weight percent catalyst solids and said liquid medium contains 10 to 20 weight percent dicarboxylic acid.

Claim 12

The process of Claim 6 wherein said slurry is at a temperature of about 25 to 100°C and agitated for about one to four hours.

Claim 13

The process of Claim 6 wherein said contacted catalyst removed from said slurry is washed with ethanol to remove excess acid and dried at subatmospheric pressure with heating.

Claim 14

A process for copolymerizing carbon dioxide and epoxide with catalyst formed from a dicarboxylic acid and a polyvalent metal oxide, hydroxide, alkoxide or organic acid salt, comprising (a) contacting said carbon dioxide and epoxide with said catalyst under copolymerization conditions in a reaction zone; (b) removing at least a portion of said catalyst from said reaction zone, the catalyst thus removed having an activity less than freshly formed catalyst prior to said contacting step; (c) separating the removed catalyst from any accompanying reaction zone materials; (d) contacting said removed catalyst with dicarboxylic acid of the type used to form said catalyst originally, in a non-­deleterious liquid medium; (e) separating contacted catalyst of step (d) from excess dicarboxylic acid to form a regenerated catalyst; and (f) contacting said regenerated catalyst with carbon dioxide and epoxide under copolymerization conditions.

Claim 15

A process for copolymerizing carbon dioxide and epoxide with catalyst formed from a dicarboxylic acid and a polyvalent metal oxide, hydroxide, alkoxide or organic acid salt, comprising (a) contacting said carbon dioxide and epoxide with said catalyst under copolymerization conditions in a reaction zone; (b) removing at least a portion of said catalyst from said reaction zone, the catalyst thus removed having an activity less than freshly formed catalyst prior to said contacting step; (c) separating the removed catalyst from any accompanying reaction zone materials; (d) contacting said removed catalyst with dicarboxylic acid of the type used to form said catalyst originally, in a non-­deleterious liquid medium; (e) separating contacted catalyst of step (d) from excess dicarboxylic acid to form a regenerated catalyst; and (f) contacting said regenerated catalyst with carbon dioxide and epoxide under copolymerization conditions.

Claim 16

The process of Claim 12 wherein each of steps (a) and (f) are batch operations and substantially all of the catalyst from step (a) is regenerated for reuse in step (f).

Claim 17

The process of Claim 12 wherein steps (a) and (f) occur in a single reaction zone for a continuous process and sufficient catalyst is removed and separated in steps (b) and (c) either continuously or in­termittently, regenerated in steps (d) and (e), and returned to said reaction zone in order to maintain a desired average level of catalyst activity for the copolymerization.