Polymerization process and product

Claim 2

A copolymer derived from the polymerization of about 60 to about 95 weight percent of lactic acid and about 40 to about 5 weight percent of glycolic acid, having an inherent viscosity in chloroform of about 0.08 to about 0.30 and a molecular weight of about 6000 to about 35000, said copolymer being substantially free of polymerization catalyst.

Claim 3

The copolymer of claim 1, said copolymer derived from about 60 to about 90 percent lactic acid and about 40 to about 10 percent glycolic acid, having an inherent viscosity of about 0.1 to about 0.25 and a molecular weight of about 15,000 to about 30,000.

Claim 4

The copolymer of claim 1, said copolymer derived from about 65 to about 80 percent lactic acid and about 35 to about 20 percent glycolic acid, having an inherent viscosity of about 0.10 to about 0.25 and a molecular weight of about 15000 to about 30000.

Claim 5

The copolymer of claim 1, said copolymer derived from about 70 to about 80 percent lactic acid and about 30 to about 20 percent glycolic acid, having an inherent viscosity of about 0.10 to about 0.25.

Claim 6

The copolymer of claim 1, said copolymer being derived from about 70 percent lactic acid and about 30 percent glycolic acid, having an inherent viscosity of about 0.10 to about 0.15.

Claim 7

The copolymer of claim 1, said copolymer being derived from about 80 percent lactic acid and about 20 percent glycolic acid, having an inherent viscosity of about 0.15 to about 0.25.

Claim 8

A process for preparing a copolymer derived by the polymerization of about 60 to about 95 weight percent of lactic acid and about 40 to about 5 weight percent of glycolic acid, said copolymer having a molecular weight of about 6000 to about 35000, with an inherent viscosity in chloroform of about 0.08 to about 0.30, comprising reacting lactic acid with glycolic acid in the presence of a readily removable strong acid ion-exchange resin at a temperature from about 100° to about 250° C. for about 3 to about 172 hours, and removing the strong acid ion-exchange resin therefrom.

Claim 9

A process for preparing a copolymer derived by the polymerization of about 60 to about 95 weight percent of lactic acid and about 40 to about 5 weight percent of glycolic acid, said copolymer having a molecular weight of about 6000 to about 35000, with an inherent viscosity in chloroform of about 0.08 to about 0.30, comprising reacting lactic acid with glycolic acid in the presence of a readily removable strong acid ion-exchange resin at a temperature from about 100° to about 250° C. for about 3 to about 172 hours, and removing the strong acid ion-exchange resin therefrom.

Claim 10

The process according to claim 7 wherein from about 60 to about 90 parts of lactic acid are reacted with from about 40 to about 10 parts of glycolic acid in the presence of a strong acid ion-exchange resin.

Claim 11

The process of claim 8 wherein the strong acid ion-exchange resin is a sulfonic acid group containing resins.

Claim 12

The process of claim 7 wherein about 70 parts of lactic acid are reacted with about 30 parts of glycolic acid in the presence of a sulfonic acid group containing ion exchange resin for about 48 to about 96 hours to give a copolymer derived from about 70 weight percent lactic acid and about 30 weight percent glycolic acid, having an inherent viscosity of about 0.10 to about 0.25.

Claim 13

The process of claim 7 wherein about 80 parts of lactic acid are reacted with about 20 parts of glycolic acid in the presence of a sulfonic acid group containing ion exchange resin for about 48 to about 96 hours to give a copolymer derived from about 80 weight percent lactic acid and about 20 weight percent glycolic acid, having an inherent viscosity of about 0.10 to about 0.25.