Depolymerization of condensation polymers involving a pre-molecular weight reduction step

Claim 2

A process for the depolymerization of a condensation polymer comprising the steps in combination: (a) intimately admixing molten condensation polymer selected from the group consisting of polyamides and polyesters with a depolymerization agent selected from the group consisting of (i) a product resulting from the complete hydrolytic depolymerization of said condensation polymer in liquid form, and (ii) water, said depolymerization agent being present in said admixture in an amount by weight of less than the weight of said condensation polymer, (b) admixing said molten condensation polymer and said depolymerization agent for a time sufficient that the molecular weight of said condensation polymer is reduced by at least 50%; and (c) subjecting said treated condensation polymer to neutral hdryolysis with a substantial excess of water based on the weight of the condensation polymer, to thereby effect substantially complete hydrolytic depolymerization of said condensation polymer.

Claim 3

The process defined in claim 1 wherein said condensation polymer is intimately admixed with said depolymerization agent at a temperature of greater than about 10° C. above the melting temperature of the condensation polymer.

Claim 4

The process defined in claim 2 wherein said temperature is greater than about 20° C. above the melting point of the condensation polymer.

Claim 5

The process defined in claim 2 wherein the depolymerization agent is a product resulting from the complete hydrolytic depolymerization of the condensation polymer.

Claim 6

The process defined in claim 3 wherein the depolymerization agent is a product resulting from the complete hydrolytic depolymerization of the condensation polymer.

Claim 7

The process defined in claim 4 wherein the condensation polymer is a polyester and the depolymerization product is a dihydric alcohol.

Claim 8

The process defined in claim 6 wherein said polyester is treated with said dihydric alcohol as the depolymerization agent at a temperature of from 260°-310° C.

Claim 9

The process defined in claim 7 wherein said treatment is conducted at a pressure of from 500-2,000 psi.

Claim 10

The process defined in claim 8 wherein said polyester is polyethylene terephthalate and said depolymerizing agent is ethylene glycol.

Claim 11

The process defined in claim 8 wherein said polyester is butylene terephthalate and said depolymerization agent is 1,4-butanediol.

Claim 12

The process defined in claim 4 wherein said condensation polymer is a polyamide.

Claim 13

The process defined in claim 11 wherein said polyamide is nylon 6 and said depolymerization agent is caprolactam.

Claim 14

The process defined in claim 11 wherein said polyamide is nylon 66 and said depolymerization agent is hexamethylenediamine.

Claim 15

The process defined in claim 4 wherein the depolymerization agent is present in an amount of less than about 25% by weight, based on the weight of the condensation polymer.

Claim 16

The process defined in claim 14 wherein said depolymerization agent is present in an amount of less than about 10% by weight, based on the weight of the condensation polymer.

Claim 17

The process defined in claim 15 wherein said temperature is greater than about 20° C. above the melting point of the condensation polymer.

Claim 18

The process defined in claim 4 wherein the total time resulting from said steps (a), (b) and (c) is less than one-half the total time which would be required to effect substantially complete hydrolysis of the condensation polymer using step (c), alone.

Claim 19

A process for the depolymerization of a condensation polymer comprising steps in combination: (a) intimately admixing in a high temperature and high pressure screw extruder under high shear conditions, a molten condensation polymer selected from the group consisting of polyamides and polyesters with a depolymerization agent comprising at least one of the products resulting from complete hydrolytic depolymerization of said condensation polymer in liquid form, said depolymerization agent being present in said admixture in an amount by weight of less than the weight of said condensation polymer, said admixture forming a homogenous mass, (b) admixing said molten condensation polymer and said depolymerization agent while passing said mixture through the barrel of said screw extruder for a time sufficient that the molecular weight of said condensation polymer is reduced by at least 50%; and (c) subjecting said treated condensation polymer to neutral aqueous hydrolysis with a substantial excess of water based on the weight of the condensation polymer, at a pressure of less than the pressure in said extruder, to thereby effect substantially complete hydrolytic depolymerization of said condensation.

Claim 20

A process for the depolymerization of a condensation polymer comprising steps in combination: (a) intimately admixing in a high temperature and high pressure screw extruder under high shear conditions, a molten condensation polymer selected from the group consisting of polyamides and polyesters with a depolymerization agent comprising at least one of the products resulting from complete hydrolytic depolymerization of said condensation polymer in liquid form, said depolymerization agent being present in said admixture in an amount by weight of less than the weight of said condensation polymer, said admixture forming a homogenous mass, (b) admixing said molten condensation polymer and said depolymerization agent while passing said mixture through the barrel of said screw extruder for a time sufficient that the molecular weight of said condensation polymer is reduced by at least 50%; and (c) subjecting said treated condensation polymer to neutral aqueous hydrolysis with a substantial excess of water based on the weight of the condensation polymer, at a pressure of less than the pressure in said extruder, to thereby effect substantially complete hydrolytic depolymerization of said condensation.

Claim 21

The process defined in claim 18 wherein said depolymerization agent is admitted to said extruder through a valve situated such that its outlet discharges into the barrel of the extruder.

Claim 22

The process defined in claim 19 wherein said intimate admixture is passed through a static mixer, in-line with said extruder, and downstream of said valve, and upstream of the hydrolysis zone.

Claim 23

The process defined in claim 18 wherein the temperature in said extruder is at least 10° above the melting point of the condensation polymer.

Claim 24

The process defined in claim 21 wherein the temperature in the extruder is at least 20° C. above the melting temperature of the condensation polymer.

Claim 25

The process defined in claim 21 wherein the depolymerization agent is present in an amount of less than about 25% by weight, based on the weight of the polymer.

Claim 26

The process defined in claim 23 wherein the depolymerization agent is present in an amount of less than about 10%, by weight, based on the weight of the condensation polymer.

Claim 27

The process defined in claim 24 wherein the condensation polymer is a polyester and the depolymerization agent is a dihydric alcohol.