Production of thermally stabilized polyester

Claim 2

A high molecular weight linear polyester stabilized against thermal degradation comprising a polyester reacted with a thermally stabilizing amount of a polycarbonate corresponding to the formula ##STR3## wherein R is a divalent hydrocarbon radical containing 2 to 15 carbon atoms and n is an integer between 2 and 100, in the presence of a catalytic amount of a phosphonium compound selected from the group consisting of tetra-n-alkylphosphonium acetates and tetra-n-alkylphosphonium halides, said n-alkyl radical containing 1 to 6 carbon atoms.

Claim 3

The polyester of claim 1 wherein the polyester is polyethylene terephthalate.

Claim 4

The polyester of claim 1 wherein the polycarbonate is polyethylene carbonate.

Claim 5

In a process for the preparation of a high molecular weight linear condensation polyester wherein terephthalic acid is esterified with a glycol containing 2 to 10 carbon atoms per molecule under esterification conditions and the resulting esterification product is polycondensed, the improvement which comprises providing a reduction in the free carboxyl content of the polyester to a carboxyl concentration of less than 12 gram equivalents per 10 6 grams of polyester by reacting the polyester in molten form with a thermally stabilizing amount of a stabilizer comprising a polycarbonate corresponding to the formula ##STR4## wherein R is a divalent hydrocarbon radical containing 2 to 15 carbon atoms and n is an integer between 2 and 100, in the presence of a catalytic amount of a phosphonium compound selected from the group consisting of tetra-n-alkylphosphonium acetates and tetra-n-alkylphosphonium halides, said n-alkyl radical containing 1 to 6 carbon atoms.

Claim 6

In a process for the preparation of a high molecular weight linear condensation polyester wherein terephthalic acid is esterified with a glycol containing 2 to 10 carbon atoms per molecule under esterification conditions and the resulting esterification product is polycondensed, the improvement which comprises providing a reduction in the free carboxyl content of the polyester to a carboxyl concentration of less than 12 gram equivalents per 10 6 grams of polyester by reacting the polyester in molten form with a thermally stabilizing amount of a stabilizer comprising a polycarbonate corresponding to the formula ##STR4## wherein R is a divalent hydrocarbon radical containing 2 to 15 carbon atoms and n is an integer between 2 and 100, in the presence of a catalytic amount of a phosphonium compound selected from the group consisting of tetra-n-alkylphosphonium acetates and tetra-n-alkylphosphonium halides, said n-alkyl radical containing 1 to 6 carbon atoms.

Claim 7

The process of claim 4 wherein the glycol is ethylene glycol.

Claim 8

The process of claim 4 wherein the polycarbonate is polyethylene carbonate.

Claim 9

In a continuous process for the preparation of a high molecular weight linear condensation polyester particularly useful for preparation of tire yarn, wherein terephthalic acid is continuously esterified with a glycol containing 2 to 10 carbon atoms per molecule under esterification conditions and the resulting esterification product is continuously polycondensed in a series of polycondensation zones at subatmospheric pressure, the improvement which comprises providing a reduction in the free carboxyl content of the polyester to a carboxyl concentration of less than 12 gram equivalents per 10 6 grams of polyester by reacting the polyester in molten form at about 270° C. to 300° C. with a thermally stabilizing amount of polycarbonate corresponding to the formula ##STR5## wherein R is a divalent hydrocarbon radical containing 2 to 15 carbon atoms and n is an integer between 4 and 50, in the presence of a catalytic amount of a phosphonium compound selected from the group consisting of tetra-n-alkylphosphonium acetates and tetra-n-alkylphosphonium halides, said n-alkyl radical containing 1 to 6 carbon atoms, said process being further characterized in that the polycarbonate and catalyst are added to the polyester process stream with mixing after the penultimate polycondensation zone and at a point to give 2 to 15 minutes reaction with the polyester before the polyester enters the last polycondensation zone, said reaction between the polycarbonate and the polyester being carried out under superatmospheric pressure.

Claim 10

In a continuous process for the preparation of a high molecular weight linear condensation polyester particularly useful for preparation of tire yarn, wherein terephthalic acid is continuously esterified with a glycol containing 2 to 10 carbon atoms per molecule under esterification conditions and the resulting esterification product is continuously polycondensed in a series of polycondensation zones at subatmospheric pressure, the improvement which comprises providing a reduction in the free carboxyl content of the polyester to a carboxyl concentration of less than 12 gram equivalents per 10 6 grams of polyester by reacting the polyester in molten form at about 270° C. to 300° C. with a thermally stabilizing amount of polycarbonate corresponding to the formula ##STR5## wherein R is a divalent hydrocarbon radical containing 2 to 15 carbon atoms and n is an integer between 4 and 50, in the presence of a catalytic amount of a phosphonium compound selected from the group consisting of tetra-n-alkylphosphonium acetates and tetra-n-alkylphosphonium halides, said n-alkyl radical containing 1 to 6 carbon atoms, said process being further characterized in that the polycarbonate and catalyst are added to the polyester process stream with mixing after the penultimate polycondensation zone and at a point to give 2 to 15 minutes reaction with the polyester before the polyester enters the last polycondensation zone, said reaction between the polycarbonate and the polyester being carried out under superatmospheric pressure.

Claim 11

The process of claim 7 wherein the glycol is ethylene glycol.

Claim 12

The process of claim 7 wherein the polycarbonate is polyethylene carbonate.

Claim 13

The process of claim 7 wherein the tetra-n-alkylphosphonium halide is chloride or bromide.