Melt polymerization process and linear aromatic polyesters prepared therefrom

Claim 2

A melt polymerization process for the preparation of a linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. which comprises (a) mixing a diphenyl ester of terephthalic acid and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and a diol of 2 to 20 carbon atoms, said oligomer having a degree of polymerization of 1 to about 20; and (b) reacting the mixture in the presence of a transesterification catalyst at an elevated temperature; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and where the weight ratio of bisphenol A to oligomer is from 95:5 to 15:85.

Claim 3

The process of claim 1 wherein the oligomer is prepared by reacting a dialkyl ester of terephthalic acid with said diol, wherein the alkyl moieties of the dialkyl ester have 1 to 10 carbon atoms.

Claim 4

The process of claim 1 wherein said diol is a 50:50 mixture of neopentyl glycol and diethylene glycol.

Claim 5

The process of claim 1 wherein said diol is diethylene glycol.

Claim 6

The process of claim 1 wherein said diol is neopentyl glycol.

Claim 7

The process of claim 1 wherein said diol is a polyalkylene ether or ester glycol.

Claim 8

The process of claim 6 wherein said diol is polyethylene glycol.

Claim 9

A process for the preparation of a linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. which comprises (a) mixing a diphenyl terephthalate and a hydroxyl component comprising bisphenol-A and an oligomer of terephthalic acid and neopentyl glycol having a degree of polymerization of 1 to about 20; and (b) reacting the mixture in the presence of a transesterification catalyst at a temperature of about 150° to 380° C.; wherein the diphenyl terephthalate component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 5 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is about 1:1.

Claim 10

A process for the preparation of a linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. which comprises (a) mixing a diphenyl terephthalate and a hydroxyl component comprising bisphenol-A and an oligomer of terephthalic acid and neopentyl glycol having a degree of polymerization of 1 to about 20; and (b) reacting the mixture in the presence of a transesterification catalyst at a temperature of about 150° to 380° C.; wherein the diphenyl terephthalate component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 5 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is about 1:1.

Claim 11

The process of claim 8 wherein the oligomer is prepared by reacting dimethyl terephthalate with neopentyl glycol.

Claim 12

A melt polymerization process for the preparation of linear aromatic polyesters having an intrinsic viscosity of at least 0.58 dl/g when measured in sym-tetrachloroethane at 25° C. which comprises (a) mixing a diphenyl ester of terephthalic acid, and a hydroxyl component comprising bisphenol-A and an oligomer of terephthalic acid and neopentyl glycol or polyethylene glycol, said oligomer having a degree of polymerization of 1 to about 20; and (b) reacting the mixture in the presence of a transesterification catalyst at an elevated temperature; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is from 95:5 to 15:85.

Claim 13

A melt polymerization process for the preparation of linear aromatic polyesters having an intrinsic viscosity of at least 0.58 dl/g when measured in sym-tetrachloroethane at 25° C. which comprises (a) mixing a diphenyl ester of terephthalic acid, and a hydroxyl component comprising bisphenol-A and an oligomer of terephthalic acid and neopentyl glycol or polyethylene glycol, said oligomer having a degree of polymerization of 1 to about 20; and (b) reacting the mixture in the presence of a transesterification catalyst at an elevated temperature; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is from 95:5 to 15:85.

Claim 14

The process of claim 10 wherein the glycol is neopentyl glycol.

Claim 15

The process of claim 10 wherein the glycol is polyethylene glycol.

Claim 16

The linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of a diphenyl ester of terephthalic acid, and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and a diol of 2 to 20 carbon atoms, said oligomer having a degree of polymerization of about 8 to about 20; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is from 95:5 to 15:85.

Claim 17

The linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of a diphenyl ester of terephthalic acid, and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and a diol of 2 to 20 carbon atoms, said oligomer having a degree of polymerization of about 8 to about 20; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is from 95:5 to 15:85.

Claim 18

The polyester of claim 13 wherein said diol is a polyalkylene ether or ester glycol.

Claim 19

A molded article of the composition of claim 13.

Claim 20

The linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of diphenyl terephthalate and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and a glycol of 2 to 20 carbon atoms having a degree of polymerization of about 8 to about 20; wherein the diphenyl terephthalate component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 5 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is about 1:1.

Claim 21

The linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of diphenyl terephthalate and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and a glycol of 2 to 20 carbon atoms having a degree of polymerization of about 8 to about 20; wherein the diphenyl terephthalate component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 5 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is about 1:1.

Claim 22

The linear aromatic polyester having an intrinsic viscosity of at least 0.6 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of a diphenyl ester of terephthalic acid, and a hydroxyl component comprising bisphenol-A and an oligomer of a terephthalic acid and neopentyl glycol, diethylene glycol or polyethylene glycol, said oligomer having a degree of polymerization of about 8 to about 20; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is from 95:5 to 15:85.

Claim 23

The linear aromatic polyester having an intrinsic viscosity of at least 0.6 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of a diphenyl ester of terephthalic acid, and a hydroxyl component comprising bisphenol-A and an oligomer of a terephthalic acid and neopentyl glycol, diethylene glycol or polyethylene glycol, said oligomer having a degree of polymerization of about 8 to about 20; wherein the diphenyl ester component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 120 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is from 95:5 to 15:85.

Claim 24

The linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of diphenyl terephthalate and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and neopentyl glycol having a degree of polymerization of about 8 to about 20; wherein the diphenyl terephthalate component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 5 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is about 1:1.

Claim 25

The linear aromatic polyester having an intrinsic viscosity of at least 0.5 dl/g when measured in sym-tetrachloroethane at 25° C. prepared by the melt transesterification and polycondensation of diphenyl terephthalate and a hydroxyl component comprising bisphenol A and an oligomer of terephthalic acid and neopentyl glycol having a degree of polymerization of about 8 to about 20; wherein the diphenyl terephthalate component and said hydroxyl component are present in proportions from stoichiometric proportions to an excess of up to about 5 percent of stoichiometric proportion of either component; and wherein the weight ratio of the bisphenol to oligomer is about 1:1.