Process for polymerization of thermotropic polyesters and polyesters

Claim 2

A process for preparing a thermotropic polyester by condensation of a monomer reaction mixture which comprises: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.09 to about 0.16 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 100 sec -1 and an ambient pressure of less than about 3 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of an aromatic dicarboxylic acid and a diphenol ester and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 3

The process of claim 1 wherein the shear rate is at least about 1000 sec -1 .

Claim 4

The process of claim 2 wherein the apparent melt viscosity of the polyester product determined at a temperature 5° C. above the temperature of formation of the anisotropic melt phase and at a shear rate of about 1000 sec -1 , is no more than about 100 Pa.s.

Claim 5

The process of claim 3 wherein the monomer reaction mixture consists essentially of a diester of a diphenol and a C 2 to C 4 monocarboxylic acid, an aromatic dicarboxylic acid, and an ester of p-hydroxybenzoic acid and a C 2 to C 4 monocarboxylic acid.

Claim 6

The process of claim 3 wherein the monomer reaction mixture consists essentially of a diester of a diphenol and a C 2 to C 4 monocarboxylic acid, an aromatic dicarboxylic acid, a C 7 to C 12 aliphatic dicarboxylic acid, and an ester of p-hydroxybenzoic acid and a C 2 to C 4 monocarboxylic acid.

Claim 7

The process of claim 4 wherein the diphenol is hydroquinone, the aromatic dicarboxylic acid is selected from the group consisting of isophthalic acid, terephthalic acid and 1,5-, 2,5-; 2,6- and 2,7-naphthalic acids and wherein the mole ratio of p-hydroxybenzoic acid ester to hydroquinone diester is in the range of about 1:4.5 to about 4:3.

Claim 8

The process of claim 6 wherein the aromatic dicarboxylic acid is isophthalic acid.

Claim 9

The process of claim 5 wherein the diphenol is hydroquinone, the aromatic dicarboxylic acid is selected from the group consisting of isophthalic acid, terephthalic acid and 1,5-, 2,5-; 2,6- and 2,7-naphthalic acids and wherein the mole ratio of p-hydroxybenzoic acid ester to hydroquionone diester is in the range of about 1:4.5 to about 3:2.

Claim 10

The process of claim 8 wherein the mole ratio of aliphatic dicarboxylic acid to aromatic dicarboxylic acid is about 1:99 to about 30:70.

Claim 11

The process of claim 9 wherein the aromatic dicarboxylic acid is isophthalic acid and the aliphatic dicarboxylic acid is azelaic acid.

Claim 12

The process of claim 4 wherein the diphenol diester is a mixture of hydroquinone diester and 2,2-bis(4-hydroxyphenyl) propane diester containing up to about 20 mole percent 2,2-bis(4-hydroxyphenyl)propane diester, wherein the mole ratio of p-hydroxybenzoic acid ester to diphenol diester is in the range of about 1:4.5 to about 4:3 and wherein the aromatic dicarboxylic acid is selected from the group consisting of isophthalic acid, terephthalic acid, and 1,5-, 2,5-, 2,6- and 2,7-naphthalic acids.

Claim 13

The process of claim 1 wherein the melt is passed through the wiped film reactor at a sufficient rate to provide a polyester product of inherent viscosity at least about 0.8 dl g -1 .

Claim 14

The process of claim 1, wherein the diphenol diester is formed in situ by reaction of an acid anhydride with the diphenol.

Claim 15

A process for preparing a thermotropic polyester by condensation of a monomer reaction mixture which comprises: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.13 to about 0.15 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 1000 sec -1 and an ambient pressure of less than 1.5 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of (i) a diester of a C 2 to C 4 monocarboxylic acid and a diphenol consisting of hydroquinone and from 0 to 20 mole percent 2,2-bis(4-hydroxyphenyl)-propane, (ii) an aromatic dicarboxylic acid selected from the group consisting of isophthalic acid, terephthalic acid, and 1,5-, 2,5-; 2,6- and 2,7-naphthalic acids, and (iii) an ester of a C 2 to C 4 monocarboxylic acid and p-hydroxybenzoic acid, and wherein the mole ratio of the p-hydroxybenzoic acid ester to the diphenol diester is in the range of about 1:4.5 to about 4:3; and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 16

A process for preparing a thermotropic polyester by condensation of a monomer reaction mixture which comprises: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.13 to about 0.15 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 1000 sec -1 and an ambient pressure of less than 1.5 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of (i) a diester of a C 2 to C 4 monocarboxylic acid and a diphenol consisting of hydroquinone and from 0 to 20 mole percent 2,2-bis(4-hydroxyphenyl)-propane, (ii) an aromatic dicarboxylic acid selected from the group consisting of isophthalic acid, terephthalic acid, and 1,5-, 2,5-; 2,6- and 2,7-naphthalic acids, and (iii) an ester of a C 2 to C 4 monocarboxylic acid and p-hydroxybenzoic acid, and wherein the mole ratio of the p-hydroxybenzoic acid ester to the diphenol diester is in the range of about 1:4.5 to about 4:3; and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 17

The process of claim 13 wherein the melt is passed through the wiped film reactor at a sufficient rate to provide a polyester product of inherent viscosity at least about 0.8 dl g -1 .

Claim 18

The process of claim 13 wherein the aromatic dicarboxylic acid is isophthalic acid.

Claim 19

A process for preparing a thermotropic polyester by condensation of a monomer reaction mixture which comprises: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.13 to about 0.15 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 1000 sec -1 and an ambient pressure of less than about 1.5 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of (i) a diester of a C 2 to C 4 monocarboxylic acid and hydroquinone, (ii) an aromatic dicarboxylic acid selected from the group consisting of isophthalic acid, terephthalic acid, and 1,5-, 2,5-; 2,6- and 2,7-napthalic acids, (iii) a C 7 to C 12 aliphatic dicarboxylic acid and (iv) an ester of a C 2 to C 4 monocarboxylic acid and p-hydroxybenzoic acid, wherein the mole ratio of the aromatic dicarboxylic acid to the aliphatic dicarboxylic acid is about 99:1 to about 70:30 and wherein the mole ratio of the p-hydroxybenzoic acid ester to the hydroquinone diester is in the range of about 1:4.5 to about 3:2; and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 20

A process for preparing a thermotropic polyester by condensation of a monomer reaction mixture which comprises: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.13 to about 0.15 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 1000 sec -1 and an ambient pressure of less than about 1.5 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of (i) a diester of a C 2 to C 4 monocarboxylic acid and hydroquinone, (ii) an aromatic dicarboxylic acid selected from the group consisting of isophthalic acid, terephthalic acid, and 1,5-, 2,5-; 2,6- and 2,7-napthalic acids, (iii) a C 7 to C 12 aliphatic dicarboxylic acid and (iv) an ester of a C 2 to C 4 monocarboxylic acid and p-hydroxybenzoic acid, wherein the mole ratio of the aromatic dicarboxylic acid to the aliphatic dicarboxylic acid is about 99:1 to about 70:30 and wherein the mole ratio of the p-hydroxybenzoic acid ester to the hydroquinone diester is in the range of about 1:4.5 to about 3:2; and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 21

The process of claim 17 wherein the melt is passed through the wiped film reactor at a sufficient rate to provide a polyester product of inherent viscosity at least about 0.8 dl g -1 .

Claim 22

The process of claim 17 wherein the aromatic dicarboxylic acid is isophthalic acid and the aliphatic dicarboxylic acid is azelaic acid.

Claim 23

A thermotropic polyester prepared by condensation of a monomer reaction mixture wherein the condensation is effected by: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.09 to about 0.16 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 100 sec -1 and an ambient pressure of less than about 3 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of an aromatic dicarboxylic acid and a diphenol ester; and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 24

A thermotropic polyester prepared by condensation of a monomer reaction mixture wherein the condensation is effected by: (A) melt polymerizing the monomer reactants to provide a prepolymer of inherent viscosity in the range of about 0.09 to about 0.16 dl g -1 ; and (B) passing the melt through a wiped film reactor to provide a molten film of polyester subjected to a shear rate of at least about 100 sec -1 and an ambient pressure of less than about 3 kPa, the rate of passage of the melt being adjusted to provide a residence time sufficient to allow the molecular weight of the thermotropic polyester to advance to a level at which the inherent viscosity of the polyester is at least about 0.5 dl g -1 , the temperature of the wiped film reactor being maintained at less than about 400° C. and in the range in which the thermotropic polyester forms an anisotropic melt phase; wherein the monomer reaction mixture consists essentially of an aromatic dicarboxylic acid and a diphenol ester; and wherein the inherent viscosity values are those obtained with solutions of polymer in a solvent pair of phenol and tetrachloroethane (60:40 by weight) containing 0.5 g of polymer per 100 ml of solvent.

Claim 25

The thermotropic polyester of claim 20 wherein the film thickness is less than about 1 mm and wherein the shear rate is at least about 1000 sec -1 .

Claim 26

The thermotropic polyester of claim 21 wherein the apparent melt viscosity of the polyester product determined at a temperature 5° C. above the temperature of formation of the anisotropic melt phase and at a rate of about 1000 sec -1 , is no more than about 100 Pa.s.

Claim 27

The thermotropic polyester of claim 20 wherein the monomer reaction mixture consists essentially of a diester of a diphenol and a C 2 to C 4 monocarboxylic acid, an aromatic dicarboxylic acid, and an ester of p-hydroxybenzoic acid and a C 2 to C 4 monocarboxylic acid.

Claim 28

The thermotropic polyester of claim 20 wherein the monomer reaction mixture consists essentially of a diester of a diphenol and a C 2 to C 4 monocarboxylic acid, an aromatic dicarboxylic acid, a C 7 to C 12 aliphatic dicarboxylic acid, and an ester of p-hydroxybenzoic acid and a C 2 to C 4 monocarboxylic acid.

Claim 29

The thermotropic polyester of claim 20 of inherent viscosity at least about 0.8 dl g -1 .

Claim 30

The thermotropic polyester of claim 23 wherein the diphenol is hydroquinone, the aromatic dicarboxylic acid is selected from the group consisting of isophthalic acid, terephthalic acid and 1,5-, 2,5-, 2,6- and 2,7-naphthalic acids and wherein the mole ratio of p-hydroxybenzoic acid ester to hydroquinone diester is in the range of about 1:4.5 to about 4:3.

Claim 31

The thermotropic polyester of claim 25 wherein the aromatic dicarboxylic acid is isophthalic acid.

Claim 32

The thermotropic polyester of claim 24 wherein the diphenol is hydroquinone, the aromatic dicarboxylic acid is selected from the group consisting of isophthalic acid, terephthalic acid and 1,5-, 2,5-, 2,6- and 2,7-naphthalic acids and wherein the mole ratio of p-hydroxybenzoic acid ester to hydroquinone diester is in the range of about 1:4.5 to about 3:2.

Claim 33

The thermotropic polyester of claim 24 wherein the mole ratio of aliphatic dicarboxylic acid to aromatic dicarboxylic acid is about 1:99 to about 30:70.

Claim 34

The thermotropic polyester of claim 28 wherein the aromatic dicarboxylic acid is isophthalic acid and the alipahtic dicarboxylic acid is azelaic acid.