Inverse interfacial polymerization for preparing certain halogenated aromatic polyesters

Claim 2

A process for preparing a halogenated aromatic polyester of the recurring structural formula ##STR6## where X which may be the same or different is chlorine or bromine, Y which may be the same or different is hydrogen, chlorine or bromine, R and R' may be the same or different and represent lower alkyl groups, hydrogen, or together constitute a cyclic hydrocarbon group, and n equals at least 13, by the inverse interfacial polymerization of a halogenated bisphenol and isophthaloyl chloride, terephthaloyl chloride or mixtures thereof which comprises: I. providing an organic phase comprising a. an organic solvent, b. a phthaloyl chloride or mixtures thereof, and c. a catalytic amount of a phase transfer catalyst; Ii. providing an aqueous phase comprising a. an aqueous solvent immiscible with said organic solvent and capable of dissolving an alkali salt of said halogenated bisphenol, b. an alkali salt of said halogenated bisphenol, and c. a base in amounts sufficient to provide a pH of at least 8 in said aqueous solution, Iii. adding the aqueous phase to the organic phase over a period of time of not less than about 20% of the total polymerization time and in a manner sufficient to sustain the uniform availability of phase transfer catalyst for reaction with the alkali salt of the bisphenol during the polymerization reaction thereby providing a polyester having a low molecular weight fraction of not greater than about 3% by weight of the polyester; Iv. recovering the resulting polyester product.

Claim 3

The process according to claim 1 wherein said halogenated aromatic polyester of the recurring structural formula is a product of a tetrabromobisphenol and a mixture of about 40 to 80% by weight isophthaloyl chloride and correspondingly about 60 to about 20% by weight terephthaloyl chloride.

Claim 4

The process according to claim 1 wherein said halogenated aromatic polyester of the recurring structural formula is a product of tetrabromobisphenol A and a mixture of about 60% by weight isophthaloyl chloride and correspondingly about 40% by weight terephthaloyl chloride.

Claim 5

The process according to claim 1 wherein the aqueous phase is added to the organic phase over a period of time of about 20 to 50% of the total polymerization time.

Claim 6

The process according to claim 1 wherein said halogenated aromatic polyester of the recurring structural formula is a product of a tetrachlorobisphenol and a mixture of about 90 to 40% by weight isophthaloyl chloride and correspondingly about 10 to 60% by weight terephthaloyl chloride.

Claim 7

The process according to claim 1 wherein said halogenated aromatic polyester of the recurring structural formula is a product of tetrachlorobishpenol A and a mixture of about 70% by weight isophthaloyl chloride and correspondingly about 30% by weight terephthaloyl chloride.

Claim 8

The process of claim 1 wherein the phase transfer catalyst is selected from the group consisting of quaternary ammonium salts, quaternary phosphonium salts, quaternary arsonium salts and tertiary sulfonium salts.

Claim 9

The process of claim 1 wherein the phase transfer catalyst is benzyltriethylammonium chloride.

Claim 10

The process of claim 1 wherein the halogenated aromatic polyester of the recurring structural formula has an intrinsic viscosity of about 0.4 to about 1.7.

Claim 11

The process of claim 1 wherein the organic solvent is methylene chloride and the aqueous solvent is water.

Claim 12

The process of claim 1 wherein the polyester is recovered from the organic phase by precipitation with a non-solvent medium.

Claim 13

A process for preparing a halogenated aromatic polyester of the recurring structural formula ##STR7## where X which may be the same or different is chlorine or bromine, Y which may be the same or different is hydrogen, chlorine or bromine, R and R' may be the same or different and represent lower alkyl groups, hydrogen, or together constitute a cyclic hydrocarbon group, n equals at least 13, by the inverse interfacial polymerization of a halogenated bisphenol and a mixture of isophthaloyl chloride, and terephthaloyl chloride which comprises: I. providing an organic phase comprising a. an organic solvent, b. a mixture of isophthaloyl and terephthaloyl chloride, and c. a catalytic amount of a phase transfer catalyst, Ii. providing an aqueous phase comprising a. water, an alkali salt of said halogenated bisphenol, and c. a base sufficient to establish a pH of said aqueous phase of at least 8; Iii. gradually adding the aqueous phase to organic phase over a period of time of about 20 to 30% of the total polymerization time and in a manner sufficient to provide a stoichmetric excess of acid chloride over the alkali salt of the bisphenol in the reaction mixture during the polymerization said stoichiometric excess being sufficient to sustain the uniform availability of the phase transfer catalyst for reaction with the alkali salt of the bisphenol thereby providing said aromatic polyester with a low molecular weight fraction of not greater than 3% by weight of the total weight of the polyester formed; and Iv. recovering the resulting polyester product.

Claim 14

A process for preparing a halogenated aromatic polyester of the recurring structural formula ##STR7## where X which may be the same or different is chlorine or bromine, Y which may be the same or different is hydrogen, chlorine or bromine, R and R' may be the same or different and represent lower alkyl groups, hydrogen, or together constitute a cyclic hydrocarbon group, n equals at least 13, by the inverse interfacial polymerization of a halogenated bisphenol and a mixture of isophthaloyl chloride, and terephthaloyl chloride which comprises: I. providing an organic phase comprising a. an organic solvent, b. a mixture of isophthaloyl and terephthaloyl chloride, and c. a catalytic amount of a phase transfer catalyst, Ii. providing an aqueous phase comprising a. water, an alkali salt of said halogenated bisphenol, and c. a base sufficient to establish a pH of said aqueous phase of at least 8; Iii. gradually adding the aqueous phase to organic phase over a period of time of about 20 to 30% of the total polymerization time and in a manner sufficient to provide a stoichmetric excess of acid chloride over the alkali salt of the bisphenol in the reaction mixture during the polymerization said stoichiometric excess being sufficient to sustain the uniform availability of the phase transfer catalyst for reaction with the alkali salt of the bisphenol thereby providing said aromatic polyester with a low molecular weight fraction of not greater than 3% by weight of the total weight of the polyester formed; and Iv. recovering the resulting polyester product.

Claim 15

The process according to claim 12 wherein said halogenated aromatic polyester of the recurring structural formula is a product of a tetrabromobisphenol and a mixture of about 40 to 80% by weight isophthaloyl chloride and correspondingly about 60 to 20% by weight terephthaloyl chloride.

Claim 16

The process according to claim 12 wherein said halogenated aromatic polyester of the recurring structural formula is a product of tetrabromobisphenol A and a mixture of about 60% by weight isophthaloyl chloride and correspondingly about 40% by weight terephthaloyl chloride.

Claim 17

The process according to claim 12 wherein said halogenated aromatic polyester of the recurring structural formula is a product of a tetrachlorobisphenol and a mixture of about 90 to 40% by weight isophthaloyl chloride and correspondingly about 10 to 60% by weight terephthaloyl chloride.

Claim 18

The process according to claim 12 wherein said halogenated aromatic polyester of the recurring structural formula is a product of tetrachlorobisphenol A and a mixture of about 70% by weight isophthaloyl chloride and correspondingly about 30% by weight terephthaloyl chloride.

Claim 19

The process of claim 12 wherein the phase transfer catalyst is selected from the group consisting of quaternary ammonium salts, quaternary phosphonium salts, quaternary arsonium salts and tertiary sulfonium salts.

Claim 20

The process of claim 12 wherein the phase transfer catalyst is benzyltriethylammonium chloride.

Claim 21

The process of claim 12 wherein the halogenated aromatic polyester of the recurring structural formula has an intrinsic viscosity of about 0.8 to about 1.2.

Claim 22

A process for preparing a brominated aromatic polyester of the recurring structural formula ##STR8## wherein X and Y are bromine, R and R' may be the same or different and represent lower alkyl groups, hydrogen, or together constitute a cyclic hydrocarbon group, and n equals at least 13, by the inverse interfacial polymerization of a brominated bisphenol and a mixture of isophthaloyl chloride and terephthaloyl chloride which comprises I. providing an organic phase comprising a. methylene chloride, b. a 60:40 mixture of isophthaloyl and terephthaloyl chloride, c. a catalytic amount of benzyltriethylammonium chloride; Ii. providing an aqueous phase comprising a. water, b. an alkali salt of said brominated bisphenol, c. sodium hydroxide in an amount sufficient to establish a pH of said aqueous phase of at least 8; Iii. gradually adding the aqueous phase to the organic phase at a rate of about 1 to about 10 mole percent per minute based on the total number of moles of the bisphenol salt originally present in the aqueous phase prior to addition; Iv. recovering the resulting polyester product.

Claim 23

A process for preparing a brominated aromatic polyester of the recurring structural formula ##STR8## wherein X and Y are bromine, R and R' may be the same or different and represent lower alkyl groups, hydrogen, or together constitute a cyclic hydrocarbon group, and n equals at least 13, by the inverse interfacial polymerization of a brominated bisphenol and a mixture of isophthaloyl chloride and terephthaloyl chloride which comprises I. providing an organic phase comprising a. methylene chloride, b. a 60:40 mixture of isophthaloyl and terephthaloyl chloride, c. a catalytic amount of benzyltriethylammonium chloride; Ii. providing an aqueous phase comprising a. water, b. an alkali salt of said brominated bisphenol, c. sodium hydroxide in an amount sufficient to establish a pH of said aqueous phase of at least 8; Iii. gradually adding the aqueous phase to the organic phase at a rate of about 1 to about 10 mole percent per minute based on the total number of moles of the bisphenol salt originally present in the aqueous phase prior to addition; Iv. recovering the resulting polyester product.

Claim 24

A process for preparing a halogenated aromatic polyester according to claim 1 wherein n of said recurring structural formula is about 40 to 400.

Claim 25

A process for preparing a halogenated aromatic polyester according to claim 12 wherein n of said recurring structural formula is about 40 to 400.

Claim 26

A process for preparing a brominated aromatic polyester according to claim 20 wherein n of said recurring structural formula is about 40 to 400.