Transesterification process for preparation of linear polyesters

Claim 2

In the process of preparing a linear aromatic polyester by the transesterification polymerization reaction of a mixture of a bisphenol and a diaryl ester of a dicarboxylic acid wherein the molar proportion of the bisphenol and the diaryl ester ranges from about 5 molar percent insufficiency of the diaryl ester over the stoichiometric equivalent proportion of the bisphenol and the diaryl-ester to an excess of the diaryl ester over said stoichiometric proportion, the improvement wherein the diaryl ester is mixed with and transesterified with a minor molar proportion of a saturated aliphatic hydrocarbon monofunctional alcohol of 8 to 45 carbon atoms prior to any reaction of the bisphenol reactant and the diaryl ester reactant, said proportion of the alcohol being based on the molar amount of the diaryl ester reactant employed in the polymerization reactant.

Claim 3

The process of claim 1 wherein the transesterification reaction of the alcohol and the diaryl ester and the transesterification polymerization reaction are carried out in the presence of a catalytically effective amount of a transesterification catalyst.

Claim 4

The process of claim 2 wherein the catalyst employed in the transesterification reaction of the alcohol and the diaryl ester is the catalyst employed in the transesterification polymerization reaction and the transesterification reaction of said alcohol and said diaryl ester is carried out to substantial completion in the polymerization reaction mixture prior to the addition of the bisphenol to the mixture.

Claim 5

The process of claim 3 wherein the molar proportion of the alcohol is about 0.1 to about 25 mole percent based on the molar amount of the diaryl ester employed in the esterification, the reaction of the alcohol and the diaryl ester is carried out at a temperature of about 100° to about 300° and at atmospheric pressure or a pressure below atmospheric pressure.

Claim 6

The process of claim 4 wherein the molar proportion of the alcohol is above about 2.5 mole percent based on the molar amount of the diaryl ester, the reaction of the alcohol and the diaryl ester is carried out at a temperature of about 150° to about 250° and at sub-atmospheric pressure.

Claim 7

The process of claim 5 wherein the molar proportion of the alcohol is about 3.0 to about 10 mole percent based on the molar amount of the diaryl ester, the reaction of the alcohol and the diaryl ester is carried out at a temperature of about 175° to about 225°.

Claim 8

The process of claim 6 wherein the bisphenol and the diaryl ester are employed in about stoichiometric equivalent proportions and the amount of catalyst employed is about 0.005% to about 2% based on the combined weight of the bisphenol and diaryl ester.

Claim 9

The process of claim 7 wherein the proportion of catalyst employed is about 0.01% to about 1% based on the combined weight of the bisphenol and the diaryl ester.

Claim 10

The process of claim 8 wherein the catalyst is lithium phenoxide.

Claim 11

The process of claim 1 wherein the diaryl ester is the diester of an aromatic monohydroxy compound of the benzene or naphthalene series of 6 to 20 carbon atoms and a dicarboxylic acid of the formula: ##STR7## wherein Z is alkylene, --Ar-- or --Ar--Y--Ar-- where Ar is aromatic, Y is alkylene, haloalkylene, ##STR8## wherein G is alkyl, haloalkyl, aryl, haloaryl, alkylaryl, haloalkylaryl, arylalkyl, haloarylalkyl, cycloalkyl or cyclohaloalkyl; and n is 0 or 1 and the alcohol is a saturated alcohol of 9 to 40 carbon atoms.

Claim 12

The process of claim 10 wherein said diaryl ester is the diester of an aromatic monohydroxy compound of the benzene series and an aromatic dicarboxylic acid and the alcohol is an acyclic alcohol of 12 to 30 carbon atoms.

Claim 13

The process of claim 11 wherein the diaryl ester is a diester of phenol and an aromatic dicarboxylic acid selected from the group consisting of isophthalic acid, terephthalic acid and mixtures thereof, the alcohol is a straight chain primary alcohol of 15 to 20 carbon atoms.

Claim 14

The process of claim 12 wherein the diaryl ester is the diphenyl ester of a mixture of about 75 to 100 mole percent of isophthalic acid and about 25 to 0 mole percent of terephthalic acid.

Claim 15

The process of claim 13 wherein the diaryl ester is the diphenyl ester of a mixture of about 75 to about 90 mole percent isophthalic acid and about 10 to about 25 mole percent terephthalic acid and the alcohol is stearyl alcohol.

Claim 16

The process of claim 1 wherein the bisphenol has the formula: ##STR9## wherein Ar is aromatic, G is alkyl, haloalkyl, aryl, haloaryl, alkylaryl, haloalkylaryl, arylalkyl, haloarylalkyl, cycloalkyl, or cyclohaloalkyl; E is divalent alkylene, haloalkylene, cycloalkylene, halocycloalkylene, arylene, or haloarylene, --O--, --S--, ##STR10## T and T' are independently selected from the group consisting of halogen, G and OG; m is an integer from 0 to the number of replaceable hydrogen atoms on E; b is an integer from 0 to the number of replaceable hydrogen atoms on Ar, and x is 0 or 1.

Claim 17

The process of claim 15 wherein the bisphenol is bisphenol-A.

Claim 18

In the process of preparing a linear aromatic polyester by the transesterification polymerization reaction of a mixture of about stoichiometric equivalent proportions of a bisphenol and a diphenyl ester of an aromatic dicarboxylic acid, the improvement wherein the diphenyl ester is transesterified at a temperature of about 100° to 300° under sub-atmospheric pressure with about 0.1 mole percent to about 25 mole percent of an aliphatic monofunctional saturated alcohol of 9 to 40 carbon atoms, based on the molar amount of the diphenyl ester reactant, prior to the addition of the bisphenol to said mixture, said transesterification reaction of the alcohol and the diphenyl ester and said transesterification polymerization reaction being carried out in the presence of about 0.005% to about 2% of a transesterification catalyst based on the combined weight of the bisphenol and the diphenyl ester to recover a linear aromatic polyester of said bisphenol and said dicarboxylic acid which contains at least about 5 mole percent of a terminal carboxylate ester group derived from the organic radical of said alcohol based on the total moles of end groups in the polyester.

Claim 19

In the process of preparing a linear aromatic polyester by the transesterification polymerization reaction of a mixture of about stoichiometric equivalent proportions of a bisphenol and a diphenyl ester of an aromatic dicarboxylic acid, the improvement wherein the diphenyl ester is transesterified at a temperature of about 100° to 300° under sub-atmospheric pressure with about 0.1 mole percent to about 25 mole percent of an aliphatic monofunctional saturated alcohol of 9 to 40 carbon atoms, based on the molar amount of the diphenyl ester reactant, prior to the addition of the bisphenol to said mixture, said transesterification reaction of the alcohol and the diphenyl ester and said transesterification polymerization reaction being carried out in the presence of about 0.005% to about 2% of a transesterification catalyst based on the combined weight of the bisphenol and the diphenyl ester to recover a linear aromatic polyester of said bisphenol and said dicarboxylic acid which contains at least about 5 mole percent of a terminal carboxylate ester group derived from the organic radical of said alcohol based on the total moles of end groups in the polyester.