Melt process for preparing copolyesters using triarylphosphine catalysts

Claim 2

In a melt phase process for preparing a copolyester in the presence of a catalyst by reacting a first polyester with either a second polyester or polyester precursors, the improvement wherein said catalyst is a triarylphosphine having a boiling point in the range of from about 200° to about 500° C.

Claim 3

The process of claim 1 wherein said copolyester is prepared at a temperature in the range of from about 200° to about 300° C. and a pressure in the range of from about 0.001 to about 10 mmHg.

Claim 4

The process of claim 1 wherein each of said polyesters has a melting point less than about 500° C. at atmospheric pressure.

Claim 5

The process of claim 1 wherein said catalyst has the formula ##STR4## wherein each of R 1 , R 2 and R 3 is aryl.

Claim 6

The process of claim 1 wherein each of said polyesters has recurring units of the formula ##STR5## and said polyester precursors have the formulae ##STR6## wherein each of R 4 , R 5 , R 7 and R 10 is a divalent aliphatic, alicyclic or aromatic radical; each of R 6 and R 8 is hydroxy or alkoxy; and each of R 9 and R 11 is a monovalent aliphatic, alicyclic or aromatic radical.

Claim 7

The process of claim 5 wherein each of R 4 , R 5 , R 7 and R 10 is alkylene, cycloalkylene or arylene; each of R 6 and R 8 is hydroxy; and each of R 9 and R 11 is alkyl, cycloalkyl or aryl.

Claim 8

The process of claim 1 comprising the steps of crystallizing and solid phase polymerizing said copolyester.

Claim 9

In a melt phase process for preparing a copolyester in the presence of a catalyst by reacting a first polyester with either a second polyester or polyester precursors, each of said polyesters having recurring units of the formula ##STR7## and said polyester precursors having the formulae ##STR8## wherein each of R 4 , R 5 , R 7 and R 10 is a divalent aliphatic, alicyclic or aromatic radical, each of R 6 and R 8 is hydroxy or alkoxy; and each of R 9 and R 11 is a monovalent aliphatic, alicyclic or aromatic radical the improvement wherein said catalyst is a triarylphosphine having a boiling point in the range of from about 200° to about 500° C.

Claim 10

In a melt phase process for preparing a copolyester in the presence of a catalyst by reacting a first polyester with either a second polyester or polyester precursors, each of said polyesters having recurring units of the formula ##STR7## and said polyester precursors having the formulae ##STR8## wherein each of R 4 , R 5 , R 7 and R 10 is a divalent aliphatic, alicyclic or aromatic radical, each of R 6 and R 8 is hydroxy or alkoxy; and each of R 9 and R 11 is a monovalent aliphatic, alicyclic or aromatic radical the improvement wherein said catalyst is a triarylphosphine having a boiling point in the range of from about 200° to about 500° C.

Claim 11

The process of claim 8 wherein said copolyester is prepared at a temperature in the range of from about 200° to about 300° C. and a pressure in the range of from about 0.001 to about 10 mmHg.

Claim 12

The process of claim 8 wherein said catalyst has the formula ##STR9## wherein each of R 1 , R 2 and R 3 is aryl of 6 to 12 carbon atoms.

Claim 13

The process of claim 8 wherein each of said polyesters has a melting point less than about 500° C. at atmospheric pressure.

Claim 14

The process of claim 8 wherein said catalyst is present in a concentration in the range of from about 0.1 to about 50 percent, by weight, based on total polyester and polyester precursor.

Claim 15

The process of claim 8 wherein each of R 4 , R 5 , R 7 and R 10 is alkylene, cycloalkylene or arylene; each of R 6 and R 8 is hydroxy; and each of R 9 and R 11 is alkyl, cycloalkyl or aryl.

Claim 16

The process of claim 8 wherein said copolyester is prepared by reacting two or more polyesters.

Claim 17

The process of claim 8 comprising the steps of crystallizing and solid phase polymerizing said copolyester.

Claim 18

In a process for preparing a copolyester, said process comprising: (A) mixing: (1) a first polyester having recurring units of the formula ##STR10## wherein each of R 4 and R 5 is alkylene, cycloalkylene or arylene; and (2) either a second polyester or at least one polyester precursor described by each of the formulae ##STR11## wherein each of R 7 and R 10 is alkylene, cycloalkylene or arylene, and each of R 9 and R 11 is alkyl, cycloalkyl or aryl; (B) reacting (1) and (2) in a melt phase in the presence of a catalyst; and (C) removing non-polymeric by-products of said reaction whereby reaction equilibrium is driven in the direction of copolyester formation, the improvement wherein said catalyst is a ##STR12## wherein each of R 1 , R 2 and R 3 is aryl of 6 to 12 carbon atoms.

Claim 19

In a process for preparing a copolyester, said process comprising: (A) mixing: (1) a first polyester having recurring units of the formula ##STR10## wherein each of R 4 and R 5 is alkylene, cycloalkylene or arylene; and (2) either a second polyester or at least one polyester precursor described by each of the formulae ##STR11## wherein each of R 7 and R 10 is alkylene, cycloalkylene or arylene, and each of R 9 and R 11 is alkyl, cycloalkyl or aryl; (B) reacting (1) and (2) in a melt phase in the presence of a catalyst; and (C) removing non-polymeric by-products of said reaction whereby reaction equilibrium is driven in the direction of copolyester formation, the improvement wherein said catalyst is a ##STR12## wherein each of R 1 , R 2 and R 3 is aryl of 6 to 12 carbon atoms.

Claim 20

The process of claim 16 wherein said catalyst is present in a concentration in the range of from about 0.1 to about 10 percent, by weight, based on total polyester and polyester precursor.

Claim 21

The process of claim 16 comprising the steps of crystallizing and solid phase polymerizing said copolyester.

Claim 22

The process of claim 16 wherein said catalyst is triphenylphosphine.