Process for producing aromatic polyesters having increased degrees of polymerization

Claim 2

A process for producing an aromatic polyester having an increased degree of polymerization which comprises reacting a hydroxyl-terminated, substantially linear, fiber-forming aromatic polyester having an aromatic dicarboxylic acid as a main acid component at an elevated temperature with a bis-cyclic imino ester compound of the formula ##STR19## wherein Y represents a divalent hydrocarbon group which may further contain a hetero atom, X represents a divalent hydrocarbon group which contains 1 or 2 carbon atoms as members of the above imino ester ring and is non-reactive under the reaction conditions, and l is 0 or 1, or of the following formula ##STR20## wherein A represents a grouping of the formula ##STR21## in which R 2 represents a monovalent hydrocarbon group, or a grouping of the formula ##STR22## in which R 2 is as defined above, R represents a tetravalent aromatic group which may further contain a hetero atom, and R 1 represents a monovalent aromatic hydrocarbon which is identical to or different from R 2 ; thereby bonding the molecular chains of the aromatic polyester to each other by the terminal hydroxyl groups thereof and forming rapidly said aromatic polyester having an increased degree of polymerization.

Claim 3

The process of claim 1 wherein said bis-cyclic imino ester compound is used in a proportion of 0.05 to 2 moles per equivalent of the terminal hydroxyl groups of said aromatic polyester.

Claim 4

The process of claim 2 wherein said bis-cyclic imino ester compound is used in a proportion of 0.1 to 1 mole per equivalent of the terminal hydroxyl groups of said aromatic polyester.

Claim 5

The process of claim 1 wherein in formula [I] representing said bis-cyclic imino ester compound, X is an aromatic hydrocarbon group which may be substituted by a substituent non-reactive under the reaction conditions.

Claim 6

The process of claim 4 wherein in formula [I] representing said bis-cyclic imino ester compound, l is 0, in which case the two imino ester rings are bonded to each other directly.

Claim 7

The process of claim 1 wherein said aromatic polyester contains terminal hydroxyl groups in a concentration of at least 50 equivalent % based on the entire terminal groups thereof.

Claim 8

The process of claim 1 wherein said reaction is carried out at atmospheric pressure or elevated pressures at a temperature at which said aromatic polyester is melted, or at a higher temperature.

Claim 9

The process of claim 7 wherein said reaction is carried out in a melt-molding machine.

Claim 10

The process of claim 8 wherein said aromatic polyester contains said bis-cyclic imino ester in the unreacted state.

Claim 11

The process of claim 8 wherein said reaction is carried out by mixing said aromatic polyester with another thermoplastic polymer containing said bis-cyclic imino ester compound in the unreacted state at a temperature above the melting point of said thermoplastic polymer and said aromatic polyester.

Claim 12

A process for producing an aromatic polyester having an increased degree of polymerization, which comprises reacting a substantially linear, fiber-forming aromatic polyester containing terminal carboxyl groups and having an aromatic dicarboxylic acid as a main acid component at an elevated temperature with a carboxyl content reducing agent capable of reacting with said terminal carboxyl groups to form terminal hydroxyl groups and a bis-cyclic imino ester of the formula ##STR23## wherein Y represents a divalent hydrocarbon group which may further contain a hetero atom, X represents a divalent hydrocarbon group which contains 1 or 2 carbon atoms as members of the above imino ester ring and is non-reactive under the reaction conditions, and l is 0 or 1, or of the following formula ##STR24## wherein A represents a grouping of the formula ##STR25## in which R 2 represents a monovalent hydrocarbon group, or a grouping of the formula ##STR26## in which R 2 is as defined above, R represents a tetravalent aromatic group which may further contain a hetero atom, and R 1 represents a monovalent aromatic hydrocarbon which is identical to or different from R 2 ; thereby converting the terminal carboxyl groups of said aromatic polyester to terminal hydroxyl groups by said carboxyl content reducing agent and bonding the molecular chains of the aromatic polyesters to each other by the terminal hydroxyl groups, and when low boiling volatile components are formed as by-products during the conversion of the carboxyl groups to the terminal hydroxyl groups, reacting at least said carboxyl content reducing agent and said aromatic polyester in the molten state, thereby forming said aromatic polyester having an increased degree of polymerization rapidly.

Claim 13

A process for producing an aromatic polyester having an increased degree of polymerization, which comprises reacting a substantially linear, fiber-forming aromatic polyester containing terminal carboxyl groups and having an aromatic dicarboxylic acid as a main acid component at an elevated temperature with a carboxyl content reducing agent capable of reacting with said terminal carboxyl groups to form terminal hydroxyl groups and a bis-cyclic imino ester of the formula ##STR23## wherein Y represents a divalent hydrocarbon group which may further contain a hetero atom, X represents a divalent hydrocarbon group which contains 1 or 2 carbon atoms as members of the above imino ester ring and is non-reactive under the reaction conditions, and l is 0 or 1, or of the following formula ##STR24## wherein A represents a grouping of the formula ##STR25## in which R 2 represents a monovalent hydrocarbon group, or a grouping of the formula ##STR26## in which R 2 is as defined above, R represents a tetravalent aromatic group which may further contain a hetero atom, and R 1 represents a monovalent aromatic hydrocarbon which is identical to or different from R 2 ; thereby converting the terminal carboxyl groups of said aromatic polyester to terminal hydroxyl groups by said carboxyl content reducing agent and bonding the molecular chains of the aromatic polyesters to each other by the terminal hydroxyl groups, and when low boiling volatile components are formed as by-products during the conversion of the carboxyl groups to the terminal hydroxyl groups, reacting at least said carboxyl content reducing agent and said aromatic polyester in the molten state, thereby forming said aromatic polyester having an increased degree of polymerization rapidly.

Claim 14

The process of claim 11 wherein said carboxyl content reducing agent is a monoepoxy compound.

Claim 15

The process of claim 11 wherein said carboxyl content reducing agent is an alkylene carbonate, a polyalkylene oxalate, a polyalkylene malonate, or a diglycol ester of oxalic or malonic acid.

Claim 16

The process of claim 11 wherein said aromatic polyester having terminal carboxyl groups is reacted with said carboxyl content reducing agent at an elevated temperature to convert them to terminal hydroxyl groups, and then said aromatic polyester having the terminal hydroxyl groups is reacted with said bis-cyclic imino ester.

Claim 17

A process for producing a molded article composed of an aromatic polyester having an increased intrinsic viscosity, which comprises mixing a hydroxylterminated, substantially linear aromatic polyester having an intrinsic viscosity, measured in o-chlorophenol at 35° C., of at least 0.3 and derived from terephthalic acid as a main acid component and ethylene glycol as a main glycol component, with 0.1 to 1 mole, per equivalent of the terminal hydroxyl groups of said aromatic polyester, of 2,2'-bis(3,1-benzoxazin-4-one) of the formula ##STR27## in a melt-molding machine at a temperature above the melting point of said aromatic polyester, thereby bonding the molecular chains of said aromatic polyester to each other by the terminal hydroxyl groups.

Claim 18

A process for producing a molded article composed of an aromatic polyester having an increased intrinsic viscosity, which comprises mixing a hydroxylterminated, substantially linear aromatic polyester having an intrinsic viscosity, measured in o-chlorophenol at 35° C., of at least 0.3 and derived from terephthalic acid as a main acid component and ethylene glycol as a main glycol component, with 0.1 to 1 mole, per equivalent of the terminal hydroxyl groups of said aromatic polyester, of 2,2'-bis(3,1-benzoxazin-4-one) of the formula ##STR27## in a melt-molding machine at a temperature above the melting point of said aromatic polyester, thereby bonding the molecular chains of said aromatic polyester to each other by the terminal hydroxyl groups.

Claim 19

The process of claim 15 wherein said aromatic polyester is polyethylene terephthalate.

Claim 20

A process for producing an aromatic polyester having an increased intrinsic viscosity, which comprises mixing a hydroxyl-terminated, substantially linear aromatic polyester having an intrinsic viscosity, measured in o-chlorophenol at 35° C. of at least 0.3 and derived from terephthalic acid as a main acid component and an alkylene glycol having 3 to 6 carbon atoms as a main glycol component, with 0.1 to 1 mole, per equivalent of the terminal hydroxyl groups of said aromatic polyester, of at least one member selected from the group consisting of 2,2'-bis(3,1-benzoxazin-4-one), 2,2'-p-phenylenebis[4,4-dimethyl-5(4H)-oxazolone], 2,2'-m-phenylenebis[4,4-dimethyl-5(4H)-oxazolone], 2,2'-p-phenylenebis[3,1-benzoxazin-4-one], 2,2'-p-phenylenebis[4-isobutyl5(4H)-oxazolone], 2,8-dimethyl-4H,6H-benzo(1,2-d:5,4-d')bis(3,1)oxazine-4,6-dione, 2,7-dimethyl-4H,6H-benzo(1,2-d:4,5-d')bis(1,3)oxazine-4,9-dione, and 6,6'-bis(2-methyl-4H,3,1-benzoxazin-4-one) in a melt-molding machine at a temperature above the melting point of said aromatic polyester, thereby bonding the molecular chains of said aromatic polyester to each other by the terminal hydroxyl groups.

Claim 21

A process for producing an aromatic polyester having an increased intrinsic viscosity, which comprises mixing a hydroxyl-terminated, substantially linear aromatic polyester having an intrinsic viscosity, measured in o-chlorophenol at 35° C. of at least 0.3 and derived from terephthalic acid as a main acid component and an alkylene glycol having 3 to 6 carbon atoms as a main glycol component, with 0.1 to 1 mole, per equivalent of the terminal hydroxyl groups of said aromatic polyester, of at least one member selected from the group consisting of 2,2'-bis(3,1-benzoxazin-4-one), 2,2'-p-phenylenebis[4,4-dimethyl-5(4H)-oxazolone], 2,2'-m-phenylenebis[4,4-dimethyl-5(4H)-oxazolone], 2,2'-p-phenylenebis[3,1-benzoxazin-4-one], 2,2'-p-phenylenebis[4-isobutyl5(4H)-oxazolone], 2,8-dimethyl-4H,6H-benzo(1,2-d:5,4-d')bis(3,1)oxazine-4,6-dione, 2,7-dimethyl-4H,6H-benzo(1,2-d:4,5-d')bis(1,3)oxazine-4,9-dione, and 6,6'-bis(2-methyl-4H,3,1-benzoxazin-4-one) in a melt-molding machine at a temperature above the melting point of said aromatic polyester, thereby bonding the molecular chains of said aromatic polyester to each other by the terminal hydroxyl groups.

Claim 22

The process of claim 15 wherein said aromatic polyester is polytetramethylene terephthalate.

Claim 23

An aromatic polyester of a high degree of polymerization produced by the process of claim 1.

Claim 24

A molded article composed of the aromatic polyester of claim 19.

Claim 25

A molded article prepared by the process of any one of claims 15 to 18.

Claim 26

The molded article of claim 20 which is in the form of fiber or film.

Claim 27

A molded article in the form of fiber or film prepared by the process of any one of claims 15 to 18.

Claim 28

An aromatic polyester of a high degree of polymerization produced by the process of claim 11.

Claim 29

A molded article composed of the aromatic polyester of claim 24.

Claim 30

The molded article of claim 25 which is in the form of fiber or film.