Polyester molding composition, process for its preparation and its use

Claim 2

A polyester molding composition, comprising substantially (A) a polyester of a reduced specific viscosity (measured at 25° C. in a 1% solution in dichloroacetic acid) of at least 0.3 dl/g, (B) a nucleating agent in the form of an alkali metal compound (C) a low-molecular organic compound as a crystallization accelerator in the presence or absence of (D) reinforcing agents or other additives, wherein (C) is an organic imide compound which comprises one or more aromatic nuclei and is of the formula ##STR4## in which A 1 is a substituted or unsubstituted divalent aromatic radical, R 1 is a branched or unbranched, unsubstituted or substituted aliphatic radical of valency a, having at least 5 carbon atoms and containing at least one --C(═O)--NH-- group, and a is 1 or 2, which component (C) has a melting point below 200° C. and is present in a quantity sufficient to reduce the crystallization temperature of the molding composition by at least 4° C. as compared with that without (C).

Claim 3

A composition as claimed in claim 1, wherein the organic imide compound (C) has a melting point below 150° C., the substituent on the imide nitrogen is an aliphatic carboxylic acid amide containing chain having 8 to 20 carbon atoms and is present in a quantity of 1 to 8% by weight, relative to the mixture of (A) to (C).

Claim 4

A composition as claimed in claim 1, wherein the groupings with heteroatoms in the radical R 1 are carboxylic acid amide groups having at least 8 carbon atoms.

Claim 5

A composition as claimed in claim 1, wherein the polyester (A) is polyethylene terephthalate or a mixture of polyethylene terephthalate and polybutylene terephthalate.

Claim 6

A composition as claimed in claim 1, wherein the alkali metal compound is a sodium salt of a monocarboxylic or polycarboxylic acid or a sodium alcoholate.

Claim 7

A composition as claimed in claim 1, wherein the melting point of (C) is below 100° C.

Claim 8

A composition as claimed in claim 1, wherein component (C) comprises a compound of the formula ##STR5## wherein m+x is greater than 5.

Claim 9

Moldings prepared from the molding composition as claimed in claim 1.

Claim 10

A process for preparing a polyester molding composition, comprising substantially (A) a polyester of a reduced specific viscosity (measured at 25° C. in a 1% solution in dichloroacetic acid) of at least 0.3 dl/g, (B) a nucleating agent in the form of an alkali metal compound, (C) a low-molecular organic compound as a crystallization accelerator in the presence or absence of (D) reinforcing agents and other additives, the polyester (A) being prepared first and components (B) and in the case component (D) is present, this component also, as well as component (C) then being added, wherein the preparation of the polyester (A) is carried out by the esterification/polycondensation process, the transesterification/polycondensation process or both, at least a part of the polyester being prepared in the presence of an alkali metal or an alkali metal compound, so that, in a first stage, a nucleated or highly nucleated polyester results initially, and the crystallization accelerator (C) alone or together with further un-nucleated polyester, then being added to this polyester in a second stage, the quantity of the crystallization accelerator being such that the crystallization temperature is reduced by at least 4° C. as compared with that of the polyester without this organic crystallization accelerator, (C) being an organic imide compound which comprises one or more aromatic nuclei and is of the formula ##STR6## in which A 1 is a substituted or unsubstituted divalent aromatic radical, R 1 is a branched or unbranched unsubstituted or substituted aliphatic radical of valency a having at least 5 carbon atoms, and containing at least one --C(═O)--NH-- group, and a is 1 or 2, which component (C) has a melting point below 200° C.

Claim 11

A process for preparing a polyester molding composition, comprising substantially (A) a polyester of a reduced specific viscosity (measured at 25° C. in a 1% solution in dichloroacetic acid) of at least 0.3 dl/g, (B) a nucleating agent in the form of an alkali metal compound, (C) a low-molecular organic compound as a crystallization accelerator in the presence or absence of (D) reinforcing agents and other additives, the polyester (A) being prepared first and components (B) and in the case component (D) is present, this component also, as well as component (C) then being added, wherein the preparation of the polyester (A) is carried out by the esterification/polycondensation process, the transesterification/polycondensation process or both, at least a part of the polyester being prepared in the presence of an alkali metal or an alkali metal compound, so that, in a first stage, a nucleated or highly nucleated polyester results initially, and the crystallization accelerator (C) alone or together with further un-nucleated polyester, then being added to this polyester in a second stage, the quantity of the crystallization accelerator being such that the crystallization temperature is reduced by at least 4° C. as compared with that of the polyester without this organic crystallization accelerator, (C) being an organic imide compound which comprises one or more aromatic nuclei and is of the formula ##STR6## in which A 1 is a substituted or unsubstituted divalent aromatic radical, R 1 is a branched or unbranched unsubstituted or substituted aliphatic radical of valency a having at least 5 carbon atoms, and containing at least one --C(═O)--NH-- group, and a is 1 or 2, which component (C) has a melting point below 200° C.

Claim 12

The process as claimed in claim 9, wherein the quantity of alkali metal or alkali metal compound in the first stage is 2×10 -2 to 1 mol per kg of the highly nucleated polyester, and wherein un-nucleated polyester of the same or a different chemical composition is added in the second stage.

Claim 13

The process as claimed in claim 9, wherein the quantity of the un-nucleated polyester added in the second stage is such that the quantity of alkali metal in the polyester (A) is 2×10 -3 to 0.1 mol per kg of this polyester.

Claim 14

The process as claimed in claim 9, wherein the transesterification/polycondensation process is used for preparing the polyester according to the first process stage.

Claim 15

A process as claimed in claim 9, wherein the organic imide compound (C) has a melting point below 150° C., the substituent on the imide nitrogen is an aliphatic carboxylic acid amide containing chain having 8 to 20 carbon atoms and is present in a quantity of 1 to 8% by weight, relative to the mixture of (A) to (C).

Claim 16

A process as claimed in claim 9, wherein the groupings with heteroatoms in the radical R 1 are carboxylic acid amide groups having at least 8 carbon atoms.

Claim 17

A process as claimed in claim 9, wherein the polyester (A) is polyethylene terephthalate or a mixture of polyethylene terephthalate and polybutylene terephthalate.

Claim 18

A process as claimed in claim 9, wherein the alkali metal compound is a sodium salt of a monocarboxylic or polycarboxylic acid or a sodium alcoholate.

Claim 19

A process as claimed in claim 9, wherein component (C) has a melting point below 100° C.