Process for the production of thermoplastic compositions containing thermotropic oligomers and compositions produced by such process

Claim 2

A polymer blending process which comprises blending a polyamide of high molecular weight which has a fusion temperature at a first temperature, has a glass transition temperature and forms as isotropic liquid above the first temperature, an effective amount of an oligomer having a melting point at a second temperature, said second temperature being not more than 50° C. less than said first temperature, nor more than 70° C. more than said first temperature, said oligomer exhibiting thermotropic behavior between said second temperature and a third temperature, said third temperature being at least about 30° C. above said second temperature and at least about 10° C. above said first temperature, said oligomer having a length to diameter ratio (L/D) of at least about 10, a glass transition temperature at least abut 10° C. greater than the glass transition temperature of said polymer, and a Small's solubility parameter within about 7 of the Small's solubility parameter of said polymer in the melt and in the presence of a blending effective amount of an effective particulate material for a time sufficient to form a substantially homogeneous blend of said isotropic polymer and said thermotropic oligomer.

Claim 3

A process according to claim 1 wherein said particulate material is selected from the group consisting of finely divided inert inorganic material.

Claim 4

A process according to claim 2 wherein said material is talc or mica.

Claim 5

A process according to claim 1 wherein the amount of said material is from about 0.05 to about 10 weight percent based on the total weight of the blend.

Claim 6

A polymer blending process which comprises blending a isotropic polymer of high molecular weight which has a fusion temperature at a first temperature, has a glass transition temperature and forms an isotropic liquid above the first temperature, an effective amount of an oligomer having a melting point at a second temperature, said second temperature being not more than 50° C. less than said first temperature, nor more than 70° C. more than said first temperature, said oligomer exhibiting thermotropic behavior between said second temperature and a third temperature, said third temperature being at least about 30° C. above said second temperature and at least about 10° C. above said first temperature, said oligomer having a length to diameter ratio (L/D) of at least about 10, a glass transition temperature at least about 10° C. greater than the glass transition temperature of said polymer, and a Small's solubility parameter within about 7 of the Small's solubility parameter of said polymer in the melt and in the presence of a blending effective amount of an effective partculate material for a time sufficient to form a substantially homogeneous blend of said isotropic polymer and said thermotropic oligomer.

Claim 7

A polymer blending process which comprises blending a isotropic polymer of high molecular weight which has a fusion temperature at a first temperature, has a glass transition temperature and forms an isotropic liquid above the first temperature, an effective amount of an oligomer having a melting point at a second temperature, said second temperature being not more than 50° C. less than said first temperature, nor more than 70° C. more than said first temperature, said oligomer exhibiting thermotropic behavior between said second temperature and a third temperature, said third temperature being at least about 30° C. above said second temperature and at least about 10° C. above said first temperature, said oligomer having a length to diameter ratio (L/D) of at least about 10, a glass transition temperature at least about 10° C. greater than the glass transition temperature of said polymer, and a Small's solubility parameter within about 7 of the Small's solubility parameter of said polymer in the melt and in the presence of a blending effective amount of an effective partculate material for a time sufficient to form a substantially homogeneous blend of said isotropic polymer and said thermotropic oligomer.

Claim 8

A process according to claim 5 wherein said isotropic polymer is selected from the group consisting of polyesters and polyamides.

Claim 9

A process according to claim 6 wherein said polymer has residues of the formula: ##STR2## wherein w, x and y are each independently integers from 4 to 16 and wherein the moles of V equal the moles of VII.

Claim 10

A process according to claim 1 wherein said polyamide is selected from the group consisting of Nylon 6, Nylon 66, Nylon 12, Nylon 11 and Nylon 610.

Claim 11

A process according to claim 8 wherein said polyamide is Nylon 6.

Claim 12

A process according to claim 9 wherein said oligomer is a thermotropic polyamide.

Claim 13

A process according to claim 9 wherein said oligomer is a thermotropic polyester.

Claim 14

A process according to claim 9 wherein said oligomer is a thermotropic poly(ester amide).

Claim 15

A process according to claim 9 wherein said oligomer is a thermotropic poly(ether amide).

Claim 16

A process according to claim 6 wherein said isotropic polymer is a polyester.

Claim 17

A process according to claim 14 wherein said polyester is selected from the group consisting of poly(alkylene terephthalates), poly(cycloalkylene terephthalates), poly(alkylene isophthalates), and poly(cycloalkylene isophthalates.)

Claim 18

A process according to claim 15 wherein said polyester is poly(alkylene terephthalates) wherein the alkylene moiety is from about 2 to about 4 carbon atoms.

Claim 19

A process according to claim 16 wherein said polyester is poly(ethylene terephthalates).

Claim 20

A process according to claim 1 wherein said oligomer is a polyester having residues selected from: ##STR3## wherein R 1 , R, R' and R" are individually 1,4-phenylene; 2,5-naphthalene; 2,6-naphthalene; 1,4-cyclohexyl; 4,4'-biphenyl; or 2,6-anthracene-9,10-dione, either substituted or unsubstituted with one or more alkyl, aryl, fluoro, chloro, bromo, or alkoxy groups.

Claim 21

A process according to claim 18 wherein said residues are terephthaloyl or substituted terephthaloyl, substituted hydroquinone and an additional biphenol wherein R is 4,4'-biphenyl or hydroquinone, each unsubstituted or substituted by methyl, chloro or t-butyl.

Claim 22

A process according to claim 19, wherein said residues are terephthaloyl and substituted hydroquinone.

Claim 23

A process according to claim 20 wherein said residues are substituted terephthaloyl, substituted 4,4'-dihydroxybiphenyl and substituted hydroquinone.

Claim 24

A process according to claim 20 wherein said residues are terephthaloyl, 2,6-naphthalenedicarboxyl and substituted hydroquinone.

Claim 25

A process according to claim 20 wherein said substituted hydroquinone is methylhydroquinone.

Claim 26

A process according to claim 18 wherein said residues are terephthaloyl or 2,6-naphthalenedicarboxyl, p-hydroxybenzoate and substituted hydroquinone.

Claim 27

A process according to claim 1 wherein L/D ratio is between about 10/1 and about 75/1.

Claim 28

A process according to claim 25 wherein said L/D ratio is between about 15/1 and about 75/1.

Claim 29

A process according to claim 26 wherein said L/D ratio is between about 20/1 and about 50/1.

Claim 30

A process according to claim 1 wherein the Small's solubility parameter of said oligomer is within about 5 of the Small's solubility parameter of said polymer.

Claim 31

A process according to claim 28 wherein the Small's solubility parameter of said oligomer is within 4 of the Small's solubility parameter of said polymer.

Claim 32

A process according to claim 29 wherein the Small's solubility paratmeter of said oligomer is within about 2 of the Small's solubility parameter of said polymer.

Claim 33

A process according to claim 1 wherein the glass transition temperature of said oligomer is at least 20° C. greater than that of said polymer.

Claim 34

A process according to claim 5 wherein said particulate material is selected from group consisting of finely divided inert inorganic material.

Claim 35

A process according to claim 5 wherein said particulate material is talc or mica.

Claim 36

A process according to claim 33 wherein said particulate material is talc.

Claim 37

A process according to claim 5 wherein the amount of said material is from about 0.05 to about 10 weight percent based on the total weight of the blend.

Claim 38

A process according to claim 35 wherein said amount is from about 0.1 to bout 5 weight percent.

Claim 39

A process according to claim 36 wherein said amount is from about 0.1 to about 1 weight percent.

Claim 40

A process according to claim 37 wherein said amount is from about 0.15 to about 0.5 weight percent.

Claim 41

A process according to claim 5 wherein the average particle size of said material is not greater than about 7 microns.

Claim 42

A process according to claim 39 wherein said size is not greater than about 5 microns.

Claim 43

A process according to claim 40 wherein said size is not greater than 2 microns.

Claim 44

A process according to claim 41 wherein siad size is not greater than about 1.5 microns.

Claim 45

The process according to claim 1 wherein the amount of oligomer is at least about 2 percent by weight of the blend.

Claim 46

A process according to claim 43 wherein said amount is from about 2 to about 20 weight percent.

Claim 47

A process according to claim 44 wherein said amount is from about 4 to about 9 weight percent.

Claim 48

A polymer blend prepared in accordance with the process of claim 5.