Process for extruding liquid crystal polymer

Claim 2

An improved process for extruding liquid crystal polymer to form shaped articles comprising the steps of: (a) providing a fluid stream of liquid crystal polymer wherein said stream has a flow pattern comprising substantial shear flow; (b) converting the flow of said fluid stream of liquid crystal polymer to a substantially elongational flow in the substantial absence of shear flow; and (c) extruding said fluid stream of liquid crystal polymer to form a shaped article having the polymer molecules oriented substantially parallel to the flow direction and exhibiting enhanced mechanical properties.

Claim 3

The process of claim 1 wherein said substantially elongational flow of step (b) has an elongation rate of at least approximately 1.0 second -1 .

Claim 4

The process of claim 2 wherein said substantially elongational flow of step (b) has an elongation rate of approximately 100 to 5,000 second -1 .

Claim 5

The process of claim 1 wherein the flow of said fluid stream of liquid crystal polymer is converted to said substantially elongational flow by converging and drawing said fluid stream of liquid crystal polymer.

Claim 6

The process of claim 4 wherein the flow of said fluid stream of liquid crystal polymer is converted to said substantially elongational flow by passing said fluid stream of liquid crystal polymer through at least one grid having a plurality of converging passages.

Claim 7

The process of claim 5 wherein the flow of said fluid stream of liquid crystal polymer is converted to said substantially elongational flow by passing said fluid stream of liquid crystal polymer through a plurality of grids disposed in series in the flowpath of said fluid stream of liquid crystal polymer, said grids having a plurality of converging passages.

Claim 8

The process of claims 5 or 6 wherein said converging passages have an exit diameter of approximately 20 to 1,000 microns.

Claim 9

The process of claim 7 wherein said converging passages have an exit diameter of approximately 75 to 150 microns.

Claim 10

The process of claim 8 wherein said converging passages have an exit diameter of approximately 100 microns.

Claim 11

The process of claims 5 or 6 wherein said converging passages are cone-shaped holes.

Claim 12

The process of claims 5 or 6 wherein said converging passages are trumpet-shaped holes.

Claim 13

The process of claim 1 wherein said fluid stream of liquid crystal polymer comprises a molten stream of melt processable polymer exhibiting an anisotropic melt phase.

Claim 14

The process of claim 12 wherein said melt processable polymer is selected from the group consisting of wholly aromatic polyesters, aromatic-aliphatic polyesters, aromatic polyazomethines, and aromatic polyester-carbonates.

Claim 15

The process of claim 13 wherein said melt processable polymer comprises wholly aromatic polyester.

Claim 16

The process of claim 1 wherein said fluid stream of liquid crystal polymer comprises a lyotropic liquid crystal polymer in a compatible solvent.

Claim 17

The process of claim 15 wherein said lyotropic liquid crystal polymer comprises a polymer selected from the group consisting of wholly aromatic polyamides, aromatic-aliphatic polyamides, aromatic polyamide-hydrazides, polybenzobisoxazoles, and polybenzobisthiazoles.

Claim 18

The process of claim 1 wherein said fluid stream of liquid crystal polymer is extruded through a die to form a film.

Claim 19

The process of claim 1 wherein said fluid stream of liquid crystal polymer is extruded through a die to form an elongated three-dimensional article.

Claim 20

The process of claim 1 wherein said fluid stream of liquid crystal polymer is extruded through a spinneret to form a plurality of filaments.

Claim 21

The process of claim 1 wherein said fluid stream of liquid crystal polymer is extrusion molded to form a molded article.

Claim 22

An improved process for extruding liquid crystal polymer to form shaped articles comprising the steps of: (a) providing a fluid stream of liquid crystal polymer wherein said stream has a flow pattern comprising substantial shear flow; (b) converting the flow of said liquid crystal polymer to a substantially elongational flow in the substantial absence of shear flow by passing said fluid stream of liquid crystal polymer through at least one grid having a plurality of converging passages, wherein said converging passages have an exit diameter of approximately 20 to 1,000 microns and wherein said substantially elongational flow has an elongation rate of at least approximately 1.0 second -1 ; and (c) extruding said liquid crystal polymer to form a shaped article having the polymer molecules oriented substantially parallel to the flow direction and exhibiting enhanced mechanical properties.

Claim 23

An improved process for extruding liquid crystal polymer to form shaped articles comprising the steps of: (a) providing a fluid stream of liquid crystal polymer wherein said stream has a flow pattern comprising substantial shear flow; (b) converting the flow of said liquid crystal polymer to a substantially elongational flow in the substantial absence of shear flow by passing said fluid stream of liquid crystal polymer through at least one grid having a plurality of converging passages, wherein said converging passages have an exit diameter of approximately 20 to 1,000 microns and wherein said substantially elongational flow has an elongation rate of at least approximately 1.0 second -1 ; and (c) extruding said liquid crystal polymer to form a shaped article having the polymer molecules oriented substantially parallel to the flow direction and exhibiting enhanced mechanical properties.

Claim 24

The process of claim 21 wherein said substantially elongational flow of step (b) has an elongation rate of approximately 100 to 5,000 second -1 .

Claim 25

The process of claim 21 wherein the flow of said fluid stream of liquid crystal polymer is converted to said substantially elongational flow by passing said fluid stream of liquid crystal polymer through a plurality of grids disposed in series in the flowpath of said fluid stream of liquid crystal polymer, said grids having a plurality of converging passages.

Claim 26

The process of claims 21 or 23 wherein said converging passages have an exit diameter of approximately 75 to 150 microns.

Claim 27

The process of claim 24 wherein said converging passages have an exit diameter of approximately 100 microns.

Claim 28

The process of claims 21 or 23 wherein said converging passages are cone-shaped holes.

Claim 29

The process of claims 21 or 23 wherein said converging passages are trumpet-shaped holes.

Claim 30

The process of claim 21 wherein said fluid stream of liquid crystal polymer comprises a molten stream of melt processable polymer exhibiting an anisotropic melt phase.

Claim 31

The process of claim 28 wherein said melt processable polymer is selected from the group consisting of wholly aromatic polyesters, aromatic-aliphatic polyesters, aromatic polyazomethines, and aromatic polyester-carbonates.

Claim 32

The process of claim 29 wherein said melt processable polymer comprises wholly aromatic polyester.

Claim 33

The process of claim 30 wherein said polyester comprises a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 350° C. consisting essentially of the recurring moieties I and II wherein: ##STR4## wherein said polyester comprises approximately 10 to 90 mole percent of moiety I, and approximately 10 to 90 mole percent of moiety II.

Claim 34

The process of claim 30 wherein said polyester comprises a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 325° C. consisting essentially of the recurring moieties I, II, and III wherein: ##STR5## wherein said polyester comprises approximately 30 to 70 mole percent of moiety I.

Claim 35

The process of claim 30 wherein said polyester comprises a melt processable polyester capable of forming an anisotropic melt phase at a temperature no higher than approximately 320° C. consisting essentially of the recurring moieties I, II, III, and IV wherein: ##STR6## R is methyl, chloro, bromo, or mixtures thereof, and is substituted for a hydrogen atom present upon the aromatic ring, and wherein said polyester comprises approximately 20 to 60 mole percent of moiety I, approximately 5 to 18 mole percent of moiety II, approximately 5 to 35 mole percent of moiety III, and approximately 20 to 40 mole percent of moiety IV.

Claim 36

The process of claim 21 wherein said fluid stream of liquid crystal polymer comprises a lyotropic liquid crystal polymer in a compatible solvent.

Claim 37

The process of claim 34 wherein said lyotropic liquid crystal polymer comprises a polymer selected from the group consisting of wholly aromatic polyamides, aromatic-aliphatic polyamides, aromatic polyamide-hydrazides, polybenzobisoxazoles, and polybenzobisthiazoles.

Claim 38

The process of claim 21 wherein said fluid stream of liquid crystal polymer is extruded through a die to form a film.

Claim 39

The process of claim 21 wherein said fluid stream of liquid crystal polymer is extruded through a die to form an elongated three-dimensional article.

Claim 40

The process of claim 21 wherein said fluid stream of liquid crystal polymer is extruded through a spinneret to form a plurality of filaments.

Claim 41

The process of claim 21 wherein said fluid stream of liquid crystal polymer is extrusion molded to form a molded article.

Claim 42

An improved process for extruding melt processable wholly aromatic polyester to form shaped articles, said polyester comprising a melt processable wholly aromatic polyester selected from the group consisting of: (i) a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 350° C. consisting essentially of the recurring moieties I and II wherein: ##STR7## wherein said polyester comprises approximately 10 to 90 mole percent of moiety I, and approximately 10 to 90 mole percent of moiety II, (ii) a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 325° C. consisting essentially of the recurring moieties I, II, and III wherein: ##STR8## wherein said polyester comprises approximately 30 to 70 mole percent of moiety I, and (iii) a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature no higher than approximately 320° C. consisting essentially of the recurring moieties I, II, III, and IV wherein: ##STR9## R is methyl, chloro, bromo, or mixtures thereof, and is substituted for a hydrogen atom present upon the aromatic ring, and wherein said polyester comprises approximately 20 to 60 mole percent of moiety I, approximately 5 to 18 mole percent of moiety II, approximately 5 to 35 mole percent of moiety III, and approximately 20 to 40 mole percent of moiety IV, said process comprising the steps of: (a) providing a fluid stream of said wholly aromatic polyester wherein said stream has a flow pattern comprising substantial shear flow; (b) converting the flow of said wholly aromatic polyester to a substantially elongational flow in the substantial absence of shear flow by passing said fluid stream of said wholly aromatic polyester through at least one grid having a plurality of converging passages, wherein said converging passages have an exit diameter of approximately 20 to 1,000 microns and wherein said substantially elongational flow has an elongation rate of at least approximately 1.0 second -1 ; and (c) extruding said wholly aromatic polyester to form a shaped article having the polymer molecules oriented substantially parallel to the flow direction and exhibiting enhanced mechanical properties.

Claim 43

An improved process for extruding melt processable wholly aromatic polyester to form shaped articles, said polyester comprising a melt processable wholly aromatic polyester selected from the group consisting of: (i) a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 350° C. consisting essentially of the recurring moieties I and II wherein: ##STR7## wherein said polyester comprises approximately 10 to 90 mole percent of moiety I, and approximately 10 to 90 mole percent of moiety II, (ii) a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 325° C. consisting essentially of the recurring moieties I, II, and III wherein: ##STR8## wherein said polyester comprises approximately 30 to 70 mole percent of moiety I, and (iii) a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature no higher than approximately 320° C. consisting essentially of the recurring moieties I, II, III, and IV wherein: ##STR9## R is methyl, chloro, bromo, or mixtures thereof, and is substituted for a hydrogen atom present upon the aromatic ring, and wherein said polyester comprises approximately 20 to 60 mole percent of moiety I, approximately 5 to 18 mole percent of moiety II, approximately 5 to 35 mole percent of moiety III, and approximately 20 to 40 mole percent of moiety IV, said process comprising the steps of: (a) providing a fluid stream of said wholly aromatic polyester wherein said stream has a flow pattern comprising substantial shear flow; (b) converting the flow of said wholly aromatic polyester to a substantially elongational flow in the substantial absence of shear flow by passing said fluid stream of said wholly aromatic polyester through at least one grid having a plurality of converging passages, wherein said converging passages have an exit diameter of approximately 20 to 1,000 microns and wherein said substantially elongational flow has an elongation rate of at least approximately 1.0 second -1 ; and (c) extruding said wholly aromatic polyester to form a shaped article having the polymer molecules oriented substantially parallel to the flow direction and exhibiting enhanced mechanical properties.

Claim 44

The process of claim 40 wherein said substantially elongational flow of step (b) has an elongation rate of approximately 100 to 5,000 second -1 .

Claim 45

The process of claim 40 wherein said converging passages have an exit diameter of approximately 75 to 150 microns.

Claim 46

The process of claim 42 wherein said converging passages have an exit diameter of approximately 100 microns.

Claim 47

The process of claim 40 wherein said converging passages are cone-shaped holes.

Claim 48

The process of claim 40 wherein said converging passages are trumpet-shaped holes.

Claim 49

In a process for extruding liquid crystal polymer to form shaped articles wherein a fluid stream of said liquid crystal polymer having a flow pattern comprising substantial shear flow is provided, the improvement comprising: (a) converting the flow of said liquid crystal polymer to a substantially elongational flow in the substantial absence of shear flow by passing said fluid stream of said liquid crystal polymer through at least one grid having a plurality of converging holes having an exit diameter of a size sufficient to convert the flow of said liquid crystal polymer to said substantially elongational flow, and (b) extruding said fluid stream of liquid crystal polymer to form a shaped article exhibiting enhanced mechanical properties wherein the polymer molecules are oriented substantially parallel to the flow direction.

Claim 50

In a process for extruding liquid crystal polymer to form shaped articles wherein a fluid stream of said liquid crystal polymer having a flow pattern comprising substantial shear flow is provided, the improvement comprising: (a) converting the flow of said liquid crystal polymer to a substantially elongational flow in the substantial absence of shear flow by passing said fluid stream of said liquid crystal polymer through at least one grid having a plurality of converging holes having an exit diameter of a size sufficient to convert the flow of said liquid crystal polymer to said substantially elongational flow, and (b) extruding said fluid stream of liquid crystal polymer to form a shaped article exhibiting enhanced mechanical properties wherein the polymer molecules are oriented substantially parallel to the flow direction.

Claim 51

The process of claim 46 wherein said substantially elongational flow has an elongation rate of at least approximately 1.0 second -1 .

Claim 52

The process of claim 46 wherein the flow of said fluid stream of liquid crystal polymer is converted to said substantially elongational flow by passing said fluid stream of liquid crystal polymer through a plurality of grids disposed in series in the flowpath of said fluid stream of liquid crystal polymer, said grids having a plurality of converging passages.

Claim 53

The process of claims 46 or 48 wherein said converging passages have an exit diameter of approximately 100 microns.

Claim 54

The process of claims 46 or 48 wherein said converging passages are cone-shaped holes.

Claim 55

The process of claims 46 or 48 wherein said converging passages are trumpet-shaped holes.

Claim 56

The process of claim 46 wherein said fluid stream of liquid crystal polymer comprises a molten stream of melt processable polymer exhibiting an anisotropic melt phase.

Claim 57

The process of claim 52 wherein said melt processable polymer is selected from the group consisting of wholly aromatic polyesters, aromatic-aliphatic polyesters, aromatic polyazomethines, and aromatic polyester-carbonates.

Claim 58

The process of claim 53 wherein said melt processable polymer comprises wholly aromatic polyester.

Claim 59

The process of claim 54 wherein said polyester comprises a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 350° C. consisting essentially of the recurring moieties I and II wherein: ##STR10## wherein said polyester comprises approximately 10 to 90 mole percent of moiety I, and approximately 10 to 90 mole percent of moiety II.

Claim 60

The process of claim 54 wherein said polyester comprises a melt processable wholly aromatic polyester capable of forming an anisotropic melt phase at a temperature below approximately 325° C. consisting essentially of the recurring moieties I, II, and III wherein: ##STR11## wherein said polyester comprises approximately 30 to 70 mole percent of moiety I.

Claim 61

The process of claim 54 wherein said polyester comprises a melt processable polyester capable of forming an anisotropic melt phase at a temperature no higher than approximately 320° C. consisting essentially of the recurring moieties I, II, III, and IV wherein: ##STR12## R is methyl, chloro, bromo, or mixtures thereof, and is substituted for a hydrogen atom present upon the aromatic ring, and wherein said polyester comprises approximately 20 to 60 mole percent of moiety I, approximately 5 to 18 mole percent of moiety II, approximately 5 to 35 mole percent of moiety III, and approximately 20 to 40 mole percent of moiety IV.

Claim 62

The process of claim 46 wherein said fluid stream of liquid crystal polymer comprises a lyotropic liquid crystal polymer in a compatible solvent.

Claim 63

The process of claim 58 wherein said lyotropic liquid crystal polymer comprises a polymer selected from the group consisting of wholly aromatic polyamides, aromatic-aliphatic polyamides, aromatic polyamide-hydrazides, polybenzobisoxazoles, and polybenzobisthiazoles.

Claim 64

The process of claim 46 wherein said fluid stream of liquid crystal polymer is extruded through a die to form a film.

Claim 65

The process of claim 46 wherein said fluid stream of liquid crystal polymer is extruded through a die to form an elongated three-dimensional article.

Claim 66

The process of claim 46 wherein said fluid stream of liquid crystal polymer is extruded through a spinneret to form a plurality of filaments.

Claim 67

The process of claim 46 wherein said fluid stream of liquid crystal polymer is extrusion molded to form a molded article.