Method for reducing melt fracture during extrusion of a molten narrow molecular weight distribution, linear, ethylene copolymer

Claim 2

A process for reducing melt fracture formed during extrusion of a molten narrow molecular weight distribution, linear, ethylene polymer, under conditions of flow rate and melt temperature which would otherwise produce higher levels of melt fracture which comprises extruding said polymer through a die having a discharge outlet defining an exit die gap formed by opposing die lip surfaces and wherein one surface of the die lip and/or die land in contact with the molten polymer extends beyond the opposing surface of the die lip and/or die land in the direction of the axis of flow of the molten polymer through the die exit whereby melt fracture is reduced on the surface of the polymer leaving the extended die lip surface.

Claim 3

A process according to claim 1 wherein said extended die lip extends from about 0.010 inch to about 0.400 inch beyond said opposing die lip surface.

Claim 4

A process according to claim 1 wherein said extended die lip extends from about 0.50 inch to about 0.250 inch beyond said opposing die lip surface.

Claim 5

A process according to claim 1 or 2 wherein the distance between said die lips is between 0.015 inch to about 0.200 inch.

Claim 6

A process according to claim 1 or 2 wherein the distance between said die lips is between 0.020 inch to about 0.100 inch.

Claim 7

A process according to claims 1, or 2 wherein said non-extended die lip tapers away from the surface of said extended die lip.

Claim 8

A process according to claim 6 wherein said non-extended die lip tapers away from the surface of said extended die lip to provide a diverging surface defining a diverging angle of less than 5° relative to the axis of flow of the molten polymer.

Claim 9

A process as in claim 1 wherein the ethylene polymer is formed into blown film.

Claim 10

A process as in claim 1 wherein the ethylene polymer is slot cast into film.

Claim 11

A process as in claim 1 wherein the ethylene polymer is formed into pipe.

Claim 12

A process as in claim 1 wherein the ethylene polymer is a linear low density ethylene hydrocarbon copolymer.

Claim 13

A process as in claim 11 in which said copolymer is a copolymer of ethylene and at least one C 3 to C 8 alpha olefin having a melt index of about ≧0.1 to about ≦20.

Claim 14

A process as in claim 12 in which said copolymer is a copolymer of ≧90 mol percent ethylene and ≦10 mol percent of at least one C 3 to C 8 alpha olefin.

Claim 15

A process as in claim 13 in which said copolymer has a molecular weight distribution of about ≧2.7 to ≦6.0 and a total unsaturation content of about ≧0.1 to ≦0.3 C=C/1000 C atoms.

Claim 16

A process for reducing melt fracture formed during extrusion of a multilayer film wherein one layer is formed from polymers which are not subject to melt fracture under the conditions of extrusion and wherein the other layer is formed from a molten narrow molecular weight distribution, linear, ethylene polymer, under conditions of flow rate and melt temperature which would otherwise produce higher levels of melt fracture which comprises extruding said polymers not subject to melt fracture and said ethylene polymer through a die having a discharge outlet defining an exit die gap formed by opposing die lip surfaces and wherein one surface of the die lip and/or die land in contact with said ethylene polymer extends beyond the opposing surface of the die lip and/or die land in the direction of the axis of flow of said polymer through the die exit whereby melt fracture is reduced on the surface of said ethylene polymer film leaving the extended die lip surface.

Claim 17

A process for reducing melt fracture formed during extrusion of a multilayer film wherein one layer is formed from polymers which are not subject to melt fracture under the conditions of extrusion and wherein the other layer is formed from a molten narrow molecular weight distribution, linear, ethylene polymer, under conditions of flow rate and melt temperature which would otherwise produce higher levels of melt fracture which comprises extruding said polymers not subject to melt fracture and said ethylene polymer through a die having a discharge outlet defining an exit die gap formed by opposing die lip surfaces and wherein one surface of the die lip and/or die land in contact with said ethylene polymer extends beyond the opposing surface of the die lip and/or die land in the direction of the axis of flow of said polymer through the die exit whereby melt fracture is reduced on the surface of said ethylene polymer film leaving the extended die lip surface.