Battery separator

Claim 2

A battery separator having at least two plies comprising a) at least one first ply in the form of a microporous sheet of a predetermined length and breadth and of less than 10 mils thickness and having pores of an average pore size of from about 0.005 to 50 microns in diameter occupying at least about 20 volume percent of said sheet, said sheet composed of a substantially unfilled first polymer composition; b) at least one second ply in the form of a microporous sheet of a predetermined length and breadth and of less than 10 mils thickness and having pores of an average pore size of from about 0.005 to 50 microns in diameter occupying at least about 20 volume percent of said sheet, said sheet composed of a substantially unfilled second polymer composition; each of said first and second ply being bonded together to provide a unitary sheet product capable of maintaining its length and breadth dimension and the viscosity of the first polymer composition and the second polymer composition are ultra-high and substantially the same at temperature of from ambient to about 70° C. while, at a transformation temperature of from about 80° C. to 150° C., said first polymer composition has a sufficient decrease in viscosity to exhibit flow to cause sheet (a) to be substantially non-porous while said second polymer composition maintains its ultra-high viscosity for at least 10° C. above the transformation temperature.

Claim 3

The product of claim 1 wherein the first polymer composition is composed of a copolymer selected from ethylene-butene or ethylene-hexene.

Claim 4

The product of claim 1 wherein the second polymer composition is composed of a polymer selected from polyethylene or polypropylene.

Claim 5

The product of claim 2 wherein the second polymer composition is composed of a polymer selected from polyethylene or polypropylene.

Claim 6

The product of claim 4 wherein the pore volume of each first ply and of each second ply is at least about 50 percent.

Claim 7

A process of forming a microporous multi-ply sheet product comprising a) forming a first polymer composition composed of an inert first polymer and a first extractable material which is miscible with the first polymer at processing temperatures; b) forming a second polymer composition composed of an inert second polymer and a second extractable material which is miscible with the second polymer at processing temperatures; said first and second extractable materials each, respectively, being a first polymer and second polymer miscible liquid at the conditions of forming initial sheet product under step (c) and being miscible in a common solvent; c) forming an initial sheet product having at least one ply composed of the first polymer composition and at least one ply composed of the second polymer composition; d) contacting the initial sheet product with the common solvent to substantially remove the first and second extractable materials therefrom; and e) recovering a final sheet product having at least two plies comprising 1) at least one first ply in the form of a microporous sheet of a predetermined length and breadth and of less than 10 mils thickness and having pores of an average pore size of from about 0.005 to 50 microns in diameter occupying at least about 20 volume percent of said sheet, said sheet composed of a substantially unfilled first polymer composition; 2) at least one second ply in the form of a microporous sheet of a predetermined length and breadth and of less than 10 mils thickness and having pores of an average pore size of from about 0.005 to 50 microns in diameter occupying at least about 20 volume percent of said sheet, said sheet composed of a substantially unfilled second polymer composition; each of said first and second ply being bonded together to provide a unitary sheet product capable of maintaining its length and breadth dimension and the viscosity of the first polymer composition and the second polymer composition are ultra-high and substantially the same at temperature of from ambient to about 70° C. while, at a transformation temperature of from about 80° C. to 150° C., said first polymer composition has a sufficient decrease in viscosity to exhibit flow to cause sheet (a) to be substantially non-porous while said second polymer composition maintains its ultra-high viscosity for at least 10° C. above the transformation temperature.

Claim 8

A process of forming a microporous multi-ply sheet product comprising a) forming a first polymer composition composed of an inert first polymer and a first extractable material which is miscible with the first polymer at processing temperatures; b) forming a second polymer composition composed of an inert second polymer and a second extractable material which is miscible with the second polymer at processing temperatures; said first and second extractable materials each, respectively, being a first polymer and second polymer miscible liquid at the conditions of forming initial sheet product under step (c) and being miscible in a common solvent; c) forming an initial sheet product having at least one ply composed of the first polymer composition and at least one ply composed of the second polymer composition; d) contacting the initial sheet product with the common solvent to substantially remove the first and second extractable materials therefrom; and e) recovering a final sheet product having at least two plies comprising 1) at least one first ply in the form of a microporous sheet of a predetermined length and breadth and of less than 10 mils thickness and having pores of an average pore size of from about 0.005 to 50 microns in diameter occupying at least about 20 volume percent of said sheet, said sheet composed of a substantially unfilled first polymer composition; 2) at least one second ply in the form of a microporous sheet of a predetermined length and breadth and of less than 10 mils thickness and having pores of an average pore size of from about 0.005 to 50 microns in diameter occupying at least about 20 volume percent of said sheet, said sheet composed of a substantially unfilled second polymer composition; each of said first and second ply being bonded together to provide a unitary sheet product capable of maintaining its length and breadth dimension and the viscosity of the first polymer composition and the second polymer composition are ultra-high and substantially the same at temperature of from ambient to about 70° C. while, at a transformation temperature of from about 80° C. to 150° C., said first polymer composition has a sufficient decrease in viscosity to exhibit flow to cause sheet (a) to be substantially non-porous while said second polymer composition maintains its ultra-high viscosity for at least 10° C. above the transformation temperature.

Claim 9

The process of claim 6 wherein the step c) is a coextrusion forming step.

Claim 10

The process of claim 7 wherein the extrusion forming step employs a multi-manifold internal combining die.

Claim 11

The process of claim 8 wherein the extrusion forming step is a blown film or cast film technique.

Claim 12

The process of claim 6 wherein the inert first polymer and inert second polymer are each selected from a polyolefin.

Claim 13

The process of claim 10 wherein the inert first polymer is selected from low density polyethylene, copolymers of ethylene/butene or copolymers of ethylene/hexene.

Claim 14

The process of claim 10 wherein the inert second polymer is selected from high density polyethylene, ultra-high molecular weight polyethylene or polypropylene.

Claim 15

The process of claim 11 wherein the inert second polymer is selected from high density polyethylene, ultra-high molecular weight polyethylene or polypropylene.

Claim 16

The process of claim 10 wherein the extractable material is selected from an aromatic dicarboxylic acid C 3 -C 5 alkyl ester or C 6 -C 9 alkanyl dicarboxylic acid C 3 -C 5 alkyl ester.

Claim 17

The process of claim 14 wherein the extractable material is selected from a C 3 -C 5 alkyl ester of sebacatic acid, a C 3 -C 5 alkyl ester of phthalic acid or a C 3 -C 5 alkyl ester of isophthalic acid.

Claim 18

The process of claim 6 wherein the initial sheet product is formed by a coextrusion process of blown film or cast film technique; the first inert polymer is selected from low density polyethylene, copolymers of ethylene/butene or copolymers of ethylene-hexene; the second inert polymer is selected from high density polyethylene, ultra-high molecular weight polyethylene, polypropylene; and the extractable material is selected from a C 3 -C 5 alkyl ester of phthalic acid, a C 3 -C 5 alkyl ester of isophthalic acid or a C 3 -C 5 alkyl ester of sebacatic acid.

Claim 19

The process of claim 16 wherein the recovery step (e) further includes stretching the sheet product to affix microporosity therein.

Claim 20

A sheet product formed according to the process of claim 6.

Claim 21

A sheet product formed according to the process of claim 7.

Claim 22

A sheet product formed according to the process of claim 10.

Claim 23

A sheet product formed according to the process of claim 13.

Claim 24

A sheet product formed according to the process of claim 14.

Claim 25

A sheet product formed according to the process of claim 15.

Claim 26

A sheet product formed according to the process of claim 16.

Claim 27

A sheet product formed according to the process of claim 17.