IP Library Granted Patent US 10,079,378
Granted Patent B2
US 10,079,378 · App. 15/312,558 · Granted Sep 18, 2018

Polyolefin microporous membrane and production method thereof

Inventors: Tomiko Matsumoto (Tochigi, JP); Masami Sugata (Tochigi, JP); Koichi Kono (Tochigi, JP)
Assignee: TORAY INDUSTRIES, INC.
H01M2/1653B01D67/002B01D67/0027B01D69/02B01D71/26B29C47/0021B29C47/0057B29C47/16B29C47/40B29C47/6087B29C47/8845B29C55/005B29C55/143C08J5/18C08J9/28C08L23/06H01M2/145B01D2325/20B01D2325/22B01D2325/24B01D2325/34B29K2023/0683B29K2105/041B29K2995/0065B29L2031/3468C08J2201/0482C08J2205/044C08J2323/06C08J2423/06C08L2207/068
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Quick Facts
Patent No.
US 10,079,378
App. No.
15/312,558
Granted
Sep 18, 2018
Kind
B2
Abstract

A polyolefin microporous membrane is disclosed. The membrane includes at least one microporous membrane layer, where the microporous membrane layer has an air permeability between about 100 sec/100 cc and about 220 sec/100 cc, a pin puncture strength of at least 550 gf, and a crystallization half time t 1/2 of from 10 to 35 minutes when subjected to isothermal crystallization at 117° C. The air permeability and the pin puncture strength are normalized to a thickness of 16 μm.

Claims (24)

1. A polyolefin microporous membrane, comprising:

at least one microporous membrane layer,

wherein the microporous membrane layer has an air permeability between 100 sec/100 cc and 220 sec/100 cc, a pin puncture strength of at least 550 gf, and a crystallization half time t 1/2 of from 10 to 35 minutes when subjected to isothermal crystallization at 117° C., wherein the air permeability and the pin puncture strength are normalized to a thickness of 16 μm, and

wherein the microporous membrane layer comprises an ultra-high molecular weight polyethylene concentration of at least 30 wt. %, and wherein the ultra-high molecular weight polyethylene has an average molecular weight of at least 1.0×10 6 and less than 2.0×10 6 .

2. The polyolefin microporous membrane according to claim 1 , wherein a curl of a 18.5 mm×95 mm section of the microporous membrane layer is less than 2 mm.

3. The polyolefin microporous membrane according to claim 1 , wherein a thickness of the microporous membrane layer is between 5 μm and 30 μm.

4. The polyolefin microporous membrane according to claim 1 , wherein the microporous membrane layer has a shrinkage in a transverse direction at 105° C. which is less than 6%, and a shrinkage in a longitudinal direction at 105° C. which is between 1.1 and 2.0 times the shrinkage in the transverse direction.

5. A separator for a non-aqueous electrolyte secondary battery comprising a polyolefin microporous membrane comprising:

at least one microporous membrane layer,

wherein the microporous membrane layer has an air permeability between 100 sec/100 cc and 220 sec/100 cc, a pin puncture strength of at least 550 gf, and a crystallization half time t 1/2 of from 10 to 35 minutes when subjected to isothermal crystallization at 117° C., wherein the air permeability and the pin puncture strength are normalized to a thickness of 16 μm, and

wherein the microporous membrane layer comprises an ultra-high molecular weight polyethylene concentration of at least 30 wt. %, and wherein the ultra-high molecular weight polyethylene has an average molecular weight of at least 1.0×10 6 and less than 2.0×10 6 .

6. A non-aqueous electrolyte secondary battery comprising the separator according to claim 5 .

7. The separator according to claim 5 , wherein a curl of a 18.5 mm×95 mm section of the microporous membrane layer is less than 2 mm.

8. The separator according to claim 5 wherein a thickness of the microporous membrane layer is between 5 μm and 30 μm.

9. The separator according to claim 5 , wherein the microporous membrane layer has a shrinkage in a transverse direction at 105° C. which is less than 6%, and a shrinkage in a longitudinal direction at 105° C. which is between 1.1 and 2.0 times the shrinkage in the transverse direction.

10. A method of producing a polyolefin microporous membrane, the method comprising:

(a) preparing a polyolefin solution by melt-kneading:

(i) a polyolefin resin containing an ultra-high molecular weight polyethylene having a concentration of at least 30 wt. % and an average molecular weight of at least 1.0×10 6 and less than 2.0×10 6 , and

(ii) a membrane-forming solvent;

(b) molding a sheet by extruding the polyolefin solution from an extruder to form an extrudate and subsequently cooling the extrudate, wherein a crystallization half time t 1/2 of the gel-like sheet between 10 and 35 minutes when subjected to isothermal crystallization at 117° C.;

(c) stretching the sheet in a longitudinal direction;

(d) stretching the sheet in a transverse direction;

(e) extracting a membrane-forming solvent from the stretched sheet; and

(f) drying the stretched sheet.

Assignments (2)
MERGER AND CHANGE OF NAME Recorded Oct 10, 2017
From: TORAY BATTERY SEPARATOR FILM CO., LTD.; TORAY INDUSTRIES, INC.
To: TORAY INDUSTRIES, INC.
Reel/Frame 044821/0223 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 25, 2017
From: MATSUMOTO, TOMIKO; SUGATA, MASAMI; KONO, KOICHI
To: TORAY BATTERY SEPARATOR FILM CO., LTD.
Reel/Frame 041083/0568 →
Priority Claims (1)
JP 2014-110595 · May 28, 2014 · national
Continuity (1)
Related Publication 20170092920A1 · Mar 30, 2017