US2010151334A1PendingUtilityA1
Microporous Polyolefin Membrane, Its Production Method, And Battery Separator
Est. expiryMay 15, 2026(expired)· nominal 20-yr term from priority
H01M 50/494H01M 50/491H01M 50/489H01M 50/417B01D 67/0025B01D 69/02B01D 2325/20B29K 2023/00B29C 55/005B01D 2325/22B01D 2325/24B29K 2105/041C08J 9/00B29K 2105/0061C08J 5/18B01D 67/0027B01D 71/262B01D 71/261C08J 2323/02B29K 2105/04Y10T428/249978Y10T428/249953B29C 67/20Y02E60/10
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Claims
Abstract
A microporous polyolefin membrane comprising a polyethylene resin, and polypropylene having a weight-average molecular weight of 6×10 5 or more and a heat of fusion of 90 J/g or more (measured by a differential scanning calorimeter), a fraction having a molecular weight of 1.8×10 6 or more being 10% or more by mass of the polypropylene.
Claims
exact text as granted — not AI-modified1 - 4 . (canceled)
5 . A microporous polyolefin membrane comprising at least one polyethylene, and at least one polypropylene having a weight-average molecular weight of 6×10 5 or more and a heat of fusion of 90 J/g or more, a fraction of said polypropylene having a molecular weight of 1.8×10 6 or more being 10% or more by mass of the polypropylene.
6 . A method for producing a microporous polyolefin membrane comprising the steps of
(1) extruding a molten blend of a polyethylene resin, polypropylene having a weight-average molecular weight of 6×10 5 or more and a heat of fusion of 90 J/g or more (measured by a differential scanning calorimeter), a fraction having a molecular weight of 1.8×10 6 or more being 10% or more by mass of said polypropylene, and a membrane-forming solvent from a die, (2) cooling the resultant extrudate to a gel-like sheet, and (3) conducting the stretching of said gel-like sheet and the removal of said membrane-forming solvent one or more times in an arbitrary order.
7 . The method for producing a microporous polyolefin membrane according to claim 2 , wherein said step (3) is removing said membrane-forming solvent after the stretching of said gel-like sheet, stretching said gel-like sheet after the removal of said membrane-forming solvent, or conducting the stretching of said gel-like sheet and the removal of said membrane-forming solvent in this order and further stretching said gel-like sheet.
8 . A battery separator formed by a microporous polyolefin membrane comprising at least one polyethylene, and at least one polypropylene having a weight-average molecular weight of 6×10 5 or more and a heat of fusion of 90 J/g or more, a fraction of said polypropylene having a molecular weight of 1.8×10 6 or more being 10% or more by mass of the polypropylene.
9 . The microporous polyolefin membrane of claim 1 , wherein said a polypropylene has a weight-average molecular weight of about 8×10 5 or more.
10 . The microporous polyolefin membrane of claim 1 , wherein said fraction of said polypropylene having a molecular weight of 1.8×10 6 or more is at least 15% or more by mass.
11 . The microporous polyolefin membrane of claim 1 , wherein said polypropylene has a heat of fusion of 95 J/g or more.
12 . The microporous polyolefin membrane of claim 1 , wherein said polypropylene comprises 20 to 80% by mass of the combined masses of the polyethylene and polypropylene.
13 . The microporous polyolefin membrane of claim 1 , wherein said at least one polyethylene resin is ultra-high-molecular-weight polyethylene, a polyethylene other than the ultra-high-molecular-weight polyethylene, or a mixture of ultra-high-molecular-weight polyethylene and polyethylene other than the ultra-high-molecular-weight polyethylene.
14 . The microporous polyolefin membrane of claim 9 , wherein said ultra-high-molecular-weight polyethylene preferably has a weight-average molecular weight of about 5×10 5 or more.
15 . The microporous polyolefin membrane of claim 10 , wherein said ultra-high-molecular-weight polyethylene has a weight-average molecular weight of about 1×10 6 to about 15×10 6 .
16 . The microporous polyolefin membrane of claim 11 , wherein said ultra-high-molecular-weight polyethylene has a weight-average molecular weight of about 1×10 6 to about 5×10 6 .
17 . The microporous polyolefin membrane of claim 9 , wherein said ultra-high-molecular-weight polyethylene comprises an ethylene homopolymer, or an ethylene.α-olefin copolymer containing an amount of an α-olefin other than ethylene.
18 . The microporous polyolefin membrane of claim 1 , wherein said at least one polyethylene resin has a weight-average molecular weight of 2×10 5 or more, and Mw/Mn of 5-300.
19 . The microporous polyolefin membrane of claim 9 , wherein said polyethylene composition comprises (a) polyethylene having a weight-average molecular weight of 5×10 5 or more, and (b) at least one selected from the group consisting of polyethylene having a weight-average molecular weight of 1×10 4 or more and less than 5×10 5 , polybutene-1 having a weight-average molecular weight of 1×10 4 to 4×10 6 , a polyethylene wax having a weight-average molecular weight of 1×10 3 to 1×10 4 , and an ethylene.α-olefin copolymer having a weight-average molecular weight of 1×10 4 to 4×10 6 .
20 . The microporous polyolefin membrane of claim 15 , wherein said polyethylene composition comprises polyethylene having a weight-average molecular weight of 5×10 5 or more, and polyethylene having a weight-average molecular weight of 1×10 4 or more and less than 5×10 5 .
21 . The microporous polyolefin membrane of claim 16 , wherein said polyethylene having a weight-average molecular weight of 1×10 4 or more and less than 5×10 5 is high-density polyethylene, medium-density polyethylene, branched low-density polyethylene, or linear low-density polyethylene.
22 . The microporous polyolefin membrane of claim 17 , wherein said polyethylene composition comprises polyethylene having a weight-average molecular weight of 5×10 5 or more, and high-density polyethylene having a weight-average molecular weight of 1×10 4 or more and less than 5×10 5 .
23 . The microporous polyolefin membrane of claim 1 , wherein the microporous polyolefin membrane has a porosity of 25-80%, an air permeability of 20-2,000 seconds/100 cc, a prick resistance of 2,000 mN/20 μm or more, and a meltdown temperature of 170° C. or more.
24 . The method of claim 1 , wherein the microporous polyolefin membrane has a porosity of 25-80%, an air permeability of 20-2,000 seconds/100 cc, a prick resistance of 2,000 mN/20 μm or more, and a meltdown temperature of 170 to 190° C.Join the waitlist — get patent alerts
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