Microporous membrane and manufacturing method
View Patent ↗A microporous membrane having a structure in which its pore size distribution curve obtained by mercury intrusion porosimetry has at least two peaks, which is produced by extruding a combination of a diluent or solvent and a polyolefin resin composition comprising (a) from about 74 to about 99% of a first polyethylene resin having a weight average molecular weight of from about 2.5×10 5 to about 5×10 5 and a molecular weight distribution of from about 5 to about 100, (b) from about 1 to about 5% of a second polyethylene resin having a weight average molecular weight of from about 5×10 5 to about 1×10 6 and a molecular weight distribution of from about 5 to about 100, and (c) from 0 to about 25% of a polypropylene resin having a weight average molecular weight of from about 3×10 5 to about 1.5×10 6 , a molecular weight distribution of from about 1 to about 100, and a heat of fusion of 80 J/g or higher, percentages based on the mass of the polyolefin composition; cooling the extrudate to form a high polyolefin content cooled extrudate; stretching the cooled extrudate in at least one direction at a high stretching temperature to form a stretched sheet; removing at least a portion of the diluent or solvent from the stretched sheet to form a membrane; stretching the membrane to a high magnification in at least one direction to form a stretched membrane; and heat-setting the stretched membrane to form the microporous membrane.
1. A microporous membrane comprising (a) from about 74 to about 99% of a first polyethylene having a weight average molecular weight of from about 2.5×10 5 to about 5×10 5 and a molecular weight distribution of from about 5 to about 100, (b) from about 1 to about 5% of a second polyethylene having a weight average molecular weight of from about 5×10 5 to about 1×10 6 and a molecular weight distribution of from about 5 to about 100, and (c) from 0 to about 25% of a polypropylene having a weight average molecular weight of from about 3×10 5 to about 1.5×10 6 , a molecular weight distribution of from about 1 to about 100, and a heat of fusion of 80 J/g or higher, percentages based on the mass of the membrane, wherein the membrane 1) comprises pores characterized by a pore size distribution curve, wherein differential pore volume is plotted on a y axis and pore diameter on an x axis, having at least two peaks, and 2) contains dense domains corresponding to a main peak in a range of 0.01 μm to 0.08 μm in the pore size distribution curve and coarse domains corresponding to at least one sub-peak in a range of more than 0.08 μm and 1.5 μm or less in the pore size distribution curve.
2. The microporous membrane of claim 1 , wherein the pore volume ratio of the dense domains to the coarse domains ranges from 0.5 to 49.
3. The microporous membrane of claim 1 , wherein the microporous membrane has surface roughness of 3×10 2 nm or more when measured as a maximum height difference between two points on the membrane.
4. The microporous membrane of claims 1 , comprising (a) from about 75 to about 98% of a first polyethylene having a weight average molecular weight of from about 2.5×10 5 to about 4×10 5 and a molecular weight distribution of from about 7 to about 50, (b) from about 2 to about 5% of a second polyethylene having a weight average molecular weight of from about 5×10 5 to about 8×10 5 and a molecular weight distribution of from about 5 to about 50, and (c) from 0 to about 25% of a polypropylene having a weight average molecular weight of from about 6×10 5 to about 1.5×10 6 , a molecular weight distribution of from about 1.1 to about 50, and a heat of fusion of from 80 to about 200 J/g, percentages based on the mass of the membrane.
5. The microporous membrane of claim 1 , wherein
(a) the first polyethylene is one or more of ethylene homopolymer or ethylene/α-olefin copolymer having a weight average molecular weight of from about 2.5×10 5 to about 5×10 5 and a molecular weight distribution of from about 5 to about 100;
(b) the second polyethylene is one or more of ethylene homopolymer or ethylene/α-olefin copolymer having a weight average molecular weight of from about 5×10 5 to about 1×10 6 and a molecular weight distribution of from about 5 to about 100; and
(c) the polypropylene is one or more of propylene homopolymer or propylene/α-olefin copolymer having a weight average molecular weight of from about 3×10 4 to about 1.5×10 6 and a molecular weight distribution of from about 1 to about 100.
6. The microporous membrane of claim 1 , wherein the membrane further comprises a third polymer selected from one or more of polybutene-1, polypentene-1, poly-4-methylpentene-1, polyhexene-1, polyoctene-1, polyvinyl acetate, polymethyl methacrylate, polystyrene, and ethylene/α-olefin copolymer.
7. The microporous membrane of claim 1 , having an air permeability measured according to JIS P8117 ranging from about 20 to about 400 seconds/100 cm 3 , a porosity ranging from about 25 to about 80%, a pin puncture strength of about 2,000 mN or more at a membrane thickness of 20 μm, a tensile strength of about 49,000 kPa or more, a tensile elongation of 100% or more, a heat shrinkage ratio of 12% or less, a thickness variation ratio of 20% or less after heat compression, an air permeability of 700 sec/100 cm 3 or less after heat compression, and a surface roughness of 3×10 2 nm or more.
8. A battery separator comprising a microporous membrane comprising (a) from about 74 to about 99% of a first polyethylene having a weight average molecular weight of from about 2.5×10 5 to about 5×10 5 and a molecular weight distribution of from about 5 to about 100, (b) from about 1 to about 5% of a second polyethylene having a weight average molecular weight of from about 5×10 5 to about 1×10 6 and a molecular weight distribution of from about 5 to about 100, and (c) from 0 to about 25% of a polypropylene having a weight average molecular weight of from about 3×10 5 to about 1.5×10 6 , a molecular weight distribution of from about 1 to 100, and a heat of fusion of 80 J/g or higher, percentages based on the mass of the membrane, wherein the membrane 1) comprises pores characterized by a pore size distribution curve, wherein differential pore volume is plotted on a y axis and pore diameter on an x axis, having at least two peaks, and 2) contains dense domains corresponding to a main peak in a range of 0.01 μm to 0.08 μm in the pore size distribution curve and coarse domains corresponding to at least one sub-peak in a range of more than 0.08 μm and 1.5 μm or less in the pore size distribution curve.
9. The battery separator of claim 8 , wherein the membrane contains dense domains corresponding to a main peak in a range of 0.01 to 0.08 μm in the pore size distribution curve and coarse domains corresponding to at least one sub-peak in a range of more than 0.08 μm and 1.5 μm or less in the pore size distribution curve.
10. The battery separator of claim 9 , wherein the pore volume ratio of the dense domains to the coarse domains ranges from 0.5 to 49.
11. The battery separator of claim 8 , wherein the microporous membrane has surface roughness of from about 3×10 2 nm to about 3×10 3 nm when measured as a maximum height difference between two points on the surface of the battery separator.
12. The battery separator of claim 8 , wherein the membrane comprises (a) from about 75 to about 98% of a first polyethylene having a weight average molecular weight of from about 2.5×10 5 to about 4×10 5 and a molecular weight distribution of from about 7 to about 50, (b) from about 2 to about 5% of a second polyethylene having a weight average molecular weight of from about 5×10 5 to about 8×10 5 and a molecular weight distribution of from about 5 to about 50, and (c) from 0 to about 25% of a polypropylene having a weight average molecular weight of from about 6×10 5 to about 1.5×10 6 , a molecular weight distribution of from about 1.1 to about 50, and a heat of fusion of from 80 to about 200 J/g, percentages based on the mass of the membrane.
13. The microporous membrane of claim 1 , wherein pore size distribution used to determine the pore size distribution curve is determined by mercury intrusion porosimetry.
14. The battery separator of claim 8 , wherein pore size distribution used to determine the pore size distribution curve is determined by mercury intrusion porosimetry.