Microporous polyolefin film, separator for battery, and production processes therefor
A microporous membrane and polyolefin technology, which is applied in battery pack parts, chemical instruments and methods, membranes, etc., can solve problems such as membrane rupture, and achieve the effect suitable for high capacity.
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[0085] (a) Preparation process of polyethylene resin solution
[0086] As the preparation process of the polyethylene resin solution, after adding a molding solvent to the polyethylene resin, melt kneading is carried out to prepare a polyolefin resin solution; as a melt kneading method, for example, Japanese Patent Publication No. 06-104736 and Japanese A method using a twin-screw extruder described in Japanese Patent No. 3347835. Since the melt-kneading method is known, description thereof will be omitted.
[0087] The molding solvent is not particularly limited as long as it can sufficiently dissolve polyethylene. For example, aliphatic or cyclic hydrocarbons such as nonane, decane, undecane, dodecane, and liquid paraffin, or mineral oil fractions having a boiling point corresponding to them, etc., are preferably non-volatile such as liquid paraffin. solvent.
[0088]The total amount of the polyethylene resin and the molding solvent is set to 100 parts by weight, and the ...
Embodiment 1
[0180] (Manufacture of polyolefin microporous membrane)
[0181] At a mass average molecular weight of 2.5×10 by 40% by mass 6 Ultra-high molecular weight polyethylene and 60% by mass with a mass average molecular weight of 2.8×10 5 In 100 parts by mass of a composition composed of high-density polyethylene, 0.375 parts by mass of tetrakis [methylene-3-(3,5-di-tert-butyl-4-hydroxyphenyl)-propionate] methane was dry mixed, Made into polyethylene composition. 30 parts by weight of the obtained polyethylene composition was charged into a twin-screw extruder. Furthermore, 70 parts by weight of liquid paraffin was supplied from the side feeder of the twin-screw extruder, and melted and kneaded to prepare a polyethylene resin solution in the extruder. Next, the polyethylene resin solution is extruded at 190°C from a die provided at the front end of the extruder, and is drawn out by a cooling roll that maintains the temperature of the internal cooling water at 25°C, while forming ...
Embodiment 2
[0185] Except having set the width to 150 mm, it carried out similarly to Example 1, and obtained the polyolefin microporous membrane B which is a base material for coating.
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