JP2010202829A5 - - Google Patents

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JP2010202829A5
JP2010202829A5 JP2009052195A JP2009052195A JP2010202829A5 JP 2010202829 A5 JP2010202829 A5 JP 2010202829A5 JP 2009052195 A JP2009052195 A JP 2009052195A JP 2009052195 A JP2009052195 A JP 2009052195A JP 2010202829 A5 JP2010202829 A5 JP 2010202829A5
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mass
parts
dop
mpa
stretched
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JP2009052195A
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Japanese (ja)
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JP2010202829A (en
JP5545928B2 (en
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[実施例1]
粘度平均分子量(Mv)25万の高密度ポリエチレン「SH800」(旭化成ケミカルズ(株)製、融点135.5℃)12.8質量部、Mv100万の超高分子量ポリエチレン「UH650」(旭化成ケミカルズ(株)製、融点136.6℃)19.2質量部、平均一次粒径が15nmであるシリカ「LP」((株)東ソー・シリカ製)20質量部、酸化防止剤0.3質量部、可塑剤としてフタル酸ジヘキシル(DOP)48質量部をヘンシェルミキサーで混合して造粒した。その後、T−ダイを装着した二軸押出機にて200℃で混練・押出し、厚さ100μmのシート状に成形した。該成形物から塩化メチレンにてDOPを抽出除去し微多孔膜とした。該微多孔膜を2枚重ねて130℃に加熱のもとMDに5倍、ロールにて延伸した後、最大温度140℃に加熱のもとTDに1.7倍、テンターにて延伸した。
得られた膜はMDの引張強度29MPa、TDの引張強度5MPa、平均孔径0.20μm、最大孔径0.27μmであった。製膜条件およびその他の膜特性を表1に示す。
[Example 1]
High-density polyethylene “SH800” with a viscosity average molecular weight (Mv) of 250,000 (manufactured by Asahi Kasei Chemicals Corporation, melting point 135.5 ° C.) 12.8 parts by mass, ultra high molecular weight polyethylene “UH650” with an Mv of 1,000,000 (Asahi Kasei Chemicals Corporation) ), Melting point 136.6 ° C.) 19.2 parts by mass, silica “LP” having an average primary particle size of 15 nm (manufactured by Tosoh Silica) 20 parts by mass, antioxidant 0.3 parts by mass, plastic As an agent, 48 parts by mass of dihexyl phthalate (DOP) was mixed with a Henschel mixer and granulated. Then, it knead | mixed and extruded at 200 degreeC with the twin-screw extruder equipped with T-die, and shape | molded in the sheet form of thickness 100 micrometers. DOP was extracted and removed from the molded product with methylene chloride to form a microporous membrane. Two of the microporous membranes were stacked and heated to 130 ° C. and stretched by MD and 5 times in a roll, and then heated to a maximum temperature of 140 ° C. and 1.7 times in TD and stretched by a tenter.
The obtained membrane had an MD tensile strength of 29 MPa, a TD tensile strength of 5 MPa, an average pore diameter of 0.20 μm, and a maximum pore diameter of 0.27 μm. Table 1 shows the film forming conditions and other film characteristics.

JP2009052195A 2009-03-05 2009-03-05 Method for producing polyolefin microporous membrane Active JP5545928B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009052195A JP5545928B2 (en) 2009-03-05 2009-03-05 Method for producing polyolefin microporous membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009052195A JP5545928B2 (en) 2009-03-05 2009-03-05 Method for producing polyolefin microporous membrane

Publications (3)

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JP2010202829A JP2010202829A (en) 2010-09-16
JP2010202829A5 true JP2010202829A5 (en) 2012-03-15
JP5545928B2 JP5545928B2 (en) 2014-07-09

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JP2009052195A Active JP5545928B2 (en) 2009-03-05 2009-03-05 Method for producing polyolefin microporous membrane

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL2832542T3 (en) 2012-03-30 2021-04-06 Toray Industries, Inc. Multilayered microporous polyolefin film
JP6277225B2 (en) 2016-05-30 2018-02-07 旭化成株式会社 Storage device separator

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01223136A (en) * 1988-03-01 1989-09-06 Toray Ind Inc Production of microcellular polyolefin film
JP2001260217A (en) * 2000-03-22 2001-09-25 Nitto Denko Corp Producing method for porous film
JP4318484B2 (en) * 2003-05-16 2009-08-26 旭化成イーマテリアルズ株式会社 Method for producing polyolefin microporous membrane
JP5005387B2 (en) * 2007-03-01 2012-08-22 旭化成イーマテリアルズ株式会社 Method for producing polyolefin microporous membrane

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