JPH02113039A - Porous film and production thereof - Google Patents

Porous film and production thereof

Info

Publication number
JPH02113039A
JPH02113039A JP26669988A JP26669988A JPH02113039A JP H02113039 A JPH02113039 A JP H02113039A JP 26669988 A JP26669988 A JP 26669988A JP 26669988 A JP26669988 A JP 26669988A JP H02113039 A JPH02113039 A JP H02113039A
Authority
JP
Japan
Prior art keywords
molecular weight
base material
porous
ultra
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP26669988A
Other languages
Japanese (ja)
Inventor
Yozo Nagai
陽三 長井
Kazuo Yamamoto
一夫 山本
Akio Yamaguchi
山口 章夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Denko Corp
Original Assignee
Nitto Denko Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nitto Denko Corp filed Critical Nitto Denko Corp
Priority to JP26669988A priority Critical patent/JPH02113039A/en
Publication of JPH02113039A publication Critical patent/JPH02113039A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a film of small pore size, having high mechanical strength and carrying a thin layer of ultra-high-molecular weight polyethylene thereon by impregnating a (non)woven fabric base with said ultra-high-molecular weight polyethylene. CONSTITUTION:The objective porous film with a thin layer of ultra-high- molecular weight polyethylene on its surface can be obtained by impregnating (A) a (non)woven fabric as base with (B) said ultra-high-molecular weight polyethylene >=500000 in viscosity-average molecular weight. Specifically, the process is as follows: ultra-high-molecular weight polyethylene >=500000 in viscosity- average molecular weight is dissolved in a good solvent and the resultant solution is made to contact with a (non)woven fabric as the base for the objective film to effect impregnation of the solution into the base and, at the same time, form a thin layer from said solution on the base surface followed by immersing the resulting product in a poor solvent and then removing the good solvent.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は基材としての織布ま九は不織布と超高分子量ポ
リエチレン(以F、σHPEと称す)から収る多孔質膜
およびその新規な製造法に関するものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a porous membrane comprising a woven fabric as a base material, a non-woven fabric and an ultra-high molecular weight polyethylene (hereinafter referred to as σHPE), and a novel method thereof. It concerns the manufacturing method.

(従来の技術) tM用セパレータ、コンデンサー相隔a、各+x分mg
等としては、ポリエチレン、ポリプロピレン ポリテト
ラフルオロエチレンから成る多孔′質膜を用いることが
知られ(例えば、特公昭46−40119号公報)、ま
た織布、不織布勿用いることも知ら几ている。
(Prior technology) Separator for tM, capacitor spacing a, each +x min mg
It is known to use porous membranes made of polyethylene, polypropylene, polytetrafluoroethylene, etc. (for example, Japanese Patent Publication No. 40119/1983), and it is also known that woven or nonwoven fabrics can be used.

(発明が解決しようとする課題) ところで、これら多孔質膜、織布あるいは不織布には、
各用途に応じ几特注が優れていること(例えば、′i!
を池用セパV−夕として用いる場合には、イオン導電性
が優几でいること)の血2機械的強度が充分なものであ
ること空孔径が小さいこと等が当然要求さ几る。
(Problem to be solved by the invention) By the way, these porous membranes, woven fabrics, or nonwoven fabrics have
Custom-made products are superior depending on each application (for example, 'i!
When used as a pond separator, it is naturally required that the ionic conductivity be excellent, the mechanical strength be sufficient, and the pore diameter be small.

しかしながら、J:、記多孔慣膜はその孔径は小さいも
のの機械的強度に方向性が百9.特に引裂強度に問題が
あり、堰扱いに注意が必要であった。
However, although the pore size of the porous membrane described in J: is small, its mechanical strength is directional. In particular, there was a problem with tear strength, and care had to be taken when handling the weir.

一方、織布、不織布は機械的強度の点での難点は無いも
のの、孔径の均一さf小孔径のものが得られ鑵いという
問題があった。
On the other hand, although woven fabrics and nonwoven fabrics do not have any disadvantages in terms of mechanical strength, they have the problem of being difficult to obtain pore diameter uniformity f and small pore diameters.

(課題を解決する友めの手段) 本発明者は従来技術の有する上記間1Iit−解決する
几め、檀々検討を行なり几。
(A Companion Means for Solving the Problem) The present inventor has conducted extensive studies to solve the above-mentioned problem that the prior art has.

先ず、多孔質膜と織布もしくは不織布を点状。First, the porous membrane and woven or non-woven fabric are dotted.

筋状等部分的に接着し、多孔質膜により孔径の均一さを
保証すると共に、織布もしくは不稙布により機械的強度
7に与えらt’uた複合多孔体を考えた。
We considered a composite porous body that is partially bonded in the form of stripes, the uniformity of the pore diameter is ensured by a porous membrane, and a mechanical strength of 7 is given by a woven fabric or a non-woven fabric.

しかしながら、これを電池用セパレータに用いた場合に
は接養剤の電解液による変質、劣化が懸念され、また分
111膜に用いた場合には1分離に寄与する面積が小さ
くなり分離効率の低下が不可避であるという問題が生じ
た。
However, when this is used in a battery separator, there are concerns about deterioration and deterioration due to the electrolyte in the culture agent, and when used in a 111 membrane, the area contributing to 1 separation becomes smaller, resulting in a decrease in separation efficiency. The problem arose that this was unavoidable.

そこで、更rζ検討金加え、織布もしくは不織布を基材
とし、こ几と特定のポリマーを特定構造となるように組
み合わせ且つ該ポリマーを多孔質とすることにより1機
械的強度が大きく、孔径の小さな多孔質部分を有する多
孔fRI!Ilが得られることを見出し1本発明を完成
するに至つ几ものである。
Therefore, in addition to further consideration, by using a woven fabric or non-woven fabric as a base material, combining this material with a specific polymer to form a specific structure, and making the polymer porous, 1) the mechanical strength is increased, and the pore diameter is Porous fRI with small porous parts! The present invention was completed by discovering that Il can be obtained.

即ち1本発明に係る多孔質膜は基材としての織布または
不織布と、粘度平均分子量(以下1分子量と略称する)
50万以とのIJMPEから成り、該Uf(PEは基材
の内部に含浸せしめられると共に基材表面に薄層状に存
在し、且つ多孔質構造を有していることを特徴とするも
のである。
Specifically, the porous membrane according to the present invention comprises a woven fabric or non-woven fabric as a base material, and a viscosity average molecular weight (hereinafter abbreviated as 1 molecular weight).
The Uf(PE) is characterized by being impregnated inside the base material, existing in a thin layer on the surface of the base material, and having a porous structure. .

以下6図面を参照しながら本発明の詳細な説明する。図
面において、lは多孔質膜の基材であり。
The present invention will be described in detail below with reference to six drawings. In the drawing, l is the base material of the porous membrane.

ガラス、ポリエステル、ポリアミド、ポリプロピレン、
アクリル等から成る織布または不織布である。基材1の
厚さは多孔質膜の用途に応じて過室選択で1例えば電池
用セパレータとしての多孔質膜の場合は1通常約lO〜
300μ漢のもの金6分離膜としての多孔質膜(lり場
合は1通常約30〜500μ満のものを用いる。
glass, polyester, polyamide, polypropylene,
It is a woven or non-woven fabric made of acrylic or the like. The thickness of the base material 1 is determined depending on the purpose of the porous membrane. For example, in the case of a porous membrane used as a battery separator, the thickness is usually about 10 to 1.
A porous membrane of 300 μm or less is used as a separation membrane (in the case of a porous membrane, a membrane of approximately 30 to 500 μm is usually used).

2は基材1の内部に含浸せしめられ、基材lが有する無
数の気孔を充填(この充填の形態は図示省略)している
Ui(PEである。このUl(PE 2は更に、基11
の表dii7icも薄層状(厚さriik常約l〜30
0μ溝)に存在せしめられている。
2 is Ui (PE) which is impregnated into the inside of the base material 1 and fills the countless pores of the base material 1 (the form of this filling is omitted from the figure).
The table dii7ic is also thin (thickness riik regular l~30
0μ groove).

そして、基材1の無数の気孔を充填し且つその表面Vc
び在するUklPE2ri、無数の気孔を有する多孔質
構造(図示省略)となっている。U)IPE 2の気孔
径および気孔率は多孔質膜の用途に応じて設定し得るが
2通常、前者は約0.1〜10μvm、@者は約30〜
90%である。
Then, the countless pores of the base material 1 are filled and the surface Vc
It has a porous structure (not shown) with numerous pores. U) The pore size and porosity of IPE 2 can be set depending on the use of the porous membrane, but usually the former is about 0.1 to 10 μvm, and the former is about 30 to
It is 90%.

と記UHPEは分子量が50万以上で、一般のポリエチ
レンのそれが約30万以下であるのに比べて大きく、か
ような分子量の大きなポリエチレンを用いることによっ
て多孔質構造の強度を実用性tVする程度に維持できる
UHPE has a molecular weight of 500,000 or more, which is larger than that of general polyethylene, which is about 300,000 or less, and by using polyethylene with such a large molecular weight, the strength of the porous structure can be improved to a practical level. Can be maintained at a certain level.

なお、 Uf(PEとしては三井石油化学工業社製。In addition, Uf (PE is manufactured by Mitsui Petrochemical Industries, Ltd.).

闇品名ハイゼツクスミリオン、ヘキスト社製、#i品名
ホスタレンGUR等が市販されている。
The black market name Hi-Zex Million, manufactured by Hoechst, #i product name Hostalen GUR, etc. are commercially available.

次に1本発明の他の態様である多孔質膜の製造法につい
て述べる。この方法は分子蓋50万以上のUHPE 1
kJafIj媒ヲ溶解せしめ1次φでこの溶液を多孔質
膜基材としての織布または不織布と接触せしめることに
エリ、基材内部に溶液を含浸させると共に基材表面に溶
液による薄層を形成し、その後これkgjlflj媒中
に浸漬し、前記良溶媒t−除去することにより、UMP
E’に多孔質化せしめることを特徴とするものである。
Next, a method for manufacturing a porous membrane, which is another embodiment of the present invention, will be described. This method uses UHPE 1 with a molecular cap of more than 500,000
By dissolving the medium and bringing this solution into contact with a woven or nonwoven fabric as a porous membrane base material, the solution is impregnated inside the base material and a thin layer of the solution is formed on the surface of the base material. , then by immersing it in kgjlflj medium and removing the good solvent, UMP
It is characterized by making E' porous.

本発明の方法においては、先ずUHPEが良溶媒に溶解
される。UHPEは前記の如く分子量が高く。
In the method of the present invention, UHPE is first dissolved in a good solvent. As mentioned above, UHPE has a high molecular weight.

比砿的JIlfII性であるので加熱醪解法全採用する
のが好ましいものである。例えば、所定の容器中にUk
lPE扮末と良溶媒倉入れ、撹拌しながら除々に昇温し
、溶解させる方法が適用でき、770熱俗解時の最終的
な温度は通常約100〜180℃であり。
Since it has typical JIlfII properties, it is preferable to use the heating melting method. For example, in a given container Uk
A method can be applied in which a PE powder is added to a good solvent, and the temperature is gradually raised while stirring to dissolve it, and the final temperature at 770°C is usually about 100-180°C.

所要時間は約062〜lO時間である。The required time is approximately 062-10 hours.

この工程において用いる溶媒はUf(PEt−溶解し得
るものであれば特に限定されず、キ7レン、デカリン、
ノナン、デカン、ウンデカン等を用いることができる。
The solvent used in this step is not particularly limited as long as it can dissolve Uf(PEt), such as xylene, decalin,
Nonane, decane, undecane, etc. can be used.

ま九、上記m解工程に2いて得られるUHP E溶液中
のUilPB 111度は、約0.1〜20億量%とす
るのが好ましいと判明している。濃度が低すぎると。
Ninth, it has been found that the UilPB 111 degree in the UHPE solution obtained in the above-mentioned solution step 2 is preferably about 0.1 to 2 billion% by weight. If the concentration is too low.

得られる多孔質膜におけるUHPE 14に亀裂を生ず
ることがあるばかりでなく、該基材の気孔を該溶液で充
填することも困難となる。一方、#度が高すぎると多孔
質基材内部への含浸性が低下し、こ7″Lまた基材の気
孔を充填することが困難となる。
Not only can the UHPE 14 in the resulting porous membrane crack, but it is also difficult to fill the pores of the substrate with the solution. On the other hand, if the # degree is too high, the impregnating property into the inside of the porous base material will be reduced, and it will be difficult to fill the pores of the base material.

上記溶解工程ICよって得られ之UHPE溶液は。The UHPE solution obtained by the above dissolution step IC is:

次いで基材としての織布または不織布と接M<Lめられ
る。この接触はUHPEm液を基材の内部に含浸させ、
基材の有する気孔を該溶液によって充填すると共に基材
表面に溶液の薄層紫形説することを目的として行なわれ
るものである。
Then, it is brought into contact with a woven or nonwoven fabric as a base material (M<L). This contact impregnates the inside of the substrate with the UHPEm liquid,
This is carried out to fill the pores of the substrate with the solution and to form a thin purple layer of the solution on the surface of the substrate.

従って、 Ui(PE 溶液と基材との接触には、(a
)基材をUHPEm液中に浸漬する方法、(b)基材表
面上にUHPEをTダイ押出法、インフレーション法等
により供給塗布する方法、(C)スプレー法、ロールコ
ータ−ナイフコーター等にエリ溶液を基材表面に塗布す
る方法、#が採用できる。なお(b)、(C)の方法の
場合は塗布後、圧力を作用させ、UHPEm液の基材内
部への含浸を確実ならしめるのがよい。ま九、UHPE
M液の流動性を増し、基材内部への含浸性勿高めるため
、該溶液を力ロ熱することができる。刀口熱する場合の
温度は1作業性、安全性等の点から約18 L) ”C
以下好ましくは100〜180℃である。
Therefore, the contact between the Ui(PE solution and the substrate requires (a
) A method in which the substrate is immersed in a UHPEm liquid; (b) A method in which UHPE is applied onto the surface of the substrate by a T-die extrusion method, an inflation method, etc.; (C) A method in which UHPE is applied onto the surface of the substrate by a T-die extrusion method, an inflation method, etc.; Method # of applying a solution to the surface of the base material can be adopted. In the case of methods (b) and (C), it is preferable to apply pressure after coating to ensure that the UHPEm liquid is impregnated into the inside of the base material. Maku, UHPE
In order to increase the fluidity of the M solution and improve its ability to impregnate the inside of the substrate, the solution can be heated. The temperature when heating the knife is approximately 18 L for workability, safety, etc.)
The temperature below is preferably 100 to 180°C.

本発明においては、 UHPEm液と接IIfJ&ぜし
めら′!″L之基材が1次いで貧浴媒中に浸漬されるう
この浸漬処理により、基材の内部および表面1#c存在
するUHPE 溶液中から良溶媒が*g媒によって抽出
除去され、<の結果、基材内部および表面にUHPE多
孔質ノーが形成される。
In the present invention, in contact with UHPEm liquid, IIfJ &Zeshimera'!``L'' substrate is then immersed in a poor bath medium. Through the immersion treatment, the good solvent is extracted and removed by the *g medium from the UHPE solution present inside and on the surface of the substrate, and the As a result, UHPE porous nodules are formed inside and on the surface of the substrate.

ここで用いる貧溶媒は、 UMPE ′J?工び基材を
溶解せず且つ前記良溶媒と相溶するものであればよく、
水f各種の有機溶媒が開用できるが、なかで41フルコ
ール類、特にメタノールが好ましい。
The poor solvent used here is UMPE'J? Any material may be used as long as it does not dissolve the processing base material and is compatible with the above-mentioned good solvent.
Water and various organic solvents can be used, but 41-fluorols, particularly methanol, are preferred.

上記工程に2いて形成されるUf(P E多孔質ノーの
気孔率および孔径は、主として用いる両溶媒の相溶性の
度合、良溶媒の*溶媒への抽出速度により決定される。
The porosity and pore size of the Uf(PE porous material) formed in step 2 above are determined mainly by the degree of compatibility of both solvents used and the rate of extraction of the good solvent into the *solvent.

従って、UHPEm液の濃度るるいは両醪媒の組み合わ
せを変えることによって、UHPE多孔質J!lの気孔
率、気孔の孔径を調整できる。
Therefore, by changing the concentration of the UHPEm liquid or the combination of both mortar, UHPE porous J! The porosity of l and the pore size of the pores can be adjusted.

本発明の方法によって得られる多孔′lt膜におけるU
HPE多孔質11の気孔″4および気孔の孔径は。
U in the porous 'lt film obtained by the method of the present invention
The pores ``4'' and the pore diameters of the HPE porous material 11 are as follows.

上記した9口〈作業条件によって檀々変わり得るが。The above-mentioned nine mouths (although the number may vary depending on the working conditions).

通常、前者は約30〜90%、後者はlJ、1−10μ
溝である。
Usually, the former is about 30-90%, the latter is lJ, 1-10μ
It's a groove.

(実施例〕 以下、実施例により本発明を更に詳細に説明す。(Example〕 Hereinafter, the present invention will be explained in more detail with reference to Examples.

る。なお、実施例中において、itを示す「部」はいず
れも「暇量部」である。
Ru. In addition, in the examples, all "parts" indicating "it" are "spare time parts".

実施例1 ガラス容器に中シレン100部、デカリン100部およ
びUHPE粉末(分子量200万1粒径30μ喝)4部
を入れ、撹拌しながら液温を25゛Cから140℃に上
昇せしめ、更に同温度に維持し1時間撹拌を続け、 U
HPEをf?I解せしめる。
Example 1 100 parts of medium silane, 100 parts of decalin, and 4 parts of UHPE powder (molecular weight: 2,000,000, particle size: 30μ) were placed in a glass container, and the liquid temperature was raised from 25°C to 140°C while stirring, and then Maintain the temperature and continue stirring for 1 hour.
HPE f? I will make you understand.

このUHPE溶液をガラス織布(厚さ100μ講、質*
98g/rlンの片面上に、Tダイ(温度135℃)を
用いて押し出す9次いで2枚のガラス板間に挾み、0.
1klil/−の圧力を作用させて1分間保持する。
This UHPE solution was applied to a glass woven cloth (thickness 100 μm, quality *
98 g/rl was extruded on one side using a T-die (temperature 135°C), and then sandwiched between two glass plates.
A pressure of 1 klil/- is applied and held for 1 minute.

なお、この際、温/Itl−135℃に保つ友。こnv
ζより、ガラス織布の有する気孔がUHPE溶液により
充填され、更に該織布の両表面にはUHPE溶液の薄層
が形成され次。
In addition, at this time, the temperature was maintained at -135°C. This nv
From ζ, the pores of the glass woven fabric are filled with the UHPE solution, and a thin layer of the UHPE solution is formed on both surfaces of the woven fabric.

次に、これをメタノール(液温25℃)中1C30分間
浸漬した後、引き上げて風乾し多孔質g(厚さ140μ
攪)全得之。
Next, this was immersed in methanol (liquid temperature 25°C) for 30 minutes at 1C, then pulled out and air-dried to form a porous g (thickness 140μ
Stirring) All benefits.

この多孔質膜に2けるUHpa多孔質ノーの多孔(イ造
は1例えば走*型鑞子顧′4I1.境(倍率は5υυυ
倍)によって観察でき几。
This porous membrane has 2 UHpa porous pores (Izo is 1, for example, a run * type 鞞子Cu'4I1. boundary (the magnification is 5υυυ
It can be observed by magnification.

実施例2 UMPEとして分子量60万1粒径1st1μ溝のもの
を用いる以外は実施例1と同様に作業して多孔質膜(厚
さ150μ鴨〕を得几。
Example 2 A porous membrane (thickness: 150 μm) was obtained in the same manner as in Example 1, except that UMPE with a molecular weight of 600,001 and a particle size of 1st and 1 μm groove was used.

比較例1 市販のポリプロピレン製多孔質膜(厚さ25μm)。Comparative example 1 Commercially available polypropylene porous membrane (thickness 25 μm).

比較例2 実施例1で用い之ガラス織布。Comparative example 2 Glass woven fabric used in Example 1.

比較例3 実施例1で用い之ガラス織布の片面に比較例1のポリプ
ロピレン製多孔質膜を接層して多孔質膜を得た。
Comparative Example 3 The polypropylene porous membrane of Comparative Example 1 was layered on one side of the glass woven fabric used in Example 1 to obtain a porous membrane.

接着はポリ酢酸ビニルを主成分とするホットメルト接着
剤を用い、塗布中2m、塗布間隔5Bで筋状に接着した
For adhesion, a hot melt adhesive containing polyvinyl acetate as a main component was used, and the adhesive was streaked at a distance of 2 m during application and an application interval of 5 B.

比較例4 U)IPEに代え1分子量25万、密度0.95の低密
度ポリエチレンを用いる以外は実施例1と同様に、作業
したところ、基材表面のポリエチレン多孔質層に無数の
亀裂が生じてしまい、実用性ある多孔質膜が得られなか
った。
Comparative Example 4 U) When working in the same manner as in Example 1 except that low-density polyethylene with a molecular weight of 250,000 and a density of 0.95 was used instead of IPE, countless cracks were observed in the polyethylene porous layer on the surface of the base material. As a result, a practical porous membrane could not be obtained.

実施例および比較例の多孔質膜について下記試験を行な
い、得られた結果t−第1表に示す。
The following tests were conducted on the porous membranes of Examples and Comparative Examples, and the results are shown in Table 1.

(A)孔径測定 走査型電子顕微鏡(倍率は比較例2では50倍。(A) Pore diameter measurement Scanning electron microscope (magnification is 50x in Comparative Example 2).

他の例では5ooo倍)によって、多孔質膜の最大孔径
(実施例)の場合はUHPE多孔質層の最大孔径)t−
覗察測定し友。
t-
A friend who observes and measures.

(BJイオン導電性 測定は25℃で行ない、J4S−C−2313に準じて
測定した。なお、電解液としてはプロピレンカーボネー
トと1. 3−ジオキソラン41量比1:1で混合し、
これに電解質として過塩素酸リチウムt−1七ル/e溶
解させ友。
(BJ ion conductivity measurements were carried out at 25°C and measured according to J4S-C-2313. The electrolyte was a mixture of propylene carbonate and 1.3-dioxolane 41 in a ratio of 1:1,
Dissolve lithium perchlorate in this as an electrolyte.

(C)引裂強度 JIS−に−6238に準じ、谷多孔質膜の縦方向およ
び横方向について測定し、その弱い+tii ?示した
(C) Tear strength Measured in the vertical and horizontal directions of the valley porous membrane according to JIS-6238, and its weak +tii? Indicated.

第  1  表 秦測定後、電解液から取り出す際に゛、ガラス域布とポ
リプロピレン多孔質膜が剥離してしまつ几。
Table 1: After measurement, the glass cloth and polypropylene porous membrane peeled off when removed from the electrolyte.

(発明の効果) 本発明は上記のように構成されており、UHPE多孔質
層を不織布または織布で担持補強するようにし友ので1
強度の大きな多孔質gを提供でき。
(Effects of the Invention) The present invention is configured as described above, and the UHPE porous layer is supported and reinforced by a nonwoven fabric or a woven fabric.
Porous g with high strength can be provided.

ま九本発明の方法によれば、かような多孔質膜金谷易に
製造し得る。
According to the method of the present invention, such a porous membrane can be easily produced.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明に係る多孔質膜の実例を示す正颯図である
。 1・・・基材  2・・・Ul−IPE2 1J)−I
PF
The drawing is a front view showing an example of the porous membrane according to the present invention. 1... Base material 2... Ul-IPE2 1J)-I
P.F.

Claims (2)

【特許請求の範囲】[Claims] (1)基材としての織布または不織布と、粘度平均分子
量50万以上の超高分子量ポリエチレンから成り、該ポ
リエチレンは基材の内部に含浸せしめられると共に基材
表面に薄層状に存在し、且つ多孔質構造を有しているこ
とを特徴とする多孔質膜。
(1) It consists of a woven or nonwoven fabric as a base material and ultra-high molecular weight polyethylene with a viscosity average molecular weight of 500,000 or more, the polyethylene is impregnated inside the base material and exists in a thin layer on the surface of the base material, and A porous membrane characterized by having a porous structure.
(2)粘度平均分子量50万以上の超高分子量ポリエチ
レンを良溶媒に溶解せしめ、次いでこの溶液を多孔質膜
基材としての織布または不織布と接触せしめることによ
り、基材内部に溶液を含浸させると共に基材表面に溶液
による薄層を形成し、その後これを貧溶媒中に浸漬し、
前記良溶媒を除去することにより、超高分子量ポリエチ
レンを多孔質化せしめることを特徴とする多孔質膜の製
造法。
(2) Ultra-high molecular weight polyethylene with a viscosity average molecular weight of 500,000 or more is dissolved in a good solvent, and then this solution is brought into contact with a woven or nonwoven fabric as a porous membrane base material to impregnate the inside of the base material with the solution. At the same time, a thin layer of solution is formed on the surface of the substrate, and then this is immersed in a poor solvent.
A method for producing a porous membrane, comprising making ultra-high molecular weight polyethylene porous by removing the good solvent.
JP26669988A 1988-10-21 1988-10-21 Porous film and production thereof Pending JPH02113039A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26669988A JPH02113039A (en) 1988-10-21 1988-10-21 Porous film and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26669988A JPH02113039A (en) 1988-10-21 1988-10-21 Porous film and production thereof

Publications (1)

Publication Number Publication Date
JPH02113039A true JPH02113039A (en) 1990-04-25

Family

ID=17434455

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26669988A Pending JPH02113039A (en) 1988-10-21 1988-10-21 Porous film and production thereof

Country Status (1)

Country Link
JP (1) JPH02113039A (en)

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