JPS59105035A - Production of microporous sheet - Google Patents

Production of microporous sheet

Info

Publication number
JPS59105035A
JPS59105035A JP21384482A JP21384482A JPS59105035A JP S59105035 A JPS59105035 A JP S59105035A JP 21384482 A JP21384482 A JP 21384482A JP 21384482 A JP21384482 A JP 21384482A JP S59105035 A JPS59105035 A JP S59105035A
Authority
JP
Japan
Prior art keywords
sheet
filler
thermoplastic resin
microporous
stretching
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.)
Granted
Application number
JP21384482A
Other languages
Japanese (ja)
Other versions
JPH0238098B2 (en
Inventor
Shingo Kaneko
金子 新吾
Kenji Okamura
岡村 健次
Kiyoshi Sumi
角 清
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.)
Tokuyama Corp
Original Assignee
Tokuyama 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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP21384482A priority Critical patent/JPS59105035A/en
Publication of JPS59105035A publication Critical patent/JPS59105035A/en
Publication of JPH0238098B2 publication Critical patent/JPH0238098B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a uniformly hazed, homogeneous microporous sheet, by laminating a thermoplastic resin sheet containing a filler of a finer particle diameter with a thermoplastic resin sheet containing a filler of a larger particle diameter, and stretching the laminate. CONSTITUTION:A thermoplastic resin such as vinyl chloride resin or acrylic resin is mixed with a filler, particle diameter <=1mu, (e.g., calcium carbonate or common salt), and the mixture is molded into a thermoplastic resin sheet (hereinafter, abbreviated as sheet A). Separately, a thermoplastic resin sheet containing a filler having a particle diameter larger than that of the filler used in sheet A (hereinafter, abbreviated as sheet B) is prepared so that the thickness of sheet B is at least three times that of sheet A. Sheet A is laminated with sheet B, and the laminate is stretched to obtain the purpose microporous sheet which is a porous sheet in which the B side consists of the microporous sheet and the diameters of the pores of sheet B side are larger than those of sheet A side.

Description

【発明の詳細な説明】 本発明は乾式法による新規な熱可塑性樹脂よりなる微多
孔シートの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a microporous sheet made of a novel thermoplastic resin by a dry method.

詳しくは、それぞれ粒径が特定された充填剤を含む複数
の熱可塑性樹脂シートをラミネートした後、延伸するこ
とを特徴とする微多孔シートの製造方法である。
Specifically, the method for producing a microporous sheet is characterized in that a plurality of thermoplastic resin sheets each containing a filler having a specified particle size are laminated and then stretched.

近年、電池セパレーター及び血液、エマルジョンの分離
等の分野において合成樹脂の多孔シートが用いられてい
る。これらの分野に用いられるシートとしては、例えば
孔径がO01μ以下の微多孔を有するもので、濾過性、
耐薬品性及び強度等に優れたものが要求される。
In recent years, porous sheets of synthetic resin have been used in fields such as battery separators and separation of blood and emulsions. Sheets used in these fields have, for example, microporous sheets with a pore size of 001μ or less, and have excellent filterability,
Materials with excellent chemical resistance and strength are required.

従来、多孔性シートを製造する方法としては、例えば熱
可塑性樹脂中に充填剤を混合し成形して得たシートを延
伸する乾式方法、或いは熱可塑性樹脂中に充填剤を混合
したものをシート化した後、該充填剤を溶剤等で抽出す
る湿式方法等がある。
Conventionally, methods for manufacturing porous sheets include, for example, a dry method in which a filler is mixed into a thermoplastic resin and then formed and the resulting sheet is stretched, or a sheet is formed by mixing a filler into a thermoplastic resin. There is a wet method in which the filler is then extracted with a solvent or the like.

ところが前者の乾式方法においては、一般にシートの孔
径は充填剤の粒径や延伸倍率に左右され、しかも均一な
孔径を得ようとすれば用する充填剤の粒径を均一にかつ
延伸倍率を均一にする必要がある。即ち、一般に無機質
充填剤を多量に充填したシート状物を延伸して多孔質シ
ートを得る場合、延伸時における白化現象、すなわち充
填剤と樹脂マトリックスの界面剥離現象を如何に均一に
行わせるかが重要である。従来、かかる均一な白化現象
を行わしめるために無機質充填剤に表面処理を施す方法
や、ガラス転移点以上、軟化点以下の温度範囲で出来る
かぎり低温側で予備的に微小延伸させて界面剥離を行わ
しめる方法等によって達成されている。しかしながら、
微多孔質シートを得るために、粒径が1μ以下でかつ多
量に無機質充填剤を用いる場合には、均一白化現象を行
わしめるのは困難であった。すなわち、粒子径1μ以下
の無機質充填剤を多量特に50重量%以上に充填し、上
述の方法をとっても、延伸時において局部的に延伸され
均質な多孔質シートは得られないばかりか、所定の延伸
倍率になるまでに破断する等のトラブルが生じ、実質的
に微多孔質シートは得られなかった。
However, in the former dry method, the pore size of the sheet generally depends on the particle size of the filler and the stretching ratio, and in order to obtain a uniform pore size, it is necessary to make the particle size of the filler used uniform and the stretching ratio uniform. It is necessary to That is, in general, when a porous sheet is obtained by stretching a sheet material filled with a large amount of inorganic filler, it is important to uniformly achieve the whitening phenomenon during stretching, that is, the interfacial peeling phenomenon between the filler and the resin matrix. is important. Conventionally, in order to achieve such a uniform whitening phenomenon, inorganic fillers have been subjected to surface treatment, or interfacial peeling has been achieved by preliminary micro-stretching at the lowest possible temperature within the temperature range above the glass transition point and below the softening point. This is achieved through methods such as implementation. however,
In order to obtain a microporous sheet, when a large amount of inorganic filler with a particle size of 1 μm or less is used, it is difficult to achieve a uniform whitening phenomenon. That is, even if a large amount, particularly 50% by weight or more, of an inorganic filler with a particle size of 1 μm or less is filled and the above-mentioned method is used, a porous sheet that is locally stretched and homogeneous during stretching cannot be obtained, and it is not possible to obtain a porous sheet that is locally stretched during stretching. Problems such as breakage occurred before the magnification was reached, and no microporous sheet was substantially obtained.

これに対して後者の湿式方法においては、充填剤を抽出
後のシートの孔径がはソ充填剤の粒径により決定される
ため均一な微多孔シートを得ることが出来る。またこの
シートを更に延伸によって高い多孔度を有する微多孔性
シートを製造する方法も知られている。しかし、これら
湿式方法では充填剤、可塑剤等の抽出に無機薬品や有機
溶剤を使用するため、時間や費用を要し煩雑である。さ
らに従来、充填剤を含有したシートを積層し延伸するこ
とによって合成紙を製造する方法が開示されている(特
公昭50−58665 、特公昭57−49011)。
On the other hand, in the latter wet method, the pore size of the sheet after the filler has been extracted is determined by the particle size of the filler, so that a uniform microporous sheet can be obtained. Also known is a method of producing a microporous sheet having high porosity by further stretching this sheet. However, these wet methods use inorganic chemicals or organic solvents to extract fillers, plasticizers, etc., and are therefore time-consuming, costly, and complicated. Furthermore, a method for manufacturing synthetic paper by laminating and stretching sheets containing fillers has been disclosed (Japanese Patent Publication No. 50-58665, Japanese Patent Publication No. 57-49011).

しかし、かかる合成紙の製造方法においては延伸による
微細空孔化が示されているものの、その目的とするとこ
ろは主に強度を保持、改良させるために積層されるもの
であり、積層されたシートは良好な透過性をもつものと
はいえない。これに対して本発明は表面層が微細な多孔
質であり、基材層も高度に多孔化した構造を有する微多
孔シートの製造を目的とするもので、明らかに異なるも
のである。
However, although the manufacturing method of such synthetic paper shows microporous formation by stretching, its purpose is mainly to maintain and improve strength, and the laminated sheets are cannot be said to have good permeability. On the other hand, the present invention is clearly different, as it aims to produce a microporous sheet in which the surface layer is finely porous and the base layer is also highly porous.

本発明者等は上記の目的を達成するために鋭意研究の結
果、特定の微粒径の充填剤を含有する樹脂シートを予め
特定の樹脂シートにラミネートすることにより延伸が可
能になり、所望の微多孔シートを容易に得ることを見い
出し本発明を提供するに至った。
As a result of intensive research to achieve the above object, the present inventors have found that by laminating a resin sheet containing a filler with a specific fine particle size onto a specific resin sheet in advance, stretching becomes possible. The inventors have discovered that a microporous sheet can be easily obtained and have provided the present invention.

即ち、本発明は最大粒径1μ以下の充填剤を含む熱可塑
性樹脂シート(以下、Aシートと記す)と、平均粒径が
上記粒子径より大なる充填剤を含む熱可塑性樹脂シート
(以下、Bシートと記す)をラミネートした・後、延伸
することを特徴とする微多孔シートの製造方法である。
That is, the present invention provides a thermoplastic resin sheet containing a filler with a maximum particle size of 1 μm or less (hereinafter referred to as A sheet), and a thermoplastic resin sheet containing a filler with an average particle size larger than the above particle size (hereinafter referred to as A sheet). This is a method for producing a microporous sheet, which is characterized by laminating and then stretching a sheet (referred to as B sheet).

本発明の方法により得られる微多孔シートFiAシート
面が微多孔なシートであり、Bシート面はAシート面よ
り大なる孔径を有する。
The microporous sheet FiA obtained by the method of the present invention is a sheet in which the sheet surface is microporous, and the B sheet surface has a larger pore diameter than the A sheet surface.

本発明の微多孔シートとはAシートとBシートをラミネ
ートした後、延伸した複合シートでもよく、更に該延伸
シートよりBシートを剥離させたものも含む総称である
The microporous sheet of the present invention may be a composite sheet obtained by laminating sheet A and sheet B and then stretching the sheet, and is a general term that also includes sheets obtained by peeling sheet B from the stretched sheet.

本発明において最も重要なことは、特定の粒径の充填剤
を含むシートそれぞれをラミネートした後、延伸するこ
とにある。即ち、一般に1μ以下の粒径の極めて小さい
充填剤を熱可塑性樹脂に所定量混合した後、シート化し
たもの(Aシート)は、ネッキング延伸状態、すなわち
、一部分から延伸され延伸多孔が不均一となるばかりで
なく、所望の延伸倍率に達する前に切断するなどの現象
が生じる。
The most important thing in the present invention is that each sheet containing a filler of a specific particle size is laminated and then stretched. That is, in general, after mixing a predetermined amount of a very small filler with a particle size of 1 μ or less into a thermoplastic resin, the sheet (A sheet) is in a necking stretched state, that is, it is stretched from one part and the stretched pores are nonuniform. Not only this, but also phenomena such as cutting occur before the desired stretching ratio is reached.

ところが、該シートに特定の補助シー)(Bシート)を
ラミネートすることによりAシートも均一に白化された
延伸微多孔シートを得ることが可能になる。
However, by laminating a specific auxiliary sheet (B sheet) to the sheet, it becomes possible to obtain a stretched microporous sheet in which the A sheet is also uniformly whitened.

本発明においては、目的とする微多孔性を有するだめの
シートがAシートであり、Aシートだけでは延伸できな
いためKBレシートともにうξネートするものでBシー
トは所謂Aシートを延伸するための一種の補助シートで
ある。そして、これらはラミネート、延伸した後は一連
の多孔シートとなるが、この際少なくとも表面(片面)
が微多孔(Aシートを延伸した微多孔シート)でそれ以
外のシートは該多孔度より太きbものであればよい。
In the present invention, the final sheet having the desired microporosity is the A sheet, and since the A sheet alone cannot be stretched, the KB sheet is also stretched, and the B sheet is a type of sheet for stretching the A sheet. This is an auxiliary sheet. After laminating and stretching, these become a series of porous sheets, but at least one surface (one side)
It is sufficient that the porosity is microporous (a microporous sheet obtained by stretching sheet A), and the other sheets have a porosity larger than the porosity.

本発明においては、2種の各々のシートに含有する充填
剤の粒径をそれぞれ特定することが重要であり、即ち、
Aシートには最大粒径1μ以下、好ましくけ0.01〜
0.5μの充填剤を用いるのに対l−てBシートには平
均粒径が一般に1〜50μ、好ましくは3〜20μで且
つAシートの充填剤より粒径の大きな充填剤を使用する
ことが必要である。
In the present invention, it is important to specify the particle size of the filler contained in each of the two types of sheets, that is,
A sheet has a maximum particle size of 1μ or less, preferably 0.01~
In contrast to the use of a filler of 0.5 μm, the average particle size of the B sheet is generally 1 to 50 μm, preferably 3 to 20 μm, and the particle size is larger than that of the filler of the A sheet. is necessary.

本発明に使用し得る充填剤は通常ゴム又はプラスチック
中に混合される充填剤、例えば炭酸カルシウム、石膏、
亜硫酸カルシウム。
Fillers that can be used in the present invention include fillers that are normally mixed into rubber or plastics, such as calcium carbonate, gypsum,
Calcium sulfite.

りん酸カルシウム、炭酸マグネシウム、塩基性炭酸マグ
ネシウム、水酸化マグネシウム。
Calcium phosphate, magnesium carbonate, basic magnesium carbonate, magnesium hydroxide.

硫酸マグネシウム、水相珪酸、無水珪酸、ソーダ灰、塩
化ナトリウム、硫酸ナトリウム。
Magnesium sulfate, aqueous silicic acid, silicic anhydride, soda ash, sodium chloride, sodium sulfate.

クレー、各種セメント、火山灰、シラス、酸化チタン、
酸化鉄、カーボンブラック、種々の金属粉、その他の無
機物又は無機物を主体とする有機物金属塩等であり、一
般に50ミクロン以下の平均粒径を有するものである。
Clay, various cements, volcanic ash, shirasu, titanium oxide,
These include iron oxide, carbon black, various metal powders, other inorganic substances, or organic metal salts mainly composed of inorganic substances, and generally have an average particle size of 50 microns or less.

とりわけ六シートに混合される充填剤としては1μ以下
に微粉砕されたもの、あるいは合成によって1μ以下と
成したものであって、後者は特に均一な粒子径を得る方
法として好ましく、これに属するものとして炭酸カルシ
ウム、水酸化マグネシウム、無水珪酸、酸化チタン等が
好適に使用される。又、本発明においてのAシートに充
填する充填剤の粒径は予め最大粒径が1μ以下にしても
、或いは樹脂の混線等の段階で1μ以下となるようにし
てもよい。これらは樹脂中に所望の多孔度に保てる量、
好ましくは30〜80重量%、特に好ましくは50〜8
0重量%含有するように添加する。
In particular, the filler to be mixed into the six sheets is one that has been finely pulverized to 1μ or less, or one that has been synthesized to a size of 1μ or less, and the latter is particularly preferred as a method of obtaining a uniform particle size, and the filler that belongs to this category As such, calcium carbonate, magnesium hydroxide, silicic anhydride, titanium oxide, etc. are preferably used. Further, the particle size of the filler filled in the A sheet in the present invention may be set to have a maximum particle size of 1 μm or less in advance, or may be made to be 1 μm or less at a stage such as cross-wire of the resin. These are the amount that can maintain the desired porosity in the resin,
Preferably 30-80% by weight, particularly preferably 50-8%
Add so that the content is 0% by weight.

本発明においては、無機質充填剤の樹脂マトリックス中
への分散性の向上や延伸工程における均一延伸性の向上
を目的として、無機質粉体にあらかじめ耐熱性のある可
塑剤、消削あるいは界面活性剤、プロセスオイル等で表
面処理されたものを用いることは特にAシートの場合好
適となる。これらの表面処理剤量としては粒径によって
異なるが、通常は充填量に対し3〜100重量部の添加
量である。
In the present invention, for the purpose of improving the dispersibility of the inorganic filler in the resin matrix and improving the uniform stretchability in the stretching process, heat-resistant plasticizers, erasing agents, or surfactants are added to the inorganic powder in advance. It is particularly suitable for A sheet to use one whose surface has been treated with process oil or the like. The amount of these surface treating agents varies depending on the particle size, but is usually 3 to 100 parts by weight based on the amount filled.

本発明においては、上記以外の種々の添加物例えば顔料
、安定剤、難燃剤等を同時に或いは別途混合することは
妨げない。
In the present invention, various additives other than those mentioned above, such as pigments, stabilizers, flame retardants, etc., may be mixed simultaneously or separately.

本発明に用いられる熱可塑性樹脂は公知のものが特に制
限なく用いられる。例えば塩化ビニル4i4JIL酢酸
ビニル樹脂、ポリスチレン。
As the thermoplastic resin used in the present invention, known thermoplastic resins can be used without particular limitation. For example, vinyl chloride 4i4JIL vinyl acetate resin, polystyrene.

A B s樹脂、アクリル樹脂、ポリエチレン。A B s resin, acrylic resin, polyethylene.

ポリプロピレン、フッ素樹脂、ポリアミド樹脂、アセタ
ール樹脂、ポリカーボネート、繊維素プラスチックなど
があるが、加工性及び耐薬品性の面から一般にポリプロ
ピレン等のポリオレフィンが好ましく用いられる。上記
に示した充填剤を含有する熱可塑性樹脂シートは、一般
に0.03〜30の厚みを有する。
Examples include polypropylene, fluororesin, polyamide resin, acetal resin, polycarbonate, cellulose plastic, and polyolefin such as polypropylene is generally preferably used from the viewpoint of processability and chemical resistance. Thermoplastic resin sheets containing the fillers shown above generally have a thickness of 0.03-30.

ラミネートの方法は、上記組成よりなるものを混線後、
カレンダー成形あるいは押出成形等によりシートをそれ
ぞれ個別に成形した後、該シートを圧縮成形に貼り合わ
せ一体とするもの、あるいはT−ダイまたは円筒状グイ
よりA樹脂及びB樹脂の溶融組成物を共押出して2層シ
ートとしてもよいし、また、Aシートの上に押出ラミネ
ート方法によって2層化する方法等、一般的な2層化の
成形方法が採用される。この際、へシートとBシートの
厚みについて、ラミネート後のシートを延伸するに際し
て、Aシートの厚みがBシートの厚みより厚くなるとA
シートの延伸性が劣るため、該状態を緩和するためには
、Bシートの厚みがAシートの6倍以上とすることが好
ましい。へシートとBシートをラミネートする際、該シ
ートの組成及び融点等の物性が大幅に異なるとラミネー
ト部の強度等が低下したり、場合によっては剥離するこ
とも生じるため、AシートとBシートは普通同種の樹脂
を用いられるが、異種の樹脂を用いることもできる。
The laminating method is to mix the above composition and then
After forming the sheets individually by calender molding or extrusion molding, the sheets are bonded together by compression molding, or by coextruding the molten composition of A resin and B resin from a T-die or cylindrical gouer. Alternatively, a general two-layer molding method such as forming two layers on the A sheet by extrusion lamination may be adopted. At this time, regarding the thickness of the A sheet and the B sheet, when stretching the laminated sheet, if the A sheet is thicker than the B sheet, the A
Since the stretchability of the sheet is poor, in order to alleviate this condition, it is preferable that the thickness of the B sheet is 6 times or more that of the A sheet. When laminating the A sheet and the B sheet, if the composition and physical properties such as melting point of the sheets are significantly different, the strength of the laminated part may decrease, and in some cases, peeling may occur. Usually the same type of resin is used, but different types of resin can also be used.

次に上記ラミネートされたシートは少なくとも1方向特
に好ましくは2軸方向に延伸することによって多孔質シ
ートを得る。該延伸方法及び装置忙ついては、公知のも
のが用いられるが、通常、熱可塑性樹脂の融点以下の温
度で165倍以上、好ましくは2倍程度延伸することに
よってシートに細孔を成形させる。
Next, the laminated sheet is stretched in at least one direction, preferably in two axial directions, to obtain a porous sheet. Although known stretching methods and equipment may be used, pores are usually formed in the sheet by stretching the sheet by 165 times or more, preferably about 2 times, at a temperature below the melting point of the thermoplastic resin.

又、延伸後、Bシートを剥離させることも可′能である
。得られた微多孔性シートは一般に厚みが0.03乃至
5I!ll11.空孔率60−90%。
It is also possible to peel off the B sheet after stretching. The resulting microporous sheet generally has a thickness of 0.03 to 5I! ll11. Porosity 60-90%.

最大孔径1μ以下のもので孔径分布が均一で且つ強度に
優れたものとなる。従って、本発明によって得られる微
多孔シートは延伸された後、このまま、あるいは適当な
溶出剤、例えば無機質粉体には酸あるいはアルカリ溶液
で抽出したり、あるいは添加された可塑剤等はアルコー
ル等の有機溶剤で抽出除去するととによって樹脂だけか
らなる微多孔質シートと成してもよく、前述のような広
範な用途に利用される。
When the maximum pore diameter is 1 μm or less, the pore diameter distribution is uniform and the strength is excellent. Therefore, after the microporous sheet obtained by the present invention is stretched, it can be used as it is, or extracted with an appropriate eluent, such as an acid or alkaline solution for inorganic powder, or an added plasticizer, etc. By extracting and removing the resin with an organic solvent, a microporous sheet consisting only of the resin may be obtained, and it can be used for a wide range of applications as described above.

以下、本発明を具体的に説明するための実施例を示すが
、本発明は以下の実施例に限定されるものではない。
EXAMPLES Hereinafter, examples will be shown to specifically explain the present invention, but the present invention is not limited to the following examples.

なお、性能評価項目の測定方法は以下の通り。The method for measuring performance evaluation items is as follows.

1)空隙率 Wo;試料片の空中重量 w+ 9試料片の水含重量 W2;試料片の水中重量 2)通気度〜JISP8117に準する。1) Porosity Wo: weight of sample piece in air w + Water content weight of 9 sample pieces W2; Weight of sample piece in water 2) Air permeability ~ According to JISP8117.

3)最大孔径〜A8TM Ii”−316−70に準す
る(エタノール使用) 実施例 1 重質炭酸カルシウム(白石カルシウム社製。
3) Maximum pore diameter ~ According to A8TM Ii''-316-70 (using ethanol) Example 1 Heavy calcium carbonate (manufactured by Shiraishi Calcium Co., Ltd.).

商品名:ホワイトノー81粒径7μ)70重量%、ポリ
プロピレン粉末(徳山曹達社製。
Product name: White No 81 (particle size 7μ) 70% by weight, polypropylene powder (manufactured by Tokuyama Soda Co., Ltd.).

商品名:徳山ポリプロYE−120)30重重量、及び
ポリエステル系可塑剤(大日本インキ社製、商品名:ポ
リサイザ−W−2300)3.0PHRより成る組成物
を3″ロールにて200Cで混線後、プレス機で厚さ0
.3%のシート(シー)B)を作成した。次いで第1表
に示す充填剤及び分散剤を用いて同様に厚さ0.1Xの
シート(シー)A)を作成し、上記シート(B)とシー
ト(A)を170℃で厚さ0.351Xの型枠の中で積
層し、プレスし厚さ0.35%のシートを得た。次いで
前記シートを実験用二軸延伸機で1soc、タテXヨコ
が2X2倍に同時2軸延伸し、得られたシートの物性を
第1表右欄(A1〜4)に示した。同A4は比較例でシ
ート(B)だけから成る延伸シートの結果を示した。
A composition consisting of 30 weight (trade name: Tokuyama Polypro YE-120) and 3.0 PHR of a polyester plasticizer (manufactured by Dainippon Ink Co., Ltd., trade name: Polycizer W-2300) was mixed at 200C with a 3″ roll. After that, use a press to reduce the thickness to 0.
.. A 3% sheet B) was prepared. Next, a sheet A) having a thickness of 0.1X was prepared in the same manner using the filler and dispersant shown in Table 1, and the sheet (B) and sheet (A) were heated to a thickness of 0.1X at 170°C. They were laminated in a 351X mold and pressed to obtain a sheet with a thickness of 0.35%. Next, the sheet was simultaneously biaxially stretched at 1 soc in an experimental biaxial stretching machine to a ratio of 2x2 in the vertical and horizontal directions, and the physical properties of the obtained sheet are shown in the right column of Table 1 (A1 to A4). A4 is a comparative example and shows the results of a stretched sheet consisting only of sheet (B).

A1〜3は^4に比べ孔径が小さく、シート(B)側の
表面はミクロフィブリル化しり微多孔質になっているこ
とがわかった。A1のシー) (B)側表面及びシート
(A)側表面の電子顕微鏡写真を夫々、第1図及び第2
図に示した。
It was found that A1 to A3 had smaller pore diameters than A4, and the surface on the sheet (B) side was microfibrillated and microporous. Electron micrographs of the (B) side surface of A1 and the sheet (A) side surface are shown in Figures 1 and 2, respectively.
Shown in the figure.

更に比較例としてシー)(B)及びA1の充填剤を含有
するシー) (A)を同様にして、それぞれ2Xの厚さ
のプレスシートを積層したシートを延伸したところ破断
が発生し、該延伸シートは得られなかった。
Further, as a comparative example, when a sheet made by laminating press sheets of 2X thickness in the same manner as sheet) (B) and sheet) (A) containing the filler A1 was stretched, breakage occurred, and the stretching Didn't get a sheet.

jス 1゛不日 実施例 2 重質炭酸カルシウム(商品名:ホワイトンーB、粒子径
7μ、白石カルシウム社製)100fに対し、3 F 
(3PHR)のポリエステル系可塑剤(商品名: W−
2300、大日本インキ社製)で表面処理されたもの7
0wt%とポリプロピレン(商品名二YE−120、徳
山ポリグロ、徳山曹達社製)30wt%よりなるペレッ
ト状組成物を60−のシリンダー径を有するT−ダイ押
出機で厚さ0−3m+のシート状として巻き取った(シ
ートB)。次に水酸化マグネシウム(商品名:キスマ4
AF。
1゛Fuji Example 2 3F for 100F of heavy calcium carbonate (trade name: Whiten-B, particle size 7μ, manufactured by Shiroishi Calcium Co., Ltd.)
(3PHR) polyester plasticizer (product name: W-
2300, manufactured by Dainippon Ink Co., Ltd.) 7
A pellet composition consisting of 0 wt% and 30 wt% of polypropylene (trade name 2YE-120, manufactured by Tokuyama Polyglo, Tokuyama Soda Co., Ltd.) was formed into a sheet with a thickness of 0-3 m+ using a T-die extruder with a cylinder diameter of 60 mm. (Sheet B). Next, magnesium hydroxide (product name: Kisuma 4)
A.F.

粒径0.6μ、協和化学社#)100fに対し10f(
10PHR)のジオクチルフタレートで表面処理された
もの55wt%とポリプロピレン45wtXより成るペ
レット状組成物を同上の押出機で厚さ7011でJil
t出なが[)、上記シートBと押出ラミネーション7云
によりニソグしながら積層状となした。
Particle size 0.6μ, Kyowa Kagakusha #) 10f (
A pellet composition consisting of 55 wt % of dioctyl phthalate (10 PHR) surface treated and 45 wt % of polypropylene was extruded using the same extruder to a thickness of 7011 mm.
Then, the sheet B was laminated with the sheet B by extrusion lamination 7.

得られた積層シートを次いで実験用延伸機で縦方向に8
00で2.5倍に、横方向に160Lで2.5倍に遂次
延伸した。延伸シートは厚さ0.25%、空隙率78%
9通気度60秒。
The resulting laminated sheet was then stretched in the longitudinal direction by an experimental stretching machine.
It was successively stretched 2.5 times at 00 and 2.5 times at 160 L in the transverse direction. The stretched sheet has a thickness of 0.25% and a porosity of 78%.
9 Air permeability 60 seconds.

最大細孔径0.8μであり、従来にない微JLを有し、
高い透過性のある微多孔質シートであった。
The maximum pore diameter is 0.8μ, and it has an unprecedented micro JL,
It was a microporous sheet with high permeability.

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

第1図は本発明の実施例に示した微多孔シートの(B)
層側表面の電子顕微鏡写真を、第2図は同様に(A)層
側表面を示す。 特許出願人 徳山曹達株式会社
Figure 1 shows (B) the microporous sheet shown in the example of the present invention.
Similarly, FIG. 2 shows an electron micrograph of the layer side surface (A). Patent applicant Tokuyama Soda Co., Ltd.

Claims (1)

【特許請求の範囲】 1)粒径1μ以下の充填剤を含む熱可塑性樹脂シー) 
(A)と上記粒径より大なる充填剤を含む熱可塑性樹脂
ソート(B)とをラミネートした後、延伸することを特
徴とする微多孔シートの製造方法 2)  (B)シートの厚みが(A)シートの6倍以上
である特許請求の範囲第」項記載の製造方法3)熱可塑
性樹脂シート(A)まだは(B)に充填剤が60〜80
重景9(重量れる特許請求の範囲第1項記載の製造方法
[Claims] 1) Thermoplastic resin sheet containing a filler with a particle size of 1 μ or less)
(A) and a thermoplastic resin sort (B) containing a filler larger than the above particle size are laminated and then stretched. 2) (B) The thickness of the sheet is ( 3) Thermoplastic resin sheet (A) still has a filler content of 60 to 80% (B)
Heavy view 9 (manufacturing method according to claim 1)
JP21384482A 1982-12-08 1982-12-08 Production of microporous sheet Granted JPS59105035A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21384482A JPS59105035A (en) 1982-12-08 1982-12-08 Production of microporous sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21384482A JPS59105035A (en) 1982-12-08 1982-12-08 Production of microporous sheet

Publications (2)

Publication Number Publication Date
JPS59105035A true JPS59105035A (en) 1984-06-18
JPH0238098B2 JPH0238098B2 (en) 1990-08-29

Family

ID=16645951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21384482A Granted JPS59105035A (en) 1982-12-08 1982-12-08 Production of microporous sheet

Country Status (1)

Country Link
JP (1) JPS59105035A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6358602U (en) * 1986-10-03 1988-04-19
JPH0277108A (en) * 1987-07-04 1990-03-16 Toray Ind Inc Electrolyte separator
US5762840A (en) * 1996-04-18 1998-06-09 Kimberly-Clark Worldwide, Inc. Process for making microporous fibers with improved properties
JP2002201298A (en) * 2000-10-30 2002-07-19 Sumitomo Chem Co Ltd Porous film, battery separator and battery
WO2008117840A1 (en) * 2007-03-23 2008-10-02 Sumitomo Chemical Company, Limited Porous film

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4953961A (en) * 1972-09-28 1974-05-25
JPS523666A (en) * 1975-06-25 1977-01-12 Mitsubishi Plastics Ind Manufacturing of synthetic paper

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4953961A (en) * 1972-09-28 1974-05-25
JPS523666A (en) * 1975-06-25 1977-01-12 Mitsubishi Plastics Ind Manufacturing of synthetic paper

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6358602U (en) * 1986-10-03 1988-04-19
JPH0277108A (en) * 1987-07-04 1990-03-16 Toray Ind Inc Electrolyte separator
US5762840A (en) * 1996-04-18 1998-06-09 Kimberly-Clark Worldwide, Inc. Process for making microporous fibers with improved properties
JP2002201298A (en) * 2000-10-30 2002-07-19 Sumitomo Chem Co Ltd Porous film, battery separator and battery
WO2008117840A1 (en) * 2007-03-23 2008-10-02 Sumitomo Chemical Company, Limited Porous film
EP2133387A1 (en) * 2007-03-23 2009-12-16 Sumitomo Chemical Company, Limited Porous film
EP2133387A4 (en) * 2007-03-23 2011-10-19 Sumitomo Chemical Co Porous film
US8323837B2 (en) 2007-03-23 2012-12-04 Sumitomo Chemical Company, Limited Porous film

Also Published As

Publication number Publication date
JPH0238098B2 (en) 1990-08-29

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