JPS58185629A - Production of microporous membrane - Google Patents

Production of microporous membrane

Info

Publication number
JPS58185629A
JPS58185629A JP6924582A JP6924582A JPS58185629A JP S58185629 A JPS58185629 A JP S58185629A JP 6924582 A JP6924582 A JP 6924582A JP 6924582 A JP6924582 A JP 6924582A JP S58185629 A JPS58185629 A JP S58185629A
Authority
JP
Japan
Prior art keywords
electrolyte
membrane
synthetic resin
foaming
film
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
JP6924582A
Other languages
Japanese (ja)
Inventor
Masao Nakajima
正雄 中島
Takahiro Fujio
藤生 隆弘
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.)
Toppan Inc
Original Assignee
Toppan Printing Co Ltd
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 Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP6924582A priority Critical patent/JPS58185629A/en
Publication of JPS58185629A publication Critical patent/JPS58185629A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To obtain a waterproof membrane having air and moisture permeability in a simple and inexpensive manner, by foaming a synthetic resin membrane in which a blowing agent and an electrolyte are uniformly dispersed and immersing the membrane in water to dissolve the electrolyte. CONSTITUTION:A mixture obtained by uniformly dispersing a blowing agent 3 and an electrolyte 4 in a synthetic resin is applied to the surface of a fiber substrate 1 to form a synthetic resin membrane 2, which then is foamed. In this foaming, the electrolyte 4 readily serves as foaming nuclei, so that open cells are formed about the electrolyte. When this is immersed in water to dissolve the electrolyte 4, the pores occupied by the electrolyte and the micropores of the blowing agent 3 are formed and form continuous pores, so that a membrane having micropores necessary to render the membrane air-permeable can be made. Formation of the synthetic resin membrane can be carried out by coating, melt extrusion or the like.

Description

【発明の詳細な説明】 本発明は、倣細な孔を4:iする合成樹脂皮膜の製造方
法に関イろものである。さらに詳しくは、通気性、透湿
性を有する防水性皮膜の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a synthetic resin film having 4:i narrow pores. More specifically, the present invention relates to a method for producing a waterproof film having air permeability and moisture permeability.

従来より、微細孔を有する皮膜の製造方法とし\ てン四弗化エチレン樹脂を用いて未焼成のフィルムyつ
くり、これヲ腫、速に延伸して、フィブリル化した多孔
質体をつくる方法や、浴剤系ウレタン但j月百を稙維華
拐V(コーティングし1こ債、ジメチルホルムアミド等
の極性有機浴剤を含む水系凝固浴中で脱溶剤をしながら
樹脂を凝固させることにより皮膜中に微細孔乞形成させ
る方法や、発泡きせ1こ水系樹脂をスクリーンコーティ
ングすることにより微細な気泡を含む皮膜を形成きせる
方法、又合成樹脂中に発泡剤ン混合し、発泡させ、微細
な気泡ン含む皮膜を形成する方法等がある。
Conventionally, methods for producing films with micropores include creating an unfired film using tetrafluoroethylene resin and rapidly stretching it to create a fibrillated porous body. The coating is formed by coagulating the resin while removing the solvent in an aqueous coagulation bath containing a polar organic bath such as dimethylformamide. A method of forming fine pores in a synthetic resin, a method of forming a film containing fine air bubbles by screen coating a foamed aqueous resin, and a method of forming a film containing fine air bubbles by mixing a foaming agent into a synthetic resin and foaming it. There are methods of forming a film containing

しかし従来より仰られているこれらの方法は、樹脂か高
価であること、又特殊な製造装置が必要であったり、又
浴剤系ウレタン樹脂を用(・て湿式凝固による方法では
、製造上、作業性ン不安定にする要素を多く含んでおり
、微細孔を有する皮膜形成の再現性を得る為には、きわ
めて煩雑な操作及び厳密な工程、管理を必要とし、又極
性有機浴剤を水中にて抽出する為、廃液処理に美大な費
用を必要とするなど、公害対策等の問題がある。一方、
単に発泡剤馨用い1こ方法では、微細孔乞皮膜表面及び
内部に均一に%ることは難しく、十分な通気性を得るこ
とは困難であり、簡易な通気性、透湿性を有する防水性
皮膜の製造方法の開発か切宅されていた。
However, in these conventional methods, the resin is expensive, special manufacturing equipment is required, and wet coagulation methods require bath agent-based urethane resins. It contains many elements that make workability unstable, and in order to reproducibly form a film with micropores, extremely complicated operations and strict processes and controls are required. There are problems with pollution control, such as the huge expense required for waste liquid treatment.On the other hand,
If this method simply uses a foaming agent, it is difficult to distribute the micropores uniformly on the surface and inside of the film, and it is difficult to obtain sufficient air permeability. The development of a manufacturing method was being developed.

不発ψ(は、この様な従来の問題を1瀘すべく考案され
1こもので、極めて簡単にかつ安価に作成できろ通気性
、透湿性、防水性皮膜の製造方法を提供するものである
The non-explosion ψ() was devised to solve these conventional problems and provides a method for producing an air-permeable, moisture-permeable, and waterproof film that can be produced extremely easily and at low cost.

即ち不発ψ]は予め合成樹脂中に微細に粉末化し1こ熱
により分解しガスを発生する薬剤(発泡剤)と電#質を
均一分散した混合物を用いて皮膜状に形成し、発泡させ
た後、水中に浸漬し、電解實馨浴出きせることにより合
成樹脂皮膜中に微細な孔を作ることを特徴とする有孔膜
作成方法である。
In other words, unexploded ψ] is made into a fine powder in a synthetic resin and then formed into a film using a mixture of a chemical (foaming agent) that decomposes and generates gas upon heating (foaming agent) and an electrolyte uniformly dispersed therein, and then foamed. This method is characterized in that fine pores are created in the synthetic resin film by immersing it in water and exposing it to an electrolytic bath.

一般に、単に発泡剤ン用いて合成m脂を発泡させ1こだ
けでは独立気泡が多く、又樹脂皮膜内部に気泡が集中し
、表向に於いては発泡か不十分であり、通気性、透湿性
を得るのは非常に離しかった。
In general, if a synthetic m resin is simply foamed using a blowing agent, there will be many closed cells, and the air bubbles will be concentrated inside the resin film, resulting in insufficient foaming on the surface and poor air permeability. It was very hard to get wet.

本発明は発泡剤と電解質を併用することにより発泡径水
中にて″ilt解質を浴出させることにより、合成樹脂
の表面及び内部に均一に微細な孔を形成イることができ
、通気性、透漫性及び防水性を有する皮膜形成を簡単に
つくることを0丁能とし1こ。
In the present invention, by using a foaming agent and an electrolyte in combination, it is possible to form fine pores uniformly on the surface and inside of the synthetic resin by bathing out the "ilt solute in foaming water", thereby making it possible to create air permeability. Our goal is to easily form a film that is permeable and waterproof.

以下図面を用いて詳細に説明する。第1図に於いて(イ
)の(りは織物、4Ii8v1:Jなどがら成る繊維基
体を示し、■は基体布帛■土に形成された合成樹脂皮膜
を示す。■は合成皮膜中に一定音、均一分散された微細
な発泡剤ン示し、■は■と同様に一定閂、均一分散され
た微細な無機電解質を示イ。次に(イ)なる構成物を加
熱し、発泡剤■を分解し発泡させる。この時、電解質■
は発泡の核となり易く、電解質(4)?中心として連続
気泡をつくる。
This will be explained in detail below using the drawings. In Fig. 1, (A) indicates a fiber base made of fabric, 4Ii8v1:J, etc., and ■ indicates a synthetic resin film formed on the base fabric and soil.■ indicates a constant sound in the synthetic film. , indicates a fine blowing agent that is uniformly dispersed, and ■ indicates a fine inorganic electrolyte that is uniformly dispersed with a constant bar as in ■.Next, the composition of (a) is heated to decompose the blowing agent ■. and foam.At this time, electrolyte ■
tends to become the nucleus of foaming, and electrolyte (4)? Create an open cell at the center.

(ロ)は発泡後の状態を示す。(4)′は発泡剤りの発
泡後の状態を示イ。その後水中に浸漬し、電解質■馨俗
出すると←Jの様に電解質■が存在していた孔と、発泡
剤■の微細な孔が共存し、連続した孔をつくり、通気性
乞有する為の微細孔2有する皮膜■′をつくることがで
きる。ここで、通常知られている事実として霧雨時の水
滴は直径約iooミクロン程度、又雷雨時のそれは30
00ミクロン程度とされている。これに対し、空気、水
蒸気のそれはo、 o o o 4ミクロン程度とされ
ている。従って本発明に使用する発泡後の発泡剤および
1t′MIJ!粉末の粒径’k 0.1〜15ミクロン
程度にすることにより、由等の水滴は遮断するが、空気
、水蒸気はfiI過する有孔膜馨再ることができる。し
かしより良い防水性?得ようとすれば1oξクロン以下
V(倣卸jに粉末化した方が良い。
(b) shows the state after foaming. (4)' shows the state of the foaming agent after foaming. After that, it is immersed in water and when the electrolyte ■ is extracted, the pores where the electrolyte ■ was present coexist with the fine pores of the foaming agent ■, creating continuous pores and improving air permeability. It is possible to create a film ``■'' having 2 micropores. Here, it is a commonly known fact that the diameter of water droplets during drizzle is about 100 microns, and that during a thunderstorm is 30 microns in diameter.
It is said to be about 0.00 microns. On the other hand, that of air and water vapor is said to be about 4 microns. Therefore, the blowing agent used in the present invention and 1t'MIJ! By setting the particle size of the powder to about 0.1 to 15 microns, water droplets can be blocked, but air and water vapor can be recirculated through the perforated membrane. But better waterproofing? If you want to obtain it, it is better to powder it to less than 1 oξ chron V (imitation wholesaler).

本発明に述べる皮膜形成用の合成樹脂としては通常のヨ
ー1イング加工やラミネート加工に用い「ンれるウレタ
ン樹脂、アクリル系樹脂、ポリアミド糸樹脂、ポリエス
テル系樹脂等皮膜形成可能な樹脂であれば良く、皮膜形
成方法としてはコーティング方式、浴融押出し方式等い
ずれの方式でも良い。
The synthetic resin for film formation described in the present invention may be any resin that can form a film, such as urethane resin, acrylic resin, polyamide thread resin, polyester resin, etc., which can be used in normal yaw processing and lamination processing. As the film forming method, any method such as a coating method or a bath melt extrusion method may be used.

本発明に述べる発泡剤としては炭酸水素アンモニウム、
炭酸水素ナトリウム、炭酸アンモニウム、ヒドロキシメ
チルチオ尿素、又アンモニウムミョウバン等の各種言水
堪物質、ジアゾアミノベンゼン、アゾビスニトリル、ア
ゾビスイソブチルニトリルの様なアゾ化合物、ジニトロ
ンペンタメチレ/、テトラミンの様な1q−ニトロソ化
合物等通常用いられている発泡剤で良い。
The blowing agents mentioned in the present invention include ammonium hydrogen carbonate,
Various fluent substances such as sodium bicarbonate, ammonium carbonate, hydroxymethylthiourea, and ammonium alum, azo compounds such as diazoaminobenzene, azobisnitrile, azobisisobutylnitrile, dinitrone pentamethylene/tetramine, etc. A commonly used blowing agent such as a 1q-nitroso compound may be used.

本発明に述べる’#tm質としては、塩化ナトリウム、
塩化カルシウム、塩化マグネシウム等の金極堪系、各種
ミョウバン等水にょく俗解するものであればいずれも使
用可能である。
The '#tm qualities mentioned in the present invention include sodium chloride,
It is possible to use any metal that is commonly understood as water, such as calcium chloride, magnesium chloride, and various alums.

又、本発明第1図に於いて述べる織物、編物等の基体布
帛としてはポリアミド線維、ポリエステル線維、ポリエ
ステル/木綿混紡線維、木綿、アクリル繊維等いずれの
繊維にも使用できる。
Further, as the base fabric of the woven fabric, knitted fabric, etc. described in FIG. 1 of the present invention, any fiber such as polyamide fiber, polyester fiber, polyester/cotton blend fiber, cotton, acrylic fiber, etc. can be used.

又、防水布として使用するには予め繊維基体を7)素糸
、シリコーン系撥水剤を用いて撥水処理−すると一層効
果が上がる。
In addition, in order to use it as a waterproof cloth, the effect is further improved if the fiber base is previously subjected to 7) water repellent treatment using yarn or a silicone water repellent.

以下実施例を示t。Examples are shown below.

〈実施例−1〉 (1)ナイロン平織布(目付659 / rri”)に
下記する処理液(イ)にて、絞り率80%なる条件で絞
った後、100℃×2分間プレ乾燥を行い、さらに16
0℃の温度条件にて2分間キーアリングを行ない撥水処
理を行った。
<Example-1> (1) After squeezing a nylon plain woven fabric (fabric weight 659 / rri'') with the treatment solution (a) below at a squeezing rate of 80%, pre-drying at 100°C for 2 minutes and then 16 more
Water repellency treatment was performed by keying for 2 minutes at a temperature of 0°C.

(イ)処理液 D I COU A、 RI)  F −70・・−田
川・=  1%重量剖(犬日本インキ社製 7ノ素系撥
水剤)(2)次に、ZllKて得られTこナイロン平織
布K ’F記する処方(ロ)から成る発泡剤と電解質を
含有するウレタン糸コーティング剤η=17000CP
SICてWetで150.p/イバーコーターにて塗布
し、さらに85°Cにて2分間加熱し1こ。
(a) Treatment liquid DI COU A, RI) F -70...-Tagawa... = 1% weight analysis (7 elemental water repellent manufactured by Inu Nippon Ink Co., Ltd.) (2) Next, the T obtained by ZllK This nylon plain woven fabric K'F Urethane thread coating agent containing a foaming agent and an electrolyte consisting of the following formulation (b) = 17000CP
SIC and wet 150. Coat with a p/var coater and heat for 2 minutes at 85°C.

(口j処理液 OCRISVON  2016EL     100i
ii部(犬日本インキ社製 コーティング加工用ウレタ
ン皮膜ン0’CRISVON  ADDI’T”IVE
  No、5 5重量部(同社製 平面平滑剤) OCRISVOrリ NX            2
Mfir部(同社製 イソシアネート系架倫剤) o  CRISVON  Accel  JAM   
   1重1部(同社製 架搗促進剤) 0炭酸アンモニウム粉末          15]i
量部0塩化カルシウム粉末           15
]iB一部0メチルエチルケトン          
 30重1部(炭酸アンモニウム、塩化カルシウムの粉
末はあらかじめボールミルにて粉砕し平均粒径201〜
15ミクロンの範囲とし1こ。)この様に加熱し1こと
ころ、ウレタン皮膜は発泡による微細孔を有する皮膜が
得られた。
(J treatment liquid OCRISVON 2016EL 100i
Part ii (urethane film for coating process manufactured by Inu Nippon Ink Co., Ltd.)
No. 5 5 parts by weight (plane smoothing agent made by the same company) OCRISVOr NX 2
Mfir part (isocyanate-based crosslinking agent manufactured by the company) o CRISVON Accel JAM
1 weight 1 part (Creating accelerator made by the same company) 0 Ammonium carbonate powder 15]i
Part 0 Calcium chloride powder 15
] iB part 0 methyl ethyl ketone
30 weight 1 part (Ammonium carbonate and calcium chloride powders are ground in a ball mill in advance to obtain an average particle size of 201~
1 piece with a range of 15 microns. ) After heating in this manner, a urethane film having micropores due to foaming was obtained.

(3)さらに(2)によって得られ1こコーティング布
を40℃なる水の中に60分間浸漬し、塩化カルシウム
を浴出させ、90℃にて1分間オープン中にて乾燥した
ところ、独立気泡であった微細孔が連続化し、通気性、
透湿性とも良好な防水性を有する皮膜な得1こ。これに
よって得られ1こ布帛の通気性、及び防水性に関する測
定値は以下の様であっ1こ。
(3) Furthermore, one coated cloth obtained in (2) was immersed in water at 40°C for 60 minutes to remove calcium chloride, and dried at 90°C for 1 minute in the open, resulting in closed cell foam. The previously fine pores have become continuous, improving breathability and
The film has good moisture permeability and waterproof properties. The measured values regarding the breathability and waterproofness of the fabric thus obtained are as follows.

耐水圧: JIS L−1092(1977) 5.1
1.A(al静水圧法透湿度:  JIS Z−020
8(力7ブ法)通気度: JIS p−alll ゛実施例−2〉 (1)ポリエステル/木綿(55/35)なる混紡ブロ
ード布(目付100g/m’)に下記する処理液(イ)
を用い、実施例−1の如く前撥水処理を行った。
Water pressure resistance: JIS L-1092 (1977) 5.1
1. A (al hydrostatic pressure method moisture permeability: JIS Z-020
8 (force 7 method) Air permeability: JIS p-all ゛Example-2〉 (1) The following treatment solution (A) was applied to a polyester/cotton (55/35) blended broadcloth (fabric weight 100 g/m').
The pre-water repellent treatment was carried out as in Example-1.

(イ)処理液 D  J、  (’:    0  [I  A、 丁
(丁)   +1’ −70・・・・ ・ ・・  ・
−1%1番1111部水              
   ・・・・曲・・・・・99% 〃(2)さらにこ
の処理布に平滑性をもたせる為、カレンダーロールにて
30 kg /鵠なる圧カ榮件にて平滑性付与ケ行っ1
こ。
(B) Processing liquid D J, (': 0 [I A, Ding (Ding) +1' -70... . . .
-1% 1 No. 1111 parts water
...Song...99% 〃(2) Furthermore, in order to give smoothness to this treated cloth, smoothness was imparted using a calender roll with 30 kg of pressure.1
child.

(3)次に、(2)にて得られた処理布に下a1する処
方(ロ)から成る発泡剤と電解質を含有するウレタン系
コーティング剤をWet  で1509/m’バージー
ターにて塗布し、さらK 120 ℃にて2分間加熱し
1こところ発泡による微細孔を有する皮膜が得られた。
(3) Next, a urethane-based coating agent containing a foaming agent and an electrolyte made from the formulation (b) below a1 was applied wet to the treated fabric obtained in (2) using a 1509/m' burgeter. Then, the film was further heated at 120° C. for 2 minutes to obtain a film having micropores due to foaming.

10)処理液 0(4RISVON  2016EL、      1
00]ii部OfJRIsVON  ADDITIVE
  N05  5軍箪部QC)(ISVQN   NX
                   2   /1
0  CRISVON   Accel−HM    
     1   ttOアンモニウムミョウバン粉末
       15 〃0塩化ナトナトリウム粉末  
        15/10メチルエチルケトン   
        30 〃(塩化ナトリウムおよびアン
モニ・ツムミョウバンの粒径は実施例−1同様01〜1
5ミクロ/の範囲としTこ。) これらの混合液の粘度は21.0OOCPS(25°C
)であっ1こ。
10) Processing liquid 0 (4RISVON 2016EL, 1
00] ii part OfJRIsVON ADDITIVE
N05 5th army store QC) (ISVQN NX
2/1
0 CRISVON Accel-HM
1 ttO ammonium alum powder 15 〃0 Sodium chloride powder
15/10 methyl ethyl ketone
30 (The particle size of sodium chloride and ammonia alum is 01 to 1 as in Example-1.
The range is 5 microns/T. ) The viscosity of these mixed liquids is 21.0OOCPS (25°C
) and one.

(4)さらにi31に、にって得られ1こコーティング
布を23℃なる水の中に50分間浸漬し、塩化す) 1
ウムを浴出させ、90℃にて1分間オーブン中にて乾燥
したところ、実施例−1同様、独立気泡が連続化し、通
気性、透湿性かつ防水性を有する加工布を得fこ。
(4) Further, in step 131, the coated cloth obtained by the method was immersed in water at 23°C for 50 minutes to be salted) 1
When the foam was extracted and dried in an oven at 90° C. for 1 minute, the closed cells became continuous as in Example 1, and a processed fabric having air permeability, moisture permeability, and waterproofness was obtained.

こnKよって得られた布帛の通気性、及び防水性に関す
る測定値は以下の様である。
The measured values regarding the breathability and waterproofness of the fabric obtained by this nK are as follows.

耐水圧: 1s o aIlllIH2o/crd4f
W度: 5.00097m’、 24 hrs通気度=
06cc/sec/Cr!
Water pressure resistance: 1s o aIllIH2o/crd4f
W degree: 5.00097m', 24 hrs ventilation =
06cc/sec/Cr!

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

図面は本発明の実施例を示し、第1図イ)〜ヒ1Gま本
発明の1−程を示す断面図。 (し)・・繊維基体   (2)・・・合成樹脂皮膜(
倶・・発泡剤    q)・・・無機電解質、W許出願
人 凸版印刷株式会社 第1図
The drawings show embodiments of the present invention, and FIGS. (shi)...Fiber base (2)...synthetic resin film (
2...Blowing agent q)...Inorganic electrolyte, W Applicant: Toppan Printing Co., Ltd. Figure 1

Claims (1)

【特許請求の範囲】[Claims] (1)合成樹脂中に発泡剤と電解質を均一分散し1こ混
合91J乞皮膜状に形成し、発削場せた後、水中に浸漬
し、電解質を溶出させることにより合成樹脂皮膜中に倣
細な孔をつくることを特徴とする有孔層の製造方法。
(1) A foaming agent and an electrolyte are uniformly dispersed in a synthetic resin, mixed together to form a 91J film, placed in a cutting place, and then immersed in water to dissolve the electrolyte and imitate it into a synthetic resin film. A method for producing a porous layer characterized by creating fine pores.
JP6924582A 1982-04-24 1982-04-24 Production of microporous membrane Pending JPS58185629A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6924582A JPS58185629A (en) 1982-04-24 1982-04-24 Production of microporous membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6924582A JPS58185629A (en) 1982-04-24 1982-04-24 Production of microporous membrane

Publications (1)

Publication Number Publication Date
JPS58185629A true JPS58185629A (en) 1983-10-29

Family

ID=13397166

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6924582A Pending JPS58185629A (en) 1982-04-24 1982-04-24 Production of microporous membrane

Country Status (1)

Country Link
JP (1) JPS58185629A (en)

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