JPS61146321A - Permselective compound membrane for gas - Google Patents
Permselective compound membrane for gasInfo
- Publication number
- JPS61146321A JPS61146321A JP59269757A JP26975784A JPS61146321A JP S61146321 A JPS61146321 A JP S61146321A JP 59269757 A JP59269757 A JP 59269757A JP 26975784 A JP26975784 A JP 26975784A JP S61146321 A JPS61146321 A JP S61146321A
- Authority
- JP
- Japan
- Prior art keywords
- layer
- thin polymer
- gas permeable
- composite membrane
- permeable composite
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/70—Polymers having silicon in the main chain, with or without sulfur, nitrogen, oxygen or carbon only
- B01D71/701—Polydimethylsiloxane
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は気体分離に使用される選択気体透過性複合膜に
関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to selective gas permeable composite membranes used for gas separation.
従来の技術
気体分離膜として均質な高分子の超薄膜を利用すること
は、従来の深冷液化法や吸着剤を用いての吸着分離法等
に比較して、コスト面や取シ扱い面での利点があり最近
注目を集めている。その中でも特に空気中より酸素を濃
縮する酸素富化膜に関して興味がもたれている。Conventional technology The use of homogeneous ultra-thin polymer membranes as gas separation membranes is less expensive and easier to handle than conventional cryogenic liquefaction methods or adsorption separation methods using adsorbents. It has been attracting attention recently due to its advantages. Among these, there is particular interest in oxygen enrichment membranes that concentrate oxygen from air.
この酸素富化膜はすでに一部実用化され、1つは酸素富
化燃焼システムへの応用であり、もう1つは医療用の酸
素富化装置である。ここで前者の膜の特徴は、気体分離
性(酸素と窒素の)が小さいが気体透過性が太きいとい
うことであり、後者は気体透過性は小さいが、気体分離
性が太きいということである。この様な差はその用途に
より必然的に決定嘔れるものであるが気体分離性が高く
、かつ気体透過性の優れる材料がないことも起因してい
る。もしこの両方の特性を満足するものが開発されれば
、用途により限定されない活気的な膜となることができ
、その市場も非常に拡大する。This oxygen-enriching membrane has already been put into practical use in some cases, one being in an oxygen-enriching combustion system and the other being an oxygen-enriching device for medical use. The characteristics of the former membrane are that it has low gas separation (oxygen and nitrogen) but high gas permeability, and the latter has low gas permeability but high gas separation. be. Although such a difference is inevitably determined by the intended use, it is also due to the lack of a material that has high gas separation properties and excellent gas permeability. If a film that satisfies both of these properties is developed, it will become a vibrant film that is not limited by use, and its market will expand significantly.
発明が解決しようとする問題点
これらの問題点を解決するため、最近高分子薄膜中KM
晶全全ブレンドた膜の開発や、シリコ−系モノマーのプ
ラズマ重合膜の複合膜等の報告があるが、その特性は、
いづれも分離性は高くなるが透過性が低く、また膜の耐
久性面でも問題を残している。Problems to be Solved by the Invention In order to solve these problems, recently KM in polymer thin films has been developed.
There have been reports on the development of a fully crystalline blended membrane and a composite membrane of a plasma-polymerized membrane of silicone monomers, but their characteristics are
In either case, the separation performance is high, but the permeability is low, and problems remain in terms of membrane durability.
そこで本発明の目的は、複合膜の特性が従来のシリコー
ン系の複合膜に対応する高気体透過性をもち、かつ気体
の分離性を向上することである。Therefore, an object of the present invention is to provide a composite membrane with high gas permeability corresponding to conventional silicone-based composite membranes and to improve gas separation performance.
問題点を解決するための手段
本発明は多孔質支持体と均質な高分子超薄膜からなる選
択気体透過性複合膜の均質な高分子超薄膜部分を2層構
造とし、更に多孔質支持体と接する第1層上に設けられ
た第2層がアセチレン系高分子よりなるものとしたので
、気体透過性が大きく、かつ分離性も酸素と窒素で2・
6〜4・6(酸素。Means for Solving the Problems The present invention provides a two-layer structure for the homogeneous ultra-thin polymer film portion of a selective gas permeable composite membrane consisting of a porous support and a homogeneous ultra-thin polymer film. Since the second layer provided on the first layer in contact with the first layer is made of acetylene-based polymer, it has high gas permeability and separation property of 2.
6-4.6 (oxygen.
室累の透過係数比)と非常に優れる膜を実現した。We have achieved a membrane with an extremely superior permeability coefficient ratio).
作用
本発明における均質な高分子超薄膜の特徴は2層構造を
有することである。この時の効果はまず第1にそれぞれ
の層単独では出現しない高気体透過性と高分離性が得ら
れる。第2にそれぞれの層にピンホールもしくは欠陥が
存在していても、複合化により十分な特性が得られる。Function: The homogeneous ultra-thin polymer film of the present invention is characterized by having a two-layer structure. The first effect in this case is that high gas permeability and high separability can be obtained, which cannot be achieved with each layer alone. Second, even if there are pinholes or defects in each layer, sufficient properties can be obtained by combining the layers.
第3に支持体。Thirdly, the support.
第1層、第2層それぞれの間の接着性が優れ、製膜が非
常に簡単である。特にアセチレンのようなガラス転位の
高く、硬い高分子の場合欠陥が出来やすく、2Nの上に
さらにオーバーコートが必要と思われたが、本発明の構
成ではその必要がなく、かつ優れた気体透過特性を示す
選択気体透過性複合膜が得られた。Adhesion between the first layer and the second layer is excellent, and film formation is very simple. In particular, in the case of hard polymers with high glass transitions such as acetylene, defects are likely to occur and an additional overcoat on top of 2N was thought to be necessary, but with the structure of the present invention, this is not necessary and excellent gas permeability is achieved. A selective gas permeable composite membrane exhibiting properties was obtained.
本発明の高分子超薄膜の多孔質支持体と接する第1層と
しては、ポリオルガノシロキサン、ポリオルガノシロキ
サンとの共重合体、ポリジメチルシロキサン、ポリジメ
チルシロキサンの架橋体。The first layer in contact with the porous support of the ultra-thin polymer film of the present invention is polyorganosiloxane, a copolymer with polyorganosiloxane, polydimethylsiloxane, or a crosslinked product of polydimethylsiloxane.
ポリヒドロキシスチレン−ポリジメチルシロキサン共重
合体、ポリヒドロキシスチレン−ポリスルホン−ポリジ
メチルシロキサン3元共重合体、ポリジメチルシロキサ
ンのブロック共重合体が望ましく、第2層としてはアセ
チレン系高分子超薄膜で一般式が
(但しR1は水素原子またはメチル基、エチル基等のア
ルキル基もしくは塩素、フッ素等の)・ロゲン原子、R
2は炭素数が1から5個までの直鎖もしくは枝別れした
アルキル基またはフェニル基、さらには−8i (CH
s)s + −Si ((zH”s) s等のトリアル
キルシリル基)で示さ汎るアセチレン系高分子を主成分
とする層である。Polyhydroxystyrene-polydimethylsiloxane copolymer, polyhydroxystyrene-polysulfone-polydimethylsiloxane ternary copolymer, and polydimethylsiloxane block copolymer are desirable, and as the second layer, an acetylene polymer ultrathin film is generally used. The formula is (where R1 is a hydrogen atom or an alkyl group such as a methyl group or an ethyl group, or a chlorine or fluorine atom), a rogene atom, R
2 is a linear or branched alkyl group having 1 to 5 carbon atoms or a phenyl group, and -8i (CH
s) This is a layer mainly composed of an acetylene polymer represented by s + -Si (trialkylsilyl group such as (zH''s) s).
そして、この複合膜で均質な超薄膜部分の厚さは0.0
1μm−0,20μmの範囲が好適である。また均質な
高分子超薄膜部分の各層は多層構造になればなる程ピン
ホール性が防止でき分離性の向上した膜となる。The thickness of the homogeneous ultra-thin film part of this composite film is 0.0
A range of 1 μm to 0.20 μm is preferred. Furthermore, the more the layers of the homogeneous ultra-thin polymer film portion have a multilayer structure, the more pinholes can be prevented and the separation properties of the film can be improved.
実施例 以下に本発明の実施例を図面を用いて説明する。Example Embodiments of the present invention will be described below with reference to the drawings.
〔実施例1〕
図に本発明の一実施例における選択気体透過性複合膜の
断面図を示す。[Example 1] The figure shows a cross-sectional view of a selective gas permeable composite membrane in an example of the present invention.
図において、1は多孔質支持体、2は多孔質支持体1に
直接接着している第1層の高分子超薄膜、3はその上に
設けられた第2層の高分子超薄膜であり、2層構造とし
たところが特徴である。In the figure, 1 is a porous support, 2 is a first layer of an ultra-thin polymer film directly adhered to the porous support 1, and 3 is a second layer of an ultra-thin polymer film provided thereon. , is characterized by its two-layer structure.
ところで多孔質支持体として、ジュラガード2400(
ポリプラスチック社製)を、均質膜材料としてポリジメ
チルシロキサン(東しシリコーン 5R−410)’i
i用いて、単一材料での複合膜を作成した。高分子の超
薄膜の製造は、ポリジメチルシロキサン:PDMSの1
0 wt%ベンゼン溶液を調整後この溶液を水面上に滴
下し、自発的に水面上に拡がった超薄膜上に支持体を接
触することにより得たOPDMSの膜厚の調整は、水面
上への溶液の滴下量で制御し、結果的に第1表の特性の
複合膜を得た。By the way, as a porous support, Duragard 2400 (
Polydimethylsiloxane (Toshi Silicone 5R-410) was used as a homogeneous film material.
A composite membrane made of a single material was created using i. The production of ultra-thin films of polymers is based on polydimethylsiloxane: PDMS.
After preparing a 0 wt% benzene solution, this solution was dropped onto the water surface, and the OPDMS film thickness was adjusted by contacting the ultra-thin film that spontaneously spread on the water surface with the support. The amount of solution added was controlled, and as a result, a composite membrane having the characteristics shown in Table 1 was obtained.
第1表 水面の面積は30×3Ocmで行なった。Table 1 The area of the water surface was 30 x 30 cm.
この様にPDMS単独では気体透過性は大きくなるが、
分離性は低く、約2.0で飽和してしまう。In this way, PDMS alone increases gas permeability, but
Separability is low and saturates at about 2.0.
また次に多孔質支持体はジュラガード2400を用い、
均質な高分子超薄膜材料としてはポIJ )リメチルシ
リルプロビン(Mw中120万):PMS Pi用いた
。この材料はトリメチルシリルプロピン(チッソ株社製
)モノマーを6塩化タンタル触媒により重合して得た。Next, the porous support uses Duraguard 2400,
Polymethylsilylprobin (Mw: 1.2 million): PMS Pi was used as a homogeneous ultra-thin polymer film material. This material was obtained by polymerizing trimethylsilylpropyne (manufactured by Chisso Corporation) monomer using a tantalum hexachloride catalyst.
この材料の2重量%のベンゼン溶液を調整し、前記PD
MSの場合と同様にして、水面上の溶液を滴下してPM
SPの超薄膜を作製した。この水面上の薄膜に多孔質支
持体を接触したが接着性が悪く複合化できないため、真
空に吸引して複合化した。また膜厚の制御は同一の膜を
積層することにより行なった。この様にして得られた複
合膜の特性を第2表に示した。A 2% by weight benzene solution of this material was prepared and the PD
In the same way as for MS, drop the solution on the water surface to remove PM.
An ultra-thin film of SP was fabricated. A porous support was brought into contact with this thin film on the water surface, but the adhesion was poor and it was not possible to form a composite, so the film was vacuum-suctioned to form a composite. Further, the film thickness was controlled by laminating identical films. The properties of the composite membrane thus obtained are shown in Table 2.
第2表に示すようにこの材料は気体透過性は非常に優れ
るが、酸素と窒素の分離比は小さく約1.6〜2・5の
範囲であった。As shown in Table 2, this material had very good gas permeability, but the oxygen to nitrogen separation ratio was small, ranging from about 1.6 to 2.5.
第2表
このように、PDMS、PMSPそれぞれ単独の気体透
過特性は、いずれの場合も気体透過性は優れるが気体の
分離性が低く、酸素、窒素の分離比で約2・4の値が最
高である。As shown in Table 2, the gas permeability properties of PDMS and PMSP are excellent in both cases, but the gas separation is low, with the highest value of approximately 2.4 for the oxygen and nitrogen separation ratio. It is.
そこで図に示すように多孔質支持体1上にまず第1層2
としてPDMSfjI:接着した後、次いで第2層3と
してPMSPi積層してその気体透過性を測定した所、
酸素の透過速度は1・31×1O−1cc/sec−(
y−atm 、酸素と窒素の分離比は3.2と単独の材
料では考えられない高い分離性を示した。Therefore, as shown in the figure, a first layer 2 is first formed on a porous support 1.
PDMSfjI: After adhesion, PMSPi was laminated as the second layer 3 and its gas permeability was measured.
The oxygen permeation rate is 1.31×1O-1cc/sec-(
y-atm, the separation ratio of oxygen and nitrogen was 3.2, showing a high separation performance that would be unimaginable with a single material.
〔実施例2〕
実施例1と同様に、高分子超薄膜層を2層構造とし、第
1層2にポリヒドロキシスチレン(PH8)−ポリスル
ホン(PS) −PDMS共重合体を、第2層3にPM
SPを用いて、複合膜を製造した。その結果は実施例1
と同様に酸素透過速度は1−82 X 10 cc/
sec−−4tmと大きく、かつ酸素と窒素の分離性は
2.80と非常に高くなった以上、実施例ではアセチレ
ン系高分子としてPMSPを、シリコーン系材料として
PDMS、PH8−PS−PDMS共重合体について示
したがその他のアセチレン系高分子でもまた、シリコー
ン系材料でもその物性、気体透過性は類似しており、同
様の効果が出ることは当該業者が容易に類推できるもの
である。[Example 2] Similar to Example 1, the ultra-thin polymer film layer had a two-layer structure, the first layer 2 was made of polyhydroxystyrene (PH8)-polysulfone (PS)-PDMS copolymer, and the second layer 3 was made of polyhydroxystyrene (PH8)-polysulfone (PS)-PDMS copolymer. PM to
A composite membrane was manufactured using SP. The result is Example 1
Similarly, the oxygen permeation rate is 1-82 x 10 cc/
sec--4tm, and the separability of oxygen and nitrogen is very high at 2.80, so in the example, PMSP was used as the acetylene polymer, PDMS was used as the silicone material, and PH8-PS-PDMS copolymer was used. Although the combination is shown above, other acetylene polymers and silicone materials have similar physical properties and gas permeability, and those skilled in the art can easily infer that similar effects can be obtained.
発明の効果
以上要するに本発明は、多孔質支持体と、その上に設け
られた均質な高分子薄膜が2層構造を有し、更に第2層
がアセチレン系高分子よりなることを特徴とするもので
、単一材料では得られない高気体透過性と気体分離性が
得られる利点を有する0Effects of the Invention In summary, the present invention is characterized in that a porous support and a homogeneous thin polymer film provided thereon have a two-layer structure, and the second layer is made of an acetylene polymer. It has the advantage of providing high gas permeability and gas separation properties that cannot be obtained with a single material.
図は本発明の第1の実施例における選択気体透過性複合
膜の断面図である。
1・・・・・・多孔質支持体、2・・・・・・第1層の
高分子超薄膜、3・・・・・・第2層の高分子超薄膜。The figure is a sectional view of a selective gas permeable composite membrane in a first embodiment of the present invention. DESCRIPTION OF SYMBOLS 1...Porous support, 2...1st layer ultra-thin polymer film, 3...2nd layer ultra-thin polymer film.
Claims (9)
た均質な高分子超薄膜とを備え、前記高分子超薄膜が2
層構造を有し、多孔質支持体と接する第1層上に設けら
れた第2層がアセチレン系高分子よりなることを特徴と
する選択気体透過性複合膜。(1) A porous support and a homogeneous ultra-thin polymer film provided on the porous support, wherein the ultra-thin polymer film has two
1. A selective gas permeable composite membrane having a layered structure, wherein a second layer provided on the first layer in contact with a porous support is made of an acetylene polymer.
キサンもしくはポリオルガノシロキサンとの共重合体で
ある特許請求の範囲第1項記載の選択気体透過性複合膜
。(2) The selective gas permeable composite membrane according to claim 1, wherein the first layer of the homogeneous ultra-thin polymer membrane is a polyorganosiloxane or a copolymer with a polyorganosiloxane.
キサンもしくはポリジメチルシロキサンの架橋体を主成
分とすることを特徴とする特許請求の範囲第1項記載の
選択気体透過性複合膜。(3) The selective gas permeable composite membrane according to claim 1, wherein the first layer of the homogeneous ultra-thin polymer membrane contains polydimethylsiloxane or a crosslinked polydimethylsiloxane as a main component.
チレン−ポリジメチルシロキサン共重合体である特許請
求の範囲第1項記載の選択気体透過性複合膜。(4) The selective gas permeable composite membrane according to claim 1, wherein the first layer of the homogeneous ultra-thin polymer membrane is a polyhydroxystyrene-polydimethylsiloxane copolymer.
チレン−ポリスルホン−ポリジメチルシロキサン3元共
重合体を主成分とする特許請求の範囲第1項記載の選択
気体透過性複合膜。(5) The selective gas permeable composite membrane according to claim 1, wherein the first layer of the homogeneous ultra-thin polymer membrane contains a polyhydroxystyrene-polysulfone-polydimethylsiloxane terpolymer as a main component.
キサンのブロック共重合体である特許請求の範囲第1項
記載の選択気体透過性複合膜。(6) The selective gas permeable composite membrane according to claim 1, wherein the first layer of the homogeneous ultra-thin polymer membrane is a block copolymer of polydimethylsiloxane.
化学式、表等があります▼ (但しR_1は水素原子またはメチル基、エチル基等の
アルキル基もしくは塩素、フッ素等のハロゲン原子、R
_2は炭素数が1から5個までの直鎖もしくは枝別れし
たアルキル基またはフェニル基さらには−Si(CH_
3)_3、−Si(C_2H_5)_3等のトリアルキ
ルシリル基)で示されるアセチレン系高分子を主成分と
することを特徴とする特許請求の範囲第1項記載の選択
気体透過性複合膜。(7) The general formula for the second layer of a homogeneous ultra-thin polymer film is ▲Math.
There are chemical formulas, tables, etc.▼ (However, R_1 is a hydrogen atom, an alkyl group such as a methyl group or an ethyl group, or a halogen atom such as chlorine or fluorine, R
_2 is a linear or branched alkyl group having 1 to 5 carbon atoms or a phenyl group, or -Si(CH_
3) The selective gas permeable composite membrane according to claim 1, characterized in that the main component is an acetylene polymer represented by a trialkylsilyl group such as _3 or -Si(C_2H_5)_3.
0.20μmの範囲であることを特徴とする特許請求の
範囲第1項記載の選択気体透過性複合膜。(8) The thickness of the homogeneous ultra-thin polymer film layer is 0.01 μm or more
The selective gas permeable composite membrane according to claim 1, characterized in that the membrane has a thickness in the range of 0.20 μm.
多層構造を有していることを特徴とする特許請求の範囲
第1項記載の選択気体透過性複合膜。(9) The selective gas permeable composite membrane according to claim 1, wherein each of the first layer and the second layer of the homogeneous ultra-thin polymer membrane has a multilayer structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59269757A JPS61146321A (en) | 1984-12-20 | 1984-12-20 | Permselective compound membrane for gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59269757A JPS61146321A (en) | 1984-12-20 | 1984-12-20 | Permselective compound membrane for gas |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61146321A true JPS61146321A (en) | 1986-07-04 |
JPH0421528B2 JPH0421528B2 (en) | 1992-04-10 |
Family
ID=17476724
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59269757A Granted JPS61146321A (en) | 1984-12-20 | 1984-12-20 | Permselective compound membrane for gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61146321A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4859215A (en) * | 1988-05-02 | 1989-08-22 | Air Products And Chemicals, Inc. | Polymeric membrane for gas separation |
US5176724A (en) * | 1987-11-10 | 1993-01-05 | Matsushita Electric Industrial Co., Ltd. | Permselective composite membrane having improved gas permeability and selectivity |
US5356461A (en) * | 1990-11-28 | 1994-10-18 | Akzo N.V. | Gas separation membrane |
US5707423A (en) * | 1996-06-14 | 1998-01-13 | Membrane Technology And Research, Inc. | Substituted polyacetylene separation membrane |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61107922A (en) * | 1984-10-30 | 1986-05-26 | Sanyo Chem Ind Ltd | Composite membrane for gas separation |
-
1984
- 1984-12-20 JP JP59269757A patent/JPS61146321A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61107922A (en) * | 1984-10-30 | 1986-05-26 | Sanyo Chem Ind Ltd | Composite membrane for gas separation |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5176724A (en) * | 1987-11-10 | 1993-01-05 | Matsushita Electric Industrial Co., Ltd. | Permselective composite membrane having improved gas permeability and selectivity |
US4859215A (en) * | 1988-05-02 | 1989-08-22 | Air Products And Chemicals, Inc. | Polymeric membrane for gas separation |
US5356461A (en) * | 1990-11-28 | 1994-10-18 | Akzo N.V. | Gas separation membrane |
US5707423A (en) * | 1996-06-14 | 1998-01-13 | Membrane Technology And Research, Inc. | Substituted polyacetylene separation membrane |
Also Published As
Publication number | Publication date |
---|---|
JPH0421528B2 (en) | 1992-04-10 |
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