JPH04317734A - Gas separating composite membrane and its production - Google Patents
Gas separating composite membrane and its productionInfo
- Publication number
- JPH04317734A JPH04317734A JP8505591A JP8505591A JPH04317734A JP H04317734 A JPH04317734 A JP H04317734A JP 8505591 A JP8505591 A JP 8505591A JP 8505591 A JP8505591 A JP 8505591A JP H04317734 A JPH04317734 A JP H04317734A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- gas separation
- gas separating
- water
- laminated
- 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
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 76
- 239000002131 composite material Substances 0.000 title claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 238000000926 separation method Methods 0.000 claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- -1 polysiloxane chlorobutane Polymers 0.000 claims abstract description 14
- 229920002379 silicone rubber Polymers 0.000 claims abstract description 7
- 239000004945 silicone rubber Substances 0.000 claims abstract description 7
- 230000001681 protective effect Effects 0.000 claims description 27
- 229920001296 polysiloxane Polymers 0.000 claims description 14
- 229920000642 polymer Polymers 0.000 claims description 9
- 239000003960 organic solvent Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 abstract description 8
- 229920001577 copolymer Polymers 0.000 abstract description 6
- 125000003545 alkoxy group Chemical group 0.000 abstract description 4
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 abstract description 4
- 239000004695 Polyether sulfone Substances 0.000 abstract description 2
- 229920006393 polyether sulfone Polymers 0.000 abstract description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 abstract description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical group C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 abstract 1
- 235000013870 dimethyl polysiloxane Nutrition 0.000 abstract 1
- 239000004205 dimethyl polysiloxane Substances 0.000 abstract 1
- 239000008246 gaseous mixture Substances 0.000 abstract 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 45
- 239000010408 film Substances 0.000 description 25
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- VFWCMGCRMGJXDK-UHFFFAOYSA-N 1-chlorobutane Chemical compound CCCCCl VFWCMGCRMGJXDK-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 239000010409 thin film Substances 0.000 description 5
- 230000035699 permeability Effects 0.000 description 4
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 4
- 238000005259 measurement Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- 125000003668 acetyloxy group Chemical group [H]C([H])([H])C(=O)O[*] 0.000 description 1
- 125000002344 aminooxy group Chemical group [H]N([H])O[*] 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920001002 functional polymer Polymers 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920000306 polymethylpentene Polymers 0.000 description 1
- 239000011116 polymethylpentene Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は混合気体を分離濃縮する
のに使用される気体分離複合膜とその製造方法に関する
。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas separation composite membrane used for separating and concentrating a gas mixture, and a method for manufacturing the same.
【0002】0002
【従来の技術】近年、有機高分子を用いた気体分離膜が
数多く提案されている。気体分離膜を用いて空気中の酸
素を安価に濃縮できるならば、燃焼,窯業,廃棄物処理
および医療などの分野で多大な貢献をすることができる
。酸素濃縮用の気体分離膜素材には、空気などのような
酸素を含む気体から選択的に酸素を分離する機能が大き
いことおよび酸素を透過させる機能が大きいこと、すな
わち、酸素選択係数および酸素透過係数が大きいことが
要求される。また、気体分離膜の製造上からは均質な薄
膜が得られること、その形成された膜に所定の強度があ
ることが要求される。このような酸素濃縮用の気体分離
膜材料として、オルガノポリシロキサンとポリカーボネ
ートとの共重合体,多官能性高分子と末端官能性高分子
の混合物とα,ω−2官能性ポリアルキルシロキサンと
の架橋型共重合体,ポリメチルペンテン,フマル酸エス
テルの重合体とその共重合体およびポリトリメチルシリ
ルプロピン等が報告されている。BACKGROUND OF THE INVENTION In recent years, many gas separation membranes using organic polymers have been proposed. If oxygen in the air could be concentrated at low cost using gas separation membranes, it could make a significant contribution to fields such as combustion, ceramics, waste treatment, and medicine. Gas separation membrane materials for oxygen concentration have a high ability to selectively separate oxygen from oxygen-containing gases such as air and a high ability to permeate oxygen, that is, oxygen selectivity coefficient and oxygen permeability. A large coefficient is required. Furthermore, from the viewpoint of manufacturing gas separation membranes, it is required that a homogeneous thin film be obtained and that the formed membrane have a predetermined strength. As gas separation membrane materials for oxygen concentration, copolymers of organopolysiloxane and polycarbonate, mixtures of polyfunctional polymers and terminally functional polymers, and α,ω-2 functional polyalkylsiloxanes are used. Crosslinked copolymers, polymethylpentene, fumarate ester polymers and their copolymers, and polytrimethylsilylpropyne have been reported.
【0003】実用上はこれらの気体分離膜を支持膜に担
持し、信頼性を確保するため、これらの気体分離膜の上
に保護膜を設ける構造が報告されている。たとえば、ビ
ニル基を有するポリオルガノシロキサンとビニルモノマ
ーとの共重合体の保護膜を設けた構造の気体分離複合膜
が報告されている(特開平2−9430号公報参照)。
気体分離複合膜を透過する気体の透過量は気体分離膜と
保護膜の膜厚に反比例することから、可能な限り気体分
離膜と保護膜を薄くする必要がある。In practice, a structure has been reported in which these gas separation membranes are supported on a support membrane and a protective film is provided on top of these gas separation membranes in order to ensure reliability. For example, a gas separation composite membrane having a structure provided with a protective film of a copolymer of a polyorganosiloxane having a vinyl group and a vinyl monomer has been reported (see JP-A-2-9430). Since the amount of gas permeating through a gas separation composite membrane is inversely proportional to the thickness of the gas separation membrane and the protective membrane, it is necessary to make the gas separation membrane and the protective membrane as thin as possible.
【0004】0004
【発明が解決しようとする課題】しかしながら上記の従
来の構成では、ポリオルガノシロキサンを有機溶剤に溶
解させて水面上に展開して保護膜を作成するため、ポリ
オルガノシロキサンが有機溶剤に完全に溶解し、また均
質に広がる必要があり、ポリオルガノシロキサンは直鎖
状高分子か、有機溶剤に溶解する程度に低分子量である
。そのため、膜強度や、ポリオルガノシロキサンの気体
分離膜内や、さらには多孔性支持膜への拡散を考慮する
と、信頼性を確保するためには保護膜であるポリオルガ
ノシロキサンの膜厚を厚くする必要があり、透過性が劣
り十分な流量を得ることができないという問題点を有し
ていた。[Problems to be Solved by the Invention] However, in the above conventional configuration, polyorganosiloxane is dissolved in an organic solvent and spread on the water surface to create a protective film, so it is difficult to completely dissolve the polyorganosiloxane in the organic solvent. However, it also needs to spread homogeneously, and the polyorganosiloxane is a linear polymer or has a low molecular weight so that it can be dissolved in organic solvents. Therefore, considering the membrane strength and the diffusion of polyorganosiloxane into the gas separation membrane and even into the porous support membrane, it is necessary to increase the thickness of the polyorganosiloxane protective membrane in order to ensure reliability. However, there was a problem in that the permeability was poor and a sufficient flow rate could not be obtained.
【0005】本発明は上記従来の問題点を解決するもの
で、透過性に優れた信頼性の高い気体分離複合膜を提供
することを目的とする。The present invention solves the above-mentioned conventional problems and aims to provide a highly reliable gas separation composite membrane with excellent permeability.
【0006】[0006]
【課題を解決するための手段】この目的を達成するため
に本発明の気体分離複合膜は、多孔性支持膜の上に高分
子よりなる気体分離膜を積層し、この気体分離膜の上に
、保護膜として水と反応して硬化して網目構造を形成し
たシリコーンゴムを積層した構成を有している。また、
本発明の気体分離複合膜の製造方法は硬化型のポリシロ
キサンを有機溶剤に溶解し、水面にこの溶液を一定量滴
下し、均一に展開し、溶剤が蒸発した後、高分子よりな
る気体分離膜を積層した多孔性支持膜を接触させること
により、気体分離膜の上に、水と反応して硬化し、網目
構造を形成したシリコーンゴムの保護膜を積層する方法
である。[Means for Solving the Problem] In order to achieve this object, the gas separation composite membrane of the present invention has a gas separation membrane made of a polymer layered on a porous support membrane, and The protective film has a structure in which silicone rubber that reacts with water and hardens to form a network structure is laminated. Also,
The method for manufacturing the gas separation composite membrane of the present invention is to dissolve a cured polysiloxane in an organic solvent, drop a certain amount of this solution onto the water surface, spread it uniformly, and then separate the gas consisting of a polymer after the solvent evaporates. This is a method in which a protective film made of silicone rubber that reacts with water and hardens to form a network structure is laminated on top of the gas separation membrane by contacting a porous support membrane on which the membranes are laminated.
【0007】[0007]
【作用】この構成によって、保護膜として硬化型のポリ
シロキサンの低分子量を有機溶剤に溶解した溶液を水面
展開するため水面上での広がりが非常によく、均質な薄
膜を水面上に形成することができ、この薄膜の状態で水
と反応するため、網目構造を形成したシリコーンゴムの
薄膜を水面上に形成することとなる。また、水と反応し
て硬化するポリシロキサンを水面上で展開し、薄膜化す
る方法によって、硬化に必要な水は十分に供給されるこ
ととなる。[Operation] With this structure, a solution of low molecular weight curable polysiloxane dissolved in an organic solvent is spread on the water surface as a protective film, so it spreads very well on the water surface and forms a homogeneous thin film on the water surface. This thin film reacts with water, resulting in the formation of a thin film of silicone rubber with a network structure on the water surface. Furthermore, by spreading polysiloxane, which cures by reacting with water, on the water surface to form a thin film, sufficient water necessary for curing can be supplied.
【0008】[0008]
(実施例1)以下本発明の一実施例について説明する。 (Example 1) An example of the present invention will be described below.
【0009】気体分離膜の材料としてジメチルポリシロ
キサンとスチレンモノマーの共重合体とポリジターシャ
リブチルフマレートとの重量比が1:1のブレンド高分
子の2重量%のクロロブタン(テトラヒドロフランを1
0%含む)溶液を調整し、表面の大きさが60cm×6
0cmの正方形の水槽のほぼ中央の水面上に0.15c
c滴下した。クロロブタンが蒸発し、気体分離膜を形成
した後、多孔性支持膜としてポリエーテルスルホンをこ
の気体分離膜の上に静かに置き完全に多孔性支持膜と気
体分離膜が接着したら、静かに水面から剥した。再度同
様にして気体分離膜を水面上に形成し、先に一層気体分
離膜を積層した多孔性支持膜を静かに置き、気体分離膜
を二層積層した。As a material for the gas separation membrane, 2% by weight of chlorobutane (tetrahydrofuran is added to
(containing 0%) solution and the surface size is 60cm x 6
0.15c above the water surface approximately in the center of a 0cm square aquarium
c dripped. After the chlorobutane has evaporated and formed a gas separation membrane, gently place polyether sulfone as a porous support membrane on top of this gas separation membrane and once the porous support membrane and gas separation membrane have completely adhered, gently remove it from the water surface. I peeled it off. A gas separation membrane was again formed on the water surface in the same manner, and the porous support membrane on which one layer of gas separation membrane had been laminated was gently placed, and two layers of gas separation membrane were laminated.
【0010】次に、保護膜の材料として水と反応して硬
化する、末端にアルコキシ基を有するポリシロキサン(
トーレ・シリコーン株式会社製、商品名「SE9157
」)の5重量%のクロロブタン(テトラヒドロフランを
10%含む)溶液を調整し、表面の大きさが60cm×
60cmの正方形の水槽のほぼ中央の水面上に0.10
cc滴下した。クロロブタンが蒸発し、保護膜を形成し
た後、気体分離膜を二層積層した多孔性支持膜をこの保
護膜の上に静かに置き完全に気体分離膜と保護膜が接着
したら、静かに水面から剥した。再度同様にして保護膜
を水面上に形成し、気体分離膜の上に保護膜を二層積層
した気体分離膜複合膜を作成した。Next, as a material for the protective film, polysiloxane (polysiloxane) having an alkoxy group at the end, which cures by reacting with water, is used.
Manufactured by Toray Silicone Co., Ltd., product name "SE9157"
Prepare a 5% by weight chlorobutane (containing 10% tetrahydrofuran) solution of
0.10 on the water surface approximately in the center of a 60cm square aquarium.
cc dripped. After the chlorobutane has evaporated and a protective film has been formed, a porous support film with two layers of gas separation membranes is gently placed on top of this protective film, and when the gas separation membrane and protective film have completely adhered, gently remove the membrane from the water surface. I peeled it off. A protective film was again formed on the water surface in the same manner, and a gas separation membrane composite membrane was created in which two layers of the protective film were laminated on top of the gas separation membrane.
【0011】(実施例2)実施例1と同様の方法で多孔
性支持膜に気体分離膜を二層積層した。次に、保護膜の
材料として水と反応して硬化する、末端にアルコキシ基
を有するポリシロキサン(トーレ・シリコーン株式会社
製、商品名「SE9176」)の5重量%のクロロブタ
ン(テトラヒドロフランを10%含む)溶液を調整し、
表面の大きさが60cm×60cmの正方形の水槽のほ
ぼ中央の水面上に0.10cc滴下した。クロロブタン
が蒸発し、保護膜を形成した後、気体分離膜を二層積層
した多孔性支持膜をこの保護膜上に静かに置き完全に気
体分離膜と保護膜が接着したら、静かに水面から剥した
。再度同様にして保護膜を水面上に形成し、気体分離膜
上に保護膜を二層積層した気体分離複合膜を作成した。
ポリシロキサンが室温において水と反応して硬化するた
めにはポリシロキサンの側鎖または末端に反応性基とし
てアルコキシ基,アセトキシ基,ケトキシム基,アミノ
キシ基等を有するものとする。(Example 2) Two layers of gas separation membranes were laminated on a porous support membrane in the same manner as in Example 1. Next, as a material for the protective film, 5% by weight of chlorobutane (containing 10% tetrahydrofuran) of polysiloxane having an alkoxy group at the end (manufactured by Toray Silicone Co., Ltd., trade name "SE9176") that cures by reacting with water is used. ) prepare the solution,
0.10 cc of the solution was dropped onto the water surface approximately in the center of a square aquarium with a surface size of 60 cm x 60 cm. After the chlorobutane has evaporated and a protective film has been formed, gently place a porous support film with two layers of gas separation membranes on top of this protective film, and when the gas separation membrane and protective film have completely adhered, gently peel it off from the water surface. did. A protective film was formed on the water surface in the same manner again to create a gas separation composite membrane in which two layers of the protective film were laminated on the gas separation membrane. In order for polysiloxane to cure by reacting with water at room temperature, the polysiloxane should have an alkoxy group, acetoxy group, ketoxime group, aminoxy group, etc. as a reactive group in the side chain or terminal.
【0012】本実施例による気体分離複合膜とビニル基
を有するポリオルガノシロキサンとビニルモノマーとの
共重合体を保護膜に用いた従来の気体分離複合膜の初期
性能を(表1)に比較して示している。Table 1 compares the initial performance of the gas separation composite membrane according to this example and a conventional gas separation composite membrane using a copolymer of polyorganosiloxane having a vinyl group and a vinyl monomer as a protective film. It shows.
【0013】[0013]
【表1】[Table 1]
【0014】この(表1)から明らかなように、本実施
例による気体分離複合膜は、酸素透過流量の点で優れた
効果が得られる。As is clear from Table 1, the gas separation composite membrane according to this example provides excellent effects in terms of oxygen permeation flow rate.
【0015】なお、(表1)の測定条件は有効膜面積は
11.3cm2,測定圧力は1.0kg/cm2および
測定温度は25℃とした。また信頼性試験としての60
℃−95%RHで1000時間の放置試験においても従
来例と同様に酸素選択係数の低下はなかった。The measurement conditions shown in Table 1 were as follows: effective membrane area was 11.3 cm2, measurement pressure was 1.0 kg/cm2, and measurement temperature was 25°C. Also, 60 as a reliability test.
Even in a standing test for 1000 hours at 95% RH, there was no decrease in the oxygen selectivity coefficient, similar to the conventional example.
【0016】以上のように本実施例によれば、硬化型の
低分子量のポリシロキサンを薄膜化した後硬化して形成
したシリコーンゴムは網目構造を有しているため膜強度
が大きく、溶剤に対しても不溶となるため、保護膜の厚
みを薄くすることができ、透過性の大きい気体分離複合
膜を得ることができる。As described above, according to this embodiment, the silicone rubber formed by thinning and then curing a curable low molecular weight polysiloxane has a network structure, has a high film strength, and is resistant to solvents. Since it is also insoluble in water, the thickness of the protective film can be reduced, and a gas separation composite membrane with high permeability can be obtained.
【0017】[0017]
【発明の効果】以上のように本発明は多孔性支持膜上に
高分子よりなる気体分離膜を積層し、この気体分離膜の
上に、保護膜として水と反応して硬化し、網目構造を形
成したシリコーンゴムを積層する構成により、また保護
膜は硬化型のポリシロキサンを有機溶剤に溶解し、水面
にこの溶液を一定量滴下し、均一に展開し、溶剤が蒸発
した後、高分子よりなる気体分離膜を積層した多孔性支
持膜を接触させることにより、水と反応して硬化し、網
目構造を形成したシリコーンゴムの保護膜を気体分離膜
の上に形成する製造方法により、透過性に優れた信頼性
の高い気体分離複合膜を実現できるものである。As described above, the present invention has a gas separation membrane made of a polymer layered on a porous support membrane, and a protective film that reacts with water and hardens to form a network structure. The protective film is created by dissolving hardening polysiloxane in an organic solvent, dropping a certain amount of this solution onto the water surface, spreading it uniformly, and after the solvent evaporates, the polymer By contacting a porous support membrane laminated with a gas separation membrane made of This makes it possible to realize a gas separation composite membrane with excellent properties and high reliability.
Claims (2)
離膜を積層し、前記気体分離膜の上に、保護膜として水
と反応して硬化して網目構造を形成したシリコーンゴム
を積層した気体分離複合膜。1. A gas separation membrane made of a polymer is laminated on a porous support membrane, and a silicone rubber which reacts with water and hardens to form a network structure is placed on the gas separation membrane as a protective film. Laminated gas separation composite membrane.
した溶液を水面に一定量滴下して均一に展開させ、溶剤
が蒸発した後、高分子よりなる気体分離膜を積層した多
孔性支持膜を接触させることにより、水と反応させて硬
化して網目構造を形成したシリコーンゴムの保護膜を前
記気体分離膜の上に積層する気体分離複合膜の製造方法
。Claim 2: A porous support film in which a solution of curable polysiloxane dissolved in an organic solvent is dropped onto the water surface in a certain amount and spread uniformly, and after the solvent has evaporated, a gas separation membrane made of polymer is laminated. A method for producing a gas separation composite membrane, in which a protective film of silicone rubber, which is cured by reacting with water to form a network structure, is laminated on the gas separation membrane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8505591A JPH04317734A (en) | 1991-04-17 | 1991-04-17 | Gas separating composite membrane and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8505591A JPH04317734A (en) | 1991-04-17 | 1991-04-17 | Gas separating composite membrane and its production |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04317734A true JPH04317734A (en) | 1992-11-09 |
Family
ID=13847964
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8505591A Pending JPH04317734A (en) | 1991-04-17 | 1991-04-17 | Gas separating composite membrane and its production |
Country Status (1)
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JP (1) | JPH04317734A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016136396A1 (en) * | 2015-02-27 | 2016-09-01 | 富士フイルム株式会社 | Gas separation membrane, gas separation module, gas separation device, and gas separation method |
WO2017122486A1 (en) * | 2016-01-12 | 2017-07-20 | 富士フイルム株式会社 | Gas separation membrane, method for producing gas separation membrane, gas separation membrane module and gas separation device |
JPWO2017038285A1 (en) * | 2015-08-31 | 2018-01-11 | 富士フイルム株式会社 | Method for producing gas separation composite membrane, liquid composition, gas separation composite membrane, gas separation module, gas separation device, and gas separation method |
-
1991
- 1991-04-17 JP JP8505591A patent/JPH04317734A/en active Pending
Cited By (7)
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WO2016136396A1 (en) * | 2015-02-27 | 2016-09-01 | 富士フイルム株式会社 | Gas separation membrane, gas separation module, gas separation device, and gas separation method |
JPWO2016136396A1 (en) * | 2015-02-27 | 2017-08-10 | 富士フイルム株式会社 | Gas separation membrane, gas separation module, gas separation device, and gas separation method |
US10507437B2 (en) | 2015-02-27 | 2019-12-17 | Fujifilm Corporation | Gas separation membrane, gas separation module, gas separation apparatus, and gas separation method |
JPWO2017038285A1 (en) * | 2015-08-31 | 2018-01-11 | 富士フイルム株式会社 | Method for producing gas separation composite membrane, liquid composition, gas separation composite membrane, gas separation module, gas separation device, and gas separation method |
US10654005B2 (en) | 2015-08-31 | 2020-05-19 | Fujifilm Corporation | Method for producing gas separation composite membrane, liquid composition, gas separation composite membrane, gas separation module, gas separation apparatus, and gas separation method |
WO2017122486A1 (en) * | 2016-01-12 | 2017-07-20 | 富士フイルム株式会社 | Gas separation membrane, method for producing gas separation membrane, gas separation membrane module and gas separation device |
JPWO2017122486A1 (en) * | 2016-01-12 | 2018-09-20 | 富士フイルム株式会社 | Gas separation membrane, gas separation membrane manufacturing method, gas separation membrane module, and gas separation device |
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