JPH01310713A - Gas separation membrane and its preparation - Google Patents
Gas separation membrane and its preparationInfo
- Publication number
- JPH01310713A JPH01310713A JP13948688A JP13948688A JPH01310713A JP H01310713 A JPH01310713 A JP H01310713A JP 13948688 A JP13948688 A JP 13948688A JP 13948688 A JP13948688 A JP 13948688A JP H01310713 A JPH01310713 A JP H01310713A
- Authority
- JP
- Japan
- Prior art keywords
- air
- glass
- oxygen
- amino
- membrane
- 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 29
- 238000000926 separation method Methods 0.000 title claims description 13
- 239000005373 porous glass Substances 0.000 claims abstract description 15
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims description 8
- 150000004703 alkoxides Chemical class 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 16
- 239000001301 oxygen Substances 0.000 abstract description 16
- 229910052760 oxygen Inorganic materials 0.000 abstract description 16
- 239000011148 porous material Substances 0.000 abstract description 13
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 10
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 abstract description 6
- 239000011521 glass Substances 0.000 abstract description 5
- 239000012141 concentrate Substances 0.000 abstract description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 abstract description 3
- -1 amino compound Chemical class 0.000 abstract description 3
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 238000009792 diffusion process Methods 0.000 abstract description 3
- 239000010936 titanium Substances 0.000 abstract description 3
- 229910052719 titanium Inorganic materials 0.000 abstract description 3
- 150000003222 pyridines Chemical class 0.000 abstract description 2
- 235000011089 carbon dioxide Nutrition 0.000 abstract 3
- 125000003545 alkoxy group Chemical group 0.000 abstract 1
- 238000007598 dipping method Methods 0.000 abstract 1
- 238000001035 drying Methods 0.000 abstract 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 26
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 7
- 238000001179 sorption measurement Methods 0.000 description 5
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 239000001569 carbon dioxide Substances 0.000 description 4
- 230000008878 coupling Effects 0.000 description 4
- 238000010168 coupling process Methods 0.000 description 4
- 238000005859 coupling reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 229910000077 silane Inorganic materials 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 229940027991 antiseptic and disinfectant quinoline derivative Drugs 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000005388 borosilicate glass Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 125000003253 isopropoxy group Chemical group [H]C([H])([H])C([H])(O*)C([H])([H])[H] 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 150000003248 quinolines Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、空気中の酸素、炭酸ガス、水蒸気を分離して
濃縮する気体分離膜、及びその製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a gas separation membrane that separates and concentrates oxygen, carbon dioxide, and water vapor in the air, and a method for manufacturing the same.
空気中の酸素や窒素、水蒸気、炭酸ガス等を分離して濃
縮する方法としては膜分離方式が知られ、この方式は安
価でほとんどメンテナンスフリーであるから近年多くの
研究が行なわれている。A membrane separation method is known as a method for separating and concentrating oxygen, nitrogen, water vapor, carbon dioxide, etc. in the air, and much research has been conducted in recent years on this method because it is inexpensive and almost maintenance-free.
この様な酸素の濃縮に関しては現在上として、医療用と
燃焼用などの省エネルギー用として利用され、窒素は防
爆なとの防災用、炭酸ガス・水蒸気は環境コントロール
等にその用途が見込まれている。At present, such concentrated oxygen is used for medical purposes and for energy-saving purposes such as combustion, while nitrogen is expected to be used for explosion-proof disaster prevention purposes, and carbon dioxide and water vapor are expected to be used for environmental control. .
前述のように空気から酸素や窒素の分離、濃縮を行なう
技術としては、空気が冷却して酸素と窒素の沸点差を利
用して装置分離する深冷分離方式。As mentioned above, the technology for separating and concentrating oxygen and nitrogen from air is the cryogenic separation method, in which the air is cooled and separated using a device that utilizes the difference in boiling point between oxygen and nitrogen.
ゼオライトやカーボンソーブ等の気体に対する吸着力や
吸着速度差利用して分離する固体表面での吸着方式、等
が知られている。Adsorption methods on the solid surface of zeolite, carbon sorb, etc. that utilize the adsorption power for gases and the difference in adsorption speed to separate the gases are known.
前者の方式であると、設備が大型となるために使用者と
離れた場所に設備を設置してパイプで使用者まで輸送し
り、ボンベに充填して使用者まで運搬しているので、コ
ストが非常に高くなってしまうと共に、使用者は高圧ガ
ス取締法の法規制を受けるから取扱上不便である。In the former method, the equipment is large, so it is installed at a location far from the user, transported to the user via pipe, and then filled into cylinders and transported to the user, which reduces costs. In addition to being extremely expensive, it is inconvenient for users to handle as they are subject to legal regulations under the High Pressure Gas Control Law.
後者の方式であると、濃度が時間に対して−定ではな(
バッチシステムにならざるを得ないし、水蒸気や極性ガ
ス等はゼオライトを失活させるので吸着以前の段階で除
去しなければならず操作が面倒となる。In the latter method, the concentration is not constant with respect to time (
A batch system has to be used, and since water vapor and polar gases deactivate the zeolite, they must be removed before adsorption, making the operation complicated.
これに対して前述の膜分離方式は前述のような課題を解
決できるばかりか、消費エネルギーも前述の2つの方式
よりも低く好ましい。On the other hand, the membrane separation method described above is preferable because it not only can solve the above-mentioned problems, but also consumes less energy than the two methods described above.
しかしながら気体を膜分離させる場合、透過速度が遅い
ので実用化は困難である。However, when gas is separated through a membrane, the permeation rate is slow, making it difficult to put it into practical use.
つまり、従来一般に行なわれている気体の膜分離技術は
、酸素と窒素などの気体分離・濃縮膜として無孔質膜を
使用し、その膜表面に原料空気を供給すると空気中の気
体は膜の片側に溶解して反対側まで拡散して行き脱落す
る。つまり、膜透過する。この特番気体によって溶解度
や拡散速度が異なるので濃縮作用が生ずることを利用し
ているので、透過速度の上昇はある程度以上不可能であ
るから、透過速度が遅くなる。In other words, conventional gas membrane separation technology uses a nonporous membrane as a membrane for separating and concentrating gases such as oxygen and nitrogen, and when feed air is supplied to the membrane surface, the gas in the air is absorbed by the membrane. It dissolves on one side, diffuses to the other side, and falls off. In other words, it passes through the membrane. Since the solubility and diffusion rate vary depending on the special gas, the concentrating effect is utilized, and since it is impossible to increase the permeation rate beyond a certain point, the permeation rate becomes slow.
そこで、本発明は透過速度を速くできるようにした気体
分離膜及びその製造方法を提供することを目的とする。Therefore, an object of the present invention is to provide a gas separation membrane that can increase the permeation rate and a method for manufacturing the same.
〔課題を解決するための手段及び作用〕本発明者は無孔
質膜の透過速度の遅さを改善しようと鋭意研究の結果、
無孔質膜を用いなくとも空気中の酸素、炭酸ガス、水蒸
気を効率良く濃縮でき、透過速度を大巾に無孔質膜より
向上する気体分離膜を見出した。[Means and effects for solving the problem] As a result of intensive research to improve the slow permeation rate of non-porous membranes, the present inventor found that
We have discovered a gas separation membrane that can efficiently condense oxygen, carbon dioxide, and water vapor in the air without using a nonporous membrane, and whose permeation rate is significantly higher than that of a nonporous membrane.
すなわち、気体平均自由行程より平均細孔直径が小さい
貫通孔を持った多孔質膜を気体が通過したとき、各気体
の透過速度は分子量の平方根に比例すると共に、この時
の気体透過速度は無孔質膜より10〜1000倍速い。In other words, when gas passes through a porous membrane that has through-holes with an average pore diameter smaller than the gas mean free path, the permeation rate of each gas is proportional to the square root of the molecular weight, and the gas permeation rate at this time is negligible. 10-1000 times faster than porous membranes.
ところが、酸素と窒素の分子量差は僅少であるから空気
から酸素又は窒素の濃縮はほとんど不可能である。However, since the difference in molecular weight between oxygen and nitrogen is small, it is almost impossible to concentrate oxygen or nitrogen from air.
また、細孔表面が酸素又は窒素等の特定の気体に対して
親和性であるならば細孔表面で気体吸着や溶解などが生
じる。その結果細孔表面で吸着した気体の濃度が上昇す
るのでその反対側では吸着した気体の濃縮作用が発生す
る。Furthermore, if the pore surface has an affinity for a specific gas such as oxygen or nitrogen, gas adsorption or dissolution will occur on the pore surface. As a result, the concentration of the gas adsorbed on the pore surface increases, and on the opposite side, a concentration effect of the adsorbed gas occurs.
他方、酸素、炭酸ガスは親電子性である。On the other hand, oxygen and carbon dioxide gas are electrophilic.
本発明者は上記の点に着目し、多孔質膜内の細孔表面を
塩基化すれば、細孔表面が空気中の酸素、炭酸ガスに対
して親和性も増加すると同時に親水性も増加し、これに
より細孔内表面で酸素、炭酸ガス、水蒸気が吸着され、
細孔表面では酸素、炭酸ガス、水蒸気の表面拡散現象が
生じるために空気中の酸素、炭酸ガス、水蒸気は細孔を
通過することで濃縮され、その結果は塩基強度が大きい
ほど著しくなることを見出した。The present inventor focused on the above points, and by making the pore surfaces in a porous membrane basic, the pore surfaces will increase their affinity for oxygen and carbon dioxide gas in the air, and at the same time increase their hydrophilicity. As a result, oxygen, carbon dioxide, and water vapor are adsorbed on the inner surface of the pores,
Surface diffusion phenomena of oxygen, carbon dioxide, and water vapor occur on the pore surface, so the oxygen, carbon dioxide, and water vapor in the air become concentrated as they pass through the pores, and this result becomes more pronounced as the base strength increases. I found it.
具体的には、多孔質ガラスの表面及び細孔表面にアミノ
系塩基化合物を有する気体分離膜であり、これによって
空気中の酸素、炭酸ガス、水蒸気濃縮できると共に、透
過速度を速くして十分実用に供することができる。Specifically, it is a gas separation membrane that has an amino base compound on the surface of porous glass and on the surface of the pores.This membrane can not only concentrate oxygen, carbon dioxide, and water vapor in the air, but also has a high permeation rate, making it suitable for practical use. It can be provided to
前記アミノ系塩基化合物としては、モノおよびジメチル
アミン、モノメチルアミン、ピリジン誘導体、キノリン
誘導体等である。Examples of the amino base compounds include mono- and dimethylamine, monomethylamine, pyridine derivatives, and quinoline derivatives.
多孔質ガラスの形状、中空状、中空管状、平板状、スパ
イラル状等でも良い。The shape of porous glass may be hollow, hollow tubular, flat, spiral, etc.
また、かかる気体分離膜を製造する方法について鋭意研
究した結果、多孔質ガラス表面をシランカップリング材
やチタンカップリング材でカップリング処理を施したの
ち、アミノ系物質と反応させて塩基化処理を行なうこと
で気体分離膜を製造できることを見た出した。In addition, as a result of intensive research into methods for manufacturing such gas separation membranes, we found that after coupling the porous glass surface with a silane coupling material or titanium coupling material, we reacted it with an amino-based substance to basify it. They found that it was possible to produce gas separation membranes by doing this.
この製造方法によれば、反応性に富んでいるので常温で
の反応が可能となり正確な反応コントロールができるか
ら、塩基化の強度を任意にコントできる。According to this production method, since it is highly reactive, the reaction can be carried out at room temperature, and the reaction can be precisely controlled, so that the strength of basification can be arbitrarily controlled.
前述のチタン及びシランカップリング材としては、メト
キシ系、エトキシ系、イソプロポキシ系などであり、こ
れらはアルコキシド基がそれぞれ存在し、普通これらの
アルコキシド基がガラス表面の水素基と反応する。The aforementioned titanium and silane coupling materials include methoxy, ethoxy, and isopropoxy, each of which has an alkoxide group, and these alkoxide groups usually react with hydrogen groups on the glass surface.
また、アミノ基などの塩基と反応する基は、5iCC,
5iC=CSSiHSSiCf!、各々組み合せて使用
するのが好ましい。In addition, groups that react with bases such as amino groups are 5iCC,
5iC=CSSiHSSiCf! , are preferably used in combination.
具体的には、アルコキシシド溶液中に多孔質ガラスを浸
漬して引き上げ、空気中に放置乾燥後アミノ系物質と反
応させて多孔質ガラスの全表面にアミノ系塩基を付着さ
せる製造方法である。Specifically, this is a manufacturing method in which a porous glass is immersed in an alkoxide solution, pulled up, left to dry in the air, and reacted with an amino-based substance to adhere an amino-based base to the entire surface of the porous glass.
前記アルコキンラドとしては、(R4O)nS I R
2、ただしR4はCH3、C2H5、C3H7、nは1
〜3、R2はH2C=CH。As the alcoquinrad, (R4O)nS I R
2, however, R4 is CH3, C2H5, C3H7, n is 1
~3, R2 is H2C=CH.
C3H8N−C2H4NH2、C3H8NH2、R2
HC−C−C−0−C3Hs、
\1
CH1
CHI −C−0−T i −(OC+ Ht −NH
−C+ Ht −NH+ )+のうちの1つが好ましく
、前記アミノ系物質としては、
CミCH2
bo38 N N
HN (CH3)2 、R2NC2R5、HN(C
2R5)2のうちの1つが好ましい。C3H8N-C2H4NH2, C3H8NH2, R2 HC-C-C-0-C3Hs, \1 CH1 CHI -C-0-T i -(OC+ Ht -NH
-C+ Ht -NH+
2R5) One of 2 is preferred.
以下本発明の詳細な説明する。 The present invention will be explained in detail below.
実施例1
無水エタノール中にアミノプロピルトリメトキシンラン
2モル%添加したアルコキシシド溶液を調製する。Example 1 An alkoxide solution containing 2 mol % of aminopropyltrimethoxine in absolute ethanol is prepared.
次に、ホウケイ酸ガラス製多孔質中空管(ボア径250
人)を、前記アルコキシシド溶液に浸漬した後空気中に
放置し細孔表面をシリル化すると共に、溶剤を蒸発除去
する。Next, a porous hollow tube made of borosilicate glass (bore diameter 250
After immersing the sample in the alkoxide solution, the pore surface is silylated and the solvent is removed by evaporation.
このようにして製造した多孔質ガラス中空管膜の空気透
過テストを行なったところ、酸素濃度は23%(圧力差
76Hg+nn+)、透過速度は8cc/ c櫂/分で
あった。When the porous glass hollow tube membrane thus produced was subjected to an air permeation test, the oxygen concentration was 23% (pressure difference 76 Hg+nn+) and the permeation rate was 8 cc/c paddle/min.
比較例として同様な多孔質ガラス中空管にポリジメチル
シロキザン膜を作製して同様の空気通過テストを行なっ
たところ、透過速度は0 、 2 cc/ cシ/分で
あった。As a comparative example, a polydimethylsiloxane membrane was prepared in a similar porous glass hollow tube and a similar air passage test was conducted, and the permeation rate was 0.2 cc/c/min.
実施例2
rグリドキシプロピルトリメトキシシランと無水エタノ
ール2モル%溶液中に、実施例1と同じ多孔質ガラス中
空管を浸漬乾燥後、キノリンとスルホン酸2%溶液中に
浸漬し、室温で10時間放置後さらに空気中に24時間
放置し、その後にメタノール溶液中に浸漬して余分なキ
ノリン分を除去して空気中で放置乾燥した。Example 2 The same porous glass hollow tube as in Example 1 was immersed in a 2 mol% solution of r-glydoxypropyltrimethoxysilane and anhydrous ethanol, dried, and then immersed in a 2% solution of quinoline and sulfonic acid, and then heated at room temperature. After being left for 10 hours, it was left in the air for another 24 hours, then immersed in a methanol solution to remove excess quinoline, and left to dry in the air.
このようにして製造した多孔質ガラス中空管膜を実施例
1と同様に空気通過テストを行なったところ、酸素濃度
は28%(圧力差76Hgmm)、透過速度5cc/e
♂/分であった。When the porous glass hollow tube membrane thus produced was subjected to an air passage test in the same manner as in Example 1, the oxygen concentration was 28% (pressure difference 76 Hgmm), and the permeation rate was 5 cc/e.
It was ♂/min.
多孔質ガラスの表面及び細孔表面にアミノ系塩基化合物
が付着しているから、空気中の酸素、炭素ガス、水蒸気
と親和性があり、空気中の酸素、炭酸ガス、水蒸気を濃
縮できる。Since the amino base compound is attached to the surface of the porous glass and the pore surface, it has an affinity for oxygen, carbon gas, and water vapor in the air, and can condense oxygen, carbon dioxide, and water vapor in the air.
また、多孔質であるから透過速度を速くして十分に実用
に供することかできる。In addition, since it is porous, the permeation rate can be increased to make it suitable for practical use.
出願人 株式会社 小 松 製 作 所代理人 弁
理士 米 原 正 章Applicant Komatsu Manufacturing Co., Ltd. Representative Patent Attorney Masaaki Yonehara
Claims (2)
することを特徴とする気体分離膜。(1) A gas separation membrane characterized by having an amino base compound on the entire surface of porous glass.
、空気中に放置乾燥してアミノ系物質と反応させて成る
気体分離膜の製造方法。(2) A method for producing a gas separation membrane, in which porous glass is immersed in an alkoxide solution, left to dry in the air, and reacted with an amino-based substance.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13948688A JPH01310713A (en) | 1988-06-08 | 1988-06-08 | Gas separation membrane and its preparation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13948688A JPH01310713A (en) | 1988-06-08 | 1988-06-08 | Gas separation membrane and its preparation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01310713A true JPH01310713A (en) | 1989-12-14 |
Family
ID=15246374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13948688A Pending JPH01310713A (en) | 1988-06-08 | 1988-06-08 | Gas separation membrane and its preparation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01310713A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59183803A (en) * | 1983-04-01 | 1984-10-19 | Nippon Oil Co Ltd | Permselective membrane for separation of gas |
JPS61101226A (en) * | 1984-10-22 | 1986-05-20 | Teijin Ltd | Separation membrane |
-
1988
- 1988-06-08 JP JP13948688A patent/JPH01310713A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59183803A (en) * | 1983-04-01 | 1984-10-19 | Nippon Oil Co Ltd | Permselective membrane for separation of gas |
JPS61101226A (en) * | 1984-10-22 | 1986-05-20 | Teijin Ltd | Separation membrane |
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