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JPH0331092B2 - - Google Patents
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JPH0331092B2 - - Google Patents

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Publication number
JPH0331092B2
JPH0331092B2 JP26907884A JP26907884A JPH0331092B2 JP H0331092 B2 JPH0331092 B2 JP H0331092B2 JP 26907884 A JP26907884 A JP 26907884A JP 26907884 A JP26907884 A JP 26907884A JP H0331092 B2 JPH0331092 B2 JP H0331092B2
Authority
JP
Japan
Prior art keywords
group
alkyl group
oxygen
permeability
substituent selected
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.)
Expired
Application number
JP26907884A
Other languages
Japanese (ja)
Other versions
JPS61146320A (en
Inventor
Shiro Asakawa
Yukihiro Saito
Midori Kawahito
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP59269078A priority Critical patent/JPS61146320A/en
Publication of JPS61146320A publication Critical patent/JPS61146320A/en
Publication of JPH0331092B2 publication Critical patent/JPH0331092B2/ja
Granted legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は酸素/窒素の分離性にすぐれ、且つ透
過係数の大きい気体透過膜に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a gas permeable membrane that has excellent oxygen/nitrogen separation properties and a large permeability coefficient.

従来例の構成とその問題点 近年高分子膜を用いての物質分離技術の進展は
著しく、液体処理は勿論、各種混合気体よりの特
定の気体の濃縮分離のの開発が、盛んに行なわれ
ている。
Configuration of conventional examples and their problems In recent years, material separation technology using polymer membranes has made remarkable progress, and not only liquid treatment but also the development of concentrated separation of specific gases from various gas mixtures has been actively conducted. There is.

中でも空気中よりの酸素濃縮による酸素富化空
気の製造は、その用途が、燃焼用、医療用、汚泥
処理用など広範に亘り、有用なため、各種の高分
子分離膜が提案されている。
Among these, the production of oxygen-enriched air by concentrating oxygen from the air is useful for a wide range of applications, including combustion, medical use, and sludge treatment, and various polymer separation membranes have therefore been proposed.

従来斯かる酸素富化空気製造用の高分子分離
膜、すなわち、酸素透過膜としては、、シリコー
ン系膜、ポリオレフイン膜、ポリフエンレンオキ
シド膜などが知られている。これらの膜は、それ
ぞれ実用可能な性能を有してはいるが、なお、そ
の分離の選択性、透過性の大きさに不満足な点を
有している。
Conventionally, silicone membranes, polyolefin membranes, polyphelene oxide membranes, and the like are known as such polymer separation membranes, ie, oxygen permeable membranes, for producing oxygen-enriched air. Although these membranes each have practical performance, they are still unsatisfactory in their separation selectivity and permeability.

たとえば、シリコーン系膜では酸素透過係数
は、〜10-8(c.c.・cm/cm2・sec・cmHg)と比較的
大きいが、酸素/窒素の選択性は〜2、と小さ
く、またその他のオレフイン系、フエニレンオキ
シド系ポリマーでは、選択性は〜4、と大きい
が、酸素透過係数は〜10-9〜10-10(c.c.・cm/cm2
sec・cmHg)と小さい。
For example, silicone membranes have a relatively high oxygen permeability coefficient of ~10 -8 (cc・cm/cm 2・sec・cmHg), but have a low oxygen/nitrogen selectivity of ~2; For phenylene oxide-based polymers, the selectivity is as high as ~4, but the oxygen permeability coefficient is ~10 -9 ~10 -10 (cc・cm/cm 2
sec・cmHg).

発明の目的 本発明は、従来の前記欠点を解消するもので、
気体透過性と気体選択性ににすぐれた気体透過膜
を提供することを目的とするものである。
OBJECT OF THE INVENTION The present invention solves the above-mentioned drawbacks of the conventional technology.
The object of the present invention is to provide a gas permeable membrane having excellent gas permeability and gas selectivity.

発明の構成 本発明者らは、選択性、透過係数の両者共に大
きな値を有する気体透過膜について、鋭意研究し
た結果、下記に示す構造から成るポリマーの膜
が、大きな選択性と透過性を有することを発見
し、本発明に到達したものである。
Structure of the Invention As a result of extensive research into gas permeable membranes that have large values for both selectivity and permeability coefficient, the present inventors have found that a polymer membrane having the structure shown below has large selectivity and permeability. This discovery led to the present invention.

すなわち、その一般式が、下記のごとき繰り返
し単位を有する直鎖状の高分子より成る気体透過
膜で、 ここで、R1〜R4はそれぞれ、水素、低級アル
キル基、アルコキシル基、ハロゲン原子、ハロゲ
ン化アルキル基より成る群から選ばれた置換基を
示し、R5,R6は、それぞれ、水素、低級アルキ
ル基、フエニル基、トリフルキルシリル基、より
成る群から選ばれた置換基を示し、またxは、芳
香族環と不飽和二重結合の含有比を示し、0.1<
x<0.9である。
That is, the general formula is a gas permeable membrane made of a linear polymer having repeating units as shown below. Here, R 1 to R 4 each represent a substituent selected from the group consisting of hydrogen, a lower alkyl group, an alkoxyl group, a halogen atom, and a halogenated alkyl group, and R 5 and R 6 each represent hydrogen, It represents a substituent selected from the group consisting of a lower alkyl group, a phenyl group, and a trifurkylsilyl group, and x represents the content ratio of aromatic ring to unsaturated double bond, and 0.1<
x<0.9.

斯かる高分子材料は、最近導電性にすぐれた材
料として注目されている。このフエニレン−ビニ
レン系ポリマーはその中間体が溶媒可溶性で、キ
ヤストして、容易にフイルム化することが出来
る。
Such polymer materials have recently attracted attention as materials with excellent conductivity. The intermediate of this phenylene-vinylene polymer is soluble in solvents and can be easily cast into a film.

本発明者らは、上記キヤストして得られたフイ
ルムの気体透過性に着目して測定した結果、これ
らのフイルムが極めてすぐれた気体透過性を示す
ことを発見した。
The present inventors focused on and measured the gas permeability of the films obtained by the above-mentioned casting, and discovered that these films exhibited extremely excellent gas permeability.

これらの高分子は、一般的には、Wittig反応
や、Knoevenagel反応を用いて合成することが出
来る。
These polymers can generally be synthesized using Wittig reaction or Knoevenagel reaction.

得られたポリマーの中間体は水溶液に可溶で、
容易にキヤストしてフイルム化することが出来
た。これを熱分解して、所定のフイルムとするこ
とが出来る。
The resulting polymer intermediate is soluble in aqueous solution;
It was easy to cast and make film. This can be thermally decomposed into a predetermined film.

個々の材料によつて、特性は異るが、酸素の透
過性を調べた結果、10-9〜10-8(c.c.・cm/cm2
sec・cmHg)値を示し、またその酸素/窒素選択
性は、2〜3.5と極めて大きい値を示した。
Characteristics vary depending on the individual material, but as a result of examining oxygen permeability, it is 10 -9 to 10 -8 (cc・cm/cm 2
sec·cmHg) value, and its oxygen/nitrogen selectivity was extremely large, ranging from 2 to 3.5.

以下、代表的な実施例を用いて詳述する。 Hereinafter, a detailed explanation will be given using typical examples.

実施例の説明 <実施例 1> P−キシリレンビス(ジエチルスルホニウムブ
ロミド)水溶液に、0〜5℃の温度条件下にて、
苛性ソーダ水溶液を滴下し、撹拌しながら、約6
時間重合させた。反応終了後、生成物を透析し、
低分子物質を分離した。精製水溶液をキヤスト
し、減圧下乾燥してフイルムを得た。得られたフ
イルムは、窒素気流中、250〜300℃に21時間熱処
理を行つた。このフイルムを所定の方法により気
体透過性を調べた。
Description of Examples <Example 1> P-xylylene bis(diethylsulfonium bromide) aqueous solution was added at a temperature of 0 to 5°C.
Add the caustic soda aqueous solution dropwise and stir for about 6 hours.
Polymerized for hours. After the reaction is completed, the product is dialyzed,
Low molecular weight substances were separated. The purified aqueous solution was cast and dried under reduced pressure to obtain a film. The obtained film was heat-treated at 250 to 300°C for 21 hours in a nitrogen stream. The gas permeability of this film was examined by a predetermined method.

o2=4.5×10-9(c.c.・cm/cm2・sec・cmHg) Po2/PN2=3.45を示した。o 2 = 4.5×10 -9 (cc・cm/cm 2・sec・cmHg) Po 2 /PN 2 = 3.45.

<実施例 2> ビス(a,α′−ジエチルスルホニウムブロミ
ド)1.4−ジエチルベンゼンを原料とした以外は、
実施例1と同様の方法でフイルムを形成した。得
られたフイルムの透過性は、 o2=1.5×10-8(c.c.・cm/cm2・sec・cmHg) Po2/PN2=3.0を示した。
<Example 2> Except that bis(a,α'-diethylsulfonium bromide) 1,4-diethylbenzene was used as the raw material,
A film was formed in the same manner as in Example 1. The obtained film had a permeability of o 2 =1.5×10 −8 (cc·cm/cm 2 ·sec·cmHg) Po 2 /PN 2 =3.0.

<実施例 3> 原料として、2.5−ジメトキシ−1.4−キシリレ
ンビス(ジエチルスルホニウムブロミド)を用
い、実施例−1と同様の方法でフイルムを形成し
た。得られたフイルムの透過性は、 o2=2.2×10-8(c.c.・cm/cm2・sec・cmHg) Po2/PN2=2.75を示した。
<Example 3> A film was formed in the same manner as in Example 1 using 2,5-dimethoxy-1,4-xylylene bis(diethylsulfonium bromide) as a raw material. The obtained film had a permeability of o 2 =2.2×10 −8 (cc·cm/cm 2 ·sec·cmHg) Po 2 /PN 2 =2.75.

発明の効果 以上要するに本発明は、一般式が、下記のごと
き繰り返し単位を有する直鎖状の高分子より成る
気体透過膜で、 ここで、R1〜R4はそれぞれ、水素、低級アル
カキル基、アルコキシル基、ハロゲン原子、ハロ
ゲン化アルキル基より成る群から選ばれた置換基
を示し、R5,R6は、それぞれ、水素、低級アル
キル基、フエニル基、トリアルキルシリル基より
成る群から選ばれた置換基を示し、またxは、芳
香族環と不飽和二重結合の含有比を示し、0.1<
x<0.9である。
Effects of the Invention In summary, the present invention provides a gas permeable membrane made of a linear polymer having a general formula having repeating units as shown below. Here, R 1 to R 4 each represent a substituent selected from the group consisting of hydrogen, a lower alkyl group, an alkoxyl group, a halogen atom, and a halogenated alkyl group, and R 5 and R 6 each represent hydrogen, It represents a substituent selected from the group consisting of a lower alkyl group, a phenyl group, and a trialkylsilyl group, and x represents the content ratio of an aromatic ring to an unsaturated double bond, and 0.1<
x<0.9.

斯かる気体透過膜は極めて気体透過性にすぐ
れ、また選択性も大きく、酸素分離に用いて酸素
富化空気を製造した場合、燃焼用、医療用、汚泥
処理用など、広範に亘り、有用なものである。
Such a gas permeable membrane has extremely high gas permeability and high selectivity, and when used for oxygen separation to produce oxygen-enriched air, it can be used for a wide range of purposes, including combustion, medical, and sludge treatment. It is something.

Claims (1)

【特許請求の範囲】 1 一般式が、下記のごとき繰り返し単位を有す
る直鎖状の高分子より成る気体透過膜。 ここで、R1〜R4はそれぞれ、水素、低級アル
キル基、アルコキシル基、ハロゲン原子、ハロゲ
ン化アルキル基より成る群から選ばれた置換基を
示し、R5,R6は、それぞれ、水素、低級アルキ
ル基、フエニル基、トリアルキルシリル基、より
なる群から選ばれた置換基を示し、またxは、芳
香族環と不飽和二重結合の含有比を示し、0.1<
x<0.9である。
[Scope of Claims] 1. A gas permeable membrane made of a linear polymer having a general formula having repeating units as shown below. Here, R 1 to R 4 each represent a substituent selected from the group consisting of hydrogen, a lower alkyl group, an alkoxyl group, a halogen atom, and a halogenated alkyl group, and R 5 and R 6 each represent hydrogen, It represents a substituent selected from the group consisting of a lower alkyl group, phenyl group, and trialkylsilyl group, and x represents the content ratio of aromatic ring to unsaturated double bond, and 0.1<
x<0.9.
JP59269078A 1984-12-19 1984-12-19 gas permeable membrane Granted JPS61146320A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59269078A JPS61146320A (en) 1984-12-19 1984-12-19 gas permeable membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59269078A JPS61146320A (en) 1984-12-19 1984-12-19 gas permeable membrane

Publications (2)

Publication Number Publication Date
JPS61146320A JPS61146320A (en) 1986-07-04
JPH0331092B2 true JPH0331092B2 (en) 1991-05-02

Family

ID=17467355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59269078A Granted JPS61146320A (en) 1984-12-19 1984-12-19 gas permeable membrane

Country Status (1)

Country Link
JP (1) JPS61146320A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5051113A (en) * 1990-06-13 1991-09-24 Du Pont Canada Inc. Air-intake system for mobile engines
US5147417A (en) * 1990-06-13 1992-09-15 Du Pont Canada Inc. Air-intake system for mobile engines
US5053059A (en) * 1990-06-13 1991-10-01 Du Pont Canada Inc. Air-intake system for residential furnaces

Also Published As

Publication number Publication date
JPS61146320A (en) 1986-07-04

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