JPH0331092B2 - - Google Patents
Info
- 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
Links
- 239000007789 gas Substances 0.000 claims description 15
- 239000012528 membrane Substances 0.000 claims description 15
- 125000000217 alkyl group Chemical group 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 6
- 125000001424 substituent group Chemical group 0.000 claims description 6
- 125000003545 alkoxy group Chemical group 0.000 claims description 3
- 125000003118 aryl group Chemical group 0.000 claims description 3
- 125000005843 halogen group Chemical group 0.000 claims description 3
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 3
- 125000004665 trialkylsilyl group Chemical group 0.000 claims description 2
- 230000035699 permeability Effects 0.000 description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 12
- 239000001301 oxygen Substances 0.000 description 12
- 229910052760 oxygen Inorganic materials 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000000926 separation method Methods 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- DSNHSQKRULAAEI-UHFFFAOYSA-N 1,4-Diethylbenzene Chemical compound CCC1=CC=C(CC)C=C1 DSNHSQKRULAAEI-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- DETPPCCUWRJLKU-UHFFFAOYSA-N diethylsulfanium bromide Chemical compound [Br-].CC[SH+]CC DETPPCCUWRJLKU-UHFFFAOYSA-N 0.000 description 2
- -1 phenylene-vinylene Chemical class 0.000 description 2
- 229920005597 polymer membrane Polymers 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- OMIHGPLIXGGMJB-UHFFFAOYSA-N 7-oxabicyclo[4.1.0]hepta-1,3,5-triene Chemical compound C1=CC=C2OC2=C1 OMIHGPLIXGGMJB-UHFFFAOYSA-N 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 238000006000 Knoevenagel condensation reaction Methods 0.000 description 1
- 238000007239 Wittig reaction Methods 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- 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)
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.
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)
| 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 |
-
1984
- 1984-12-19 JP JP59269078A patent/JPS61146320A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61146320A (en) | 1986-07-04 |
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