JPS5986612A - Polymer membrane - Google Patents

Polymer membrane

Info

Publication number
JPS5986612A
JPS5986612A JP19640382A JP19640382A JPS5986612A JP S5986612 A JPS5986612 A JP S5986612A JP 19640382 A JP19640382 A JP 19640382A JP 19640382 A JP19640382 A JP 19640382A JP S5986612 A JPS5986612 A JP S5986612A
Authority
JP
Japan
Prior art keywords
group
general formula
repeating unit
triorganosiloxy
polymer
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
Application number
JP19640382A
Other languages
Japanese (ja)
Inventor
Masao Abe
正男 阿部
Takashi Ichinose
一瀬 尚
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.)
Nitto Denko Corp
Original Assignee
Nitto 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 Nitto Electric Industrial Co Ltd filed Critical Nitto Electric Industrial Co Ltd
Priority to JP19640382A priority Critical patent/JPS5986612A/en
Publication of JPS5986612A publication Critical patent/JPS5986612A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:A polymer membrane excellent in oxygen permeability and mechanical properties and useful as a gas separation membrane, prepared from polystyrene having a tris(triorganosiloxy)siloxanyl group in the side chain. CONSTITUTION:The desired polymer membrane is obtained from polystyrene having a tris(triorganosiloxy)siloxyanyl group in the side chain, either having a repeating unit of formula I [wherein X is -NH- or -O-, A and B are each an organic group selected from the group consisting of -OR-, -OSiR3, -OSiR2- OSiR3, and -OSi(OSiR3)3, and R is a 1-5C alkyl or a phenyl] or having both the above repeating unit and a repeating unit of formula II (wherein Y is H, or CHO, Z is an organic group selected from those of formula III, wherein M is -NR2, R is a 1-5C alkyl or phenyl, R<1> is a 1-5C alkylene, or phenylene).

Description

【発明の詳細な説明】 本発明は重合体膜に関し、詳しくは、側鎖にトリス(ト
リオルガノシロキシ)シロキサニル基を有するポリスチ
レンからなり、気体骨%ilt膜として好適に用いるこ
とができる重合体膜に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polymer membrane, and more specifically, a polymer membrane made of polystyrene having a tris(triorganosiloxy)siloxanyl group in a side chain and which can be suitably used as a gaseous bone membrane. Regarding.

近年、有機重合体膜による気体分離、特に空気の酸素富
化が注目されており、既に呼吸器系疾患の患者に対する
治療や、また、燃焼炉用の空気の酸素富化等が試みられ
、或いは既に一部実用化されている。
In recent years, gas separation using organic polymer membranes, especially the oxygen enrichment of air, has been attracting attention, and attempts have already been made to treat patients with respiratory diseases, and to enrich the air for combustion furnaces with oxygen. Some of them have already been put into practical use.

一般に気体の透過速度は次式で与えられる。Generally, the gas permeation rate is given by the following equation.

ここに、Pは透過係数(CI・Cm / CI・秒・c
mHg)、Δpは膜両側の気体の分圧の差、Aは膜の面
ljl (c+J) 、eは膜の厚さくcut)である
。従って、膜が実用的な気体分離性を有するには、単に
透過係数Pが大きいだけではなく、膜厚βを小さくし得
ることが重要であり、更に、分離対象である気体の透過
係数比が大きい程よい。
Here, P is the permeability coefficient (CI・Cm / CI・sec・c
mHg), Δp is the difference in gas partial pressure on both sides of the membrane, A is the membrane surface ljl (c+J), and e is the membrane thickness (cut). Therefore, in order for a membrane to have practical gas separation properties, it is important not only to have a large permeability coefficient P but also to be able to reduce the membrane thickness β. The bigger the better.

−ダーであって、従来、知られている重合体膜の中では
最大であるが、この膜は機械的強度が小さいために、膜
厚を100μ以上にする必要があり、従って、透過係数
は大きくとも、透過速度を大きくすることができない。
This membrane is the largest of the conventionally known polymer membranes, but as this membrane has low mechanical strength, it is necessary to have a thickness of 100μ or more, and therefore the permeability coefficient is Even if it is large, the permeation speed cannot be increased.

また、窒素に対する酸素の透過係数比も精々2程度であ
って、酸素の選択分離性に劣る。このため、米国特許第
3,189,662号には、ポリシロキサン/ポリカー
ボネートブロック共重合体からなる気体分離膜が提案さ
れている。この膜は膜厚1μ以下に薄膜化が可能であり
、また、ジメチルシロキサン含量によって透過係数を制
御し得るが、酸素の透過係数が5X10−9cJ(ST
P )  ・cm / cut・秒・cml1g以上で
あるジメチルシロキサン含量の領域では、窒素に対する
酸素の透過係数比は2〜2.7程度である。
Further, the permeability coefficient ratio of oxygen to nitrogen is about 2 at most, and the selective separation of oxygen is poor. For this reason, US Pat. No. 3,189,662 proposes a gas separation membrane made of a polysiloxane/polycarbonate block copolymer. This membrane can be made as thin as 1μ or less, and the permeability coefficient can be controlled by the dimethylsiloxane content, but the oxygen permeability coefficient is 5X10-9cJ (ST
P ) ·cm/cut·sec·cml In the range of dimethylsiloxane content of 1 g or more, the permeability coefficient ratio of oxygen to nitrogen is about 2 to 2.7.

このように透過速度を高めるために薄膜化が可能な重合
体膜でも、透過係数をポリジメチルシロキサン程度まで
高くすると、透過係数比が小さくなり、透過係数比を3
〜4倍にまで高めるときは、透過係数は10−9cl 
(STP )  ・cm / cra ・秒・cmHg
のオーダーまで低下する。
Even with polymer membranes that can be made thinner to increase the permeation rate, when the permeability coefficient is increased to the level of polydimethylsiloxane, the permeability coefficient ratio decreases, and the permeability coefficient ratio decreases to 3.
When increasing to ~4 times, the permeability coefficient is 10-9cl
(STP) ・cm/cra ・sec・cmHg
decreases to the order of .

本発明者らは、上記した問題を解決するために鋭意研究
した結果、ポリスチレンの側鎖にトリス(トリオルガノ
シロキシ)シロキサニル基を導入することにより、酸素
の透過性及び選択性にすぐれると共に、薄膜化も可能で
あることを見出して、本発明に至ったものである。
As a result of intensive research to solve the above problems, the present inventors have found that by introducing tris(triorganosiloxy)siloxanyl groups into the side chains of polystyrene, it has excellent oxygen permeability and selectivity, and The present invention was achieved by discovering that it is also possible to make the film thinner.

本発明による第1の重合体膜は、一般式(1) (但し、Xは−NH−又は−〇−を示し、A及びBは −OR・−O5]、R3・−〇5jR20SjR3及び
 −O5l(os j+< 3) 3よりなる群から選
ばれる有機基であり、Rは炭素数1〜5のアルキル基又
はフェニル基を示す。)で表わされる繰返し単位を有す
るトリス(+−リオルガノシロキシ)シロキナニル基を
側鎖にもつポリスチレンよりなることを特徴とする。
The first polymer film according to the present invention has the general formula (1) (wherein, (os j+ < 3) Tris(+-liorganosiloxy) having a repeating unit represented by an organic group selected from the group consisting of 3, where R represents an alkyl group having 1 to 5 carbon atoms or a phenyl group. It is characterized by being made of polystyrene with siloquinanyl groups in its side chains.

また、本発明による第2の重合体膜は、上記一般式(1
)で表わされる繰返し単位と、一般式■ (Il) (但し、Yは−H又は−CH3を示し、Zはよりなる群
から選ばれる有機基を示し、Mは−NR2を示し、Rは
炭素数1〜5のアルキル基又はフェニル基を示し、R’
は炭素数1〜5のアルキレン基又はフェニレン基を示す
。)で表わされる繰返し単位とを有するトリス(トリオ
ルガノシロキシ)シロキサニル基を側鎖にもつ実質的に
線状であるポリスチレンよりなることを特徴とする。
Further, the second polymer film according to the present invention has the above general formula (1
) and the general formula ■ (Il) (where Y represents -H or -CH3, Z represents an organic group selected from the group consisting of, M represents -NR2, and R represents carbon Represents an alkyl group or phenyl group of numbers 1 to 5, R'
represents an alkylene group or phenylene group having 1 to 5 carbon atoms. ) is characterized in that it is made of substantially linear polystyrene having a tris(triorganosiloxy)siloxanyl group as a side chain.

一般式(I)で表わされる繰返し単位を有するポリスチ
レンからなる本発明による第1の重合体膜は、一般式 ([) (但し、X、、A、B及びRは前記と同じ)で表わされ
るトリス(+−リオルガノシロキシ)シロキサニル基を
側鎖にもつスチレン誘導体単量体を、適宜の有機溶剤中
にて重合開始剤を用いて、通常のビニル重合を行なわせ
て重合体を得、これを後述する方法にて製膜することに
より得ることができる。尚、Rがアルキル基である場合
、好ましい具体例としてメチル基、エチル基等を挙げる
ことができるが、すべてのRが同一である必要はない。
The first polymer membrane according to the present invention made of polystyrene having a repeating unit represented by the general formula (I) is represented by the general formula ([) (where X, , A, B and R are the same as above) A styrene derivative monomer having a tris(+-liorganosiloxy)siloxanyl group in its side chain is subjected to ordinary vinyl polymerization using a polymerization initiator in an appropriate organic solvent to obtain a polymer. It can be obtained by forming a film using the method described below. In addition, when R is an alkyl group, a methyl group, an ethyl group, etc. can be mentioned as a preferable example, However, It is not necessary that all R's are the same.

一般式(1)においても同じである。The same applies to general formula (1).

一般式(III)で表わされるスチレン誘導体単量体は
、硫酸の存在下に一般式 () (但し、X及びRは前記と同じ) で表わされるトリアルコキシシラン化合物と、一般式 %式%) () (但し、Rは前記と同じ) で表わされるトリス(トリオルガノシロキシ)アセトキ
シシラン、又はこれと次の一般式%式% () () (但し、Rは前記と同じ) で表わされるアセトキシトリオルガノシラン又はアセト
キシペンタオルガノジシロキサンとの混合物を反応させ
ることにより行なうことができる。
The styrene derivative monomer represented by the general formula (III) is combined with a trialkoxysilane compound represented by the general formula () (where X and R are the same as above) in the presence of sulfuric acid, and a trialkoxysilane compound represented by the general formula (% formula %) () (However, R is the same as above) Tris(triorganosiloxy)acetoxysilane, or this and the following general formula % Formula % () () (However, R is the same as above) This can be carried out by reacting a mixture of triorganosilane or acetoxypentaroganodisiloxane.

一般式(IV)で表わされるトリアルコキシシラン化合
物は、一般式 (■) (但し、Xは前記と同じ) で表わされる核置換スチレンと、一般式0式%) () (但し、Rは前記と同じ) で表わされるγ−イソシアナトプロピルトリアルコキシ
シランとの反応によって得ることができる。
The trialkoxysilane compound represented by the general formula (IV) is composed of a nuclear-substituted styrene represented by the general formula (■) (where, It can be obtained by reaction with γ-isocyanatopropyltrialkoxysilane represented by

ここに、T−イソシアナトプロピルトリアルコキシシラ
ンはシランカップリング剤として市販されている。
Here, T-isocyanatopropyltrialkoxysilane is commercially available as a silane coupling agent.

以上のようにして得られた一般式(II[)で表わされ
るトリス(トリオルガノシロキシ)シロキサニル基を側
鎖にもつスチレン誘導体単量体は、塊状重合、又は適宜
の有機溶剤中、重合開始剤を用いる通常の溶液重合等の
方法によりビニル重合を行なえば、前記一般式(1)で
表わされる繰返し1 単位を有する重合体を得ることができる。
The styrene derivative monomer having a tris(triorganosiloxy)siloxanyl group in the side chain represented by the general formula (II[) obtained as described above can be polymerized in bulk or in an appropriate organic solvent using a polymerization initiator. If vinyl polymerization is carried out by a conventional method such as solution polymerization using the above-mentioned general formula (1), a polymer having one repeating unit represented by the general formula (1) can be obtained.

上記ビニル重合の方法は、特に制限されず、ラジカル重
合、カチオン重合、アニオン重合のいずれであってもよ
い。重合開始剤はそれぞれの重合方法により適宜に選ば
れるが、例えば、ラジカル重合の場合は、ベンゾイルパ
ーオキサイド等の過酸化物や、アゾビスイソブチロニト
リル等のアゾ化合物が用いられる。場合によっては、無
触媒熱重合も可能である。また、カチオン重合の場合は
、三フッ化ホウ素ジエチルエーテラート等、アニオン重
合の場合はn−ブチルリチウム等が用いられる。尚、必
要に応じて、上記重合において、他の単量体を共重合成
分として用いてよいのは勿論である。
The vinyl polymerization method is not particularly limited, and may be radical polymerization, cationic polymerization, or anionic polymerization. The polymerization initiator is appropriately selected depending on the respective polymerization method, and for example, in the case of radical polymerization, a peroxide such as benzoyl peroxide or an azo compound such as azobisisobutyronitrile is used. In some cases, non-catalytic thermal polymerization is also possible. Further, in the case of cationic polymerization, boron trifluoride diethyl etherate and the like are used, and in the case of anionic polymerization, n-butyllithium and the like are used. It goes without saying that other monomers may be used as copolymerization components in the above polymerization, if necessary.

上記の一般式(I[[)で表わされるスチレン誘導体単
量体の重合を有機溶剤中で行なう場合、溶剤としては、
この単量体を溶解すると共に、これに対して不活性であ
り、更に、生成する重合体をも溶解させる溶剤が用いら
れるが、特に、ベンゼン等の芳香族炭化水素が好ましく
用いられる。
When polymerizing the styrene derivative monomer represented by the above general formula (I[[) in an organic solvent, the solvent may be
A solvent that dissolves this monomer and is inert to it and also dissolves the produced polymer is used, and aromatic hydrocarbons such as benzene are particularly preferably used.

2 溶剤の使用量は特に制限されないが、単量体の濃度が1
〜100ii量%、好ましくは10〜50重量%程度と
なるように用いるのが適当である。
2 The amount of solvent used is not particularly limited, but if the monomer concentration is 1
It is appropriate to use it in an amount of about 100% by weight, preferably about 10 to 50% by weight.

重合温度は、通常、室温乃至100℃の範囲が適当であ
り、反応時間は通常、1時間乃至24時間が適当である
The polymerization temperature is usually in the range of room temperature to 100°C, and the reaction time is usually in the range of 1 hour to 24 hours.

上記のようにして得られるトリス(トリオルガノシロキ
シ)シロキサニル基を側鎖に有するポリスチレンは、通
常、0.1〜1.0の対数粘度(ベンゼン中、0.5 
g / dβの濃度で30℃で測定)を有し、すぐれた
製膜性を有する。
The polystyrene having a tris(triorganosiloxy)siloxanyl group in the side chain obtained as described above usually has a logarithmic viscosity of 0.1 to 1.0 (in benzene, 0.5
g/dβ (measured at 30°C), and has excellent film forming properties.

本発明による第1の重合体膜は、以上のようにして得ら
れるポリスチレンを後述するようにして製膜することに
より製造される。
The first polymer film according to the present invention is produced by forming the polystyrene obtained as described above into a film as described below.

次に、本発明による第2の重合体膜は、前記一般式(I
)で表わされる繰返し単位に加えて、一般式(n)で表
わされる繰返し単位を有効量含む実質的に線状である共
重合体からなる。
Next, the second polymer film according to the present invention has the general formula (I
) In addition to the repeating unit represented by formula (n), the copolymer is composed of a substantially linear copolymer containing an effective amount of the repeating unit represented by general formula (n).

一般式(II)において、Rは前記したとおりであるが
、R゛は炭素数1〜5のアルキレン基又は3 フェニレン基を示し、アルキレン基の好ましい具体例と
゛して、−CH2CH2−1−CH(CH3) CH2
−等を挙げることができる。
In general formula (II), R is as described above, but R' represents an alkylene group having 1 to 5 carbon atoms or a 3-phenylene group, and a preferred specific example of the alkylene group is -CH2CH2-1-CH (CH3) CH2
- and so on.

このような第2の重合体膜は、前記一般式(I[)で表
わされるトリス(トリオルガノシロキシ)シロキサニル
基を側鎖に有するスチレン誘導体と、一般式 () (但し、Y及びZは前記と同じ) で表わされるエチレン性不飽和単量体とを共重合するこ
とにより得られる。共重合の方法は前記と同じく、ビニ
ル重合であれば、特に制限されるものではない。
Such a second polymer film is made of a styrene derivative having a tris(triorganosiloxy)siloxanyl group represented by the general formula (I[) in its side chain, and a styrene derivative represented by the general formula (I[)] (wherein Y and Z are It can be obtained by copolymerizing with an ethylenically unsaturated monomer represented by As mentioned above, the copolymerization method is not particularly limited as long as it is vinyl polymerization.

一般式(X)で表わされるエチレン性不飽和単量体にお
いて、Yは−H又は−CH3−であり、2の好ましい具
体例として、 4 等を挙げることができる。従って、本発明において用い
得る好ましいエチレン性不飽和単量体として、スチレン
、p−ジメチルアミノスチレン、エチルメククリレート
、2−ジメチルアミノエチルメタクリレート、4−ビニ
ルピリジン等を挙げることができる。
In the ethylenically unsaturated monomer represented by the general formula (X), Y is -H or -CH3-, and preferred specific examples of 2 include 4 and the like. Therefore, preferred ethylenically unsaturated monomers that can be used in the present invention include styrene, p-dimethylaminostyrene, ethyl meccrylate, 2-dimethylaminoethyl methacrylate, and 4-vinylpyridine.

上記トリス(トリオルガノシロキシ)シロキサニル基を
側鎖に有するポリスチレン、又は上記一般式(X)で表
わされる単量体との共重合体から本発明による重合体膜
を種々の方法によって製造することができる。通常は、
以上のようにして得られた重合体を適宜の有機溶剤に熔
解して均一な製膜溶液とし、これを適宜の支持基材上に
流延塗布した後、溶剤を蒸発させて、均質な膜を得る。
The polymer film according to the present invention can be produced by various methods from the above polystyrene having a tris(triorganosiloxy)siloxanyl group in the side chain or a copolymer with a monomer represented by the above general formula (X). can. Normally,
The polymer obtained as described above is dissolved in an appropriate organic solvent to obtain a uniform film-forming solution, which is cast onto an appropriate support base material, and then the solvent is evaporated to form a homogeneous film. get.

また、上記製膜溶液をこの溶液よりも大きい比重5 を有する液体上に注いで、展開させ、次いで、溶剤を蒸
発させることによっても薄膜を得ることができる。製膜
溶液を調製するための溶剤としては、前記したベンゼン
、トルエン等の芳香族炭化水素が好ましいが、また、テ
トラヒドロフランも用いられる。
A thin film can also be obtained by pouring the film-forming solution onto a liquid having a specific gravity 5 higher than that of the solution, developing it, and then evaporating the solvent. As the solvent for preparing the film-forming solution, aromatic hydrocarbons such as the above-mentioned benzene and toluene are preferred, but tetrahydrofuran is also used.

気体の透過速度を大きくするためには、膜厚は薄い程よ
く、0.05〜30μが好ましい。従って、製膜溶液の
重合体濃度は10重量%以下が好ましい。
In order to increase the gas permeation rate, the thinner the film thickness, the better, and preferably 0.05 to 30μ. Therefore, the polymer concentration of the membrane forming solution is preferably 10% by weight or less.

本発明による膜は、以上のように、ポリスチレン又はそ
の共重合体が側鎖にトリス(トリオルガノシロキシ)シ
ロキサニル基を有し、これらトリオルガノシロキシ基が
酸素透過のための場を形成するので、極めて高い酸素透
過性を有する。また、重合体主鎖が剛直な炭素−炭素骨
格で形成されているため、本発明による膜は機械的緒特
性にすぐれ、薄膜化も可能である。
As described above, in the membrane according to the present invention, polystyrene or its copolymer has tris(triorganosiloxy)siloxanyl groups in the side chains, and these triorganosiloxy groups form a field for oxygen permeation. It has extremely high oxygen permeability. Further, since the polymer main chain is formed of a rigid carbon-carbon skeleton, the film according to the present invention has excellent mechanical properties and can be made thin.

以下に実施例を挙げて本発明を説明するが、本発明はこ
れら実施例により何ら限定されるもので6 はない。尚、以下の実施例において、気体の透過係数P
は25℃の温度で高真空法により求めたものである。
The present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples in any way. In addition, in the following examples, the gas permeability coefficient P
was determined by the high vacuum method at a temperature of 25°C.

実施例1 (alN−(ペンタキス(トリメチルシロキシ)シロキ
サニルプロプル)、N’−p−スチリル尿素の合成 少量の重合禁止剤、p−t−ブチルカテコールの存在下
に、p−アミノスチレン83.3g(0,70モル)の
ベンゼン(750g)溶液中に、ffl拌しながら、T
−イソシアナトプロピルトリエトキシシラン162g(
0,74モル)を徐々に滴下し、室温で3時間反応させ
た。反応の進行はガスクロマトグラフィーにより追跡し
た。
Example 1 Synthesis of (alN-(pentakis(trimethylsiloxy)siloxanylpropyl), N'-p-styrylurea) In the presence of a small amount of polymerization inhibitor, pt-butylcatechol, p-aminostyrene 83 In a solution of .3 g (0.70 mol) of benzene (750 g), with stirring, T
-162g of isocyanatopropyltriethoxysilane (
0.74 mol) was gradually added dropwise, and the mixture was reacted at room temperature for 3 hours. The progress of the reaction was monitored by gas chromatography.

次いで、反応混合物を氷水にて10℃以下に冷却しなが
ら、トリス(トリメチルシロキシ)アセトキシシラン2
48g(0,70モル)とトリメチルアセトキシシラン
185g(1,4モル)を加えた。攪拌を続けながら、
硫酸のエタノール溶液(30重量%、50g)を1時間
を要してゆつく7 り滴下した後、反応混合物を室温に戻して20時  □
間反応させた。
Next, tris(trimethylsiloxy)acetoxysilane 2 was added while cooling the reaction mixture to below 10°C with ice water.
48 g (0.70 mol) and 185 g (1.4 mol) of trimethylacetoxysilane were added. While continuing to stir,
An ethanol solution of sulfuric acid (30% by weight, 50 g) was slowly added dropwise over a period of 1 hour, and the reaction mixture was returned to room temperature at 8:00 p.m.
It was allowed to react for a while.

この後、反応混合物に蒸留水200gを加えて洗蒔し、
分離した水層を除いた後、炭酸水素ナトリウム水溶液で
洗滌し、再び蒸留水で洗滌した後、硫酸マグネシウム上
で乾燥した。
After this, 200 g of distilled water was added to the reaction mixture and washed.
After removing the separated aqueous layer, it was washed with an aqueous sodium bicarbonate solution, washed again with distilled water, and then dried over magnesium sulfate.

このようにして得られた単量体溶液は、アスピレータに
接続したエバポレータにて減圧しつつ、60℃に加温し
て溶剤を除去し、次いで、真空ポンプにより0.5 m
m l(gの減圧下に80℃に加熱して、残存する揮発
性物質を除去した。
The monomer solution thus obtained was heated to 60°C while reducing the pressure with an evaporator connected to an aspirator to remove the solvent, and then heated to 0.5 m with a vacuum pump.
The remaining volatiles were removed by heating to 80° C. under reduced pressure of ml (g).

(b1重合体の合成 上記fa)で得た単量体であるN−(ペンタキス(トリ
メチルシロキシ)シロキサニルプロプル〕。
(B1 Synthesis of Polymer N-(pentakis(trimethylsiloxy)siloxanylpropyl), which is the monomer obtained in fa) above].

N’−p−スチリル尿素10gをベンゼン40gと共に
コック付のガラス製アンプルに仕込み、次に、10重量
%の過酸化ベンゾイルのベンゼン溶液3gを仕込んだ後
、ドライアイス−メタノール浴で冷却しながら、真空ラ
インに接続して脱気し、窒素置換、融解、冷却のサイク
ルを繰返して、系8 中の酸素を除去した。この後、系を真空に保って、アン
プルを溶封した。
10 g of N'-p-styrylurea and 40 g of benzene were charged into a glass ampoule with a cock, and then 3 g of a 10% by weight benzoyl peroxide solution in benzene was charged, and while cooling in a dry ice-methanol bath, The system was connected to a vacuum line for degassing, and a cycle of nitrogen substitution, melting, and cooling was repeated to remove oxygen in system 8. After this, the system was kept in vacuum and the ampoule was sealed.

70℃の恒温槽中にアンプルを放置し、震とうさせて、
16時間重合させた。アンプルを開封し、反応混合物を
大量のメタノール中に注いで、重合体を沈殿させた。こ
の重合体をメタノールで洗滌した後、濾別し、60℃の
温度で8時間真空乾燥して、重合体9.2gを得た。こ
の重合体の対数粘度は0.55であった。
The ampoule was left in a thermostat at 70°C and shaken.
Polymerization was carried out for 16 hours. The ampoule was opened and the reaction mixture was poured into a large amount of methanol to precipitate the polymer. After washing this polymer with methanol, it was filtered and vacuum-dried at a temperature of 60° C. for 8 hours to obtain 9.2 g of a polymer. The logarithmic viscosity of this polymer was 0.55.

Tel気体分離膜の製造 上で得た重合体をベンゼン−メタノール系にて再沈殿法
により精製した後、5重量%のベンゼン溶液とし、4μ
の濾紙にて異物を除去して、製膜溶液とした。バットに
40℃に加温した蒸留水を入れ、この水面上に製膜溶液
を注射器にて静かに注いで展開させ、薄膜を形成させた
。この薄膜を多孔質ポリプロピレン膜(ポリプラスチッ
ク社製ジュラガード)にてすくい上げ、60℃で8時間
真空乾燥した。このようにして得られた薄膜は厚み4μ
の均質膜であった。
The polymer obtained in the production of the Tel gas separation membrane was purified by the reprecipitation method in a benzene-methanol system, then made into a 5% by weight benzene solution, and 4μ
Foreign matter was removed using a filter paper to obtain a membrane forming solution. Distilled water heated to 40° C. was placed in a vat, and the film forming solution was gently poured onto the water surface using a syringe and spread to form a thin film. This thin film was scooped up with a porous polypropylene membrane (Duraguard manufactured by Polyplastics) and vacuum-dried at 60° C. for 8 hours. The thin film thus obtained has a thickness of 4 μm.
It was a homogeneous film.

9 高真空法により測定した気体の透過係数は、酸素につい
て6.5 X 10−9ca (STP )  ・Cm
/cn−秒・印Hg、窒素について1.7X10  c
+11(STP)  ・印/d・秒・(至)Hgであっ
た。
9 The gas permeability coefficient measured by the high vacuum method is 6.5 x 10-9ca (STP) ・Cm for oxygen.
/cn-sec・mark Hg, 1.7X10 c for nitrogen
+11 (STP) ・mark/d・sec・(to) Hg.

実施例2 実施例1で得た単量体5gとp−ジメチルアミノスチレ
ン5gとを用いて、実施例1と同様にして、対数粘度0
.62の共重合体を得た。
Example 2 Using 5 g of the monomer obtained in Example 1 and 5 g of p-dimethylaminostyrene, the procedure was carried out in the same manner as in Example 1 until the logarithmic viscosity was 0.
.. 62 copolymers were obtained.

この共重合体を用いて、実施例1と全く同様にして均質
膜を調製し、透過係数を測定したところ、・CI+1/
cIa・秒・cmHgであって、窒素に対する透過係数
比は5であり、酸素の透過係数を考慮すれば、極めて高
性能膜であることが理解される。
Using this copolymer, a homogeneous membrane was prepared in exactly the same manner as in Example 1, and the permeability coefficient was measured.
It is cIa·sec·cmHg, and the permeability coefficient ratio to nitrogen is 5, and if the permeability coefficient of oxygen is considered, it is understood that it is an extremely high performance membrane.

実施例3 前記一般式において、X、A、B、R,Y及びZを種々
に変えて、実施例1と同様にして膜を得た。これらの膜
についての透過係数PX10cJ(STP )  ・c
m/aa−秒・cmlgを下表に示す。
Example 3 Membranes were obtained in the same manner as in Example 1, except that X, A, B, R, Y, and Z in the general formula were variously changed. Permeability coefficient PX10cJ(STP)・c for these membranes
m/aa-sec.cmlg is shown in the table below.

0

Claims (2)

【特許請求の範囲】[Claims] (1)  一般式 (但し、Xは−NH−又は−〇−を示し、A及びBは −OR・−03iR3・−QSiR2−08j−R3及
び −08i (O8iR3)3 よりなる群から選ばれる有機基であり、Rは炭素数1〜
5のアルキル基又はフェニル基を示す。)で表わされる
繰返し単位を有するトリス(トリオルガノシロキシ)シ
ロキサニル基を側鎖にもつポリスチレンよりなることを
特徴とする重合体膜。
(1) General formula (wherein, is a group, and R has 1 to 1 carbon atoms.
5 represents an alkyl group or a phenyl group. ) A polymer film comprising polystyrene having a tris(triorganosiloxy)siloxanyl group in a side chain having a repeating unit represented by:
(2)一般式 (但し、Xは−NH−又は−O−を示し、A及びBは −OR・−05xR3・−08IR20SiR3及び 
−O5L (O5iR3)3 よりなる群から選ばれる有機基であり、Rは炭素数1〜
5のアルキル基又はフェニル基を示す。)で表わされる
繰返し単位と、 一般式 Y ■ (但し、Yは−H又は−CH3を示し、Zはよりなる群
から選ばれる有機基を示し、Mは−N R2を示し、R
は炭素数1〜5のアルキル基又はフェニル基を示し、R
゛は炭素数1〜5のアルキレン基又はフェニレン基を示
す。)で表わされる繰返し単位とを有する1−リス(ト
リオルガノシロキシ)シロキサニル基を側鎖にもつ実質
的に線状であるポリスチレンよりなることを特徴とする
重合体膜。
(2) General formula (where, X represents -NH- or -O-, A and B represent -OR・-05xR3・-08IR20SiR3 and
-O5L (O5iR3)3 is an organic group selected from the group consisting of
5 represents an alkyl group or a phenyl group. ), and a repeating unit represented by the general formula Y (where, Y represents -H or -CH3, Z represents an organic group selected from the group consisting of, M represents -N R2, and R
represents an alkyl group or phenyl group having 1 to 5 carbon atoms, and R
" represents an alkylene group or a phenylene group having 1 to 5 carbon atoms. ) A polymer film comprising substantially linear polystyrene having a 1-lith(triorganosiloxy)siloxanyl group in a side chain having a repeating unit represented by:
JP19640382A 1982-11-08 1982-11-08 Polymer membrane Pending JPS5986612A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19640382A JPS5986612A (en) 1982-11-08 1982-11-08 Polymer membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19640382A JPS5986612A (en) 1982-11-08 1982-11-08 Polymer membrane

Publications (1)

Publication Number Publication Date
JPS5986612A true JPS5986612A (en) 1984-05-18

Family

ID=16357277

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19640382A Pending JPS5986612A (en) 1982-11-08 1982-11-08 Polymer membrane

Country Status (1)

Country Link
JP (1) JPS5986612A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4633003A (en) * 1985-11-25 1986-12-30 Alcon Laboratories, Inc. Siloxane monomers for ophthalmic applications
US4813983A (en) * 1985-03-13 1989-03-21 Asahi Kasei Kogyo Kabushiki Kaisha Composite membrane for use in gas separation
EP0985443A3 (en) * 1998-09-10 2007-08-08 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Semipermeable membranes
US20110120344A1 (en) * 2008-07-29 2011-05-26 E.I. Dupont De Nemours And Company Surface active blocked isocyanates and coating compositions thereof
US20220119421A1 (en) * 2018-12-31 2022-04-21 Dow Silicones Corporation Branched organosilicon compound, method of preparing same, and related compositions

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4813983A (en) * 1985-03-13 1989-03-21 Asahi Kasei Kogyo Kabushiki Kaisha Composite membrane for use in gas separation
US4633003A (en) * 1985-11-25 1986-12-30 Alcon Laboratories, Inc. Siloxane monomers for ophthalmic applications
EP0985443A3 (en) * 1998-09-10 2007-08-08 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Semipermeable membranes
US20110120344A1 (en) * 2008-07-29 2011-05-26 E.I. Dupont De Nemours And Company Surface active blocked isocyanates and coating compositions thereof
US8784555B2 (en) * 2008-07-29 2014-07-22 Axalta Coating Systems Ip Co., Llc Surface active blocked isocyanates and coating compositions thereof
US20220119421A1 (en) * 2018-12-31 2022-04-21 Dow Silicones Corporation Branched organosilicon compound, method of preparing same, and related compositions

Similar Documents

Publication Publication Date Title
US4689267A (en) Composite hollow fiber
US5166298A (en) Oxygen-permeable transparent polymer compositions for contact lenses of the rigid type
US3665052A (en) Method of preparing a block copolymer containing a poly-alpha-methylstyrene block and a polydiorganosiloxane block
WO2002081485A1 (en) Monomer, polymer, and ocular lens and contact lens each obtained therefrom
JPS6140709B2 (en)
JPS5986612A (en) Polymer membrane
JPS6178402A (en) Separation of organic liquid mixture
US4968750A (en) Block copolymers containing polysiloxane segments
Kawakami et al. Relationships between structure, permeability and glass transition temperature of oligodimethylsiloxanyl substituted polymers
JP3141958B2 (en) Gas permeable polymer and method for producing the same
JP3484591B2 (en) Plastic molded article, method for producing the same, and optical article
JPH02258815A (en) (meth)acrylate copolymer
JPH0784516B2 (en) Method for producing a polymer having a polyether repeating unit in its side chain
JP2005154742A (en) Film-like material, its manufacturing method and its use
JPS60110303A (en) Permselective membrane and composite film
JPS5840127A (en) Gas-permeable membrane
JP3290461B2 (en) Diphenylacetylene polymer
JPH0632834A (en) Silicon-containing polymer and molded product using the same
JPH0625832B2 (en) Contact lens material
JP2959060B2 (en) Separation membrane
JPH041655B2 (en)
JPS60225606A (en) Gas permselective membrane
JPS63277210A (en) Gas-permeable material
JPS59123502A (en) Selective permeable membrane
JP4686840B2 (en) Monomer, polymer and ophthalmic lens using the same