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JPH03296425A - Silicon-modified polyether imide and selectivity gas-permeable membrane - Google Patents

Silicon-modified polyether imide and selectivity gas-permeable membrane

Info

Publication number
JPH03296425A
JPH03296425A JP9629490A JP9629490A JPH03296425A JP H03296425 A JPH03296425 A JP H03296425A JP 9629490 A JP9629490 A JP 9629490A JP 9629490 A JP9629490 A JP 9629490A JP H03296425 A JPH03296425 A JP H03296425A
Authority
JP
Japan
Prior art keywords
membrane
polyether imide
gas
integer
silicon
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
JP9629490A
Other languages
Japanese (ja)
Inventor
Yoshio Murashige
村重 義雄
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP9629490A priority Critical patent/JPH03296425A/en
Publication of JPH03296425A publication Critical patent/JPH03296425A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Silicon Polymers (AREA)

Abstract

PURPOSE:To obtain the membrane having an excellent character of selective gas permeability by a method wherein the membrane consists mainly of silicon- modified polyether imide, the product of reaction between a specific polyether imide and a specific modified polydimethylsiloxane. CONSTITUTION:The subject membrane consists mainly of the silicon-modified polyether imide produced by reaction between the polyether imide having the repeating unit represented by the general formula I (wherein n is an integer of 1-7) and the modified polydimethylsiloxane having the repeating units of dimethylsiloxane represented by the general formula II (wherein R is 1-6C alkylene group, m is an integer not less than 5, l is an integer not less than 1 and the number of primary amino group is one per one polymer molecule) and the primary amino group in the side chain. This reaction product is dissolved in chlorine solvents such as dichloromethane and chloroform to form the membrane. This selectively gas-permeable membrane has an excellent selective gas permeability and heat resistance, solvent resistance and a high strength.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はガス混合物の分離、精製に用いられるガス選択
透過性膜に関し、またガス選択透過性膜に適する化合物
に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a gas selectively permeable membrane used for separation and purification of gas mixtures, and also relates to compounds suitable for gas selectively permeable membranes.

〔従来の技術〕[Conventional technology]

近年ガス混合物の分離・精製をガス選択透過性膜で行う
ことが積極的に検討されている。例えば空気から酸素を
選択的に透過させて酸素富化空気を得て医療あるいは燃
焼システムに利用する試みがなされている。又、石炭、
天然ガス、オイルサンド等を水蒸気改質や熱分解処理等
することによって得られる水素、−酸化炭素、メタン等
を含む合成カスから水素を出発原料としてメタノール等
の基礎化学品を製造する試み等もなされている。
In recent years, active consideration has been given to separating and purifying gas mixtures using gas selectively permeable membranes. For example, attempts have been made to selectively permeate oxygen from air to obtain oxygen-enriched air for use in medical treatment or combustion systems. Also, coal,
Attempts have also been made to produce basic chemicals such as methanol using hydrogen as a starting material from synthetic sludge containing hydrogen, carbon oxide, methane, etc. obtained by steam reforming or thermal decomposition of natural gas, oil sands, etc. being done.

これらの用途に用いられるガス選択透過性膜にはガス選
択性とガス透過性がいずれも大きい事、耐熱性、耐薬品
性、高強度を有していること等の特性が要求されている
Gas selectively permeable membranes used in these applications are required to have characteristics such as high gas selectivity and gas permeability, heat resistance, chemical resistance, and high strength.

ガス選択性とは特定ガスと他のガスとの透過速度の比で
表される偵であり、ガス選択性が大きい事はガス分離能
がすぐわていることを意味する。
Gas selectivity is expressed as the ratio of permeation rates between a specific gas and other gases, and a high gas selectivity means excellent gas separation ability.

又、ガス透過性が大きいとは、膜を透過するガスの絶対
量が多いことであり大量のガスを処理しうろことを意味
する。
Furthermore, the term "high gas permeability" means that the absolute amount of gas that permeates through the membrane is large, meaning that a large amount of gas can be processed.

例えば空気中の酸素透過選択性が優れた膜としてポリエ
ーテルイミドからなるもの(米国特許第4.156,5
97号)が知られており、又、ガス透過速度の大きい膜
としてポリジメチルシロキサン等のシリコーン系ポリマ
ーからなるものが知られている。
For example, a membrane made of polyetherimide with excellent oxygen permeation selectivity in air (U.S. Pat. No. 4,156,5
No. 97) is known, and membranes made of silicone polymers such as polydimethylsiloxane are also known as membranes with a high gas permeation rate.

(発明が解決しようとする課題〕 しかし、二わら従来の高分子重合体または共重合体の単
一素材で前記の要求特性のすべてを満たすことはできな
い。すなわちガス選択性の大きい高分子素材はガス透過
性が低い点2又ガス透過性の優れた高分子素材はガス選
択性が不充分な点が問題である。
(Problem to be solved by the invention) However, it is not possible to satisfy all of the above required characteristics with a single conventional polymer or copolymer material.In other words, a polymer material with high gas selectivity cannot Another problem is that polymeric materials with excellent gas permeability have insufficient gas selectivity.

例えば、米国特許第4,156,597号に記載されて
いるポリエーテルイミドからなる気体分離膜のガス選択
性は大きく、酸素の窒素に対する選択性は7〜8倍程度
であるが、その透過係数(単位厚さにおける透過速度)
は極めて小さいためこの膜素材単独をガス選択透過性膜
として使用可能な範囲は著しく限定される。
For example, the gas selectivity of the gas separation membrane made of polyetherimide described in U.S. Pat. (Transmission rate per unit thickness)
Since this membrane material is extremely small, the range in which this membrane material alone can be used as a gas selectively permeable membrane is extremely limited.

又、ポリジメチルシロキサンはそのシロキサン結合から
高分子素材中もっとも高いガス透過性を与えるものであ
るが、ガス選択性が小さくて機械的特性が弱く、さらに
他の高分子との相溶性が低いという欠点を有している。
In addition, polydimethylsiloxane has the highest gas permeability among polymer materials due to its siloxane bonds, but it has low gas selectivity, weak mechanical properties, and low compatibility with other polymers. It has drawbacks.

本発明は、これらの問題点を解決すべくなされたもので
あって、ガス選択性とガス透過性がいずれも大きく、か
つ耐熱性、耐薬品性、強度特性に優れた物質、およびそ
の物質からなるガス透過性膜を供給することを目的とす
る。
The present invention has been made to solve these problems, and is directed to a material that has both high gas selectivity and gas permeability, and has excellent heat resistance, chemical resistance, and strength properties, and a material made from the material. The purpose is to provide a gas-permeable membrane with the following properties.

(課四を解決するための手段) 本発明は、−数式工 ■ (ただしnは1〜7の整数を示す。) で示される縁り返し単位を有するポリエーテルイミド及
び−数式■ H2 (ただし、Rは炭素数1勺6のアルキレン基、mは5以
上の整数、1は1以上の整数を示す。−級アミノ基の数
はポリマー−分子あたり一個。)で示される、ジメチル
シロキサンの縁り返し単位を有し、側鎖に一級アミノ基
を有する変性ポリジメチルシロキサンとの反応生成物で
あるシリコーン変性ポリエーテルイミドおよびこれを主
成分とするガス選択透過性膜である。
(Means for Solving Section 4) The present invention provides a polyetherimide having an edge-reversing unit represented by -Math.■ (where n is an integer from 1 to 7) and -Math.H2 (However, , R is an alkylene group having 1 to 6 carbon atoms, m is an integer of 5 or more, and 1 is an integer of 1 or more.The number of amino groups is one per polymer molecule. These are silicone-modified polyetherimide, which is a reaction product of a modified polydimethylsiloxane having repeating units and a primary amino group in its side chain, and a gas-selective permeable membrane containing the silicone-modified polyetherimide as a main component.

〔作 用〕[For production]

本発明に用いるポリエーテルイミドは式1で表わざわる
構造単位を有するもので、好ましくは実質的に式■で表
わされる構造単位からなる重合体である。このようなポ
リエーテルイミドはフェノオキシフエニルジカルボン酸
無水物とフェニレンシアミンとの縮重合によって得られ
る重合体であり、CnH2,基は直鎖構造あるいは分岐
構造をとることが出来る。
The polyetherimide used in the present invention has a structural unit represented by formula 1, and is preferably a polymer consisting essentially of structural units represented by formula (2). Such polyetherimide is a polymer obtained by condensation polymerization of phenoxyphenyldicarboxylic anhydride and phenylenecyamine, and the CnH2 group can have a linear structure or a branched structure.

該重合体の代表例として、2.2−ビス(4−(3,4
ジカルボキシフエノオキシ)フェニル〕プロパン無水物
とメタフェニレンジアミンとの縮重合反応によって得ら
九る を挙げることができる。
A typical example of the polymer is 2,2-bis(4-(3,4
Examples include those obtained by a polycondensation reaction of dicarboxyphenoxyphenyl]propane anhydride and metaphenylenediamine.

これらのポリエーテルイミドにおいては芳香族イミド構
造が剛性を与え、又、エーテル結合が流動性と加工性を
与え、全体として優れた耐熱性、耐薬品性、機械的特性
を有している。
In these polyetherimides, the aromatic imide structure provides rigidity, the ether bond provides fluidity and processability, and overall they have excellent heat resistance, chemical resistance, and mechanical properties.

本発明において用いられるポリエーテルイミドはGPC
法における数平均分子量が5000〜100000の範
囲内のものであることが好ましい。
The polyetherimide used in the present invention is GPC
The number average molecular weight in the method is preferably within the range of 5,000 to 100,000.

本発明のシリコーン変性ポリエーテルイミドはポリエー
テルイミドを不活性溶剤に溶解し、次いで側鎖に一級ア
ミノ基を持つ変性ポリジメチルシロキサン(以下「変性
シリコーン」という)を添加、混合し加熱により両ポリ
マーを反応させることによって得ることができる。反応
生成物の構造は特に限定されないが、成膜性の点からポ
リエーテルイミドを主鎖とし変性シリコーンを櫛の刃状
に結合した構造のものであることが好ましい。反応時に
おける混合溶液の温度はおよそ30〜300℃程度であ
ればよく、使用する不活性溶剤の種類によって適宜選択
される。
The silicone-modified polyetherimide of the present invention is produced by dissolving polyetherimide in an inert solvent, then adding modified polydimethylsiloxane having a primary amino group in the side chain (hereinafter referred to as "modified silicone"), mixing, and heating to produce both polymers. It can be obtained by reacting. The structure of the reaction product is not particularly limited, but from the viewpoint of film-forming properties, it is preferable to have a structure in which polyetherimide is the main chain and modified silicone is bonded in a comb blade shape. The temperature of the mixed solution during the reaction may be approximately 30 to 300°C, and is appropriately selected depending on the type of inert solvent used.

反応生成物中の同成分の存在割合は特に限定されないが
、一方の成分が15〜85重量%の範囲であることが好
ましい。これは一方の成分の比率が15重量%より少な
いとその成分の有用な特性が発現しがたいからである。
Although the proportion of the same components in the reaction product is not particularly limited, it is preferable that one component is in the range of 15 to 85% by weight. This is because if the ratio of one component is less than 15% by weight, it is difficult for that component to exhibit its useful properties.

例えばポリエーテルイミドの存在割合が15重量%未満
であれば大きいガス選択性とすぐれた機械的特性が充分
に発現せず、又、変性シリコーンの存在割合が15%未
満であれば高いガス透過性が充分に発現しない傾向があ
る。同成分の割合は30〜70重量%の範囲であること
がより好ましい。
For example, if the proportion of polyetherimide is less than 15% by weight, high gas selectivity and excellent mechanical properties will not be fully expressed, and if the proportion of modified silicone is less than 15% by weight, high gas permeability will occur. tends not to be fully expressed. More preferably, the proportion of the same component is in the range of 30 to 70% by weight.

次に製膜法について説明する。Next, the film forming method will be explained.

前記反応生成物をジクロロメタン、クロロホルムなどの
塩素系溶剤等に溶解し、製膜することによって本発明の
優れたガス選択透過性膜を得ることができる。
The excellent gas selective permeability membrane of the present invention can be obtained by dissolving the reaction product in a chlorinated solvent such as dichloromethane or chloroform and forming a membrane.

通常製膜はポリマー溶液を塗布、流延等することによフ
て行われる。又、浸漬、流延等によフて適当な多孔質支
持体上に製膜してもよい。チューブあるいは中空糸状等
の多孔質支持体をもちいる場合はこれらの支持体をポリ
マー溶液中に浸漬し、引き上げ、次いで溶剤を蒸発させ
て膜を支持体上に形成させる。フィルム状多孔質支持体
を用いる場合には、その上に溶液を薄く塗布し、次いで
溶剤を蒸発除去する方法であってもよい。液体表面上で
製膜する方法は溶液が極めて薄く展延し薄膜状物を得る
ことができるので好ましい方法のひとつである。
Film formation is usually carried out by applying, casting, etc. a polymer solution. Alternatively, a film may be formed on a suitable porous support by dipping, casting, or the like. When a porous support such as a tube or hollow fiber is used, the support is immersed in a polymer solution, pulled up, and then the solvent is evaporated to form a membrane on the support. When using a film-like porous support, a method may be employed in which a solution is thinly applied onto the support and then the solvent is removed by evaporation. The method of forming a film on the liquid surface is one of the preferred methods because the solution can be spread extremely thinly and a thin film can be obtained.

本発明においては変性シリコーンは反応生成物に高いガ
ス透過性を与えるものである。分子構造が前記のもので
あればよく、分子量等は特に限定されないが、GPC法
による数平均分子量が500〜35000の範囲内のも
のが好ましく用いられる。その例として、たとえば信越
化学社製のシリコーンモノアミンを挙げることができる
In the present invention, the modified silicone imparts high gas permeability to the reaction product. The molecular structure may be as described above, and the molecular weight etc. are not particularly limited, but those having a number average molecular weight in the range of 500 to 35,000 by GPC method are preferably used. As an example, silicone monoamine manufactured by Shin-Etsu Chemical Co., Ltd. can be cited.

尚、他のシリコーン系ポリマー、たとえばポリジメチル
シロキサン等の通常のシリコーン系ポリマーを用いるこ
とによって得られるポリエーテルイミドとの反応生成物
の場合は、成膜性と分離膜のガス選択性が劣る点が問題
となる。
In addition, in the case of reaction products with polyetherimide obtained by using other silicone-based polymers, for example, ordinary silicone-based polymers such as polydimethylsiloxane, the film-forming properties and gas selectivity of the separation membrane are inferior. becomes a problem.

〔実施例〕〔Example〕

以下実施例により本発明を具体的に説明する。 The present invention will be specifically explained below using Examples.

実施例、1 ポリエーテルイミド70g(ゼネラルエレク←リック社
製、ウルテム1000)を1リツトルの攪拌装置付三つ
ロフラスコに秤りとり、これにクロロホルム500mI
Lを加え、攪拌しポリマーを溶解した。ついでシリコー
ンモノアミン(信越化学社製、X−22−098) 3
0 gを添加し、50℃にて72時間放置した。反応後
ポリマー溶液をメタノール2リツトルを入れたビーカー
に滴下し、反応生成物(2元ポリマー)を回収した。
Example 1 70 g of polyetherimide (manufactured by General Electric Company, Ultem 1000) was weighed into a 1 liter three-necked flask equipped with a stirrer, and 500 mI of chloroform was added to the flask.
L was added and stirred to dissolve the polymer. Next, silicone monoamine (manufactured by Shin-Etsu Chemical Co., Ltd., X-22-098) 3
0 g was added and left at 50°C for 72 hours. After the reaction, the polymer solution was dropped into a beaker containing 2 liters of methanol, and the reaction product (binary polymer) was collected.

なお、上記ポリエーテルイミドは1式においてH3 (:、H2n−を−C−としたもので分子量Mn= 2
2000、H3 また上記シリコーンモノアミンは式■においてRをC1
12(:H2CH2としたもので分子JiMn=650
0である。
In addition, the above-mentioned polyetherimide has H3 (:, H2n- replaced with -C- in Formula 1) and has a molecular weight Mn=2
2000, H3 Also, in the above silicone monoamine, R is C1 in the formula (■).
12(:H2CH2, molecule JiMn=650
It is 0.

同様にして、上記ポリエーテルイミドとシリコーンモノ
アミンとの添加割合を種々変えて複合ポリマーを得た。
Similarly, composite polymers were obtained by varying the addition ratios of the polyetherimide and silicone monoamine.

比較のため未変性のポリジメチルシロキサンの系につい
ても同様にして複合ポリマーを製造し、こ九らの複合ポ
リマーの耐熱性、機械的特性を測定し、第1表に示した
For comparison, composite polymers of unmodified polydimethylsiloxane systems were produced in the same manner, and the heat resistance and mechanical properties of these composite polymers were measured and are shown in Table 1.

(以下余白) 第 表 *: 分子量5000の未変性ポリジメチルシロキサン
次に、実施例1〜5およびそれと同様に上記ポリエーテ
ルイミドとシリコーン千ノアミンの割合を変化させて得
られた複合ポリマーをそれぞれジクロロメタンに溶解し
てその8重量%溶液を調製し、清浄なガラス板上に厚さ
約100ミクロンに塗布し、室1(20〜30℃)にて
溶剤を蒸発させた。得られた膜に空気を透過させて膜の
酸素透過係数および酸素/窒素の選択性を求め、その結
果を第1図にまとめた。複合ポリマー中の上記ポリエー
テルイミドの比率が高くなるにつれ選択性が大きくなる
が、特に15%を越えてから急激に立ち上がることがわ
かる。
(Leaving space below) Table *: Unmodified polydimethylsiloxane with a molecular weight of 5000 Next, composite polymers obtained by varying the proportions of the polyetherimide and silicone amine in Examples 1 to 5 and in the same manner as in Examples 1 to 5 were each mixed with dichloromethane. An 8% by weight solution was prepared by dissolving the solution and coating it on a clean glass plate to a thickness of about 100 microns, and the solvent was evaporated in room 1 (20-30°C). Air was permeated through the obtained membrane to determine the oxygen permeability coefficient and oxygen/nitrogen selectivity of the membrane, and the results are summarized in FIG. It can be seen that the selectivity increases as the proportion of the polyetherimide in the composite polymer increases, but it increases rapidly especially when it exceeds 15%.

〔発明の効果〕〔Effect of the invention〕

本発明のシリコーン変性ポリエーテルイミドは優わた耐
熱性、耐溶剤性、高強度を有し、ガス選択性の大きいポ
リエーテルイミドとガス透過性にすぐれた変性ポリジメ
チルシロキサンとの複合体であるため、優れたガス選択
透過性と耐熱性、耐溶剤性、高強度を有する選択透過性
膜を与える。
The silicone-modified polyetherimide of the present invention has excellent heat resistance, solvent resistance, and high strength, and is a composite of polyetherimide with high gas selectivity and modified polydimethylsiloxane with excellent gas permeability. This provides a permselective membrane with excellent gas permselectivity, heat resistance, solvent resistance, and high strength.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は実施例で得られたポリエーテルイミド含有率の
異なる各種ガス選択透過性膜の酸素透過係数及び酸素/
窒素の選択性を示す図である。 第1図
Figure 1 shows the oxygen permeability coefficients and oxygen/permeability of various gas selectively permeable membranes with different polyetherimide contents obtained in Examples.
It is a figure showing selectivity of nitrogen. Figure 1

Claims (1)

【特許請求の範囲】 1、一般式 ▲数式、化学式、表等があります▼ (ただし、nは1〜7の整数) で示される繰り返し単位を有するポリエーテルイミド及
び一般式 ▲数式、化学式、表等があります▼ (ただし、Rは炭素数1〜6のアルキレン基であり、m
は5以上の整数、lは1以上の整数)で示される変性ポ
リジメチルシロキサンが反応してなるシリコーン変性ポ
リエーテルイミド。 2、請求項1に記載のシリコーン変性ポリエーテルイミ
ドからなる選択透過性膜。
[Claims] 1. Polyetherimide having a repeating unit represented by the general formula ▲ Numerical formula, chemical formula, table, etc. (where n is an integer from 1 to 7) and the general formula ▲ Numerical formula, chemical formula, table, etc. etc.▼ (However, R is an alkylene group having 1 to 6 carbon atoms, and m
is an integer of 5 or more, l is an integer of 1 or more). 2. A permselective membrane comprising the silicone-modified polyetherimide according to claim 1.
JP9629490A 1990-04-13 1990-04-13 Silicon-modified polyether imide and selectivity gas-permeable membrane Pending JPH03296425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9629490A JPH03296425A (en) 1990-04-13 1990-04-13 Silicon-modified polyether imide and selectivity gas-permeable membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9629490A JPH03296425A (en) 1990-04-13 1990-04-13 Silicon-modified polyether imide and selectivity gas-permeable membrane

Publications (1)

Publication Number Publication Date
JPH03296425A true JPH03296425A (en) 1991-12-27

Family

ID=14161038

Family Applications (1)

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JP9629490A Pending JPH03296425A (en) 1990-04-13 1990-04-13 Silicon-modified polyether imide and selectivity gas-permeable membrane

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