JPS62177039A - Production of porous membrane from thermosetting resin - Google Patents
Production of porous membrane from thermosetting resinInfo
- Publication number
- JPS62177039A JPS62177039A JP1994386A JP1994386A JPS62177039A JP S62177039 A JPS62177039 A JP S62177039A JP 1994386 A JP1994386 A JP 1994386A JP 1994386 A JP1994386 A JP 1994386A JP S62177039 A JPS62177039 A JP S62177039A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- water
- thermosetting resin
- organic solvent
- porous 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
- 229920005989 resin Polymers 0.000 title claims abstract description 33
- 239000011347 resin Substances 0.000 title claims abstract description 33
- 239000012528 membrane Substances 0.000 title claims abstract description 18
- 229920001187 thermosetting polymer Polymers 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 239000003960 organic solvent Substances 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 10
- 229920000049 Carbon (fiber) Polymers 0.000 claims abstract description 3
- 239000004917 carbon fiber Substances 0.000 claims abstract description 3
- 239000003365 glass fiber Substances 0.000 claims abstract description 3
- 229920003002 synthetic resin Polymers 0.000 claims abstract description 3
- 239000000057 synthetic resin Substances 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 16
- 229920000642 polymer Polymers 0.000 claims description 15
- 239000012210 heat-resistant fiber Substances 0.000 claims description 7
- 229920001721 polyimide Polymers 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 5
- 239000003822 epoxy resin Substances 0.000 claims description 4
- 229920000647 polyepoxide Polymers 0.000 claims description 4
- 239000009719 polyimide resin Substances 0.000 claims description 4
- 229920005749 polyurethane resin Polymers 0.000 claims description 4
- 239000007849 furan resin Substances 0.000 claims description 3
- 239000005011 phenolic resin Substances 0.000 claims description 3
- 229920003235 aromatic polyamide Polymers 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 1
- 239000002657 fibrous material Substances 0.000 abstract description 9
- 230000000379 polymerizing effect Effects 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 239000004744 fabric Substances 0.000 description 10
- 239000011521 glass Substances 0.000 description 9
- XQUPVDVFXZDTLT-UHFFFAOYSA-N 1-[4-[[4-(2,5-dioxopyrrol-1-yl)phenyl]methyl]phenyl]pyrrole-2,5-dione Chemical compound O=C1C=CC(=O)N1C(C=C1)=CC=C1CC1=CC=C(N2C(C=CC2=O)=O)C=C1 XQUPVDVFXZDTLT-UHFFFAOYSA-N 0.000 description 7
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 7
- 229920003192 poly(bis maleimide) Polymers 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000000605 extraction Methods 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 229920001568 phenolic resin Polymers 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000004641 Diallyl-phthalate Substances 0.000 description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- QUDWYFHPNIMBFC-UHFFFAOYSA-N bis(prop-2-enyl) benzene-1,2-dicarboxylate Chemical compound C=CCOC(=O)C1=CC=CC=C1C(=O)OCC=C QUDWYFHPNIMBFC-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000013020 steam cleaning Methods 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- LGZNZXOHAFRWEN-UHFFFAOYSA-N 3-[4-(2,5-dioxopyrrol-3-yl)triazin-5-yl]pyrrole-2,5-dione Chemical compound O=C1NC(=O)C(C=2C(=NN=NC=2)C=2C(NC(=O)C=2)=O)=C1 LGZNZXOHAFRWEN-UHFFFAOYSA-N 0.000 description 1
- 229920001730 Moisture cure polyurethane Polymers 0.000 description 1
- 239000004962 Polyamide-imide Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- XPFVYQJUAUNWIW-UHFFFAOYSA-N furfuryl alcohol Chemical compound OCC1=CC=CO1 XPFVYQJUAUNWIW-UHFFFAOYSA-N 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000003495 polar organic solvent Substances 0.000 description 1
- 229920002312 polyamide-imide Polymers 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920005597 polymer membrane Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000013557 residual solvent Substances 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は熱硬化性樹脂による多孔質膜の製造法、更に詳
しくは、熱硬化性樹脂の初期重合体を用い、特定操作で
該初期重合体の多孔性皮膜を形成した後、乾燥、次いで
加熱して重合を完結せしめることから成る、水蒸気洗浄
にも十分耐えうる沖過膜(フィルター)等に有用な多孔
質膜の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for producing a porous membrane using a thermosetting resin, and more specifically, to a method for producing a porous membrane using a thermosetting resin. The present invention relates to a method for producing a porous membrane useful for filters, etc., which can sufficiently withstand steam cleaning, and which comprises forming a porous membrane, drying it, and then heating it to complete polymerization.
従来技術と解決すべき問題点
従来より、高分子多孔質膜はフィルター等の用途に多用
され、広範囲の樹脂から多岐にわたって製造されている
。しかし、熱硬化性樹脂による多孔質膜は、一部焼結法
等により製造されているものの、製法の多様性が乏しく
、水蒸気洗浄など耐熱性を要する用途や、あるいはポリ
イミド樹脂などの耐放射性を活かした原子力関係の沖過
膜としての要求に十分こたえていないのが現状である。Prior Art and Problems to Be Solved Hitherto, porous polymer membranes have been widely used in filters and the like, and have been manufactured in a wide variety of ways from a wide variety of resins. However, although porous membranes made of thermosetting resins are partially manufactured using sintering methods, there is a lack of diversity in manufacturing methods, and they are used for applications that require heat resistance such as steam cleaning, or for applications that require radiation resistance such as polyimide resins. The current situation is that it does not fully meet the requirements for nuclear power-related offshore membranes.
本発明者は、これらの要求に満足する多孔質膜の製造法
を提供するため鋭意研究を進めた結果、ポリイミド樹脂
を含めた広範囲の熱硬化性樹脂を対象とし、これら樹脂
の初期重合体を水溶性有機溶剤に溶解した溶液を、ガラ
スクロスなどの耐熱性繊維材昏こ含浸または合成樹脂フ
ィルムなどの担体(後に剥離除去)上に塗布した後、水
中に浸漬させて水溶性有機溶剤を抽出すれば、上記初期
重合体の多孔性皮膜が形成され、これを乾燥、次いで加
熱により重合を完結することOこより、所望の多孔質膜
が得られることを見出し、本発明を完成させるに至った
。As a result of intensive research in order to provide a method for manufacturing porous membranes that satisfies these requirements, the present inventor targeted a wide range of thermosetting resins, including polyimide resins, and developed initial polymers of these resins. A solution dissolved in a water-soluble organic solvent is applied onto a carrier (later peeled off) such as a heat-resistant fiber impregnated with glass cloth or a synthetic resin film, and then immersed in water to extract the water-soluble organic solvent. Then, a porous film of the above-mentioned initial polymer is formed, and the inventors discovered that by drying this and then completing the polymerization by heating, a desired porous film could be obtained, and the present invention was completed. .
すなわち、本発明は、水溶性有機溶剤に溶解した熱硬化
性樹脂初期重合体の溶液を耐熱性繊維材に含浸させるか
または担体上に塗布し、水中に浸漬させて水溶性有機溶
剤を抽出し、乾燥、次いで加熱して重合を完結せしめる
ことを特徴とする熱硬化性樹脂による多孔質膜の製造法
を提供するものである。That is, the present invention impregnates a heat-resistant fiber material with a solution of a thermosetting resin initial polymer dissolved in a water-soluble organic solvent or coats it on a carrier, and immerses it in water to extract the water-soluble organic solvent. The present invention provides a method for producing a porous membrane using a thermosetting resin, which comprises drying and then heating to complete polymerization.
本発明で対象とする熱硬化性樹脂としては、例エバフェ
ノールm脂(フェノールホルムアルデヒド樹脂)、エポ
キシ樹脂、フラン樹脂(フルフリルアルコール樹脂)、
DAP(ジアリルフタレート)樹脂、ポリイミド樹脂(
トリアジンビスマレイミド、ポリアミノビスマレイミド
、ポリアミドイミド)、ポリウレタン樹脂等が挙げられ
、特に400℃以上の温度に対しても良好な耐熱性をも
つもの、例えばポリアミノビスマレイミドカ好マしい。Thermosetting resins targeted by the present invention include, for example, evaphenol resin (phenol formaldehyde resin), epoxy resin, furan resin (furfuryl alcohol resin),
DAP (diallyl phthalate) resin, polyimide resin (
Examples include triazine bismaleimide, polyamino bismaleimide, polyamideimide), polyurethane resins, and those having good heat resistance even at temperatures of 400° C. or higher, such as polyamino bismaleimide, are particularly preferred.
本発明においては、これら熱硬化性樹脂の初期重合体(
所謂βステージと呼ばれる重縮合段階のもの)を使用す
る。具体例として、ポリアミノビスマレイミドの場合で
は、プレプレグ作製用材料として市販されている日本ポ
リイミド(株)製の「ケルイミド」が挙げられる。フェ
ノール樹脂の場合では、圧縮成形用等に市販されている
材料が挙げられ、これは既に水溶性を失い、極性の強い
有機溶剤に可溶である。ポリウレタン樹脂の場合では、
ポリウレタンプレポリマーに後加熱で解離して活性化す
るブロックインシアネートを配合したものが挙げられる
。In the present invention, the initial polymer (
The so-called β-stage polycondensation stage) is used. As a specific example, in the case of polyamino bismaleimide, "Kelimide" manufactured by Nippon Polyimide Co., Ltd., which is commercially available as a material for preparing prepregs, can be mentioned. In the case of phenolic resins, examples include commercially available materials for compression molding, etc., which have already lost their water solubility and are soluble in highly polar organic solvents. In the case of polyurethane resin,
Examples include polyurethane prepolymers blended with blocked incyanate that dissociates and activates upon post-heating.
上記熱硬化性樹脂の初期重合体(以下、樹脂釜で表わす
こともある)は、適当な水溶性有機溶剤に溶解した溶液
状態で使用に供されるが、その水溶性有機溶剤の具体例
は以下の通りである。ポリアミノビスマレイミドの場合
N−メチルピロリドン、ジメチルホルムアミド(DMF
)またはこれらの混合物が適当である(フェノール樹脂
、エポキシ樹脂等の場合も同様)。ポリウレタン樹脂の
場合DMF、テトラヒドロフラン(THF)またはこれ
らの混合物が適当である。フラン樹脂の場合は樹脂構成
によりアルコール類の単独または混合使用も可能である
。これらの水溶性有機溶剤は、高度に精製した無水のも
のが好ましいが、溶剤機能に支障を来さない範囲であれ
ば水分を含むものであってもよい。従って、水溶性有機
溶剤に別途水を併用することも可能であり、この場合樹
脂の凝集速度を早め、工程時間の短縮化につながること
もある。なお、水と任意の割合で混合しうる溶剤たけで
なく、一部混合可能な溶剤(例えばアセトン)を併用し
てもよい。The initial polymer of the thermosetting resin (hereinafter sometimes referred to as a resin pot) is used in the form of a solution dissolved in a suitable water-soluble organic solvent. Specific examples of the water-soluble organic solvent are as follows. It is as follows. In the case of polyamino bismaleimide, N-methylpyrrolidone, dimethylformamide (DMF
) or mixtures thereof (the same applies to phenolic resins, epoxy resins, etc.). In the case of polyurethane resins DMF, tetrahydrofuran (THF) or mixtures thereof are suitable. In the case of furan resin, alcohols can be used alone or in combination depending on the resin composition. These water-soluble organic solvents are preferably highly purified anhydrous ones, but may contain water as long as they do not interfere with the solvent function. Therefore, it is also possible to separately use water in combination with the water-soluble organic solvent, and in this case, the rate of aggregation of the resin can be accelerated, which may lead to a reduction in process time. Note that not only a solvent that can be mixed with water in an arbitrary ratio, but also a solvent that is partially miscible (for example, acetone) may be used in combination.
また本発明におけるかかる初期重合体の溶液としては、
当該水溶性有機溶剤中で前記βステージの段階まで重合
を進めて得られるワ子ス状物で使用することもできる。In addition, the solution of such an initial polymer in the present invention includes:
It can also be used as a wax-like material obtained by proceeding polymerization to the β stage in the water-soluble organic solvent.
上記初期重合体溶液の濃度は、初期重合体の種類や重合
状態に応じて加工上適切な粘度が得られるように選定す
ればよい。一般的に、濃度が高いと、後記抽出処理で形
成される皮膜気孔の空孔率が減少し、かつ孔径が微細化
し、逆に濃度が低いと、空孔率は高(なるが、孔径が粗
大化する傾向にある。低濃度で加工に適した粘度を得る
には、増粘剤や酸化珪素粉末の使用が場合により有効で
ある。樹脂重合度が比較的高い場合、低濃度でも高い粘
度が付与される。ポリアミノビスマレイミドの場合、溶
解直後は低粘度を示すが、経時変化により増粘すること
が認められる。また孔径の粗大化を防ぐため、溶液中に
界面活性剤を添加することも可能である。The concentration of the initial polymer solution may be selected so as to obtain a viscosity suitable for processing depending on the type and polymerization state of the initial polymer. In general, when the concentration is high, the porosity of the film pores formed in the extraction process described later decreases, and the pore size becomes finer. Conversely, when the concentration is low, the porosity increases (although the pore size becomes smaller). It tends to become coarser.In order to obtain a viscosity suitable for processing at low concentrations, the use of thickeners or silicon oxide powder may be effective in some cases.If the degree of resin polymerization is relatively high, high viscosity may be obtained even at low concentrations. In the case of polyamino bismaleimide, it exhibits a low viscosity immediately after dissolution, but it is observed that the viscosity increases over time.In addition, a surfactant should be added to the solution to prevent coarsening of the pore size. is also possible.
本発明で用いる耐熱性繊維材としては、水溶性有機溶剤
(および後記抽出処理に用いる水)に侵されがたいこと
が必要であり、例えばガラス繊維、カーボン繊維、ポリ
アラミツド繊維もしくは金属繊維の織成物、不織布状物
、マット状物等が挙げられる。The heat-resistant fiber material used in the present invention must be resistant to being attacked by water-soluble organic solvents (and the water used in the extraction process described later), such as woven glass fibers, carbon fibers, polyaramid fibers, or metal fibers. Examples include non-woven materials, mat-like materials, and the like.
上記耐熱性繊維材の代わりに用いる担体としては、後述
の如く剥離除去されるものであるから耐熱性である必要
はなく、通常の合成樹脂フィルム(ポリエステル、ポリ
カーボネート、ナイロン、ポリプロピレン、セルロース
等の市販フィルム)や剥離紙(好ましくは耐熱性のもの
)が採用されてよい。The carrier used in place of the above-mentioned heat-resistant fiber material does not need to be heat-resistant because it can be peeled off as described later. A film) or a release paper (preferably heat-resistant) may be employed.
本発明に係る熱硬化性樹脂による多孔質膜の製造法は、
以下の要領で実施することができる。The method for producing a porous membrane using a thermosetting resin according to the present invention includes:
It can be carried out as follows.
1)上述の所定濃度(または粘度)に調整した初期重合
体溶液を耐熱性繊維材に含浸させる。含浸は常法に従っ
て行なえばよく、例えば初期重合体溶液の系に繊維材を
浸漬せしめ、要すれば繊維材に付着した気泡を除去した
後余分な溶液を絞り取り、系から含浸繊維材を取出す。1) A heat-resistant fiber material is impregnated with the initial polymer solution adjusted to the above-mentioned predetermined concentration (or viscosity). Impregnation may be carried out according to a conventional method, for example, the fiber material is immersed in the system of the initial polymer solution, and if necessary, after removing air bubbles attached to the fiber material, the excess solution is squeezed out, and the impregnated fiber material is taken out from the system. .
なお、必要に応じて繊維材と樹脂膜の接着力を高めるた
め、繊維材の表面にプライマー処理あるいはカップリン
グ処理を施こしておくことが好ましい。In addition, in order to increase the adhesive force between the fiber material and the resin film, it is preferable to perform a primer treatment or a coupling treatment on the surface of the fiber material, if necessary.
また、かかる含浸法に代えて、上記初期重合体溶液を担
体上に通常100〜1000 f//dの量で塗布す
る。Moreover, instead of such an impregnation method, the above-mentioned initial polymer solution is applied onto the carrier in an amount of usually 100 to 1000 f//d.
1) 上記含浸または塗布を行った後、繊維材または
担体を常温または0〜70℃の水中に3〜30分間浸漬
せしめる。ここで、水溶性有機溶剤を水中に抽出し、こ
れによって凝集した初期重合体の多孔性皮膜が繊維材中
または担体上に形成される。1) After the above impregnation or coating, the fiber material or carrier is immersed in water at room temperature or 0 to 70°C for 3 to 30 minutes. Here, the water-soluble organic solvent is extracted into water, whereby a porous film of agglomerated initial polymer is formed in the fiber material or on the carrier.
111)このように抽出処理を行った後、常法に従って
乾燥処理に付す。なお、多孔性皮膜を担体上に形成した
場合は、当該乾燥前または乾燥後に担体を剥離除去する
。乾燥は通常、水や有機溶剤の沸点付近の温度で行われ
るが、多孔性皮膜中に有機溶剤が残存する場合、いきな
り高い温度で行うと、初期重合体の再溶解が起こり、皮
膜の多孔質構造が崩れる場合があるため、通常は水の乾
燥、次いで有機溶剤の留去となるように徐々に乾燥温度
を上げて行くことが好ましい。また有機溶剤の留去のた
め、真空乾燥機中で乾燥することも有効である。111) After performing the extraction treatment in this manner, it is subjected to a drying treatment according to a conventional method. In addition, when a porous film is formed on a carrier, the carrier is peeled off and removed before or after the drying. Drying is usually carried out at a temperature near the boiling point of water or organic solvent, but if organic solvent remains in the porous film, if the drying is carried out at a suddenly high temperature, the initial polymer will re-dissolve, causing the film to become porous. Since the structure may collapse, it is generally preferable to gradually increase the drying temperature by drying the water and then distilling off the organic solvent. It is also effective to dry in a vacuum dryer to remove the organic solvent.
lv)最後に重合を完結せしめるための加熱処理(通常
、オーブン中で実施)に付す。加熱条件は熱硬化性樹脂
の種類に応じて選定すればよく、ポリアミノビスマレイ
ミドでは200℃×48時間〜250℃×24時間、エ
ポキシ樹脂では150〜b
この加熱処理の場合も、有機溶剤が残存した状態で急に
温度を上げると、重合体の再溶解によって硬化に支障(
硬化不十分)を来たすので、急速な温度上昇は避けるべ
きである。また多数の枚数を同時に加熱処理する場合、
それぞれの間に弗素樹脂をコートした布あるいはガラス
布を挾み、積重ねた状態で加熱処理することができる。lv) Finally, it is subjected to a heat treatment (usually carried out in an oven) to complete the polymerization. Heating conditions can be selected depending on the type of thermosetting resin; for polyamino bismaleimide, 200°C x 48 hours to 250°C x 24 hours; for epoxy resin, 150°C - 24 hours. Even in the case of this heat treatment, organic solvent remains. If the temperature is suddenly raised in a state where the
Rapid temperature rises should be avoided as this may result in insufficient curing. Also, when heat treating a large number of sheets at the same time,
A fluororesin-coated cloth or glass cloth is sandwiched between each layer, and heat treatment can be performed in a stacked state.
なお、上記の方法で樹脂の溶剤溶液中に無機充填剤、補
強性短繊維等を配合してもよい。Incidentally, an inorganic filler, reinforcing short fibers, etc. may be blended into the resin solvent solution using the above method.
このようをこして耐熱性を有する多孔質膜を、繊維材に
支持または支持なしの状態で得ることができ、これらは
いずれも、広範な用途の沖過膜として利用することがで
きる。In this way, a heat-resistant porous membrane can be obtained with or without support on a fibrous material, and either of these can be used as a membrane for a wide range of applications.
次に実施例を挙げて、本発明をより具体的に説明する。Next, the present invention will be explained in more detail with reference to Examples.
実施例1
ポリアミノビスマレイミドの初期重合体(日本ポリイミ
ド(株)製、ケルイミド601)を約50℃のN−メチ
ルピロリドンに溶解して、濃度45重量多の樹脂液を得
る。この樹脂液を室温で保存すると、徐々に粘度が上昇
し、2週間後に約3000Cpsに達した。Example 1 An initial polymer of polyamino bismaleimide (manufactured by Nippon Polyimide Co., Ltd., Kelimide 601) is dissolved in N-methylpyrrolidone at about 50°C to obtain a resin liquid having a concentration of 45% by weight. When this resin liquid was stored at room temperature, the viscosity gradually increased and reached about 3000 Cps after two weeks.
かかる樹脂液を平皿状容器に入れ、これに重量約200
97dの平織りガラスクロスを浸す。樹脂液中のガラス
クロスを棒状物でしごいて、ガラスクロスに付着した気
泡を除いた後、ガラスクロスの一端をもち、2本の棒状
物にて軽く挾んだ間を通しながら、余分の樹脂液をかき
落しつつ、ガラスクロスを樹脂液より取出し、直ちに常
温の水中に浸漬する。水浸1頁後よりガラスクロスの表
面は白く変化し、樹脂の凝集が認められたがそのまま5
分間、更に水道の蛇口の下で水を流しつつ5分間、合計
10分間の水浸を行う。水浸後表面の水を軽く拭い、乾
燥処理に付す。先ず水分の乾燥のため95℃のオーブン
中にて15分間5次いで残留溶剤の留去のため120℃
で20分、150℃で20分の加熱乾燥を行い、膜状物
を得る。その後、重合完結のため膜状物のそれぞれの間
にガラス布を挾み、積車ねた状態でオーブンに入れ、2
00℃で48時間の加熱処理を行う。このようOこして
、かなりの硬度を有する板状物が得られる。これは表面
が淡黄白色で、肉眼ではその気孔自体を判別できなかっ
たが、タバコの煙の通過が認められ、多孔質であること
がわかった。The resin liquid is put into a flat container, and the weight is about 200 ml.
Soak a 97d plain weave glass cloth. After squeezing the glass cloth in the resin liquid with a stick to remove any air bubbles attached to the glass cloth, hold one end of the glass cloth and squeeze it between the two sticks, and squeeze out the excess. While scraping off the resin liquid, remove the glass cloth from the resin liquid and immediately immerse it in water at room temperature. After 1 page of water immersion, the surface of the glass cloth turned white and resin agglomeration was observed, but it remained as it was for 5 days.
1 minute, then 5 minutes under running water under the tap for a total of 10 minutes. After soaking in water, gently wipe off the water from the surface and dry. First, it was placed in an oven at 95°C for 15 minutes to dry the moisture, and then at 120°C to distill off the residual solvent.
Heat drying is performed at 150° C. for 20 minutes and at 150° C. for 20 minutes to obtain a film-like product. After that, in order to complete the polymerization, a glass cloth was placed between each of the film-like materials, and the stack was placed in an oven for 2 hours.
Heat treatment is performed at 00°C for 48 hours. By straining in this way, a plate-like material having considerable hardness is obtained. The surface of this material was pale yellowish white, and although the pores themselves could not be discerned with the naked eye, cigarette smoke was observed to pass through, indicating that the material was porous.
Claims (1)
の溶液を耐熱性繊維材に含浸させるかまたは担体上に塗
布し、水中に浸漬させて水溶性有機溶剤を抽出し、乾燥
、次いで加熱して重合を完結せしめることを特徴とする
熱硬化性樹脂による多孔質膜の製造法。 2、熱硬化性樹脂がフェノール樹脂、エポキシ樹脂、フ
ラン樹脂、DAP樹脂、ポリイミド樹脂またはポリウレ
タン樹脂である前記第1項記載の製造法。 3、耐熱性繊維材がガラス繊維、カーボン繊維、ポリア
ラミッド繊維もしくは金属繊維の織成物、不織布状物ま
たはマット状物である前記第1項記載の製造法。 4、担体が合成樹脂フィルムまたは剥離紙である前記第
1項記載の製造法。[Scope of Claims] 1. A heat-resistant fiber material is impregnated with a solution of a thermosetting resin initial polymer dissolved in a water-soluble organic solvent, or applied onto a carrier, and immersed in water to remove the water-soluble organic solvent. A method for producing a porous membrane using a thermosetting resin, which comprises extracting, drying, and then heating to complete polymerization. 2. The manufacturing method according to item 1 above, wherein the thermosetting resin is a phenol resin, an epoxy resin, a furan resin, a DAP resin, a polyimide resin, or a polyurethane resin. 3. The manufacturing method according to item 1 above, wherein the heat-resistant fiber material is a woven, nonwoven, or mat-like material of glass fiber, carbon fiber, polyaramid fiber, or metal fiber. 4. The manufacturing method according to item 1 above, wherein the carrier is a synthetic resin film or a release paper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1994386A JPS62177039A (en) | 1986-01-30 | 1986-01-30 | Production of porous membrane from thermosetting resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1994386A JPS62177039A (en) | 1986-01-30 | 1986-01-30 | Production of porous membrane from thermosetting resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62177039A true JPS62177039A (en) | 1987-08-03 |
Family
ID=12013288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1994386A Pending JPS62177039A (en) | 1986-01-30 | 1986-01-30 | Production of porous membrane from thermosetting resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62177039A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11310658A (en) * | 1998-04-27 | 1999-11-09 | Ube Ind Ltd | Polyimide porous membrane and its production |
JP2000306568A (en) * | 1999-04-23 | 2000-11-02 | Ube Ind Ltd | Porous film and battery separator used therewith |
JP2001009222A (en) * | 1999-06-24 | 2001-01-16 | Ube Ind Ltd | Porous film for filter and filter |
JP2007169661A (en) * | 2007-03-22 | 2007-07-05 | Ube Ind Ltd | Polyimide porous film |
JP2010058062A (en) * | 2008-09-04 | 2010-03-18 | Sumitomo Electric Ind Ltd | Porous fluororesin membrane, method of manufacturing the same, and filter |
JP4794104B2 (en) * | 1999-09-13 | 2011-10-19 | 帝人株式会社 | POLYMETHAPHENYLENEISOPHALAMIDE POLYMER MEMBRANE, PROCESS FOR PRODUCING THE SAME, AND SEPARATOR |
JP2013031851A (en) * | 2012-11-09 | 2013-02-14 | Nitto Denko Corp | Epoxy resin porous membrane |
WO2016039299A1 (en) * | 2014-09-10 | 2016-03-17 | 東京応化工業株式会社 | Method for producing porous polyimide film |
-
1986
- 1986-01-30 JP JP1994386A patent/JPS62177039A/en active Pending
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11310658A (en) * | 1998-04-27 | 1999-11-09 | Ube Ind Ltd | Polyimide porous membrane and its production |
JP2000306568A (en) * | 1999-04-23 | 2000-11-02 | Ube Ind Ltd | Porous film and battery separator used therewith |
JP2001009222A (en) * | 1999-06-24 | 2001-01-16 | Ube Ind Ltd | Porous film for filter and filter |
JP4794104B2 (en) * | 1999-09-13 | 2011-10-19 | 帝人株式会社 | POLYMETHAPHENYLENEISOPHALAMIDE POLYMER MEMBRANE, PROCESS FOR PRODUCING THE SAME, AND SEPARATOR |
JP2007169661A (en) * | 2007-03-22 | 2007-07-05 | Ube Ind Ltd | Polyimide porous film |
JP2010058062A (en) * | 2008-09-04 | 2010-03-18 | Sumitomo Electric Ind Ltd | Porous fluororesin membrane, method of manufacturing the same, and filter |
JP2013031851A (en) * | 2012-11-09 | 2013-02-14 | Nitto Denko Corp | Epoxy resin porous membrane |
WO2016039299A1 (en) * | 2014-09-10 | 2016-03-17 | 東京応化工業株式会社 | Method for producing porous polyimide film |
KR20170056585A (en) * | 2014-09-10 | 2017-05-23 | 도쿄 오카 고교 가부시키가이샤 | Method for producing porous polyimide film |
CN106795314A (en) * | 2014-09-10 | 2017-05-31 | 东京应化工业株式会社 | The manufacture method of Porous polyimide film |
JPWO2016039299A1 (en) * | 2014-09-10 | 2017-06-22 | 東京応化工業株式会社 | Method for producing porous polyimide membrane |
US10177357B2 (en) | 2014-09-10 | 2019-01-08 | Tokyo Ohka Kogyo Co., Ltd. | Method for producing porous polyimide film |
CN106795314B (en) * | 2014-09-10 | 2019-11-12 | 东京应化工业株式会社 | The manufacturing method of Porous polyimide film |
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