JPH03284337A - Separating membrane made of cross-linked thin film of sericin and production thereof - Google Patents
Separating membrane made of cross-linked thin film of sericin and production thereofInfo
- Publication number
- JPH03284337A JPH03284337A JP8659990A JP8659990A JPH03284337A JP H03284337 A JPH03284337 A JP H03284337A JP 8659990 A JP8659990 A JP 8659990A JP 8659990 A JP8659990 A JP 8659990A JP H03284337 A JPH03284337 A JP H03284337A
- Authority
- JP
- Japan
- Prior art keywords
- sericin
- cross
- soln
- water
- thin film
- 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.)
- Granted
Links
- 108010013296 Sericins Proteins 0.000 title claims abstract description 52
- 239000012528 membrane Substances 0.000 title claims abstract description 30
- 239000010409 thin film Substances 0.000 title claims abstract description 21
- 238000004132 cross linking Methods 0.000 claims abstract description 10
- 239000010408 film Substances 0.000 claims abstract description 8
- 229920002803 thermoplastic polyurethane Polymers 0.000 claims abstract description 3
- 239000007864 aqueous solution Substances 0.000 claims description 27
- 238000000926 separation method Methods 0.000 claims description 17
- 238000005266 casting Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 6
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims description 3
- 229920006037 cross link polymer Polymers 0.000 claims 1
- 239000003431 cross linking reagent Substances 0.000 abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 13
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract description 10
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 9
- 239000011521 glass Substances 0.000 abstract description 4
- 229920006254 polymer film Polymers 0.000 abstract 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- 238000011160 research Methods 0.000 description 4
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108010022355 Fibroins Proteins 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 238000005373 pervaporation Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000583281 Sugiura Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 150000003949 imides Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005597 polymer membrane Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- OVARTBFNCCXQKS-UHFFFAOYSA-N propan-2-one;hydrate Chemical compound O.CC(C)=O OVARTBFNCCXQKS-UHFFFAOYSA-N 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明はセリシンを架橋成形して分離膜とすることを目
的としたセリシンの架橋薄膜化方法及びその分離膜とし
ての利用方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for forming a crosslinked thin film of sericin for the purpose of crosslinking and forming sericin into a separation membrane, and a method for utilizing the same as a separation membrane.
本発明によるセリシンをベースとする分離膜は、セリシ
ンが多官能性であるために非晶質構造をとり易くしたが
って結晶化度の小さい薄膜となって優れた分離性能を発
揮し、水−アルコール分離など化学工業やバイオインダ
ストリー等の産業分野に広く利用することができる。The sericin-based separation membrane according to the present invention has a polyfunctional nature, so sericin easily takes an amorphous structure, and therefore forms a thin film with low crystallinity, exhibiting excellent separation performance, and water-alcohol separation. It can be widely used in industrial fields such as chemical industry and bioindustry.
従来の技術
生糸繊維は結晶性・配向性の高いフィブロインとそれを
保護するセリシンという2種の蛋白質から構成されてい
る。絹はこのうちほとんどのセリシンを精錬によってと
り除いたフィブロインを主体とする繊維であり、従来こ
のセリシンをいかに経済的にとり除くかが大きな技術課
題であった。Conventional technology Raw silk fibers are composed of two types of proteins: fibroin, which has high crystallinity and orientation, and sericin, which protects it. Silk is a fiber whose main component is fibroin, from which most of the sericin has been removed through refining, and a major technical challenge has been how to economically remove this sericin.
ところで、セリシンが高温水に溶解しうること。By the way, sericin can be dissolved in high temperature water.
すなわち比較的親水性に冨むこと、多官性能であり反応
性に冨むこと、すなわちたとえばホルムアルデヒドで架
橋しうること、非晶性に冨むことなどは絹科学の分野で
は良く知られている(石川成造監修「繊維」81ページ
東京電機大字出版局1び322ペ一ジ関西衣生活研究会
1981年など)、また近年セリシンを天然資源として
有効利用しようとする気運もあり、たとえばセリシンを
グルタルアルデヒドで架橋薄膜化した酵素固定化膜(宮
人、杉浦、Journal of Fermentat
ion Technol。In other words, it is well known in the field of silk science that it is relatively hydrophilic, has multifunctional properties and is highly reactive, for example, can be crosslinked with formaldehyde, and is highly amorphous. (Seizo Ishikawa, "Textiles," Tokyo Denki Oaza Publishing Bureau, p. 1 and 322, Kansai Clothing Lifestyle Research Group, 1981, etc.) In recent years, there has also been a movement to effectively utilize sericin as a natural resource. Enzyme-immobilized membrane cross-linked with glutaraldehyde (Miyato, Sugiura, Journal of Fermentat)
ion Technol.
gy56@4号303ページ1978年)などの報告も
見られる。しかしながらセリシン薄膜を分離膜として利
用することについての研究は従来報告されていない、一
方、水−エタノール、水−イソブロビルアルコール、水
−アセトンなど水溶性有機物の濃厚溶液から水を選択的
に透過分離させろ水選択分離膜については近年着しく研
究が進み、一部は実用に供されるに至っている。しかし
ながら、高性能、安定でありかつ安価な水選択分離膜へ
のニーズは今後なお継続すると思われ、研究開発の一環
としてセリシンのごとき天然高分子化合物の膜素材とし
ての利用にも期待の大きいのが現状である。gy56@No.4, page 303, 1978). However, no research has been reported on the use of sericin thin films as separation membranes.On the other hand, there are studies on selectively permeating and separating water from concentrated solutions of water-soluble organic substances such as water-ethanol, water-isobrobyl alcohol, and water-acetone. Research into selective water separation membranes has progressed steadily in recent years, and some of them have been put into practical use. However, the need for high-performance, stable, and inexpensive water-selective separation membranes is expected to continue in the future, and there are great expectations for the use of natural polymer compounds such as sericin as membrane materials as part of research and development. is the current situation.
発明が解決しようとする課題
しかしながら一方で生糸重量の20%をしめる除去セリ
シンは、年給2000トンが排水中に放出されて環境汚
染の一因となるなどその放出防止及び有効利用について
は古くから大きな期待がかけられていた。Problems to be Solved by the Invention However, on the other hand, 2000 tons of removed sericin, which accounts for 20% of the weight of raw silk, is released into wastewater annually, contributing to environmental pollution. Prevention and effective use of sericin have long been a problem. There were high expectations.
本発明は、このようにこれまで利用されていなかったセ
リシンを用いて分離膜として有用な高分子膜を得ること
を目的としてなされたものである。The present invention was made for the purpose of obtaining a polymer membrane useful as a separation membrane by using sericin, which has not been used hitherto.
課題を解決するための手段
本発明者らは、鋭意研讐を進めた結果、ガラス板上に流
延したある種の架橋剤を含む流延用セリシン水溶液が架
橋薄膜を形成し、かつこれが水−アルコール系における
水の選択的分離にすぐれた性能を発揮することを見出し
て本発明をなすに到った。すなわち本発明はセリシンの
架橋薄膜化方法と該架橋薄膜からなる高分子分離膜に関
するものである。Means for Solving the Problems As a result of intensive research, the present inventors found that a sericin aqueous casting solution containing a certain type of crosslinking agent cast onto a glass plate formed a crosslinked thin film, and this formed a crosslinked thin film. - The present invention has been completed by discovering that it exhibits excellent performance in selectively separating water in alcohol systems. That is, the present invention relates to a method for forming a crosslinked thin film of sericin and a polymer separation membrane comprising the crosslinked thin film.
本発明は親水性であるため水を選択的に透過さ材料に比
べ透過性が大きいと予想されること、多官能性であるた
め適当な架橋剤によって強度大なる薄膜が形成しうろこ
と等セリシンのもつ性質を積極的に活用して水選択透過
型の分l11膜を製造したものであり5 具体的にはセ
リシン水溶液に架橋剤を加えてガラス板等平滑面上に流
延し、しかる後に架橋を進行させて架橋薄膜とし、洗浄
してセリシン分離膜とする。流延すべき架橋剤含有セリ
シン水溶液すなわち流延用セリシン水溶液はセリシン水
溶液、塩酸、架橋剤A水溶液、架橋剤B水溶液から構成
される。セリシン水溶液の濃度は望ましくは1〜10%
、さらに望ましくは1〜3%であり、10%以上では水
溶液全体がゲル化して流動性を失うことがある。塩酸水
溶液の濃度には、特に制限はないが、通常1%の程度が
望ましい。Since the present invention is hydrophilic, it is expected to have higher permeability than materials that selectively allow water to permeate, and because it is polyfunctional, a strong thin film can be formed with an appropriate crosslinking agent. A water-selective permeation type 11 membrane was manufactured by actively utilizing the properties of sericin. Crosslinking is progressed to form a crosslinked thin film, which is then washed to form a sericin separation membrane. The crosslinking agent-containing sericin aqueous solution to be cast, that is, the sericin aqueous solution for casting, is composed of a sericin aqueous solution, hydrochloric acid, a crosslinking agent A aqueous solution, and a crosslinking agent B aqueous solution. The concentration of the sericin aqueous solution is preferably 1 to 10%.
More desirably, it is 1 to 3%; if it exceeds 10%, the entire aqueous solution may gel and lose fluidity. There is no particular limit to the concentration of the hydrochloric acid aqueous solution, but it is usually desirable to have a concentration of about 1%.
架橋剤A rtホルムアルデヒド、グルタルアルデヒド
などセリシン分子中のアミノ基、カルボキシル基などと
架橋反応を起こしやすいアルデヒド類でその水溶液濃度
はホルムアルデヒドの場合望ましくは5〜40%、さら
に望ましくは30%であり、グルタルアルデヒドの場合
で望ましくは5〜25%、さらに望ましくは10%であ
る。架橋剤Bはウレタン結合によってセリシン分子間を
強固に架橋し、薄膜の強度向上に役立つものであり、熱
反応型水溶性ウレタン樹脂と呼ばれるものである。Crosslinking agent A rt Aldehydes such as formaldehyde and glutaraldehyde that easily cause crosslinking reactions with amino groups, carboxyl groups, etc. in sericin molecules, and the concentration of the aqueous solution is preferably 5 to 40% in the case of formaldehyde, more preferably 30%, In the case of glutaraldehyde, it is preferably 5 to 25%, more preferably 10%. Crosslinking agent B strongly crosslinks sericin molecules through urethane bonds and is useful for improving the strength of the thin film, and is called a heat-reactive water-soluble urethane resin.
その水溶液は、市販品をそのまま使用することが可能で
ある。流延用セリシン水溶液は、上記の各構成成分水溶
液を混合して調整する。この場合セリシン水溶液は80
〜90部、架橋剤A水溶液0〜10部、架橋剤B水溶液
2〜20部、計100部とすることが好適である。塩酸
水溶液は必要に応じ、全体としてのpHが4〜6程度と
なるよう添加する。セリシン水溶液量の多少は薄膜の膜
厚に関係する。架橋剤A量の多少は主に薄膜内の架橋度
に関係し、多ければ架橋構造が密となる。架橋剤Bは強
固な架橋構造を形成し従ってその量の多少は、薄膜の強
度に関係する。As the aqueous solution, commercially available products can be used as they are. The aqueous sericin solution for casting is prepared by mixing the aqueous solutions of each of the above constituent components. In this case, the sericin aqueous solution is 80
90 parts of crosslinking agent A aqueous solution, 0 to 10 parts of crosslinking agent A aqueous solution, and 2 to 20 parts of crosslinking agent B aqueous solution, preferably 100 parts in total. An aqueous hydrochloric acid solution is added as necessary so that the overall pH is about 4 to 6. The amount of sericin aqueous solution is related to the thickness of the thin film. The amount of crosslinking agent A is mainly related to the degree of crosslinking within the thin film, and the larger the amount, the denser the crosslinked structure. Crosslinking agent B forms a strong crosslinked structure, and therefore its amount is related to the strength of the thin film.
以上のように調整された流延用セリシン水溶液を、でき
るだけ清浄な環境条件下、室温で平滑板イミドフィルム
等が好適である。流延後は室温条件下あるいは好ましく
はほこりの付着を避けるため相対湿度50%程度、20
℃前後に調節された乾燥機中に40〜50時間静置して
架橋剤Aによる架橋を進行させ、しかる後100〜15
0℃好ましくは120℃付近の熱風で5〜20分間好ま
しくは約10分間処理して架橋剤Bによる架橋を進行さ
せる0以上の手順により、セリシン架橋膜が形成される
。このようなセリシン架橋膜の形成にあたり塩酸を添加
して流延用セリシン水溶液をpH4〜6程度の酸性側に
保つようにしてもよい。The sericin aqueous solution for casting prepared as described above is preferably cast onto a smooth imide film at room temperature under as clean an environment as possible. After casting, the temperature should be kept at room temperature or preferably at a relative humidity of about 50% and 20% to avoid dust.
The crosslinking agent A is allowed to stand for 40 to 50 hours in a dryer adjusted to around 100 to 150 °C.
A sericin crosslinked film is formed by the above steps of treating with hot air at 0°C, preferably around 120°C, for 5 to 20 minutes, preferably about 10 minutes, to advance crosslinking with crosslinking agent B. In forming such a sericin crosslinked film, hydrochloric acid may be added to maintain the aqueous sericin solution for casting on the acidic side of about 4 to 6 pH.
これにより架橋剤A、 Bによる架橋が促進されるが
、酸成分存在下での100〜150℃の熱風処理のため
、セリシン架橋膜が脆化する場合があり、この点に留意
して処理時間を短縮する等の対策を構じる必要がある。This promotes crosslinking by crosslinking agents A and B, but the sericin crosslinked film may become brittle due to hot air treatment at 100 to 150°C in the presence of acid components, so keep this in mind when adjusting the treatment time. It is necessary to take measures such as shortening the time.
形成されたセリシン架橋膜を分離膜として用いるに際し
ては該膜を十分水洗した後多孔性担持体上に保持して使
用する。水−アルコール系など水溶性有機物水溶液を対
象とする膜分離の方法としては、該膜の一方に水溶性有
機物水溶液を置きもう一方の側を減圧として、水溶液を
膜透過・蒸発させつつ分離させる浸透気化法が好適であ
る0次に実施例により本発明をさらに詳細に説明する。When the formed sericin crosslinked membrane is used as a separation membrane, the membrane is thoroughly washed with water and then held on a porous carrier. A membrane separation method for an aqueous solution of a water-soluble organic substance such as a water-alcohol system involves placing an aqueous solution of a water-soluble organic substance on one side of the membrane, applying reduced pressure on the other side, and separating the aqueous solution while passing through the membrane and evaporating. The present invention will be explained in further detail using a zero-order example in which the vaporization method is preferred.
実施例
セリシンの2.4%水溶液90重量部、35%ホルムア
ルデヒド水溶液5重量部、熱反応型水溶性ポリウレタン
樹脂(第−工業鯛薬株式会社製、エラストロンE−37
)5重量部からなる流延用セリシン水溶液を調製した。Examples 90 parts by weight of a 2.4% aqueous solution of sericin, 5 parts by weight of a 35% formaldehyde aqueous solution, heat-reactive water-soluble polyurethane resin (manufactured by Dai-Kogyo Taiyaku Co., Ltd., Elastron E-37)
) A sericin aqueous solution for casting consisting of 5 parts by weight was prepared.
流延用セリシン水滴液をガラス板上にポリイミドフィル
ムをおいた金型に入れ、約50%RHの乾燥機中に40
〜50時間静置乾燥した。このようにしてできた薄膜を
さらに120℃の熱風で10分間処理しセリシン薄膜と
した。2度の乾燥により、金型中の流延用セリシン水溶
液の液高さ6mmは0.13mmに減少し薄膜となった
。該膜の一部を切取り、重量514mgの小片を40℃
の温水中に放置したと9mgとなった。放置26時間で
、該膜内の未架橋セリシンなど水溶性物質は除去された
と考えられる1次に分離性能測定に必要な大きさの膜を
切取り40℃温水中に26時間放置した後、浸透気化分
離装置に該膜を設置し、40℃で83.9重。The sericin water droplet solution for casting was placed in a mold with a polyimide film placed on a glass plate, and placed in a dryer at approximately 50% RH for 40 minutes.
It was left to dry for ~50 hours. The thin film thus produced was further treated with hot air at 120° C. for 10 minutes to obtain a sericin thin film. By drying twice, the liquid height of the sericin aqueous solution for casting in the mold was reduced from 6 mm to 0.13 mm, resulting in a thin film. A part of the membrane was cut out, and a small piece weighing 514 mg was heated at 40°C.
When left in warm water, the amount was 9 mg. Water-soluble substances such as uncrosslinked sericin in the membrane are thought to have been removed after being left for 26 hours.A membrane of the size required for the primary separation performance measurement was cut and left in warm water at 40°C for 26 hours, then pervaporation. The membrane was installed in a separator, and the weight was 83.9 at 40°C.
量%エタノール水溶液を対象に浸透気化実験を行った。A pervaporation experiment was conducted using a % ethanol aqueous solution.
その時の透過液濃度は34.2重量%であり、エタノー
ル水溶液は薄められて透過した。・すなわち該膜は水選
択透過性の分離膜として有効であることがわかる。また
透過量は0.201g/時であった。The permeate concentration at that time was 34.2% by weight, and the ethanol aqueous solution was diluted and permeated. - In other words, it can be seen that the membrane is effective as a water selectively permeable separation membrane. The amount of permeation was 0.201 g/hour.
が比較的反応性に冨んだ蛋白質であることに注目してこ
れを積極的に活用しようとするものであり、形成された
膜は水−アルコール系分離膜として賓用であるのみなら
ず、セリシンの排水への放出を抑制することになる。ま
た本発明の架橋製膜法はセリシンを広く天然資源として
活用することに有効であって、たとえば酵素固定化用の
糸状担体、芳香剤用球状担体として利用することができ
る。Noting that this is a protein with relatively high reactivity, the aim is to actively utilize this protein, and the membrane thus formed is not only suitable for use as a water-alcohol separation membrane for guests; This will inhibit the release of sericin into wastewater. Furthermore, the crosslinking film forming method of the present invention is effective in widely utilizing sericin as a natural resource, and can be used, for example, as a filamentous carrier for enzyme immobilization or a spherical carrier for aromatic agents.
Claims (2)
レタン樹脂を含む混合水溶液を平滑面上に流延して薄膜
とし、しかるのち該膜内のセリシンを架橋して固体化す
ることを特徴とするセリシンの架橋薄膜化方法。(1) Sericin characterized by casting a mixed aqueous solution containing sericin, formaldehyde, and a heat-reactive water-soluble urethane resin onto a smooth surface to form a thin film, and then crosslinking the sericin in the film to solidify it. cross-linked thin film method.
をベースとして成る架橋高分子分離膜。(2) A sericin-based crosslinked polymer separation membrane formed by the method according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2086599A JPH0651105B2 (en) | 1990-03-30 | 1990-03-30 | Separation membrane with cross-linked thin film of sericin and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2086599A JPH0651105B2 (en) | 1990-03-30 | 1990-03-30 | Separation membrane with cross-linked thin film of sericin and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03284337A true JPH03284337A (en) | 1991-12-16 |
JPH0651105B2 JPH0651105B2 (en) | 1994-07-06 |
Family
ID=13891480
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2086599A Expired - Lifetime JPH0651105B2 (en) | 1990-03-30 | 1990-03-30 | Separation membrane with cross-linked thin film of sericin and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0651105B2 (en) |
-
1990
- 1990-03-30 JP JP2086599A patent/JPH0651105B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0651105B2 (en) | 1994-07-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Arthanareeswaran et al. | Synthesis, characterization and thermal studies on cellulose acetate membranes with additive | |
JP4504963B2 (en) | Ultrafiltration membranes and methods of manufacturing and using ultrafiltration membranes | |
US5009824A (en) | Process for preparing an asymmetrical macroporous membrane polymer | |
Zeng et al. | Control of pore sizes in macroporous chitosan and chitin membranes | |
US20120000846A1 (en) | Polymer coated hydrolyzed membrane | |
EP0566097B1 (en) | Process for forming porous polymeric product from a nonporous polymeric composition and product | |
HU213925B (en) | Composite a symmetric membrane and process for selectively removing viral particles from solutions and process for forming a composite membrane | |
JPH0515498B2 (en) | ||
JPH05508344A (en) | Polytetramethylene adipamide or nylon 46 membrane with narrow pore size distribution and method for producing the same | |
JP2001513437A (en) | Polyion complex separation membrane with double structure | |
JPS5824447B2 (en) | Manufacturing method of reverse osmosis membrane | |
JPS61281138A (en) | Composite membrane selectively transmitting water from ethanol/water mixture and its production | |
JPH03284337A (en) | Separating membrane made of cross-linked thin film of sericin and production thereof | |
CN1124175C (en) | Preparation method of dry type polyacrylointrile ultrafiltration membrane | |
JPS63130105A (en) | Production of permselective composite membrane | |
JPS63283705A (en) | Selective semipermeable membrane of polyamideimide | |
JPH0516290B2 (en) | ||
Seggiani et al. | Collagen-based bioartificial materials—evaluation as membranes for extracorporeal blood purification | |
KR0123279B1 (en) | Method for semipermeable composite membrane | |
JPH09239248A (en) | Method for treatment of pervaporation membrane | |
JPS63182005A (en) | Polyion complex separation membrane | |
Tamura et al. | Synthesis and permeability of special polymer membranes: XIII. Ultrafiltration and adsorption characteristics of cellulose nitrate-activated charcoal membranes | |
CN117679976A (en) | Preparation method of reverse osmosis membrane with stable desalination rate | |
Bigelow et al. | Collodion membranes | |
JPH1176774A (en) | Separation membrane for dehydration and its production |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |