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JPS6151927B2 - - Google Patents
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JPS6151927B2 - - Google Patents

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Publication number
JPS6151927B2
JPS6151927B2 JP414381A JP414381A JPS6151927B2 JP S6151927 B2 JPS6151927 B2 JP S6151927B2 JP 414381 A JP414381 A JP 414381A JP 414381 A JP414381 A JP 414381A JP S6151927 B2 JPS6151927 B2 JP S6151927B2
Authority
JP
Japan
Prior art keywords
tube
core
bag
shaped core
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.)
Expired
Application number
JP414381A
Other languages
Japanese (ja)
Other versions
JPS57117301A (en
Inventor
Shigenori Matsumoto
Shusaku Tamaru
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 JP414381A priority Critical patent/JPS57117301A/en
Publication of JPS57117301A publication Critical patent/JPS57117301A/en
Publication of JPS6151927B2 publication Critical patent/JPS6151927B2/ja
Granted legal-status Critical Current

Links

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  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 本発明は管状透過膜の製造方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a tubular permeable membrane.

精密過膜、限外過膜及び逆浸透膜等(これ
らを以下、透過膜という)は各種の形態で液体分
離装置として利用されているが、その中でも管状
透過膜を用いた液体分離装置は、原液を高速、高
圧で流すことができるので、濃度分極の影響が小
さく濁質液の処理が可能であり、さらに装置の洗
浄が容易であるという利点があるため、広く利用
されている。
Precision membranes, ultrafiltration membranes, reverse osmosis membranes, etc. (hereinafter referred to as permeation membranes) are used as liquid separation devices in various forms, but among them, liquid separation devices using tubular permeation membranes are It is widely used because the stock solution can be flowed at high speed and high pressure, making it possible to treat turbid liquids with less influence of concentration polarization, and also because the equipment is easy to clean.

そしてこのとき用いる管状透過膜は、管内面に
製膜液を展延し、この展延された薄膜を凝固処理
することにより製造されている。
The tubular permeable membrane used at this time is manufactured by spreading a membrane-forming liquid on the inner surface of the tube and subjecting the spread thin film to a coagulation process.

従来より管内面に製膜液を展延する場合、管を
水平に支持し、該管の一端部内に製膜液を充填す
ると共に前記管内径よりもやや小さな外径の弾丸
状の中子を配し、しかるのちに該中子を紐で牽引
したり圧縮空気を吹込むことによつて、上記管端
部から該管他端部へ管内に走行させていた。
Conventionally, when spreading a membrane-forming liquid on the inner surface of a tube, the tube is supported horizontally, one end of the tube is filled with the membrane-forming liquid, and a bullet-shaped core having an outer diameter slightly smaller than the inner diameter of the tube is inserted. The core was then moved from one end of the tube to the other end of the tube by pulling the core with a string or blowing compressed air.

しかしながら、前記弾丸状中子の重量が該中子
と同体積を占める製膜液の重量より大きいため、
製膜の際に該中子の重量によつて管円周方向の下
部の膜厚が上部のそれと比較して薄くなり膜の偏
肉が生じ不均一な透過膜となるという欠点があつ
た。
However, since the weight of the bullet-shaped core is greater than the weight of the film-forming liquid occupying the same volume as the core,
During membrane formation, due to the weight of the core, the thickness of the membrane at the bottom in the circumferential direction of the tube becomes thinner than that at the top, resulting in uneven thickness of the membrane, resulting in an uneven permeable membrane.

本発明はかかる従来技術の欠点を解決するため
に鋭意研究の結果、袋状の中子を管内に走行させ
ることによつて、極めて偏肉の少ない管状透過膜
が得られるということを見い出し、本発明に至つ
たものである。
In order to solve the drawbacks of the prior art, the present invention has been made based on the discovery that by running a bag-shaped core inside the tube, a tubular permeable membrane with extremely low thickness unevenness can be obtained. This led to the invention.

すなわち本発明は、管の一端部内に、製膜液を
充填すると共に前記管内径よりもやや小さな外径
の中子を配し、しかるのち該中子を前記管端部か
ら該管他端部へ管内に走行させることにより、上
記の製膜液を管内面に展延する手段を含む管状透
過膜の製造方法において、上記中子として袋状中
子を用いることを特徴とする管状透過膜の製造方
法を提供するものである。
That is, in the present invention, one end of the tube is filled with a membrane-forming liquid and a core with an outer diameter slightly smaller than the inner diameter of the tube is disposed, and then the core is passed from the tube end to the other end of the tube. A method for producing a tubular permeable membrane comprising means for spreading the membrane-forming liquid on the inner surface of the tube by running it inside the tube, characterized in that a bag-shaped core is used as the core. A manufacturing method is provided.

以下にその実例を示す図面に基づいて本発明を
説明する。
The present invention will be explained below based on the drawings showing examples thereof.

第1図において、1は管であり支持具2、2′
により水平に支持されている。3は製膜液、4は
袋状中子でそれぞれ管端部内に充填されている。
ここで該袋状中子4は、第2図に示すように空洞
部41、先端部42および円筒部4′により構成
されている。5は圧縮空気吹込み用ノズルで上記
管端部に弾性的に嵌入されており、管他端部側に
は袋状中子4に対する安全カバー6が配置されて
いる。7はエアコンプレツサー、8は蓄圧タンク
であり、これらはフイルター9ならびに調圧弁1
0を介して配管11により連通されている。12
は圧力スイツチであり、蓄圧タンク8内の圧力が
一定圧力に達すると調圧弁10が閉塞され、コン
プレツサー7からの圧縮空気はリリーフ弁13よ
り排出される。14は蓄圧タンク8と圧縮空気吹
込み用ノズル5とを連通する配管、15は開閉バ
ルブである。16は圧力計であり、この圧力計1
6によつて蓄圧タンク8内の圧力が規定圧力に達
したことを確認したのちは、バルブ15を開通
し、蓄圧タンク8からの圧縮空気により袋状中子
4を管内に走行させることができる。
In FIG. 1, 1 is a tube and supports 2, 2'
It is supported horizontally by Reference numeral 3 denotes a film-forming liquid, and 4 a bag-shaped core, each of which is filled in the end of the tube.
As shown in FIG. 2, the bag-shaped core 4 is composed of a hollow portion 41, a tip portion 42, and a cylindrical portion 4'. A nozzle 5 for blowing compressed air is elastically fitted into the end of the tube, and a safety cover 6 for the bag-shaped core 4 is arranged at the other end of the tube. 7 is an air compressor, 8 is a pressure storage tank, and these are connected to a filter 9 and a pressure regulating valve 1.
They are communicated via piping 11 via 0. 12
is a pressure switch, and when the pressure in the pressure storage tank 8 reaches a certain pressure, the pressure regulating valve 10 is closed and the compressed air from the compressor 7 is discharged from the relief valve 13. 14 is a pipe that communicates the pressure accumulation tank 8 and the compressed air blowing nozzle 5, and 15 is an on-off valve. 16 is a pressure gauge, and this pressure gauge 1
After confirming that the pressure in the pressure storage tank 8 has reached the specified pressure by step 6, the valve 15 is opened and the bag-shaped core 4 can be moved into the pipe by compressed air from the pressure storage tank 8. .

本発明において用いる中子は、袋状の如き形状
のものであり、さらに詳しくは従来の弾丸状の中
子を、該中子の軸心を中心としてほぼ対称形であ
る空洞部を有するように、該中子の背面からくり
抜かれた形状のものである。このとき得られる袋
状中子の重量は、通常前記弾丸状の中子の重量の
約1/2以下(通常の下限値は1/10)とすると共
に、その重心は上記袋状中子の円筒部4′のほぼ
中心に位置するようにするのが好ましい。そして
このようにして得られる袋状中子を本発明におい
て適用する場合には、用いる製膜液の比重を考慮
して通常使用される。すなわち製膜液の比重をS
としたとき、この製膜液を用いて透過膜を製造す
る際、用いる袋状中子の比体積当りの比重(空洞
部も中子容積として積算した場合の袋状中子の比
重)は通常0.8S〜4Sとされる。
The core used in the present invention has a bag-like shape, and more specifically, a conventional bullet-shaped core is modified to have a hollow portion that is approximately symmetrical about the axis of the core. , which is hollowed out from the back surface of the core. The weight of the bag-shaped core obtained at this time is usually about 1/2 or less of the weight of the bullet-shaped core (the lower limit is usually 1/10), and the center of gravity is the weight of the bag-shaped core. Preferably, it is located approximately at the center of the cylindrical portion 4'. When the bag-shaped core obtained in this way is applied to the present invention, it is usually used in consideration of the specific gravity of the membrane-forming liquid used. In other words, the specific gravity of the film forming solution is S
When manufacturing a permeable membrane using this membrane forming solution, the specific gravity per specific volume of the bag-shaped core used (the specific gravity of the bag-shaped core when the cavity is also integrated as the core volume) is usually It is said to be 0.8S to 4S.

本発明において用いる袋状中子の肉厚は、該中
子の所定重量によつて決定され、通常0.3〜2mm
程度である。また上記袋状中子の製作上の煩雑さ
や該中子のひずみ等の問題により、該袋状中子の
肉厚は第2図に示すように、すべての周縁部にお
いてほぼ均一であることが好ましい。
The wall thickness of the bag-shaped core used in the present invention is determined by the predetermined weight of the core, and is usually 0.3 to 2 mm.
That's about it. Furthermore, due to problems such as the complexity of manufacturing the bag-shaped core and the distortion of the core, the wall thickness of the bag-shaped core cannot be approximately uniform at all peripheral parts, as shown in Fig. 2. preferable.

第2図において、袋状中子4の外径dは管1の
内径よりもやや小さいものとし、形成すべき膜厚
により適宜決定される。また製膜液3の粘度は通
常100〜5000ポイズに調整されており、袋状中子
4の円筒部4′の長さl1は製膜液の粘度により異
なるが、通常l1=1.2〜3dとするのが好ましい。l1
が1.2d未満の場合は、中子が管内を走行する際
に、中子が安定して走行しにくいため均一な膜を
得ることがむずかしいという不都合が生じる。
In FIG. 2, the outer diameter d of the bag-shaped core 4 is slightly smaller than the inner diameter of the tube 1, and is appropriately determined depending on the thickness of the film to be formed. Further, the viscosity of the film-forming liquid 3 is usually adjusted to 100 to 5000 poise, and the length l 1 of the cylindrical portion 4' of the bag-shaped core 4 varies depending on the viscosity of the film-forming liquid, but usually l 1 = 1.2 to 1.2. It is preferable to use 3D. l 1
If it is less than 1.2d, it is difficult for the core to run stably in the pipe, resulting in the inconvenience that it is difficult to obtain a uniform film.

またl1が3dをこえる場合、圧縮空気により中子
を走行させる際には該中子に作用する製膜液の抵
抗が大きくなり製膜速度が極端に遅くなり、また
モーターを用いて紐で中子を引張る際には製膜速
度は一定であるが、製膜液の抵抗が大きくなるた
めモーターには大出力が必要となるという不都合
が生じる。また上記袋状中子4の重心が該中子の
円筒部4′のほぼ中心に位置するのが好ましいこ
とから、該中子の先端部42の長さl2は円筒部
4′の長さl1によつて決定され、通常0.3〜1l1とす
るのが好ましい。そして該中子の先端部42の形
状は、該中子が管内の軸心を安定して走行できる
ように円錐状好ましくはなめらかな円錐状として
いる。
In addition, if l 1 exceeds 3d, the resistance of the film-forming liquid acting on the core becomes large when the core is driven by compressed air, and the film-forming speed becomes extremely slow. Although the film forming speed is constant when the core is pulled, the resistance of the film forming liquid increases, resulting in the inconvenience that a large output is required from the motor. Furthermore, since it is preferable that the center of gravity of the bag-shaped core 4 is located approximately at the center of the cylindrical portion 4' of the core, the length l 2 of the tip portion 42 of the core is equal to the length of the cylindrical portion 4'. It is determined by l 1 and is usually preferably between 0.3 and 1 l 1 . The shape of the tip 42 of the core is a conical shape, preferably a smooth conical shape, so that the core can run stably on the axis inside the tube.

中子4の材質としては、金属材料やプラスチツ
ク材料が用いられるが、通常はその表面に傷やゴ
ミがつきにくく、かつ製膜液に対するぬれ性の良
い金属材料、例えばステンレス鋼等が好ましい。
Metal or plastic materials are used as the material for the core 4, but metal materials such as stainless steel, which are resistant to scratches and dirt on the surface and have good wettability with the film-forming solution, are usually preferred.

本発明において、管としては不織布管、ガラス
管、金属製管等が用いられる。
In the present invention, a nonwoven fabric tube, a glass tube, a metal tube, etc. are used as the tube.

第1図の装置を用いて本発明を実施するには、
まず管1を水平に支持し、管端部内に製膜液3な
らびに袋状中子4を充填し、次いで上記管端部に
圧縮空気吹込み用ノズル5を弾性的に嵌入する。
次に蓄圧タンク8からの圧縮空気を圧縮空気吹込
み用ノズル5から上記管端部内へ送入することに
よつて、袋状中子4を管内に走行させる。このよ
うにして管1内に充填した製膜液3を上記中子4
の外面と管1の内面で形成される環状間隙に流動
させて管内面へ製膜液を環状薄膜3′として展延
させる。上記中子4が管内走行後管端部から安全
カバー6に放出されると開閉バルブ15が閉じら
れ、圧縮空気の吹込みを停止する。ここで圧縮気
体としては上記の空気の他に、窒素、炭酸ガスの
ような不活性気体が好適である。
To carry out the invention using the apparatus of FIG.
First, the tube 1 is supported horizontally, the membrane-forming liquid 3 and the bag-shaped core 4 are filled into the tube end, and then the compressed air blowing nozzle 5 is elastically fitted into the tube end.
Next, compressed air from the pressure accumulating tank 8 is fed into the tube end through the compressed air blowing nozzle 5, thereby causing the bag-shaped core 4 to travel inside the tube. The film-forming liquid 3 filled in the tube 1 in this way is poured into the core 4.
The film-forming liquid is caused to flow through the annular gap formed between the outer surface of the tube 1 and the inner surface of the tube 1, and is spread onto the inner surface of the tube as an annular thin film 3'. When the core 4 is discharged from the end of the pipe into the safety cover 6 after traveling in the pipe, the opening/closing valve 15 is closed and the blowing of compressed air is stopped. In addition to the above-mentioned air, the compressed gas is preferably an inert gas such as nitrogen or carbon dioxide.

本発明の前出の実例においては、圧縮空気を用
いて前記袋状中子4を管内に走行させることによ
つて製膜液を管内面に展延しているが、その先端
部に透孔を有する袋状中子を用いて、該透孔に紐
を貫通してその紐により該中子を牽引して管内に
走行させることによつて製膜液を管内面に展延す
ることも可能である。
In the above-mentioned example of the present invention, the film-forming liquid is spread on the inner surface of the tube by moving the bag-shaped core 4 inside the tube using compressed air, but there is a hole in the tip of the membrane-forming liquid. It is also possible to spread the film-forming liquid onto the inner surface of the tube by using a bag-shaped core having a core with a string passed through the through hole and pulling the core with the string to make it travel inside the tube. It is.

このようにして管内面に製膜液を展延し薄膜を
形成したのちは、通常の方法に従い、凝固処理を
施す。例えば、製膜液としてセルロース系誘導体
の溶液を使用した場合は、薄膜形成後の放置によ
り上記製膜液中の溶剤を部分的に蒸発させ、次い
で冷水浸漬によりゲル化させ、更に熱水処理を行
う。
After the film-forming liquid is spread on the inner surface of the tube to form a thin film in this manner, a coagulation process is performed according to a conventional method. For example, when a cellulose derivative solution is used as a film-forming solution, the solvent in the film-forming solution is partially evaporated by leaving it to stand after forming a thin film, gelling it by immersion in cold water, and then subjecting it to hot water treatment. conduct.

その他、湿式製膜の場合は、管内面に薄膜を形
成したのち、管を製膜液の非溶剤中に浸漬する方
法、製膜液中の添加剤を抽出することにより微孔
を形成する場合は、管内面に薄膜を形成したの
ち、管を添加剤の溶剤中に浸漬する方法等が用い
られる。
Other methods of wet film forming include forming a thin film on the inner surface of the tube and then immersing the tube in a non-solvent of the film forming solution, and forming micropores by extracting additives from the film forming solution. The method used is to form a thin film on the inner surface of the tube and then immerse the tube in an additive solvent.

以上に述べた如く、本発明の管状透過膜の製造
方法において用いる中子は袋状の如き形状である
ため、該袋状中子の重量が従来の弾丸状の中子よ
り極めて小さく、そのため製膜の際に中子の重量
による影響がなく極めて偏肉の少ない管状透過膜
を製造することができるという利点がある。
As mentioned above, since the core used in the method for producing a tubular permeable membrane of the present invention has a bag-like shape, the weight of the bag-shaped core is extremely smaller than that of a conventional bullet-shaped core, and therefore This method has the advantage that it is possible to manufacture a tubular permeable membrane with extremely little thickness deviation without being affected by the weight of the core during membrane formation.

また本発明の前出の実例においては、管を水平
に支持しているが、例えば管を傾斜状態に支持し
ても同様に中子の重量による管状透過膜の偏肉化
を防止できる。
Further, in the above-mentioned embodiment of the present invention, the tube is supported horizontally, but even if the tube is supported in an inclined state, for example, uneven thickness of the tubular permeable membrane due to the weight of the core can be similarly prevented.

さらに、本発明の管状透過膜の製造方法におい
て、圧縮空気を用いて袋状中子を管内に走行させ
て製膜液を管内面に展延する場合には、その圧縮
空気による圧力がほとんど上記袋状中子の先端部
の内面に作用するため、従来において弾丸状の中
子の背面に圧力が作用する場合と比較して、製膜
液を管内面に展延する際に上記袋状中子の先端部
のふらつきが生じないため該中子の走行が安定
し、そのため極めて均一な管状透過膜が得られる
という利点もある。
Furthermore, in the method for manufacturing a tubular permeable membrane of the present invention, when compressed air is used to move the bag-shaped core into the tube and spread the membrane forming liquid on the inner surface of the tube, the pressure due to the compressed air is almost the same. Because the pressure acts on the inner surface of the tip of the bag-shaped core, compared to the conventional case where pressure acts on the back surface of the bullet-shaped core, when the film-forming liquid is spread on the inner surface of the tube, Since the tip of the core does not wobble, the core can run stably, which has the advantage that an extremely uniform tubular permeable membrane can be obtained.

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

第1図は本発明を実施する際に用いられる装置
の実例の説明図、第2図は第1図において使用す
る袋状中子の縦断面図である。 1……管、3……製膜液、3′……環状薄膜、
4……袋状中子、5……圧縮空気吹込み用ノズ
ル。
FIG. 1 is an explanatory diagram of an example of the apparatus used in carrying out the present invention, and FIG. 2 is a longitudinal sectional view of the bag-shaped core used in FIG. 1. 1...tube, 3...film forming liquid, 3'...annular thin film,
4... Bag-shaped core, 5... Nozzle for blowing compressed air.

Claims (1)

【特許請求の範囲】[Claims] 1 管の一端部内に、製膜液を充填すると共に前
記管内径よりもやや小さな外径の中子を配し、し
かるのち該中子を前記管端部から該管他端部へ管
内に走行させることにより、上記製膜液を管内面
に展延する手段を含む管状透過膜の製造方法にお
いて、上記中子として袋状中子を用いることを特
徴とする管状透過膜の製造方法。
1 One end of the tube is filled with a membrane-forming solution and a core with an outer diameter slightly smaller than the inner diameter of the tube is placed, and then the core is run into the tube from the tube end to the other end. A method for producing a tubular permeable membrane, comprising means for spreading the membrane-forming liquid on the inner surface of the tube by spreading the membrane-forming solution onto the inner surface of the tube, the method comprising using a bag-shaped core as the core.
JP414381A 1981-01-14 1981-01-14 Production of tubular permeable membrane Granted JPS57117301A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP414381A JPS57117301A (en) 1981-01-14 1981-01-14 Production of tubular permeable membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP414381A JPS57117301A (en) 1981-01-14 1981-01-14 Production of tubular permeable membrane

Publications (2)

Publication Number Publication Date
JPS57117301A JPS57117301A (en) 1982-07-21
JPS6151927B2 true JPS6151927B2 (en) 1986-11-11

Family

ID=11576548

Family Applications (1)

Application Number Title Priority Date Filing Date
JP414381A Granted JPS57117301A (en) 1981-01-14 1981-01-14 Production of tubular permeable membrane

Country Status (1)

Country Link
JP (1) JPS57117301A (en)

Also Published As

Publication number Publication date
JPS57117301A (en) 1982-07-21

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