JP2003213538A - Method for stretching hollow fiber membrane - Google Patents

Method for stretching hollow fiber membrane

Info

Publication number
JP2003213538A
JP2003213538A JP2002001946A JP2002001946A JP2003213538A JP 2003213538 A JP2003213538 A JP 2003213538A JP 2002001946 A JP2002001946 A JP 2002001946A JP 2002001946 A JP2002001946 A JP 2002001946A JP 2003213538 A JP2003213538 A JP 2003213538A
Authority
JP
Japan
Prior art keywords
hollow fiber
fiber membrane
belts
stretching
belt
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
Application number
JP2002001946A
Other languages
Japanese (ja)
Other versions
JP3928927B2 (en
Inventor
Katsuhiko Hamanaka
克彦 浜中
Tetsuo Shimizu
哲生 清水
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.)
Asahi Kasei Corp
Original Assignee
Asahi Kasei Corp
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 Asahi Kasei Corp filed Critical Asahi Kasei Corp
Priority to JP2002001946A priority Critical patent/JP3928927B2/en
Publication of JP2003213538A publication Critical patent/JP2003213538A/en
Application granted granted Critical
Publication of JP3928927B2 publication Critical patent/JP3928927B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for stretching a hollow fiber membrane in a good accuracy, not giving damage and defect to the yarn, and preventing the hollow fiber membrane from flattening and compressing to become dense. <P>SOLUTION: This method for stretching the hollow fiber membrane continuously by making the yarn-conveying speed in the down stream side faster than that of the up stream side between ≥2 yarn conveying means is characterized by using a pair of opposing endless type belts as each of the yarn conveying means, sending yarn by nipping the hollow fiber membrane between the opposing belts and moving the both belts at a same speed in the same direction, sending out the hollow fiber membrane from between the belt in the same direction to the moving direction of the opposing belts making a contact with each other in the up stream side, and feeding the hollow fiber membrane into the belts in the same direction of the direction of moving the opposing belts making contact with each other in the down stream side. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、除濁等の濾過分野
に好適な、緻密な細孔と高い透水性能を持ち、耐久性に
優れた中空糸膜に関する。に関する。
TECHNICAL FIELD The present invention relates to a hollow fiber membrane suitable for the field of filtration such as turbidity, which has fine pores and high water permeability and is excellent in durability. Regarding

【0002】[0002]

【従来の技術】精密濾過膜や限外濾過膜等の多孔膜を用
いた除菌や除濁粒子等の濾過操作は、自動車産業(電着
塗料回収再利用システム)、半導体産業(超純水製
造)、医薬食品産業(除菌、酵素精製)などの多方面に
わたって実用化されてきたが、特に近年は河川水等を除
濁して飲料水や工業用水を製造する上水分野や、下水
(下水二次処理水)の除濁浄化等の下水分野への応用が
盛んになっている。こうした分野で膜が広く使われるた
めには、さらに高透過性、高強度であり有機物等による
汚染(目詰まり)をできるだけ起こさせないような膜が
必要である。そのような要求に対して、延伸による中空
糸膜の製造法あるいは改質法は高透過性、高強度化が期
待できる方法ではあるが、中空糸膜ゆえの問題により実
用化がもう一つ進んでいなかった。
2. Description of the Related Art Bacteria removal using a porous membrane such as a microfiltration membrane and an ultrafiltration membrane and filtration of turbid particles are carried out in the automobile industry (electrodeposition paint recovery and reuse system), the semiconductor industry (ultra pure water). Production), pharmaceutical food industry (sterilization, enzyme purification), etc., but it has been put to practical use in many fields, especially in recent years, in the tap water field for producing drinking water and industrial water by turbidizing river water, etc. Secondary application of sewage (secondarily treated water) is being actively applied to the field of sewage such as clarification and purification. In order for the membrane to be widely used in such fields, it is necessary to have a membrane that has higher permeability and strength and that does not cause contamination (clogging) with organic substances as much as possible. In response to such demands, the method for producing or modifying the hollow fiber membrane by stretching is a method that can be expected to have high permeability and high strength, but due to problems due to the hollow fiber membrane, another practical application is progressing. It wasn't.

【0003】従来の延伸方法としては、周速度の異なる
複数の延伸駆動ロールの間で延伸を行なう、ロール延伸
法が用いられていた。中空糸を糸長方向に延伸する力は
延伸駆動ロールと中空糸との摩擦を利用して中空糸につ
たえられるため、中空糸を延伸ロールに半周ほど抱かせ
る方式となる。このため、下記の問題点が発生してい
た。 (1)ロールと中空糸膜との摩擦力が不足しやすく、す
べりとなり延伸ムラにつながっていた。 (2)延伸力がロールと接している部分では中空糸膜に
対する圧縮圧力となるため中空糸膜がつぶれやすい。圧
縮圧力はロール径が大きいほど分散して減少するため装
置が大型化する要因となっていた。 (3)延伸倍率を正確に設定するためには延伸ロールの
周速度が正確である必要がある。従って周長の変化しな
い硬い延伸ロールが使用されていた。硬い延伸ロールで
あると中空糸膜のロールと接する面が平らになり圧密化
したり、円形断面が偏平につぶれ易くなる。また異物が
ロールに付着した場合、膜を傷つけ易いといった欠点が
あった。いったん偏平につぶれた中空糸膜は、外圧濾過
で使用する際にはさらに偏平につぶれやすい。また中空
部が偏平になると透過水の流動抵抗が大きいため透過性
が低くなる。さらに内圧での逆洗操作が入った運転では
断面形状が偏平から真円への変形が繰り返され縦割れし
やすくなる。
As a conventional stretching method, a roll stretching method has been used in which stretching is performed between a plurality of stretching drive rolls having different peripheral speeds. The force for stretching the hollow fiber in the yarn length direction is retained in the hollow fiber by utilizing the friction between the stretching drive roll and the hollow fiber. Therefore, the hollow fiber is held around the stretching roll for about half a circumference. Therefore, the following problems have occurred. (1) The frictional force between the roll and the hollow fiber membrane was likely to be insufficient, resulting in slippage and uneven drawing. (2) Since the stretching force acts as a compression pressure on the hollow fiber membrane at the portion in contact with the roll, the hollow fiber membrane is easily crushed. The compression pressure was dispersed and decreased as the roll diameter increased, which was a factor of increasing the size of the apparatus. (3) In order to accurately set the draw ratio, the peripheral speed of the drawing roll needs to be accurate. Therefore, a hard drawing roll having a constant circumferential length has been used. If the roll is a hard stretch roll, the surface of the hollow fiber membrane in contact with the roll is flattened and compacted, or the circular cross section is easily flattened. Further, there is a drawback that the film is easily damaged when foreign matter adheres to the roll. A hollow fiber membrane that has been flattened is more likely to be flattened when used in external pressure filtration. Further, when the hollow portion is flat, the flow resistance of the permeated water is high and the permeability is low. Further, in the operation including backwashing operation at the internal pressure, the cross-sectional shape is repeatedly deformed from a flat shape to a perfect circle, and vertical cracking easily occurs.

【0004】(4)柔らかい延伸ロールであるとロール
の有効径が引張り力により変化するため引き取り速度が
変化し、延伸の場合は延伸倍率や延伸速度が変動してし
まう。また異物がロールに付着した場合は、ロール径が
中空糸膜のロールへの接圧により変化して、周速が一定
でないために異物が膜をこすって傷をつけ易い。 (5)延伸経路が延伸ロールにより交互に屈曲した経路
となるため、太い中空糸膜を延伸する場合は余計な力が
かかり糸が折れたりつぶれたりした。このようなロール
延伸方法の問題のため、従来、中空糸膜の延伸は、つぶ
れにくく、細い中空糸膜の延伸に限られていたのが現状
である。
(4) In the case of a soft stretching roll, the effective diameter of the roll changes due to the tensile force, so that the take-up speed changes, and in the case of stretching, the draw ratio and the drawing speed change. Further, when foreign matter adheres to the roll, the diameter of the roll changes due to the contact pressure of the hollow fiber membrane to the roll, and the peripheral speed is not constant, so the foreign matter is likely to rub the membrane and scratch it. (5) Since the drawing path is a path in which the drawing rolls are alternately bent, extra force was applied when the thick hollow fiber membrane was drawn, and the thread was broken or crushed. Due to such a problem of the roll stretching method, conventionally, the stretching of the hollow fiber membrane is difficult to be crushed and is limited to the stretching of the thin hollow fiber membrane under the present circumstances.

【0005】[0005]

【発明が解決しようとする課題】本発明は、中空糸膜の
延伸において精度良く、糸傷欠陥を与えずに、中空糸膜
の偏平化、圧密化を防いだ延伸方法を提供することを目
的とする。
DISCLOSURE OF THE INVENTION It is an object of the present invention to provide a stretching method in which a hollow fiber membrane can be stretched with high precision and without causing yarn scratch defects, while preventing flattening and consolidation of the hollow fiber membrane. And

【0006】[0006]

【課題を解決するための手段】本発明者等は、前記課題
を解決するため無限軌道ベルトからなる引き取り機を用
いた中空糸膜の延伸方法を見出し、本発明をなすに至っ
た。すなわち、本発明は、 1.下流側の糸送り速度を上流側の糸送り速度より速く
して、中空糸膜を2以上の糸送り手段間で連続的に延伸
処理するにあたり、それぞれの糸送り手段として相対す
る一対の無限軌道式ベルトを使用し、相対するベルト間
に中空糸膜を挟んで双方のベルトを同速度で同方向へ移
動させることにより糸送りを行うこと、上流側において
は相対するベルトが接して移動する方向と同方向へ向か
ってベルト間より中空糸膜を送りだすこと、下流側にお
いては相対するベルトが接して移動する方向と同方向へ
向かって中空糸膜をベルト間に供給することを特徴とす
る延伸方法。 2.延伸処理を空間で行う1記載の延伸方法。 3.延伸処理を中空糸膜を曲げずに直線的に行なう1記
載の延伸方法。 4.無限軌道式ベルトが、表面が実質的に平滑な弾性体
からなる1記載の延伸方法である。
The present inventors have found a method for stretching a hollow fiber membrane using a take-up machine comprising an endless track belt in order to solve the above problems, and have completed the present invention. That is, the present invention is: When the hollow fiber membrane is continuously stretched between two or more yarn feeding means by increasing the yarn feeding speed on the downstream side from the yarn feeding speed on the upstream side, a pair of endless tracks facing each other as the yarn feeding means. A type belt is used, and the yarn is fed by moving both belts at the same speed and in the same direction with a hollow fiber membrane sandwiched between the opposing belts. On the upstream side, the direction in which the opposing belts contact and move And stretching the hollow fiber membranes between the belts in the same direction, and on the downstream side, the hollow fiber membranes are fed between the belts in the same direction as the direction in which the opposing belts make contact and move. Method. 2. The stretching method according to 1, wherein the stretching treatment is performed in space. 3. The stretching method according to 1, wherein the stretching treatment is performed linearly without bending the hollow fiber membrane. 4. The drawing method according to 1, wherein the endless track belt is made of an elastic body having a substantially smooth surface.

【0007】以下、詳細に本発明を説明する。本発明の
特長は下記(1)〜(7)である。 (1)相対する一対の無限軌道式ベルトを用いて、相対
するベルト間中空糸膜を挟むため摩擦力が大きく取れ延
伸時にすべることが防げる。 (2)ベルトの円周部分は直線部分に比べベルトの厚み
に由来する分だけ速度が速くなって糸送り速度とは異な
っているが、延伸中の中空糸膜はベルトの(速度の速
い)円周部分には接触しないため、ベルトと中空糸膜の
間のこすれの機会がなく、糸傷がつきにくい。 (3)延伸処理が糸送り手段の間の空間で行なわれるた
め、精度良く、傷なく行なえる。
The present invention will be described in detail below. The features of the present invention are the following (1) to (7). (1) Since a pair of opposing endless track type belts are used to sandwich the hollow fiber membranes between the opposing belts, a large frictional force can be obtained and slippage during stretching can be prevented. (2) The circumference of the belt is different from the yarn feeding speed because the speed is faster than that of the straight part due to the thickness of the belt, but the hollow fiber membrane during stretching is (the speed is high) of the belt. Since it does not contact the circumferential portion, there is no chance of rubbing between the belt and the hollow fiber membrane, and yarn scratches are less likely to occur. (3) Since the drawing process is performed in the space between the yarn feeding means, the drawing process can be performed accurately and without damage.

【0008】(4)中空糸膜の延伸を曲げずに直線的に
行なうためで中空糸膜に余計な変形を与えずに済み、太
糸の延伸が出きる。 (5)ベルトが実質的に平滑な弾性体であるため糸送り
時に中空糸膜が滑りにくく、つぶれにくい。 (6)ベルトが弾性体で柔らかく、厚みが変化しても糸
送り部分では糸送り速度が変化しないため精度の高い延
伸ができる。 (7)ベルトあるいは中空糸膜に異物が付着してもベル
トは弾性体のため異物が中空糸膜を押す力は少なく押し
傷になりにくい。中空糸膜とベルトは同速度で動くため
異物と中空糸膜との速度差もないのでこすり傷もつきに
くい。
(4) Since the hollow fiber membrane is stretched linearly without bending, unnecessary deformation is not given to the hollow fiber membrane, and the thick fiber can be stretched. (5) Since the belt is a substantially smooth elastic body, the hollow fiber membrane is less likely to slip and crush during yarn feeding. (6) Since the belt is made of an elastic material and is soft and the yarn feeding speed does not change at the yarn feeding portion even if the thickness changes, highly accurate drawing can be performed. (7) Even if foreign matter adheres to the belt or the hollow fiber membrane, since the belt is an elastic body, the foreign matter has less force to push the hollow fiber membrane and is less likely to be pressed. Since the hollow fiber membrane and the belt move at the same speed, there is no difference in speed between the foreign matter and the hollow fiber membrane, so that scratches are less likely to occur.

【0009】本発明で中空糸膜というのは中空糸状に成
型された膜を意味する。膜の孔径としても、孔径の小さ
な逆浸透膜からはじまって限外濾過膜、精密濾過膜とい
ずれにも使用できる。中空糸膜の素材としても、各種高
分子樹脂からできた中空糸膜を使用できる。中でもポリ
オレフィン、ポリフッ化ビニリデン、ハロゲン化ポリオ
レフィン、ポリスルホン、ポリエーテルスルホン、ポリ
アクリロニトリル等の高分子樹脂が耐熱性、耐薬品性、
強度等からみて好適に用いられる。
In the present invention, the hollow fiber membrane means a membrane formed into a hollow fiber shape. With regard to the pore size of the membrane, it can be used as an ultrafiltration membrane or a microfiltration membrane starting from a reverse osmosis membrane having a small pore size. As a material for the hollow fiber membrane, hollow fiber membranes made of various polymer resins can be used. Among them, polymer resins such as polyolefin, polyvinylidene fluoride, halogenated polyolefin, polysulfone, polyether sulfone, and polyacrylonitrile are heat resistant, chemical resistant,
It is preferably used in terms of strength and the like.

【0010】また本発明の中空糸膜には、まだ工程上中
空糸膜になっていない中空糸膜前駆体もふくむ。従って
無孔性中空糸を延伸して中空糸膜とする事、及び延伸し
てから所定の工程を経て中空糸膜とする事も本発明に含
まれる。例えば中空糸を延伸して開孔し多孔膜とする場
合は、延伸される前の中空糸はまだ膜ではないが中空糸
前駆体である。また高分子と溶剤とから熱相分離法で多
孔膜を作る場合、加熱混合された溶液を中空状に押し出
してから冷却固定された段階では高分子と溶剤からなる
ミクロなスケールで絡み合った相分離構造が形成される
が、これも中空糸膜前駆体であり、これから溶剤を抽出
した段階で微細な空孔を持った中空糸膜となる。
The hollow fiber membrane of the present invention also includes a hollow fiber membrane precursor which has not yet become a hollow fiber membrane in the process. Therefore, the present invention also includes stretching the non-porous hollow fiber to form a hollow fiber membrane, and stretching and then performing a predetermined process to form a hollow fiber membrane. For example, when a hollow fiber is stretched to form pores to form a porous membrane, the hollow fiber before being stretched is not a membrane but a hollow fiber precursor. When a porous film is formed from a polymer and a solvent by the thermal phase separation method, the heated and mixed solution is extruded into a hollow shape and then cooled and fixed. Although a structure is formed, this is also a hollow fiber membrane precursor, and when the solvent is extracted from this precursor, it becomes a hollow fiber membrane having fine pores.

【0011】中空糸膜の外径は特に限定しないが、本発
明の延伸方法は膜つぶれおよび延伸精度の面から、特に
太糸膜の延伸に適しており、外径0.5mm以上10mm
以下、更に好適には外径0.7mm以上7mm以下、更
に好適には外径1mm以上5mm以下の中空糸膜の延伸
に適している。無限軌道式ベルトの材質は内側は機械的
強度を有すために繊維補強ベルト等が用いられる。外側
の中空糸膜に接触する部分は、使用する温度、水分、溶
剤等の環境に耐えてかつ中空糸と摩擦が大きい材質から
選ばれ、傷や延伸むらの点から表面が実質的に平滑な弾
性体であることが好ましい。中でも弾性体としてシリコ
ーンゴム系のスポンジで出来たベルトは、耐熱性、耐薬
品にすぐれ好適に用いられる。又中空糸膜とベルトとの
接触面積を増やすため、平滑なベルトの表面に把持する
中空糸膜の太さに相当した、糸送りする中空糸膜が一部
入るような溝が延伸方向に平行にあっても良い。
The outer diameter of the hollow fiber membrane is not particularly limited, but the stretching method of the present invention is particularly suitable for stretching a thick fiber membrane from the viewpoint of film collapse and stretching accuracy, and an outer diameter of 0.5 mm or more and 10 mm.
The following is more preferably suitable for stretching a hollow fiber membrane having an outer diameter of 0.7 mm or more and 7 mm or less, and even more preferably an outer diameter of 1 mm or more and 5 mm or less. As the material of the endless track belt, a fiber reinforced belt or the like is used because it has mechanical strength inside. The part that contacts the outer hollow fiber membrane is selected from materials that can withstand the environment of temperature, moisture, solvent, etc., and have a large friction with the hollow fiber, and the surface is substantially smooth from scratches and uneven drawing. It is preferably an elastic body. Above all, a belt made of a silicone rubber type sponge as an elastic body is excellent in heat resistance and chemical resistance and is preferably used. In addition, to increase the contact area between the hollow fiber membrane and the belt, a groove that corresponds to the thickness of the hollow fiber membrane gripped on the surface of a smooth belt and that partially contains the hollow fiber membrane for thread feeding is parallel to the stretching direction. May be there.

【0012】弾性体の厚み方向の圧縮弾性率は把持する
中空糸の径方向の圧縮弾性率にたいして1/100以上
1以下であることが好ましく、さらに好適には1/50
以上1/2以下、さらに好適には1/20以上1/5以
下である。ベルトの厚みは特に限定しないが、糸つぶれ
と糸すべりから見て、弾性体部分の厚みが把持する中空
糸の直径に対して1〜100の範囲が好ましく、更に好
ましくは3〜50の範囲が好ましい。
The compressive elastic modulus in the thickness direction of the elastic body is preferably 1/100 or more and 1 or less, more preferably 1/50, of the compressive elastic modulus in the radial direction of the hollow fiber to be gripped.
It is not less than 1/2 and more preferably not less than 1/20 and not more than 1/5. Although the thickness of the belt is not particularly limited, the thickness of the elastic body portion is preferably in the range of 1 to 100, more preferably in the range of 3 to 50, with respect to the diameter of the hollow fiber to be grasped in view of the thread crushing and the thread sliding. preferable.

【0013】無限軌道式ベルトは相対する一対の2本の
ベルトで糸送り手段を構成するが、相対するベルトの間
隙を調整する方法は間隙の長さを一定にする方法、及び
二つのベルト間の押しつけ圧力を一定にする方法があ
り、ベルト間隙の長さを一定にする方法がベルトが振動
しにくく延伸しやすい。中空糸膜を連続的に延伸処理す
るに際し、中空糸膜が2以上の糸送り手段の間で直線的
に引き取られることとは、途中中空糸膜が曲がらずに延
伸処理でき、余計な変形を与えずに済む利点がある。更
にはベルトの円周部分では周速度がベルトのロール径に
対する厚み分の比だけ速度が増大しているため、中空糸
膜とベルトの間に余計なこすれを生じ、糸傷の原因とな
るため、その円周部分に接触せず、糸傷がつきにくい利
点を有する。
The endless track type belt comprises a pair of two belts which face each other as a yarn feeding means. The method of adjusting the gap between the belts facing each other is to keep the length of the gap constant, and between the two belts. There is a method of making the pressing pressure of the belt constant, and a method of making the length of the belt gap constant makes it difficult for the belt to vibrate and stretch easily. When the hollow fiber membrane is continuously stretched, the hollow fiber membrane is linearly drawn between the two or more yarn feeding means, which means that the hollow fiber membrane can be stretched without being bent and extra deformation is caused. There is an advantage of not giving. Furthermore, in the circumferential portion of the belt, the circumferential speed increases by the ratio of the thickness to the roll diameter of the belt, which causes excessive rubbing between the hollow fiber membrane and the belt, which may cause yarn scratches. , And has an advantage that it does not come into contact with the circumferential portion and is less likely to be damaged by yarn.

【0014】[0014]

【発明の実施の形態】以下本発明を実施例に基づいて説
明する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described below based on Examples.

【0015】[0015]

【実施例1】Mw値(粉体が完全に濡れるメタノールの
容量%)が50%、平均一次粒径0.016μm、比表
面積110m2/gの疎水性シリカ(アエロジルR−9
72(商品名))23重量%、フタル酸ジオクチル3
0.8重量%、フタル酸ジブチル6.2重量%をヘンシ
ェルミキサーで混合し、これに重量平均分子量2420
00のポリフッ化ビニリデン(クレハKFポリマー#1
000(商品名))40重量%を添加し再度ヘンシェル
ミキサーで混合した。
Example 1 Hydrophobic silica (Aerosil R-9) having an Mw value (volume% of methanol that completely wets powder) of 50%, an average primary particle size of 0.016 μm and a specific surface area of 110 m 2 / g.
72 (trade name)) 23% by weight, dioctyl phthalate 3
0.8% by weight and 6.2% by weight of dibutyl phthalate were mixed in a Henschel mixer, and the weight average molecular weight was 2420.
00 polyvinylidene fluoride (Kureha KF Polymer # 1
000 (trade name) 40% by weight was added and mixed again with a Henschel mixer.

【0016】該混合物を30mmφ二軸押し出し機で混
合し、ペレットにした。このペレットを30mmφ二軸
押し出し機に中空糸状紡口を取り付けた中空糸製造装置
にて空中を経て40℃の水槽中に20m/minの紡速
で溶融押し出しして中空糸状に成形し中空糸膜前駆体を
得た。相対する一対の無限軌道式ベルトを使用し、相対
するベルト間に挟んで双方のベルトを同速度で同方向へ
移動させる糸送り手段を2つ空間距離1.2mをへだて
て同高さに並べ、該中空糸膜前駆体をまず上流側の糸送
り手段で真横に20m/minの速度で引き取り、温度
100℃に制御した加熱空間(0.8m長)を経由し
て、30m/minで動く下流側の糸送り手段で引き取
り1.5倍に延伸し、その後カセで巻き取った。上流側
糸送り手段の糸の入口から下流側糸送り手段の糸の出口
まで中空糸膜は一直線状に配置され、曲げずに直線的に
延伸した。
The mixture was mixed with a 30 mmφ twin-screw extruder and pelletized. This pellet was melt extruded at a spinning speed of 20 m / min into a water tank at 40 ° C. through the air in a hollow fiber manufacturing apparatus equipped with a 30 mmφ twin-screw extruder with a hollow fiber-shaped spinneret to form a hollow fiber membrane. A precursor was obtained. Using a pair of opposing endless track type belts, sandwiching between the opposing belts, two yarn feeding means for moving both belts in the same direction at the same speed are arranged at the same height with a space distance of 1.2 m. First, the hollow fiber membrane precursor is first taken up by a yarn feeding means on the upstream side at a speed of 20 m / min, and moves at 30 m / min via a heating space (0.8 m length) controlled to a temperature of 100 ° C. The yarn was taken up by the yarn feeding means on the downstream side and drawn 1.5 times, and then wound up with a cassette. The hollow fiber membrane was arranged in a straight line from the yarn inlet of the upstream yarn feeding means to the yarn outlet of the downstream yarn feeding means, and was stretched linearly without bending.

【0017】上流側及び下流側の糸送り手段の無限軌道
式ベルトは4mm厚の繊維強化ベルトの外側に11mm
厚の表面が実質的に平滑なシリコーンゴム製のスポンジ
状の弾性体が一体的に接着されている。該糸送り手段は
前後約400mmの間隔で離れた2つの直径80mmの
金属ロール(一方が駆動ロール)の間に無限軌道式ベル
トが張られており、ベルト幅は80mm、ベルト長は繊
維強化ベルト部分で測って一周約1050mmであっ
た。該ベルト2組からなる同速度、同方向に直線的に動
くベルト隙間に、中空糸膜前駆体をはさんで延伸を行な
った。ベルト間隔は共に1.0mmで行なった。中空糸
膜前駆体の直径は延伸前は1.25mm延伸後は1.2
4mmであった。中空糸前駆体の径方向の圧縮弾性率は
延伸前で7MPa、延伸後で5MPaであった。シリコ
ーンゴム製のベルトの厚み方向の圧縮弾性率は0.9M
Paであった。
The endless belt of the yarn feeding means on the upstream side and the downstream side is 11 mm outside the fiber reinforced belt having a thickness of 4 mm.
A sponge-like elastic body made of silicone rubber having a substantially smooth surface is integrally bonded. The yarn feeding means has an endless track type belt stretched between two metal rolls (one of which is a drive roll) having a diameter of 80 mm, which are separated by a distance of about 400 mm in the front and back. The belt width is 80 mm and the belt length is a fiber reinforced belt. The circumference was about 1050 mm as measured at the portion. The hollow fiber membrane precursor was sandwiched between the two belts, which were linearly moved in the same direction at the same speed and in the same direction, and stretched. The belt intervals were both 1.0 mm. The diameter of the hollow fiber membrane precursor is 1.25 mm before stretching and 1.2 after stretching.
It was 4 mm. The compression modulus in the radial direction of the hollow fiber precursor was 7 MPa before stretching and 5 MPa after stretching. The compression elastic modulus in the thickness direction of the silicone rubber belt is 0.9M
It was Pa.

【0018】中空糸膜の圧縮弾性率は圧縮測定機(島津
製作所製:AGS−H/EZTest)で5mm幅の圧
縮用治具を用い中空糸膜の長さ5mm分について圧縮変
位と荷重を圧縮速度1mm/minで測定し、初期中空
糸膜直径に対して0.1%変位時と5%変位時の荷重か
ら100%変位時の荷重を求め、初期中空糸直径と中空
糸膜長5mmで得られる投影断面積で規格化し算出し
た。ベルトの弾性率は直径5mmの圧縮用治具を用い、
同様に行なった。
The compressive elastic modulus of the hollow fiber membrane was measured by using a compression measuring machine (manufactured by Shimadzu Corporation: AGS-H / EZTest) with a compression jig having a width of 5 mm to compress the compression displacement and the load for a length of 5 mm. Measured at a speed of 1 mm / min, the load at 100% displacement was calculated from the load at 0.1% displacement and 5% displacement with respect to the initial hollow fiber diameter, and the initial hollow fiber diameter and hollow fiber membrane length were 5 mm. The projected cross-sectional area obtained was standardized and calculated. For the elastic modulus of the belt, a compression jig with a diameter of 5 mm is used.
The same was done.

【0019】ついで巻き取った膜を30℃の塩化メチレ
ン中に1時間浸漬を3回繰り返してフタル酸ジオクチ
ル、フタル酸ジブチルを抽出した後、60℃で乾燥し
た。ついで50%エタノール水溶液に30分間浸漬し、
更に水中に移して30分間浸漬して、中空糸膜を水で濡
らした。更に40℃の5%苛性ソーダ水溶液中への1時
間浸漬を2回行い疎水性シリカを抽出した後、60℃の
熱水で12時間水洗し、60℃で乾燥した。
Then, the wound film was immersed in methylene chloride at 30 ° C. for 1 hour three times to extract dioctyl phthalate and dibutyl phthalate, and then dried at 60 ° C. Then, soak in 50% ethanol aqueous solution for 30 minutes,
Further, the hollow fiber membrane was transferred to water and immersed for 30 minutes to wet the hollow fiber membrane with water. After further dipping in a 5% caustic soda aqueous solution at 40 ° C. for 1 hour twice to extract the hydrophobic silica, it was washed with hot water at 60 ° C. for 12 hours and dried at 60 ° C.

【0020】得られた中空糸膜は外径1.22mm、内
径0.65mmで断面形状は円形でありつぶれ及び膜表
面の傷は認められなかった。延伸時のすべりもなく2つ
の糸送り手段の間の空間で延伸され、均一な延伸が出来
た。
The hollow fiber membrane thus obtained had an outer diameter of 1.22 mm, an inner diameter of 0.65 mm and a circular cross-sectional shape, and neither crushing nor scratches on the membrane surface were observed. There was no slippage during drawing, and drawing was performed in the space between the two yarn feeding means, and uniform drawing was possible.

【0021】[0021]

【発明の効果】本発明の処理方法を用いれば、中空糸膜
の延伸において延伸むらなく、糸傷なしに、円形断面の
中空糸を連続的に得ることができる。
EFFECTS OF THE INVENTION By using the treatment method of the present invention, it is possible to continuously obtain a hollow fiber having a circular cross section without unevenness in drawing in the drawing of the hollow fiber membrane and without any yarn scratches.

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

【図1】本発明の延伸方法を示す模式図FIG. 1 is a schematic diagram showing a stretching method of the present invention.

【符号の説明】[Explanation of symbols]

1:無限軌道式糸送り手段(上流側) 2:無限軌道式糸送り手段(下流側) 3:中空糸膜 4:無限軌道式ベルト 5:フリーロール 6:駆動ロール 1: Endless track type yarn feeding means (upstream side) 2: Endless track type yarn feeding means (downstream side) 3: Hollow fiber membrane 4: Endless track belt 5: Freeroll 6: Drive roll

フロントページの続き Fターム(参考) 4D006 GA03 GA06 GA07 HA01 MA01 MB11 MB15 MB16 MC22X MC25X MC29X MC39X MC62X MC63X NA21 NA25 NA34 NA64 PB04 PC02 PC41 4L036 MA04 MA19 PA03 RA13 UA08Continued front page    F-term (reference) 4D006 GA03 GA06 GA07 HA01 MA01                       MB11 MB15 MB16 MC22X                       MC25X MC29X MC39X MC62X                       MC63X NA21 NA25 NA34                       NA64 PB04 PC02 PC41                 4L036 MA04 MA19 PA03 RA13 UA08

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 下流側の糸送り速度を上流側の糸送り速
度より速くして、中空糸膜を2以上の糸送り手段間で連
続的に延伸処理するにあたり、それぞれの糸送り手段と
して相対する一対の無限軌道式ベルトを使用し、相対す
るベルト間に中空糸膜を挟んで双方のベルトを同速度で
同方向へ移動させることにより糸送りを行うこと、上流
側においては相対するベルトが接して移動する方向と同
方向へ向かってベルト間より中空糸膜を送りだすこと、
下流側においては相対するベルトが接して移動する方向
と同方向へ向かって中空糸膜をベルト間に供給すること
を特徴とする延伸方法。
1. When the hollow fiber membrane is continuously stretched between two or more yarn feeding means by setting the downstream yarn feeding speed to be higher than the upstream yarn feeding speed, the hollow fiber membranes are used as respective yarn feeding means. Using a pair of endless track type belts, the hollow fiber membrane is sandwiched between the opposing belts and both belts are moved in the same direction at the same speed to perform yarn feeding. Sending out the hollow fiber membrane from between the belts in the same direction as the contacting and moving direction,
On the downstream side, the hollow fiber membrane is fed between the belts in the same direction as the belts facing each other move in the same direction.
【請求項2】 延伸処理を空間で行う請求項1記載の延
伸方法。
2. The stretching method according to claim 1, wherein the stretching treatment is performed in space.
【請求項3】 延伸処理を中空糸膜を曲げずに直線的に
行なう請求項1記載の延伸方法。
3. The stretching method according to claim 1, wherein the stretching treatment is performed linearly without bending the hollow fiber membrane.
【請求項4】 無限軌道式ベルトが、表面が実質的に平
滑な弾性体からなる請求項1記載の延伸方法。
4. The stretching method according to claim 1, wherein the endless track belt is made of an elastic body having a substantially smooth surface.
JP2002001946A 2002-01-09 2002-01-09 Method for drawing hollow fiber membrane Expired - Lifetime JP3928927B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002001946A JP3928927B2 (en) 2002-01-09 2002-01-09 Method for drawing hollow fiber membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002001946A JP3928927B2 (en) 2002-01-09 2002-01-09 Method for drawing hollow fiber membrane

Publications (2)

Publication Number Publication Date
JP2003213538A true JP2003213538A (en) 2003-07-30
JP3928927B2 JP3928927B2 (en) 2007-06-13

Family

ID=27641939

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002001946A Expired - Lifetime JP3928927B2 (en) 2002-01-09 2002-01-09 Method for drawing hollow fiber membrane

Country Status (1)

Country Link
JP (1) JP3928927B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016159305A1 (en) * 2015-03-31 2016-10-06 東レ株式会社 Hollow fiber membrane manufacturing method
CN106592047A (en) * 2016-12-19 2017-04-26 绵阳美能材料科技有限公司 Stretching mechanism for hollow fiber membrane wire

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016159305A1 (en) * 2015-03-31 2016-10-06 東レ株式会社 Hollow fiber membrane manufacturing method
JPWO2016159305A1 (en) * 2015-03-31 2017-04-27 東レ株式会社 Method for producing hollow fiber membrane
CN106592047A (en) * 2016-12-19 2017-04-26 绵阳美能材料科技有限公司 Stretching mechanism for hollow fiber membrane wire

Also Published As

Publication number Publication date
JP3928927B2 (en) 2007-06-13

Similar Documents

Publication Publication Date Title
JP5068168B2 (en) Vinylidene fluoride resin hollow fiber porous membrane
JP5204384B2 (en) Crystalline polymer microporous membrane, method for producing the same, and filter for filtration
KR101539608B1 (en) Polyvinylidene fluoride Hollow Fiber Membranes and Preparation Thereof
JP5552289B2 (en) Method for producing vinylidene fluoride resin porous membrane
WO2016006670A1 (en) Membrane distillation apparatus and hydrophobic porous membrane
KR101657307B1 (en) Fluorinated hollow fiber membrane and method for preparing the same
JP4941865B2 (en) Tube for support of porous multilayer hollow fiber membrane and porous multilayer hollow fiber membrane using the same
JP5154784B2 (en) filter
JP2008062229A (en) Porous polyvinylidene fluoride membrane and method for preparing the same
JPWO2012026373A1 (en) Hollow fiber type reverse osmosis membrane and method for producing the same
US20170151534A1 (en) Substrate for liquid filter and method for producing the same
JP2006169497A (en) Porous body and manufacturing method thereof
JPWO2007032331A1 (en) Vinylidene fluoride resin hollow fiber porous membrane and method for producing the same
KR101790174B1 (en) A PVA coated hollow fiber mambrane and a preparation method thereof
JP4864707B2 (en) Method for producing vinylidene fluoride resin porous water treatment membrane
KR102384030B1 (en) An organic solvent nanofiltration membrane comprising molybdenum disulfide and a manufacturing method thereof
US20210106953A1 (en) Porous polymeric membrane and related filters and methods
JP2003213538A (en) Method for stretching hollow fiber membrane
TWI621653B (en) Ptfe/pfsa blended membrane
JP2007283232A (en) Vinylidene fluoride type resin hollow filament porous membrane and its manufacturing method
KR101453801B1 (en) Multilayer PTFE hollow fiber type membrane for membrane distillation and manufacturing method thereof
KR101426000B1 (en) PTFE hollow fibertype membrane for membrane distillation and manufacturing method thereof
JP5620665B2 (en) Method for producing stretched resin porous membrane
KR101464721B1 (en) Multilayer PTFE hollow fiber membrane having porosity and manufacturing method thereof
CN112088041A (en) Hollow fiber membrane and method for producing hollow fiber membrane

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20041216

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20061120

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20061128

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070129

RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20070129

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070301

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20070302

R150 Certificate of patent or registration of utility model

Ref document number: 3928927

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100316

Year of fee payment: 3

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100316

Year of fee payment: 3

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110316

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110316

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120316

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120316

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130316

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140316

Year of fee payment: 7

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term