JPH04197425A - Hollow fiber membrane filter module - Google Patents

Hollow fiber membrane filter module

Info

Publication number
JPH04197425A
JPH04197425A JP32607490A JP32607490A JPH04197425A JP H04197425 A JPH04197425 A JP H04197425A JP 32607490 A JP32607490 A JP 32607490A JP 32607490 A JP32607490 A JP 32607490A JP H04197425 A JPH04197425 A JP H04197425A
Authority
JP
Japan
Prior art keywords
solvent
cylindrical case
hollow fiber
cap
fiber 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
Application number
JP32607490A
Other languages
Japanese (ja)
Inventor
Manabu Yanou
学 矢能
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP32607490A priority Critical patent/JPH04197425A/en
Publication of JPH04197425A publication Critical patent/JPH04197425A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To accelerate the permeation of a solvent and to achieve uniform adhesion by providing a gap between a cylindrical case and the leading end part of a cap for forming a liquid collecting chamber over the entire periphery of the case and providing an opening part allowing the gap to communicate with the outside. CONSTITUTION:Hollow fiber membranes 2 bundled in a U-shape are received in a cylindrical case 1 and the U-shape end parts of the hollow fiber membranes and the cylindrical case 1 are integrally fixed by a resin fixing layer 3. A larger number of flow path holes 6 are provided to the side surface of the cylindrical case 1 and a fluid flows in the cylindrical case from these flow path holes to be filtered from the outsides of the hollow fiber membranes 2 to the insides thereof and moves to a liquid collecting chamber 5 to flow to a liquid passing port 7. A solvent injection port 9 and a solvent permeation part 10 are provided to the connection part of the cap 4 for forming the liquid collecting chamber and the cylindrical case 1. A solvent is injected from the solvent injection port 9 using a syringe having an injection needle to be allowed to flow in the solvent permeation part 10. The solvent flowing in the solvent permeation part 10 further permeates in a fitting part 11 to bond the cap and the case.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は中空糸模型濾過モジュールに関する。[Detailed description of the invention] [Industrial application fields] The present invention relates to a hollow fiber model filtration module.

[従来の技術] 近年、流体濾過能力を有する膜モジュールが医療分野、
液体及び気体処理分野などに多く用いられるようになっ
てきた。
[Prior Art] In recent years, membrane modules with fluid filtration capabilities have been used in the medical field.
It has come to be widely used in the fields of liquid and gas processing.

その一種として、中空糸の外側から内側に濾過された濾
過水を集液し通水口(他の機器や配管に接続される)へ
導くための集液室を持つモジュールが利用されている。
One type of module is a module that has a liquid collection chamber that collects the filtered water from the outside of the hollow fiber to the inside and guides it to a water port (connected to other equipment or piping).

[発明が解決しようとする課題] このような中空糸膜型濾過モジュールの場合、筒状ケー
スに樹脂で固定された中空糸膜を開孔させるため樹脂固
定部層を切断し、その後、集液室形成用キャップを接続
させなければならない。該キャップを筒状ケースに接着
させる方法としては、接着剤による接着、熱的融着、溶
剤接着等の公知の接着方法が挙げられる。溶接、超音波
ウェルト、摩擦溶接等、熱的融着方法は、接着が均一に
行える反面、熱的な歪の発生を制御する事が困難であり
、又接着剤による接着は、接合部に接着剤と云う異った
層が形成されるので、一般的には強力な□接合力を得る
事が困難である。これらの接着方法の中で、溶剤接着は
作業が容易で、高い強度が得られ、残留応力も少なく、
奇麗に接着を行える利点を有している。しかし、中空糸
膜型濾過モジュールの集液室形成用キャップと筒状ケー
スを溶剤接着させる場合、溶剤が通常揮発し易いため、
径の大きなモジュールでは、最初に溶剤を塗布した場所
と最後に塗布した場所では、膨潤、溶解の度合いが異な
り、粘度差が生じ接着が均一に行われない。また接着面
積が大きい場合、溶剤塗布後ただちに接着を行っても溶
剤の未浸透部が発生し、接着部からの漏れの原因となる
。さらに、未浸透部の発生したモジュールの修正はキャ
ップを取り外せないため不可能であるという欠点を有し
ている。
[Problems to be Solved by the Invention] In the case of such a hollow fiber membrane type filtration module, the resin fixing layer is cut in order to open holes in the hollow fiber membrane fixed with resin in the cylindrical case, and then the liquid collecting layer is cut. A chamber-forming cap must be connected. As a method for adhering the cap to the cylindrical case, known adhesion methods such as adhesive adhesion, thermal fusion, and solvent adhesion can be used. Although thermal bonding methods such as welding, ultrasonic welting, and friction welding can achieve uniform bonding, it is difficult to control the occurrence of thermal distortion, and bonding with adhesives does not adhere to the joint. Generally, it is difficult to obtain a strong □ bonding force because a different layer called a bonding agent is formed. Among these bonding methods, solvent bonding is easy to work with, provides high strength, and has low residual stress.
It has the advantage of being able to adhere neatly. However, when bonding the liquid collection chamber forming cap and the cylindrical case of a hollow fiber membrane type filtration module with a solvent, the solvent usually evaporates easily.
In large-diameter modules, the degree of swelling and dissolution differs between the area where the solvent is applied first and the area where it is applied last, resulting in a viscosity difference and uneven adhesion. Furthermore, if the bonding area is large, even if bonding is performed immediately after applying the solvent, there will be areas where the solvent has not penetrated, causing leakage from the bonded area. A further disadvantage is that it is impossible to repair a module in which an unpenetrated portion has occurred because the cap cannot be removed.

[課題を解決するための手段] 本発明は、少なくとも一方の端部が開口された筒状ケー
スと、該筒状ケース内にU字状もしくはほぼ直線状に集
束して収納され、少なくとも一端が開口された中空糸膜
と、中空糸膜の端部と筒状ケースの開口端部内面とを液
密に固定する樹脂固定層と、筒状ケースの開口端の外側
に嵌合され、中空糸膜の中空部と連通された通□液口を
有する集液室形成用キャップとからなる中空糸膜濾過モ
ジュールにおいて、 筒状ケースと集液室形成用キャップとの嵌合部の該ケー
スと該キャップ先端部との間に全周にわたっ、間隙が設
は蹴れ、ヵ、つ工。間隙と外部とを連通させる開口部が
設けられたことを特徴とする中空糸膜濾過モジュールで
ある。
[Means for Solving the Problems] The present invention includes a cylindrical case with at least one end open, and a cylindrical case that is housed in a U-shape or substantially linear shape, and that has at least one end opened. an open hollow fiber membrane; a resin fixing layer that liquid-tightly fixes the end of the hollow fiber membrane and the inner surface of the open end of the cylindrical case; In a hollow fiber membrane filtration module consisting of a cap for forming a liquid collection chamber having a communication port communicating with the hollow part of the membrane, the case and the cap at the fitting part of the cylindrical case and the cap for forming the liquid collection chamber are A gap is provided around the entire circumference between the tip of the cap and the tip of the cap. This hollow fiber membrane filtration module is characterized by being provided with an opening that communicates the gap with the outside.

上記開口部は溶剤を上記間隙に注入するための溶剤注入
口であり、上記間隙は注入口から注入された溶剤を嵌合
部全周にわたって浸透させるための溶剤浸透部である。
The opening is a solvent injection port for injecting a solvent into the gap, and the gap is a solvent penetration part for allowing the solvent injected from the injection port to penetrate all around the fitting part.

キャップ先端部に設けられる間隙(溶剤浸透部)は好ま
しくは一定幅の帯状であり、例えばケース、キャップの
いずれかあるいは両方に、切欠きあるいは溝を設けるこ
とによって得られる。
The gap (solvent permeation part) provided at the tip of the cap is preferably in the form of a band with a constant width, and can be obtained, for example, by providing a notch or a groove in either or both of the case and the cap.

溶剤注入口は外部からこの溶剤浸透部に溶剤を注入でき
る構造であればよく、通常はキャップの全周にわたって
設けられるが、複数個の孔を全周にわたって均等に配置
した構造であってもよい。
The solvent injection port need only have a structure that allows the solvent to be injected from the outside into this solvent penetration part, and is usually provided around the entire circumference of the cap, but it may also have a structure in which a plurality of holes are arranged evenly around the entire circumference. .

本発明で用いられる多孔質中空糸膜の素材としては、ポ
リオレフィン系、セルロース系、ポリスルホン系、ポリ
ビニルアルコール系、ポリアクリロニトリル系を始めと
して公知のものを特に制限なく用いることができる。こ
れらの中空糸膜はU字状もしくはほぼ直線状に集束して
筒状ケース内に収納される。U字状に集束された中空糸
膜はそのU字端部が樹脂固定され、直線状に集束された
中空糸膜は一端もしくは両端が樹脂固定される。
As the material for the porous hollow fiber membrane used in the present invention, known materials including polyolefin, cellulose, polysulfone, polyvinyl alcohol, and polyacrylonitrile can be used without particular limitation. These hollow fiber membranes are bundled into a U-shape or a substantially straight line and housed in a cylindrical case. Hollow fiber membranes bundled in a U-shape have their U-shaped ends fixed with a resin, and hollow fiber membranes bundled in a straight line have one or both ends fixed with a resin.

樹脂固定端部の中空糸膜は開口状態とされるが、樹脂固
定されない直線状集束中空糸膜の端部は閉鎖される。
The hollow fiber membrane at the resin-fixed end is left open, but the end of the linear focused hollow fiber membrane that is not fixed with the resin is closed.

また本発明のモジュールの他の要素の形状・大きさ・材
質等も公知のものを特に制限なく適用できる。
Furthermore, known shapes, sizes, materials, etc. of other elements of the module of the present invention can be used without particular limitation.

以下図面を参照しつつ本発明を説明する。The present invention will be described below with reference to the drawings.

第1図は本発明の中空糸膜濾過モジュールの一例を示す
模式縦断面図であり、第2図は溶剤注入口及び溶剤浸透
部を示すための拡大図である。U字状に束ねられた中空
糸膜2が筒状ケース1内に収納され、中空糸膜のU字端
部と筒状ケースは樹脂固定層3で一体的に固定されてい
る。尚、図において中空糸膜2の大部分は省略されてい
る。
FIG. 1 is a schematic vertical sectional view showing an example of the hollow fiber membrane filtration module of the present invention, and FIG. 2 is an enlarged view showing a solvent inlet and a solvent permeation part. Hollow fiber membranes 2 bundled in a U-shape are housed in a cylindrical case 1, and the U-shaped ends of the hollow fiber membranes and the cylindrical case are integrally fixed with a resin fixing layer 3. Note that most of the hollow fiber membrane 2 is omitted in the figure.

この膜モジュールにおいては、筒状ケース1の側面に流
路孔6が多数設けられており、この流路孔から流体が流
入し、中空糸膜2の外側から内側へ濾過され、集液室5
へと移動し、通液ロアへと流れる。ここで0−リング8
は膜モジュールを濾過装置本体へ据え付ける際のシール
部材としての役割をはだすものである。
In this membrane module, a large number of flow passage holes 6 are provided on the side surface of the cylindrical case 1, and fluid flows into the flow passage holes and is filtered from the outside to the inside of the hollow fiber membrane 2.
and flows to the liquid passage lower. Here 0-ring 8
serves as a sealing member when installing the membrane module into the main body of the filtration device.

集液室形成用キャップ4と筒状ケース1の接合部には溶
剤注入口9及び溶剤浸透部10が設けである。溶剤注入
口9より注射針付きのシリンジ等を用いて溶剤を注入し
、溶剤浸透部10へ流し込むようにする。溶剤浸透部1
0へ流入した溶剤はさらに嵌合部11へと浸透し接着さ
れることとなる。溶剤注入口としては、周上全体に溝状
に配置されてもよいし、注入口として周上に何口かが均
等に配置されてもよい。注入口の大きさは最低注射針が
入るぐらいの大きさが確保されればよい。
A solvent inlet 9 and a solvent permeation part 10 are provided at the joint between the cap 4 for forming a liquid collection chamber and the cylindrical case 1. The solvent is injected from the solvent injection port 9 using a syringe with a needle, etc., and is caused to flow into the solvent penetration part 10. Solvent penetration part 1
The solvent that has flowed into the fitting portion 11 further penetrates into the fitting portion 11 and is bonded thereto. The solvent injection ports may be arranged in a groove shape all over the circumference, or several injection ports may be arranged evenly on the circumference. The injection port should be large enough to accommodate at least a syringe needle.

また溶剤浸透部としては周上に溶剤が少量保持されるだ
けの空間を持てばよい。さらに嵌合部11の嵌合度合は
密着されていると同時に溶剤浸透部10から溶剤が浸透
し易い度合いが好ましい。密着し過ぎると嵌合部へ浸透
せず、接着不良となり、嵌合度合いが甘いとまた接着不
良となる恐れがある。
Further, the solvent permeation portion only needs to have a space on the periphery that is large enough to hold a small amount of the solvent. Furthermore, it is preferable that the fitting degree of the fitting part 11 is such that the fitting part 11 is in close contact and at the same time allows the solvent to easily permeate from the solvent permeation part 10. If the fit is too close, it will not penetrate into the fitting portion, resulting in poor adhesion, and if the degree of fit is too loose, there is a risk of poor adhesion.

使用する溶剤としては、筒状ケースと集液室形成用キャ
ップの材料及び溶剤の沸点、溶解性、溶解速度を考慮し
て選定するのが好ましい。例えば材質がポリカーボネー
トの場合、エチレンクロライド(二塩化エタン)等、ポ
リスルフォンの場合、塩化メチレン等が好ましい。
The solvent to be used is preferably selected in consideration of the material of the cylindrical case and the cap for forming the liquid collection chamber, and the boiling point, solubility, and dissolution rate of the solvent. For example, when the material is polycarbonate, ethylene chloride (ethane dichloride) and the like are preferred, and when the material is polysulfone, methylene chloride and the like are preferred.

乾燥方法としては、200 kg/am”程度の接着程
度で良い場合は常温で24時間放置するのみでよい。し
かし、更に高い強度を必要としたり、高温雰囲気中で使
用する場合は60℃で24時間乾燥させることが好まし
い。
As for the drying method, if an adhesion level of about 200 kg/am" is sufficient, it is sufficient to leave it at room temperature for 24 hours. However, if higher strength is required or if it is used in a high temperature atmosphere, drying at 60°C for 24 hours is sufficient. It is preferable to dry it for a long time.

また、従来は一度接着を行い溶剤浸透不良部が発生すれ
ば、そこから流体の漏れを生じ、モジュールとしては使
用出来ない状態であった。しかし、本発明では、溶剤浸
透不良部が発生しても、溶剤注入口9として予めスペー
スを設けであるので、この溶剤注入口9より再度、注射
針付きのシリンジ等を用いて溶剤を注入、不良部の修正
を行う事が可能である。
Furthermore, in the past, once adhesive was bonded and a defective solvent penetration area occurred, fluid would leak from there and the module could not be used. However, in the present invention, even if a solvent penetration failure occurs, a space is provided in advance as the solvent injection port 9, so the solvent can be injected again from the solvent injection port 9 using a syringe with a needle, etc. It is possible to repair defective parts.

[実施例コ 以下実施例により本発明を説明する。[Example code] The present invention will be explained below with reference to Examples.

実施例1 第1図に示すような通液ロアが閉鎖された集液室形成用
キャップ(ポリカーボネート製、内径φ64mm、肉厚
3mm)、またキャップと接着されない側の端部が閉鎖
され、かっ流路孔6が閉鎖された周上ケース(ポリカー
ボネート製、内径φ64mm、肉厚3mm、長さ215
mm)を作製した。この時のケースとキャップの嵌合度
合は嵌合部接触長さが6mmで、嵌合させてキャップ側
を下にした時少し軽く振ると落ちるような度合いに設定
した。
Example 1 A cap for forming a liquid collection chamber (made of polycarbonate, inner diameter φ64 mm, wall thickness 3 mm) with a closed liquid passage lower as shown in Fig. Circumferential case with closed passage hole 6 (made of polycarbonate, inner diameter φ64 mm, wall thickness 3 mm, length 215 mm)
mm) was produced. At this time, the degree of fitting between the case and the cap was set to such a degree that the contact length of the fitting part was 6 mm, and that when they were fitted and the cap side was facing down, it would fall off when shaken slightly.

次に嵌合させた状態で溶剤注入口からエチレンクロライ
ドを注射針付きシリンジを使用して注入し、溶剤浸透部
、嵌合部まで溶剤を浸透させた。
Next, in the fitted state, ethylene chloride was injected from the solvent injection port using a syringe with a needle, and the solvent penetrated into the solvent permeation area and the fitting area.

この後、60℃で24時間乾燥させた。After that, it was dried at 60°C for 24 hours.

このようにして得られたモジュール(2個)について、
常温で、筒状のケースの閉鎖端部側から3、0Kg/c
m2の水圧を10秒間、圧力解除10秒間を1サイクル
とする繰り返し耐水圧試験を行い接着部からの漏れを検
査したところ第1表の結果が得られた。
Regarding the modules (2 pieces) obtained in this way,
At room temperature, 3.0 kg/c from the closed end side of the cylindrical case
A repeated water pressure test was conducted in which one cycle consisted of applying a water pressure of m2 for 10 seconds and releasing the pressure for 10 seconds to check for leakage from the bonded portion, and the results shown in Table 1 were obtained.

通例モジュールに要求されるこの条件での目標サイクル
数は25000以上である。
The target number of cycles under this condition typically required for a module is 25,000 or more.

表1表 実施例2 実施例1と全く同様にモジュールを作製し、水圧を5.
0Kg/cm”を10秒間、圧力解除10秒間を1サイ
クルとして繰り返し耐水圧試験を行い、接着部からの漏
れを検査したところ第2表の結果が得られた。
Table 1 Table Example 2 A module was produced in exactly the same manner as in Example 1, and the water pressure was set to 5.
A water pressure test was repeated with one cycle of 0 Kg/cm'' for 10 seconds and 10 seconds of pressure release, and leakage from the bonded portion was examined, and the results shown in Table 2 were obtained.

通例モジュールに要求されるこの条件での目標サイクル
数は18000以上である。
The target number of cycles under this condition that is normally required for the module is 18,000 or more.

表2表 実施例3および比較例1 集液室形成用キャップ、筒状ケースの材質をポリスルフ
ォン製として、実施例1と全く同様のモジュールを作製
し、溶剤として塩化メチレンを用いて接着、その後60
℃で24時間乾燥させた。
Table 2 Table Example 3 and Comparative Example 1 A module completely similar to Example 1 was prepared using polysulfone as the material for the cap for forming the liquid collection chamber and the cylindrical case, and the module was bonded using methylene chloride as a solvent. 60
It was dried at ℃ for 24 hours.

このようにして得られたモジュールについて、第3表に
示す温度の熱水中で、筒状ケースの閉鎖端部側から第3
表に示す水圧を10秒間、圧力解除10秒間を1サイク
ルとする繰り返し耐水圧試験を行い、接着部からの漏れ
を検査したところ第3表の結果が得られた。
The module obtained in this way was placed in hot water at the temperature shown in Table 3 in the third section from the closed end side of the cylindrical case.
A repeated water pressure test was conducted in which the water pressure shown in the table was applied for 10 seconds and the pressure was released for 10 seconds as one cycle, and leakage from the bonded portion was examined, and the results shown in Table 3 were obtained.

また実施例3の溶剤接着の代りにエポキシ樹脂による接
着を行った場合の試験を比較例1として第3表に示す。
Further, Table 3 shows a test as Comparative Example 1 in which adhesion using epoxy resin was performed instead of the solvent adhesion in Example 3.

表3表 実施例4 実施例3と全く同様に作製されたモジュールについて、
90℃熱水中に5分、0℃冷水中に5分を1サイクルと
するヒートサイクル試験を100サイクル行い、その後
常温にて筒状ケースの閉鎖端部側から5.0Kg/cm
”の水圧を10秒間、圧力解除10秒間を1サイクルと
する繰り返し耐水圧試験を行い接着部からの漏れを検査
した所、第4表の結果が得られた。
Table 3 Table Example 4 Regarding the module manufactured in exactly the same way as Example 3,
A heat cycle test of 5 minutes in 90℃ hot water and 5 minutes in 0℃ cold water was conducted for 100 cycles, and then 5.0Kg/cm was applied from the closed end side of the cylindrical case at room temperature.
A repeated water pressure test was conducted in which one cycle was a water pressure of 10 seconds and a pressure release for 10 seconds to check for leakage from the bonded portion, and the results shown in Table 4 were obtained.

表4表 [発明の効果] 本発明の膜モジ亙−ルは以下に掲げるような優れた効果
を奏するものである。
Table 4 [Effects of the Invention] The membrane module of the present invention exhibits the following excellent effects.

(1)溶剤注入口及び溶剤浸透部を設けたことにより、
溶剤の浸透が速やかになり、均等に接着することが可能
である。
(1) By providing a solvent inlet and a solvent penetration part,
The solvent penetrates quickly and it is possible to bond evenly.

(2)溶剤注入口及び溶剤浸透部を設けたことにより、
溶剤未浸透部が発生した場合においても修正が可能であ
る。
(2) By providing a solvent inlet and a solvent penetration part,
Even if a solvent-unpenetrated area occurs, it can be corrected.

(3)径の大きなモジュールや接着面積を大きく取ろう
とするモジュールにおいても容易にかつ奇麗に接着する
ことが可能である。
(3) Even modules with large diameters or modules requiring a large bonding area can be bonded easily and neatly.

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

第1図は本発明の中空糸膜濾過モジュールの縦断面模式
図であり、第2図はその嵌合部の一部の拡大図である。 1:筒状ケース   2:中空糸膜 3:樹脂固定層 4:集液室形成用キャップ 5:集液室 6:流路孔 7:通液口 8:0−リング 9:溶剤注入口(開口部) 1o:溶剤浸透部(間隙) 11:嵌合部 特許出願人 三菱レイヨンン株式会社
FIG. 1 is a schematic vertical cross-sectional view of the hollow fiber membrane filtration module of the present invention, and FIG. 2 is an enlarged view of a part of the fitting portion thereof. 1: Cylindrical case 2: Hollow fiber membrane 3: Resin fixed layer 4: Cap for forming liquid collection chamber 5: Liquid collection chamber 6: Channel hole 7: Liquid passage port 8: 0-Ring 9: Solvent injection port (opening Part) 1o: Solvent penetration part (gap) 11: Fitting part Patent applicant Mitsubishi Rayon Co., Ltd.

Claims (1)

【特許請求の範囲】 少なくとも一方の端部が開口された筒状ケースと、該筒
状ケース内にU字状もしくはほぼ直線状に集束して収納
され、少なくとも一端が開口された中空糸膜と、中空糸
膜の端部と筒状ケースの開口端部内面とを液密に固定す
る樹脂固定層と、筒状ケースの開口端の外側に嵌合され
、中空糸膜の中空部と連通された通液口を有する集液室
形成用キャップとからなる中空糸膜濾過モジュールにお
いて、 筒状ケースと集液室形成用キャップとの嵌合部の該ケー
スと該キャップ先端部との間に全周にわたって間隙が設
けられ、かつこの間隙と外部とを連通させる開口部が設
けられたことを特徴とする中空糸膜濾過モジュール。
[Scope of Claims] A cylindrical case with at least one end opened, and a hollow fiber membrane stored in the cylindrical case in a U-shape or substantially straight line and with at least one end opened. , a resin fixing layer that liquid-tightly fixes the end of the hollow fiber membrane and the inner surface of the opening end of the cylindrical case; In a hollow fiber membrane filtration module that includes a cap for forming a liquid collection chamber and a cap for forming a liquid collection chamber, there is a gap between the case and the tip of the cap at the fitting part between the cylindrical case and the cap for forming the liquid collection chamber. A hollow fiber membrane filtration module characterized in that a gap is provided along the circumference, and an opening is provided to communicate the gap with the outside.
JP32607490A 1990-11-29 1990-11-29 Hollow fiber membrane filter module Pending JPH04197425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32607490A JPH04197425A (en) 1990-11-29 1990-11-29 Hollow fiber membrane filter module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32607490A JPH04197425A (en) 1990-11-29 1990-11-29 Hollow fiber membrane filter module

Publications (1)

Publication Number Publication Date
JPH04197425A true JPH04197425A (en) 1992-07-17

Family

ID=18183820

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32607490A Pending JPH04197425A (en) 1990-11-29 1990-11-29 Hollow fiber membrane filter module

Country Status (1)

Country Link
JP (1) JPH04197425A (en)

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