JPH01284305A - Production of hollow fiber membrane filter module - Google Patents
Production of hollow fiber membrane filter moduleInfo
- Publication number
- JPH01284305A JPH01284305A JP11189188A JP11189188A JPH01284305A JP H01284305 A JPH01284305 A JP H01284305A JP 11189188 A JP11189188 A JP 11189188A JP 11189188 A JP11189188 A JP 11189188A JP H01284305 A JPH01284305 A JP H01284305A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- hollow fiber
- fiber membrane
- resin liquid
- cylindrical body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 53
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 39
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 229920005989 resin Polymers 0.000 claims abstract description 89
- 239000011347 resin Substances 0.000 claims abstract description 89
- 239000007788 liquid Substances 0.000 claims description 45
- 238000003780 insertion Methods 0.000 claims description 17
- 230000037431 insertion Effects 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 13
- 238000005374 membrane filtration Methods 0.000 claims description 3
- 238000002347 injection Methods 0.000 abstract description 3
- 239000007924 injection Substances 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract description 2
- -1 polyethylene Polymers 0.000 description 5
- 239000004698 Polyethylene Substances 0.000 description 4
- 229920000573 polyethylene Polymers 0.000 description 4
- 238000003860 storage Methods 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 238000003466 welding 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〕
本発明は各種流体の分離に有効な中空糸膜濾過モジュー
ルの製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for manufacturing a hollow fiber membrane filtration module that is effective in separating various fluids.
近年、流体分離能力を有する中空糸膜モジュールが、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
うになりてきた。そして、これらの膜モジュールの代表
的な形状としては中空糸膜の両端が開口状態で樹脂固定
されているものと、一端が封止され他端が開口状態で樹
脂固定されているものがある。又、端部な樹脂で固定す
る方法としては、遠心力を作用させつつ中空糸膜の端部
であって、束ねられた中空糸膜間及び中空糸膜とケース
壁間の空間に樹脂を供給する方法が一般的である。この
場合、通常中空糸膜を収納したケースとその側方に配置
された樹脂液貯めを連結チューブで接続した膜モジユー
ル製造用セットを遠心機内に収納して遠心力を作用させ
る方法が採用されている。In recent years, hollow fiber membrane modules having fluid separation capabilities have come to be widely used in the medical field, liquid and gas processing fields, and the like. Typical shapes of these membrane modules include those in which both ends of the hollow fiber membrane are open and fixed with resin, and those in which one end is sealed and the other end is fixed with resin in an open state. In addition, as a method of fixing with resin at the ends, applying centrifugal force, resin is supplied to the ends of the hollow fiber membranes, between the bundled hollow fiber membranes and the space between the hollow fiber membranes and the case wall. The most common method is to In this case, a method is usually adopted in which a membrane module manufacturing set consisting of a case containing the hollow fiber membrane and a resin liquid reservoir placed on the side thereof connected by a connecting tube is housed in a centrifuge and centrifugal force is applied. There is.
しかし、このような樹脂注入方法では遠心機内において
一つの膜モジユールセットに対シ℃より多くのスペース
が要求され生産効率が向上でき難い。又、この方法では
第3図に示すように、膜モジュールの収納ケースと樹脂
液貯めにおいて樹脂液の面(B −B’面)の位置が等
しくなるように樹脂固定されろため、樹脂液貯め中と連
結チューブ中に無駄な樹脂が使用されることになる。更
に樹脂液を収納ケースの側方かも注入すると、中空糸膜
の均一分散固定が困難となり、たとえば第4図に示すと
と(中空糸膜が不均一分散状態で固定されることになる
。又、粘度の低い樹脂液を用い強遠心力下で注入すると
、第6図に示すように中空糸膜束の側面を樹脂がはい上
がり易く、樹脂の均一分配固定が困難である。However, in this resin injection method, one membrane module set requires more space than the temperature of the centrifuge, making it difficult to improve production efficiency. In addition, in this method, as shown in Fig. 3, the resin must be fixed so that the positions of the resin liquid surfaces (B-B' planes) are the same in the membrane module storage case and the resin liquid reservoir. Resin will be wasted in the inside and connecting tube. Furthermore, if the resin liquid is also injected into the sides of the storage case, it becomes difficult to uniformly disperse and fix the hollow fiber membranes. For example, as shown in FIG. 4, the hollow fiber membranes will be fixed in a non-uniformly dispersed state. If a resin liquid with low viscosity is used and injected under strong centrifugal force, the resin tends to creep up the sides of the hollow fiber membrane bundle as shown in FIG. 6, making it difficult to uniformly distribute and fix the resin.
本発明は、前記欠点を改良した膜モジユール製造方法の
提供を目的とするものであり、従来使用されていた遠心
機内で膜モジユールセット収納数を増し、樹脂の無駄を
減らし、樹脂固定操作を容易にし、樹脂固定時の中空糸
膜の偏りをなりシ1分散性を向上させる方法を提供する
ことを目的とする。The present invention aims to provide a membrane module manufacturing method that improves the above-mentioned drawbacks, and increases the number of membrane module sets stored in conventional centrifuges, reduces waste of resin, and facilitates resin fixing operations. It is an object of the present invention to provide a method for easily improving the dispersibility of hollow fiber membranes by reducing the bias of the hollow fiber membrane during resin fixation.
〔課題を解決するための手段〕
本発明の要旨は、一端が閉鎖され他端が開口された筒状
体の内部に、樹脂固定される端部が筒状体の閉鎖端側と
なるように中空糸膜束を収納し、筒状体の開口端側に樹
脂液貯めを配置し、その一端が樹脂液貯めと連通された
樹脂液挿入管をその他端が筒状体の閉鎖端近傍に位置す
るように中空糸膜束のほぼ中央部において筒状体と実質
的に平行に延在させた状態で、これらを遠心機内に設置
し、遠心力作用下において樹脂液貯めから樹脂液挿入管
を介して樹脂液を筒状体の閉鎖端部へ注入することによ
り中空糸膜束の端部を樹脂固定する中空糸膜濾過モジュ
ールの製造方法にある。[Means for Solving the Problems] The gist of the present invention is to provide a cylindrical body with one end closed and the other end open so that the end to which the resin is fixed is on the closed end side of the cylindrical body. A hollow fiber membrane bundle is housed, a resin liquid reservoir is arranged on the open end side of the cylindrical body, and a resin liquid insertion tube whose one end is communicated with the resin liquid reservoir is located at the other end near the closed end of the cylindrical body. The hollow fiber membrane bundle is placed in a centrifuge with its central part extending substantially parallel to the cylindrical body, and the resin liquid insertion tube is inserted from the resin liquid reservoir under the action of centrifugal force. The present invention provides a method for manufacturing a hollow fiber membrane filtration module, in which an end portion of a hollow fiber membrane bundle is fixed with a resin by injecting a resin liquid into the closed end portion of a cylindrical body.
第1図は樹脂固定された直後の状態を示す模式断面図で
あるが、この図面に基づい1本・発明の製造方法を説明
する。図において一端が閉鎖され他端が開口された筒状
体は、両端が開口された円筒本体1と閉鎖部材2から構
成されており、両者は固定用リング3により密着されて
いる。筒状体はこのように複数の部材から構成されてい
てもよく、又、全体が一体成形されたものであってもよ
い。但し、樹脂固定後に樹脂固定部と共に切断する必要
があるため、少なくとも切断予定部分が容易に切断可能
な材質であることが好ましい。FIG. 1 is a schematic sectional view showing the state immediately after being fixed with resin, and the manufacturing method of the present invention will be explained based on this drawing. In the figure, the cylindrical body with one end closed and the other end open is composed of a cylindrical body 1 and a closing member 2, both of which are open at both ends, and both are tightly attached by a fixing ring 3. The cylindrical body may be composed of a plurality of members as described above, or may be integrally molded as a whole. However, since it is necessary to cut the resin fixing part together with the resin fixing part after fixing the resin, it is preferable that at least the part to be cut is made of a material that can be easily cut.
図においては樹脂液が浸入しないように融着又は圧着等
によりて端部が実質的に封鎖された中空糸膜がU字状に
集束され、その端部が前記筒状体の閉鎖端に接するよう
に収納されている。In the figure, hollow fiber membranes whose ends are substantially sealed by welding or pressure bonding to prevent resin liquid from entering are bundled into a U-shape, and the ends are in contact with the closed end of the cylindrical body. It is stored like this.
中空糸膜はU字状とする代わりにほぼ平行に集束配置し
てもよいが、この場合は樹脂固定されない側の端部は完
全に封鎖されていることが必要である。Instead of having a U-shape, the hollow fiber membranes may be arranged in substantially parallel bundles, but in this case, it is necessary that the end on the side to which the resin is not fixed is completely sealed.
又、中空糸膜束として耳部な切断することなく折り返さ
れた中空糸膜編物を用いてもよい。Alternatively, a hollow fiber membrane knitted fabric which is folded back without cutting the edges may be used as the hollow fiber membrane bundle.
中空糸膜としては、たとえばポリエチレン、ポリビニル
アルコール、ポリスルホン、ポリメチルメタクリレート
、セルロース等からなる公知のものを用いることができ
る。又、樹脂液としてはポリウレタン、不飽和ポリエス
テル、エポキシ樹脂、シリコン樹脂等の公知の液状樹脂
を用いることができる。As the hollow fiber membrane, for example, known membranes made of polyethylene, polyvinyl alcohol, polysulfone, polymethyl methacrylate, cellulose, etc. can be used. Further, as the resin liquid, known liquid resins such as polyurethane, unsaturated polyester, epoxy resin, silicone resin, etc. can be used.
樹脂液貯めは前記筒状体の開口端側に配置されるが、保
持を容易にするため、その一部が筒状体の内側に収納さ
れるように配置することが好ましい。この樹脂液貯めは
その一端の中央部に樹脂液挿入管と接続するための開口
部6aを有している。図におい工は他端に開口部6bが
あり、この部分から必要量の樹脂液を入れるが該開口部
の位置は特に限定されず、たとえば側方部の位置にあっ
てもよい。樹脂液貯めの大きさは樹脂固定に必要とされ
る量の樹脂液を収納できればよく、特に限定されない。The resin liquid reservoir is disposed on the open end side of the cylindrical body, but in order to facilitate retention, it is preferably disposed such that a portion thereof is housed inside the cylindrical body. This resin liquid reservoir has an opening 6a in the center of one end thereof for connection to a resin liquid insertion tube. The odor holder in the figure has an opening 6b at the other end, from which a necessary amount of resin liquid is poured, but the position of the opening is not particularly limited, and may be located, for example, on the side. The size of the resin liquid reservoir is not particularly limited as long as it can accommodate the amount of resin liquid required for fixing the resin.
樹脂液挿入管(以下「挿入管」という)は中空糸膜束の
中央部に配置されるが、樹脂液の粘度を考慮してそのサ
イズを適宜法めることができる。長さは特に限定されな
いが、筒状体の閉鎖端側に配置される先端部の位置が筒
状体の閉鎖端の近傍となるようにする。通常は樹脂固定
後において樹脂固定部中に先端部が埋没しない程度で可
能な限り長くするように決められるが挿入管の先端部は
樹脂固定部中に埋没しても差支えない。但し、その場合
は挿入管が膜モジユール中に残されたまま使用に供され
ることになる。挿入管は通常樹脂液貯めの接続部と嵌合
等によりて接続されるものであるが、樹脂液貯めと一体
成形されたものでもよい。但し、その場合は樹脂固定後
に樹脂液貯めと共に系外へ取り出すことが必要なため、
先端部の位置が樹脂固定部中に埋没しないように長さを
決めることが好ましい。The resin liquid insertion tube (hereinafter referred to as "insertion tube") is arranged at the center of the hollow fiber membrane bundle, and its size can be determined as appropriate in consideration of the viscosity of the resin liquid. Although the length is not particularly limited, the tip portion disposed on the closed end side of the cylindrical body should be located near the closed end of the cylindrical body. Usually, it is decided to make the insertion tube as long as possible without burying the distal end in the resin fixing part after fixing with the resin, but the distal end of the insertion tube may be buried in the resin fixing part. However, in that case, the insertion tube remains in the membrane module and is used. The insertion tube is usually connected to the connecting portion of the resin liquid reservoir by fitting or the like, but it may be integrally molded with the resin liquid reservoir. However, in that case, it is necessary to remove the resin from the system together with the resin liquid reservoir after fixing the resin.
It is preferable to determine the length so that the position of the tip part is not buried in the resin fixing part.
筒状体中への中空糸膜と挿入管の収納の順序は特に限定
されず、どちらか一方を先に収納してもよ(、両者を同
時に収納してもよい。The order in which the hollow fiber membrane and the insertion tube are housed in the cylindrical body is not particularly limited, and either one may be housed first (or both may be housed at the same time).
以上のようにして筒状体、中空糸膜、挿入管、樹脂液貯
めを所定の位置にセットし、通常は第1図に示すように
樹脂液貯めが上方に(るよ5な状態で樹脂液貯め中に必
要量の樹脂液を入れ遠心力を作用させる。遠心力(工公
知の遠心機にて作用させるが、回転数、運転時間は多孔
質膜の細孔径や樹脂液の粘度を考慮して適宜設定すれば
よい。As described above, the cylindrical body, hollow fiber membrane, insertion tube, and resin liquid reservoir are set in the predetermined positions, and normally the resin liquid reservoir is placed upward (as shown in Figure 1). Pour the required amount of resin liquid into the liquid reservoir and apply centrifugal force.Centrifugal force (apply using a known centrifuge, but the rotation speed and operating time should take into account the pore diameter of the porous membrane and the viscosity of the resin liquid. and set as appropriate.
樹脂固定後は通常の方法に従って樹脂固定端部を切断す
ることにより膜モジュールとして使用することができる
。After fixing with the resin, it can be used as a membrane module by cutting the ends fixed with the resin according to a conventional method.
以下、実施例により本発明を説明する。 The present invention will be explained below with reference to Examples.
実施例1
第1図とほば同様の膜上ジュールセットを用いた。内径
40tmφ、長さ105WNのポリカーボネート製円筒
の一端にポリエチレン製の鋳槃枠(閉鎖部材)を固定用
リングでとりつけ筒状体を作製した。次に外径0.38
tlφのポリエチレン中空糸膜2600本を8字状に束
ね、長さが100翼鳳となるように端部な切り揃えると
共に端部を封止し筒状体内に収納した。続いて予め樹脂
液貯めと接続した挿入管を挿入管が中空糸膜の中央部に
なるように配置した。挿入管としては外径61jlφ、
内径4關φ、長さ80mのポリエチレン製のものを用い
た。Example 1 A membrane joule set almost similar to that shown in FIG. 1 was used. A polyethylene molding frame (closing member) was attached to one end of a polycarbonate cylinder having an inner diameter of 40 tmφ and a length of 105 WN using a fixing ring to produce a cylindrical body. Next, the outer diameter is 0.38
2,600 tlφ polyethylene hollow fiber membranes were bundled into a figure 8 shape, the ends were trimmed to a length of 100 wings, the ends were sealed, and the membranes were housed in a cylindrical body. Subsequently, an insertion tube previously connected to a resin liquid reservoir was placed so that the insertion tube was in the center of the hollow fiber membrane. The insertion tube has an outer diameter of 61jlφ,
A polyethylene tube with an inner diameter of 4 mm and a length of 80 m was used.
このよ5な膜モジユール用セットを24組準準し、各々
の樹脂液貯めにウレタン樹脂的25Iを投入し、直ちに
遠心機内に設置して遠心機を作動させた。遠心機の回転
数は220 rpmとし、80分間運転した。遠心工程
終了後、膜モジユールセットを取り出して観察したとこ
ろ、投入した樹脂液の全てが樹脂固定用に使用されてお
り、樹脂固定部中の樹脂の分布にほば均一であり遠心機
からの取り出しも容易でありた。Twenty-four sets of these 5 membrane modules were prepared, and urethane resin 25I was poured into each resin liquid reservoir, and immediately placed in a centrifuge and the centrifuge was operated. The rotation speed of the centrifuge was 220 rpm, and the centrifuge was operated for 80 minutes. After the centrifugation process was completed, the membrane module set was taken out and observed, and it was found that all of the resin liquid put in was used for resin fixation, and the distribution of resin in the resin fixation part was almost uniform, indicating that there was no flow from the centrifuge. It was also easy to take out.
そのままの状態で一日放置後、樹脂液貯めと固定用リン
グをとりはずし、次いで第2図のA−A′面の位置にお
いて樹脂固定端部を封止部材とともに切断して膜モジュ
ールを得た。中空糸の分散状態は良好であり、その切断
面は第5図に示すようであった。After leaving it as it was for one day, the resin liquid reservoir and the fixing ring were removed, and then the resin fixed end was cut along with the sealing member at the line AA' in FIG. 2 to obtain a membrane module. The hollow fibers were well dispersed, and the cut surface was as shown in FIG.
本発明の方法は以下に掲げるような優れた効果を奏する
ものである。The method of the present invention has the following excellent effects.
(1) glモジュールセクトの遠心機内における占
有率が少なく、従来と同一の遠心機を用いた場合、−度
に2〜3倍の膜モジュールを生産することができる。(1) The occupancy rate of the GL module section in the centrifuge is small, and when the same centrifuge as the conventional one is used, two to three times as many membrane modules can be produced at a time.
(2)樹脂液の無駄がない。(2) There is no waste of resin liquid.
(3) 樹脂固定部において、中空糸膜の分布に偏り
を生じさせることなく樹脂固定できる。(3) In the resin fixing part, the resin can be fixed without causing a bias in the distribution of the hollow fiber membranes.
(4)膜モジユールセットの配置がコンパクトであり操
作が容易である。(4) The arrangement of the membrane module set is compact and easy to operate.
(5) 以上の点を総合して、膜モジユール製造にお
いて、作業の合理化と製造コストの低減に極めて有効で
ある。(5) Taking all of the above points into account, this method is extremely effective in streamlining operations and reducing manufacturing costs in membrane module manufacturing.
第1図は本発明の方法において、樹脂固定直後の膜モジ
ユールセットの模式断面図を示す。
第2図は第1図の工程後に樹脂液貯めと固定用リングを
とりはずした時の膜モジユールセットの模式断面図を示
す。
1・・・・・円筒本体
2・・・・・閉鎖部材(鋳型枠)
3・・・・・固定用リング
4・・・・・中空糸膜
5・・・・・樹脂液挿入管
6・・・・・樹脂液貯め
才3図
X4−図 才り国
fglヨ
手続補正書
昭和63年8月 3日
l−、’1FIG. 1 shows a schematic cross-sectional view of a membrane module set immediately after resin fixation in the method of the present invention. FIG. 2 shows a schematic sectional view of the membrane module set with the resin liquid reservoir and fixing ring removed after the process shown in FIG. 1. 1... Cylindrical body 2... Closing member (mold flask) 3... Fixing ring 4... Hollow fiber membrane 5... Resin liquid insertion tube 6.・・・Resin liquid storage 3 diagram
Claims (1)
固定される端部が筒状体の閉鎖端側となるように中空糸
膜束を収納し、筒状体の開口端側に樹脂液貯めを配置し
、その一端が樹脂液貯めと連通された樹脂液挿入管をそ
の他端が筒状体の閉鎖端近傍に位置するように中空糸膜
束のほぼ中央部において筒状体と実質的に平行に延在さ
せた状態で、これらを遠心機内に設置し、遠心力作用下
において樹脂液貯めから樹脂液挿入管を介して樹脂液を
筒状体の閉鎖端部へ注入することにより中空糸膜束の端
部を樹脂固定する中空糸膜濾過モジュールの製造方法。A hollow fiber membrane bundle is housed inside a cylindrical body with one end closed and the other open, so that the end to be fixed with resin is on the closed end side of the cylindrical body, and the hollow fiber membrane bundle is placed on the open end side of the cylindrical body. A resin liquid reservoir is arranged in the hollow fiber membrane bundle, and a resin liquid insertion tube whose one end communicates with the resin liquid reservoir is inserted into the cylindrical body at approximately the center of the hollow fiber membrane bundle such that the other end is located near the closed end of the cylindrical body. These are placed in a centrifuge in a state in which they extend substantially parallel to the cylinder, and under the action of centrifugal force, resin liquid is injected from the resin liquid reservoir into the closed end of the cylindrical body through the resin liquid insertion tube. A method for manufacturing a hollow fiber membrane filtration module, in which an end portion of a hollow fiber membrane bundle is fixed with a resin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11189188A JPH01284305A (en) | 1988-05-09 | 1988-05-09 | Production of hollow fiber membrane filter module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11189188A JPH01284305A (en) | 1988-05-09 | 1988-05-09 | Production of hollow fiber membrane filter module |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01284305A true JPH01284305A (en) | 1989-11-15 |
Family
ID=14572733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11189188A Pending JPH01284305A (en) | 1988-05-09 | 1988-05-09 | Production of hollow fiber membrane filter module |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01284305A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03102232U (en) * | 1990-02-05 | 1991-10-24 | ||
JP2006281051A (en) * | 2005-03-31 | 2006-10-19 | Daicen Membrane Systems Ltd | Method of manufacturing hollow fiber membrane module |
JP2009112922A (en) * | 2007-11-05 | 2009-05-28 | Mitsubishi Rayon Eng Co Ltd | Method of manufacturing separation membrane module |
JP2013158695A (en) * | 2012-02-03 | 2013-08-19 | Mitsubishi Rayon Cleansui Co Ltd | Resin injection tool |
JP2016137468A (en) * | 2015-01-29 | 2016-08-04 | 三菱レイヨン株式会社 | Manufacturing method of hollow fiber membrane module |
-
1988
- 1988-05-09 JP JP11189188A patent/JPH01284305A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03102232U (en) * | 1990-02-05 | 1991-10-24 | ||
JP2006281051A (en) * | 2005-03-31 | 2006-10-19 | Daicen Membrane Systems Ltd | Method of manufacturing hollow fiber membrane module |
JP4699790B2 (en) * | 2005-03-31 | 2011-06-15 | ダイセン・メンブレン・システムズ株式会社 | Method for producing hollow fiber membrane module |
JP2009112922A (en) * | 2007-11-05 | 2009-05-28 | Mitsubishi Rayon Eng Co Ltd | Method of manufacturing separation membrane module |
JP2013158695A (en) * | 2012-02-03 | 2013-08-19 | Mitsubishi Rayon Cleansui Co Ltd | Resin injection tool |
JP2016137468A (en) * | 2015-01-29 | 2016-08-04 | 三菱レイヨン株式会社 | Manufacturing method of hollow fiber membrane module |
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