JPS6068006A - filtration device - Google Patents
filtration deviceInfo
- Publication number
- JPS6068006A JPS6068006A JP17681183A JP17681183A JPS6068006A JP S6068006 A JPS6068006 A JP S6068006A JP 17681183 A JP17681183 A JP 17681183A JP 17681183 A JP17681183 A JP 17681183A JP S6068006 A JPS6068006 A JP S6068006A
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- fiber bundle
- liquid
- fixing part
- lid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000001914 filtration Methods 0.000 title claims description 23
- 239000012510 hollow fiber Substances 0.000 claims description 98
- 239000007788 liquid Substances 0.000 claims description 54
- 239000000853 adhesive Substances 0.000 claims description 12
- 230000001070 adhesive effect Effects 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 10
- 238000012856 packing Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 60
- 239000000126 substance Substances 0.000 description 15
- 239000012528 membrane Substances 0.000 description 11
- 238000007789 sealing Methods 0.000 description 11
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- 230000007547 defect Effects 0.000 description 7
- 229920005989 resin Polymers 0.000 description 6
- 239000011347 resin Substances 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000008119 colloidal silica Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 229920002492 poly(sulfone) Polymers 0.000 description 5
- 239000008213 purified water Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 230000001954 sterilising effect Effects 0.000 description 5
- 238000004659 sterilization and disinfection Methods 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 4
- 239000004593 Epoxy Substances 0.000 description 4
- 238000011109 contamination Methods 0.000 description 4
- 229910021642 ultra pure water Inorganic materials 0.000 description 4
- 239000012498 ultrapure water Substances 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000012466 permeate Substances 0.000 description 3
- -1 polypropylene Polymers 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000011550 stock solution Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229920002239 polyacrylonitrile Polymers 0.000 description 2
- 229920000768 polyamine Polymers 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002510 pyrogen Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 1
- 241000282994 Cervidae Species 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000991587 Enterovirus C Species 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 229930182556 Polyacetal Natural products 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 229920006037 cross link polymer Polymers 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 229920006015 heat resistant resin Polymers 0.000 description 1
- 150000002460 imidazoles Chemical class 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene 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
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000008223 sterile water Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は中空糸を用いて外圧全濾過や外圧循環濾過(被
処理液を中空糸の外側に供給して中空糸の内側よシ処理
液を取シ出す)、あるいは内圧全濾過(被処理液を中空
糸の内側に供給して中空糸の外側より処理液を取り出す
)によシ被処理液から望ましくない成分を除去する装置
、よシ詳しくは中空糸が劣化したシ、目づまシしたシ、
破損した場合に容易に中空糸束だけを交換できるように
工夫された装置に関するものである。本発明は以下原水
から細菌などの望ましくない成分を除去する浄水の製造
装置について説明するが、果汁、タンパク、糖類の濃縮
、精製、回収または水溶液、有機液体の濾過あるいは工
場廃水の処理などにt使用することもできる。Detailed Description of the Invention The present invention uses hollow fibers to perform external pressure total filtration, external pressure circulation filtration (supplying the liquid to be treated to the outside of the hollow fibers and removing the treated liquid from the inside of the hollow fibers), or A device that removes undesirable components from the liquid to be treated using internal pressure total filtration (supplying the liquid to be treated inside the hollow fiber and taking out the treated liquid from the outside of the hollow fiber). Wow, I'm blind.
This invention relates to a device devised so that only the hollow fiber bundle can be easily replaced in the event of damage. The present invention will be described below as a water purification device for removing undesirable components such as bacteria from raw water. You can also use
従来より無菌水、パイロジエンフリー水の製造には蒸溜
法、膜沖過性などが用いられてきたが、蒸溜法は飛沫、
泡沫の同伴による汚染、加熱による装置材料の溶解によ
る汚染その能の原因によって、その精製度が低下すると
云う欠点があった。Traditionally, distillation methods and membrane permeability methods have been used to produce sterile water and pyrogen-free water, but distillation methods produce droplets,
There is a drawback that the degree of purification is reduced due to contamination due to entrainment of foam and contamination due to dissolution of equipment materials due to heating.
一方膜濾過性の場合、菌やパイロジエンを阻止する膜を
使えば理論的には菌、パイロジエンのいづれもが高度に
除去されるはずであるが、この場合もp液(処理液)が
菌やパイロジエンに汚染されることがある。特に長時間
にわたって濾過を行ったとき汚染されることが多く、そ
の原因として、(1)膜そのものに生じた欠陥、(2)
膜の接着部の不完全、(3)装置内の機械的シール、例
えば、0−リングのシール不完全などによシろ液への原
水の漏洩が考えられるが、これらの漏洩は一般に極めて
微細なものであるので、汚染の原因と経路をチェックす
ることは甚だむつかしい。しかし浄水の製造においては
加液中に細菌が1ケでも洩れ込むと直ちに繁殖して除菌
の目的を全く果せなくなるため原水のp液中への洩れは
厳に回避しなければならない。最近の分離膜の研究の急
速な進歩によシ中空糸の欠陥や中空糸の集束固定部の不
完全による原水の漏洩についてはほぼ完全に防止されつ
つあるが、装置内のシール部の不完全による原水(被処
理液)の洩れの問題は依然残されたままであった。特に
原水入口と原液出口が直線上となっているインフィン用
の装置は、設置し易い、コンパクトである、使い易い、
中空糸束の着脱が容易であるなどの優れた特長を有して
いるが、この装置はシール部材の欠陥によって原水がp
液側に洩れても外部からは全く洩れを検知することがで
きず、さらにp液の細菌検査で原水が沖液側に洩れてい
ることがわかってもその原因がシール部材によって生じ
た非シール性と、中空糸の欠陥によって生じた非シール
性との区別がつかないというのが現状であった。On the other hand, in the case of membrane filtration, if a membrane that blocks bacteria and pyrogienes is used, both bacteria and pyrogienes should theoretically be removed to a high degree, but in this case as well, the p liquid (processing liquid) May be contaminated with pyrogens. In particular, contamination often occurs when filtration is performed for a long period of time, and the causes of this are (1) defects in the membrane itself; (2)
Leakage of raw water into the filtrate may occur due to imperfections in the membrane adhesion, (3) mechanical seals within the device, such as imperfect seals on the O-ring, but these leaks are generally extremely minute. Therefore, it is extremely difficult to check the causes and routes of contamination. However, in the production of purified water, if even one bacteria leaks into the solution, it will immediately multiply and the purpose of sterilization will no longer be achieved, so leakage of raw water into the p-liquid must be strictly avoided. Recent rapid progress in research on separation membranes has almost completely prevented leakage of raw water due to defects in hollow fibers or imperfections in the focusing and fixing parts of hollow fibers; However, the problem of leakage of raw water (liquid to be treated) still remains. In particular, the equipment for Infin, in which the raw water inlet and raw solution outlet are in a straight line, is easy to install, compact, and easy to use.
Although this device has excellent features such as the ease of attaching and detaching the hollow fiber bundle, this device does not allow raw water to leak due to defects in the sealing member.
Even if it leaks to the liquid side, it cannot be detected from the outside at all, and furthermore, even if a bacterial test of the P liquid reveals that raw water is leaking to the offshore liquid side, the cause is a non-seal caused by the sealing member. At present, it is difficult to distinguish between sealability and non-sealability caused by defects in the hollow fibers.
本発明者らはシール部材の欠陥によって流出した漏出液
が沖液側に洩れるのを確実に防止するとトカでき、かつ
シール部材によって生じた非シール性を検知することの
できる濾過装置を提供するため鋭意検討した結果本発明
に到達したものである。すなわち本発明は下端が実質的
に封止され、上端が開口した多数の中空糸の上端を接着
剤で集束固定した中空糸束を、上端に開口を有する筐体
内に収容し、かつ該中空糸束の集束固定部または該集束
固定部に接続固定されたキャップ体を、相互間隔をおい
て配置された少くとも2つのパツキンを介して、底壁に
被処理液(原水)入口及び処理液(加液)出口と連通ず
る2つの開口を有する蓋体の一方の開口内に液密に挿入
し、さらに上記筐体を蓋体に液密に取着して、中空糸束
の集束固定部または該集束固定部に接続固定されたキャ
ップ体の挿入状態を保持するとともに、上記蓋体の側壁
に複数のパツキンの間に開口する洩出液出口を穿設した
ことを特徴とする濾過装置である。The present inventors have provided a filtration device that can reliably prevent leakage liquid caused by a defect in a sealing member from leaking to the offshore liquid side, and can detect non-sealing properties caused by the sealing member. The present invention was arrived at as a result of intensive study. That is, the present invention accommodates a bundle of hollow fibers in which the upper ends of a large number of hollow fibers whose lower ends are substantially sealed and whose upper ends are open are collected and fixed with an adhesive in a casing having an opening at the upper end; The convergence fixing part of the bundle or the cap body connected and fixed to the convergence fixing part is connected to the bottom wall through at least two gaskets arranged at a distance from each other, to the inlet of the liquid to be treated (raw water) and the inlet of the liquid to be treated (raw water). Liquid addition) The casing is liquid-tightly inserted into one opening of a lid body having two openings that communicate with the outlet, and the housing is liquid-tightly attached to the lid body to form a convergence fixing part for a hollow fiber bundle or The filtration device is characterized in that a cap body connected and fixed to the focusing fixing part is maintained in an inserted state, and a leakage liquid outlet opening between a plurality of gaskets is bored in a side wall of the lid body. .
本発明の新規な着想は原水入口とp液出口の両方を蓋体
に設けたことにある。かかる着想によシ、装置を実際の
ラインに取シ付ける際に]02シ付けが容易で、また中
空糸束を交換する際には筐体と中空糸束を同じ方向に着
脱するため、着脱時のスペークが僅かでよいうえ、中空
糸束の交換時にp液側が汚染され難いという優れた効果
を有している。The novel idea of the present invention is that both the raw water inlet and the p-liquid outlet are provided in the lid. Based on this idea, when installing the device on the actual line, it is easy to attach the 02, and when replacing the hollow fiber bundle, the housing and the hollow fiber bundle are attached and detached in the same direction, so it is easy to attach and detach. It has the excellent effect that the space required at the time is small and that the p-liquid side is not easily contaminated when the hollow fiber bundle is replaced.
特に原水入口と原液出口が一直線上(インライン型)に
なるよう構成するとよシ効果的である。本発明の飴の新
規な着想は中空糸束の集束固定部または該集束固定部に
接続固定されたキャップ体を相互に澗隔をおいて配置さ
れた少くとも2つのパツキンを介して蓋体の開口内に挿
入して、この挿入状態を保持するとともに蓋体の側壁に
複数のパツキン間に開口する洩出液出口を穿設したこと
にある。かかる着想によシパッキンの欠陥によって流出
した原水がp液側に洩れるのを確実に防止できるととも
に、パツキンの欠陥による原水の漏出を作業員が見える
ように装置外部に誘導することによシパッキンの欠陥を
外部から知ることができるのである。It is particularly effective to configure the raw water inlet and raw solution outlet to be in a straight line (in-line type). The novel concept of the candy of the present invention is that the convergence fixing part of the hollow fiber bundle or the cap body connected and fixed to the convergence fixing part are connected to the lid body through at least two gaskets arranged at a distance from each other. The lid body is inserted into the opening and maintained in this inserted state, and a leakage liquid outlet is bored in the side wall of the lid body between the plurality of gaskets. With this idea, it is possible to reliably prevent raw water that has leaked out due to a defect in the packing from leaking into the p-liquid side, and also to guide the leakage of raw water due to a defect in the packing to the outside of the equipment so that it can be seen by the operator. can be known from the outside.
次に本発明の濾過装置の一実施例を図面にて説明する。Next, one embodiment of the filtration device of the present invention will be described with reference to the drawings.
本発明装置には被処理液を中空糸の外側または内側に供
給する、いわゆる外圧式と内圧式があるが、以下すべて
外圧式の装置について説明する。第1図〜第9図に示す
ように本発明装置は上部が開口した円筒状筐体1と該筐
体1内に収容される中空糸束3及び筐体の上部開口に取
着される蓋体2で構成されている。また本発明装置では
中空糸束の集束固定部5または該集束固定部に接続固定
されたキャップ体4(通常先端が中空糸束の集束固定部
より小径の錐状体である)を蓋体2に設けた開口へ挿入
するが、該集束固定部またはキャップ体の開口への挿入
状態を保持する方法として、2つの方法、すなわち中空
糸束3の集束固定部5を支持する上部支持方式と中空糸
束3を自立性部材6で支え、かつ中空糸束の下端が封止
されるよう接着剤で固定した固定部5′を筐体の下部に
突出して設けた支持体36で支持する下部支持方式があ
る。上部支持方式の中空糸束としては例えば第10図に
示すように各中空粕′の上端が開口するよう接着剤で集
束同熱し、一方下端の開口より接着剤を封入して下端開
口を閉塞した中空糸束、第11図に示すように中空糸i
の下端をループ状に形成した中空糸束、この場合下端の
ループをリング状に配列すると中空糸束の内側に空洞が
でき沖過効率が向上する利点がある。第12図に示すよ
うに下端を封止した中空糸束をプラスチックや金属から
なる自立性の網状あるいは多孔状の筒体6内に収容した
中空糸束あるいは第15図に示すように下端を封止した
中空糸束をセラミックや樹脂製の1次p適用の多孔質保
護筒7内に収容した中空糸束などがある。一方下部支持
方式の中空糸束としては、第13図に示すように中空糸
束を自立性の網状あるいは多孔状の筒体6内に収容し、
中空糸束3の下端が接着剤中に埋没するように該第1−
.4J1つ
状体とともに接着固定貯喝玉コ帽吋執中空糸束の上端は
開口を有するように県東固定5した中空糸束あるいは第
14図に示すように自立性の中芯8のまわシに中空糸滌
交差状に巻回して下端を接着剤中に埋没固定弓し、上端
が開口するように上端を集束固定5した中空糸束などが
ある。The apparatuses of the present invention include so-called external pressure type and internal pressure type apparatuses that supply the liquid to be treated to the outside or inside of the hollow fibers, and below, all external pressure type apparatuses will be explained. As shown in FIGS. 1 to 9, the present invention comprises a cylindrical casing 1 with an open top, a hollow fiber bundle 3 housed in the casing 1, and a lid attached to the top opening of the casing. It is composed of 2 bodies. In addition, in the apparatus of the present invention, the convergence fixing part 5 of the hollow fiber bundle or the cap body 4 connected and fixed to the convergence fixing part (usually a cone-shaped body whose tip end is smaller in diameter than the convergence fixing part of the hollow fiber bundle) is attached to the lid body 2. There are two methods for maintaining the insertion state of the bundle fixing part or the cap body into the opening provided in the opening, namely, an upper support method that supports the bundle fixing part 5 of the hollow fiber bundle 3, and A lower support in which the yarn bundle 3 is supported by a self-supporting member 6, and a fixing part 5' fixed with adhesive so as to seal the lower end of the hollow fiber bundle is supported by a support 36 provided protruding from the lower part of the casing. There is a method. For example, as shown in Fig. 10, a top-support type hollow fiber bundle is made by condensing and heating each hollow fiber bundle with adhesive so that the top end of each hollow fiber is open, and then sealing the bottom opening with adhesive from the opening at the bottom end. Hollow fiber bundle, as shown in FIG.
A hollow fiber bundle whose lower end is formed into a loop shape, in this case, arranging the loops at the lower end in a ring shape creates a cavity inside the hollow fiber bundle, which has the advantage of improving overflow efficiency. As shown in FIG. 12, a hollow fiber bundle with its lower end sealed is housed in a self-supporting net-like or porous cylindrical body 6 made of plastic or metal, or as shown in FIG. 15, the lower end is sealed. There is a hollow fiber bundle in which the stopped hollow fiber bundle is housed in a porous protective tube 7 made of ceramic or resin and applied with primary p. On the other hand, as a hollow fiber bundle of the lower support type, as shown in FIG.
The first -
.. 4J A hollow fiber bundle is fixed with adhesive and a storage ball cap with a single-shaped body, and the upper end of the hollow fiber bundle has an opening. There is also a hollow fiber bundle in which the hollow fibers are wound in a crisscross pattern, the lower end is buried and fixed in an adhesive, and the upper end is bundled and fixed 5 so that the upper end is open.
さらに上記中空糸束は必要に応じて敷束固定部5に例え
ば円錐状のキャップ体4を接続固定することができる。Further, the hollow fiber bundle can be connected to, for example, a conical cap body 4 and fixed to the bundle fixing section 5 as required.
上記中空糸束5の集束固定部5あるいは該1束固定部に
接続固定されたキャップ体4の突出部9には第16図及
び第17図に示すように相互間隔をおいて複数の環状溝
10が形成されており、該環状溝に01Jングが装着さ
れる。上記環状溝10は通常2ケ形成されているが、シ
ールを確実にするため3ヶ以上形成してもよい。The convergence fixing part 5 of the hollow fiber bundle 5 or the protruding part 9 of the cap body 4 connected and fixed to the single bundle fixing part has a plurality of annular grooves spaced apart from each other as shown in FIGS. 16 and 17. 10 is formed, and an 01J ring is installed in the annular groove. Usually, two annular grooves 10 are formed, but three or more may be formed to ensure sealing.
第1図は中空糸束の1束固定部5に円錐状のキャップ体
4を接着固定した上部支持方式の中空糸束3を用いた装
置の例である。FIG. 1 shows an example of an apparatus using a hollow fiber bundle 3 of an upper support type in which a conical cap body 4 is adhesively fixed to a bundle fixing part 5 of the hollow fiber bundle.
上部に開口を有する円筒状筐体1は、その内部に中空糸
束の鹿束固定部5を支持する7フンジ11が設けられて
おシ、該フフンジには原水が通過する複数の孔12ある
いは切9欠きが穿設されている。上記筐体内に第10図
、第11図、第12図あるいは第15図に示す中空糸束
の集束固定部575;フフンジで支持されるよう収容さ
れている。A cylindrical casing 1 having an opening at the top is provided with seven flange 11 for supporting a deer bundle fixing part 5 of the hollow fiber bundle inside the cylindrical casing 1, and the flange 11 has a plurality of holes 12 through which raw water passes or Nine notches are bored. The hollow fiber bundle shown in FIG. 10, FIG. 11, FIG. 12, or FIG. 15 is accommodated in the housing so as to be supported by a convergence fixing part 575;
一方筐体1の開口に液密に装着される蓋体2は、その底
壁の中心に炉液出口15に連通する開口がまた該開口に
隣接して原水入口14に連通ずる開口が設けられている
。上記炉液出口13と原水人口14に連通ずる開口は蓋
体内で90°流路を変えて同一直線上に開口しておシ、
それぞれろ液導出管(図示せず)と原水導入管(図示せ
ず)に接続けてもよい。上記炉液出口13に連通する開
口に中空糸束の集束固定部5に接続固定された錐状キャ
ップ体4の突出部9が挿入され、該突出部と蓋体に設け
た開口の隙間は2つのOリング15によシシーμされて
いる。原水入口と炉液出口を逆にして用いれば内圧p過
として用いることができる。On the other hand, the lid body 2, which is attached to the opening of the housing 1 in a liquid-tight manner, has an opening in the center of its bottom wall that communicates with the furnace liquid outlet 15, and an opening that communicates with the raw water inlet 14 adjacent to the opening. ing. The openings communicating with the reactor liquid outlet 13 and the raw water intake 14 are opened on the same straight line with the flow paths changed by 90° within the lid body.
They may be connected to a filtrate outlet pipe (not shown) and a raw water inlet pipe (not shown), respectively. The protrusion 9 of the conical cap body 4 connected and fixed to the convergence fixing part 5 of the hollow fiber bundle is inserted into the opening communicating with the furnace liquid outlet 13, and the gap between the protrusion and the opening provided in the lid is 2. It is sealed by two O-rings 15. If the raw water inlet and reactor liquid outlet are reversed, it can be used as an internal pressure filter.
また蓋体2の外側には蓋体内に挿入されたキャップ体の
突出部9と蓋体2とをシールする2つのOリング15間
に開口する洩出液出口16が穿設されている。17は筐
体1と蓋体2をパツキン18を介して液密に連結するバ
ンドカップリングである。これらのパツキン18とOリ
ング15によって原水室19とp液室20は中空糸の壁
膜をへだてて液密構造となっている。すなわち原水は原
水導入管より中空糸の外側の原水室19に入り、中空糸
を透過する成分の一部は中空糸を透過して中空糸内側の
通路を通り沖液室20に集められキャップ体4を通って
加液導出管よシ取シ出される。Further, a leakage liquid outlet 16 is bored on the outside of the lid 2 and opens between two O-rings 15 that seal the lid 2 and the protrusion 9 of the cap inserted into the lid. A band coupling 17 liquid-tightly connects the housing 1 and the lid 2 via a gasket 18. These gaskets 18 and O-rings 15 make the raw water chamber 19 and the p-liquid chamber 20 have a liquid-tight structure by separating the wall membrane of the hollow fibers. That is, raw water enters the raw water chamber 19 outside the hollow fiber from the raw water introduction pipe, and a part of the components that permeate through the hollow fiber pass through the hollow fiber and pass through the passage inside the hollow fiber, and are collected in the offshore liquid chamber 20 and collected in the cap body. The liquid is taken out through the liquid supply outlet pipe 4.
一方中空糸を透過しない成分は筐体1の下部排出口21
より適宜取り出される。On the other hand, components that do not pass through the hollow fibers are removed from the lower discharge port 2 of the housing 1.
It is taken out as appropriate.
上記装置において原水がp液側に洩出する部位は蓋体2
の底壁に設けられた加液導出口13iC連通する開口と
、該開口内に挿入された中空糸束3の凛束固定部5に接
続固定されたキャップ体4の突出部9との隙間からであ
るが、該隙間は2つの0リング15で完全にシールされ
ている。しかし01Jングが破損してシール性を失った
場合加圧側の原水が蓋体に穿設した大気開放洩出液出口
16よシ装置の外部に流出するため原水がp液側へ洩れ
ることはない。また原水が洩出液出口よシ外部に流出す
るため作業員または適当な測定装置によシ洩れを検知す
ることができる。上記突出体と蓋体に設けた開口の隙間
をシールするパツキンは0リングの能に平パツキンなど
を用いることもできる。また平パツキンとOリングを併
用して用いてもよい。錐状キャップ体にパツキンを3ヶ
装着した場合にはそれぞれのパツキンの間に開口する洩
出液出口を蓋体の外側に設けることが好ましい。In the above device, the part where raw water leaks to the p liquid side is the lid 2.
From the gap between the opening communicating with the liquid supply outlet 13iC provided in the bottom wall of the opening and the protrusion 9 of the cap body 4 connected and fixed to the Rin bundle fixing part 5 of the hollow fiber bundle 3 inserted into the opening. However, the gap is completely sealed by two O-rings 15. However, if the 01J ring is damaged and the sealing performance is lost, the raw water on the pressurized side will flow out of the device through the atmospheric leakage liquid outlet 16 drilled in the lid, so the raw water will not leak to the P liquid side. . Furthermore, since the raw water flows out through the leakage outlet, leakage can be detected by an operator or by a suitable measuring device. As the gasket for sealing the gap between the protrusion and the opening provided in the lid, a flat gasket or the like may be used instead of an O-ring. Further, a flat packing and an O-ring may be used in combination. When three gaskets are attached to the conical cap, it is preferable to provide a leakage liquid outlet between the gaskets on the outside of the lid.
かかる複数の洩出液出口を設けること忙よシどのパツキ
ンがシール性を失ったかを検知することができる。浄水
の製造時かかる中空糸束が劣化したシ、目詰シしたとき
姉はまず筐体内の原水を排出口21よシ抜き取った後バ
ンドカップリング17を外して蓋体2と筐体1を分離し
て中空糸束3を筐体から取シ出し、その後新しい中空糸
束を筐体内に収容して該筐体を蓋体に取着することにょ
シ容易に中空糸束を取シ替ることができる。By providing such a plurality of leakage liquid outlets, it is possible to detect which gasket has lost its sealing properties. When the hollow fiber bundle used during the production of purified water deteriorates or becomes clogged, my sister first drains the raw water inside the housing through the outlet 21, then removes the band coupling 17 and separates the lid body 2 and the housing 1. The hollow fiber bundle 3 can be easily replaced by removing the hollow fiber bundle 3 from the housing, then storing a new hollow fiber bundle in the housing and attaching the housing to the lid. can.
上記装置は第1図に示すように蓋体が筐体の上部建配置
された状態で使用されるが、p過装置の取シ付は場所に
よシ到立させた状態で使用されることがある。この場合
には筐体内の原水の排出口を原水配管に設けることが好
ましい。The above device is used with the lid mounted on top of the housing as shown in Figure 1, but the P-pass device must be installed with the lid mounted on top of the housing. There is. In this case, it is preferable to provide an outlet for the raw water inside the housing in the raw water piping.
第2図は円錐状のキャップ体4を有する下部支持方式の
中空糸束5を収容した装置の例であシ、筐体1の下部に
突出して設けた支持体36上に、中空糸の下端を接着剤
中に埋没固定した固定部5′を絨aして、該筐体を蓋体
に取り付けたときにキャップ体4の突出部9が蓋体の底
壁に設けた炉液出口13に連通する開口に挿入され、か
つこの挿入状態が保持されるようになっている。FIG. 2 shows an example of an apparatus in which a hollow fiber bundle 5 of a lower support type having a conical cap body 4 is housed. When the fixing part 5', which is embedded and fixed in the adhesive, is attached to the lid body, the protruding part 9 of the cap body 4 will reach the furnace liquid outlet 13 provided on the bottom wall of the lid body. It is inserted into the communicating opening and maintained in this inserted state.
第3図は円錐状のキャップ体4を有する中空糸束5を筐
体1に接着固定して一体化した例であシ、筐体1の上部
には原水流入用の複数の開口22が設けられ、かつ該開
口の下部に蓋体に筐体を取シ付けるためのフランジ25
が設けられている。原水は蓋体に設けられた原水入口1
4より導入して筐体1の上部開口22よシ筐体内に入る
。この装置では中空糸が劣化したシ、目づまりした場合
には中空糸束を117春した筐体1ごと取シ替えること
ができる。FIG. 3 shows an example in which a hollow fiber bundle 5 having a conical cap body 4 is glued and fixed to the housing 1 and integrated, and the upper part of the housing 1 is provided with a plurality of openings 22 for inflowing raw water. and a flange 25 for attaching the housing to the lid at the bottom of the opening.
is provided. Raw water is supplied through raw water inlet 1 provided in the lid.
4 and enters the housing through the upper opening 22 of the housing 1. In this device, when the hollow fibers deteriorate or become clogged, the entire casing 1 containing the hollow fiber bundle can be replaced.
第4図は中空糸束6の集束固定部5の外側に設けた環状
溝10にOリング15を取り付けた上部支持方式の中空
糸束を収容した装置の例であシ、第5図は下部支持方式
の中空糸束を収容した装置の例である。第4図及び第5
図はそれぞれ第1図及び第2図の装置と同一場所に同一
符号をつけて説明を省略する。第6図〜第8図は筐体1
と中空糸束5′fc一体化した例であり、第6図は0リ
ング15を装着した中間リング24内に中空糸束3を収
束固定し、かつ該中間リングは筐体に接着固定されたリ
ング状板25と一体化されている。該リング状板には蓋
体2の底壁に設けた原水入口14と連通ずる開口に対応
する開口26が穿設されている。第7図は第3図に対応
する装置であ勺同−場所に同一符号を記して説明を省略
する。第8図は第6図に示す中空糸束3を収容する中間
リング24及びリング状板25を中空糸束の収束固定用
の接着剤で一体に形成した例である。中空糸束は筐体1
の上端に接続固定されておシ、該中空糸束の集束固定部
5は蓋体2に設けた開口に挿入される突出部27と筐体
の上端開口を閉止するリング状部28で形成され、該リ
ング状部には蓋体の底壁に設けた原水入口と連通ずる開
口に対応する位置に原人を筐体内に導入するため開口2
6が設けられている。第9図は中空糸束3の集束固定部
をナツト29により蓋体2に固定した例である。上記ナ
ツトの曲に種々のワンタッチ接続法を適用することがで
きる。FIG. 4 shows an example of an apparatus that accommodates a hollow fiber bundle of an upper support type in which an O-ring 15 is attached to an annular groove 10 provided on the outside of the bundle fixing part 5 of the hollow fiber bundle 6, and FIG. 5 shows a lower part of the hollow fiber bundle. This is an example of a device that accommodates a support-type hollow fiber bundle. Figures 4 and 5
In the figures, the same reference numerals are given to the same parts as in the apparatus of FIGS. 1 and 2, and the explanation thereof will be omitted. Figures 6 to 8 are for housing 1.
This is an example in which the hollow fiber bundle 5'fc and the hollow fiber bundle 5'fc are integrated, and FIG. 6 shows a case in which the hollow fiber bundle 3 is converged and fixed in the intermediate ring 24 equipped with the O ring 15, and the intermediate ring is adhesively fixed to the housing. It is integrated with the ring-shaped plate 25. The ring-shaped plate is provided with an opening 26 that corresponds to an opening that communicates with the raw water inlet 14 provided on the bottom wall of the lid 2. FIG. 7 shows a device corresponding to FIG. 3, and the same reference numerals are used in the same places, and the explanation thereof will be omitted. FIG. 8 shows an example in which the intermediate ring 24 accommodating the hollow fiber bundle 3 shown in FIG. 6 and the ring-shaped plate 25 are integrally formed with an adhesive for converging and fixing the hollow fiber bundle. Hollow fiber bundle is in housing 1
The convergence fixing part 5 of the hollow fiber bundle is formed by a protrusion 27 inserted into an opening provided in the lid body 2 and a ring-shaped part 28 that closes the upper end opening of the casing. , the ring-shaped part has an opening 2 for introducing the human into the housing at a position corresponding to the opening communicating with the raw water inlet provided on the bottom wall of the lid body.
6 is provided. FIG. 9 shows an example in which the bundle fixing portion of the hollow fiber bundle 3 is fixed to the lid body 2 with a nut 29. Various one-touch connection methods can be applied to the above Natsu songs.
本発明装置を浄水の製造に用いる場合、使用される中空
糸は80Å以上の物質を実質的に透過させない、いわゆ
る限外濾過オーダーの分画性を有する中空糸を用いるこ
とが好ましい。When the apparatus of the present invention is used to produce purified water, it is preferable that the hollow fibers used have a fractionation property on the order of so-called ultrafiltration, which does not substantially allow substances of 80 Å or more to pass through.
aoA以上の物質を実質的に透過させない中空糸とは平
均粒径が80人のコロイダルシリカの排除率Rを次の条
件で測定し、且が95%以上のものをいう。Hollow fibers that do not substantially allow substances of aoA or higher to permeate are those whose average particle diameter is 95% or more when the rejection rate R of colloidal silica of 80 people is measured under the following conditions.
排除率の測定方法
(1)中空糸束;中空糸長20α、外径基準の膜面積2
00dの中空糸束を作製し使用。Method for measuring rejection rate (1) Hollow fiber bundle; hollow fiber length 20α, membrane area based on outer diameter 2
A 00d hollow fiber bundle was prepared and used.
(11)測定液;平均粒径80人のコロイダルシリカ1
%液(日産化学工業株式会社製スノーテックス−S(コ
ロイダルシリカで最小粒径のもの)を蒸留水にて稀釈)
。(11) Measurement solution; colloidal silica 1 with average particle size of 80 people
% solution (Snowtex-S manufactured by Nissan Chemical Industries, Ltd. (colloidal silica with the smallest particle size) diluted with distilled water)
.
(II+)濾過条件;外圧全濾過方式、濾過圧0.5に
9膚、温度25°C0なお中空糸束は使用前によく水を
きり、かつ中空糸壁内もコロイダルシリカ液に置換後加
圧し、濾過を開始する。(II+) Filtration conditions: External pressure total filtration method, filtration pressure 0.5 to 9 degrees, temperature 25°C 0. Before use, the hollow fiber bundle should be thoroughly drained of water, and the inside of the hollow fiber wall should also be replaced with colloidal silica liquid. Press down and begin filtration.
動サンプリング;加圧直前の測定原液及び加圧後の′I
5iの初流よJ10cc毎に5回サンプリングする。得
られた6コのサンプルを100°CX16hr乾燥し、
固型分濃度を測定する。Dynamic sampling; measurement stock solution just before pressurization and 'I after pressurization
The first flow of 5i is sampled 5 times every 10cc. The six samples obtained were dried at 100°C for 16 hours.
Measure the solids concentration.
(v)排除率Rの算出;測定原液の固型分濃度CDと5
個の原液中で最も高い固型分濃度Cpmaxよシ次式に
より几をめる。(v) Calculation of exclusion rate R; solid content concentration CD of measurement stock solution and 5
Calculate the highest solid content concentration Cpmax in each stock solution using the following formula.
■= (1−CpmaxloD) X 100なお本測
定法の如く、コロイド液を用いると粒子以外の溶解物質
を含有している可能性があシ、几を重量法でめるため、
凡が97%と出ても、80人の粒子が6%透過している
ことを意味しておらず、Rが95%以上であれば80Å
以上の粒子は全く透過していないと考えてよい。■= (1-CpmaxloD)
Even if the average is 97%, it does not mean that 80 particles are transmitting 6%, and if R is 95% or more, it is 80 Å.
It can be considered that the above particles do not transmit at all.
またかかる中空糸は外面あるいは内面あるいは内外両面
に80Å以上の物質を実質的に透過させない活性層を有
するもの、あるいは膜の内部に100Å以上の物質を実
質的に通過させない微細構造を有するものならばいずれ
でもよい。このような80Å以上の物質f:実質的に透
過させない中空糸を用いることにより、原水中の88分
たとえば微生物やコロイド状物は完全に除去出来るとと
もに最も小さいウィルスといわれているポリオウィルス
やコロイド状物質の最小物である100人のコロイド状
シリカをも除去出来るため高度に精製された浄水を得る
ことが出来る。In addition, if such hollow fibers have an active layer on the outer surface, inner surface, or both of the inner and outer surfaces that substantially does not allow substances with a diameter of 80 Å or more to pass through, or have a fine structure inside the membrane that does not substantially allow substances with a diameter of 100 Å or more to pass through, Either is fine. Such substances f of 80 Å or more: By using hollow fibers that are virtually impermeable, for example, microorganisms and colloidal substances in raw water can be completely removed in 88 minutes, and poliovirus, which is said to be the smallest virus, and colloidal substances can be completely removed. Because it can remove even the smallest substance, colloidal silica, highly purified purified water can be obtained.
上記中空糸の素材としてはポリスルホン系、ポリアクリ
ロニトリル系、酢酸セルロースなどのセルロース系、ポ
リアミド系、ポリカーボネート系、ポリビニルアルコー
ル系など中空糸膜素材として通常知られている素材を使
用することが出来る力(、ポリスルホン系が耐熱性、お
よび耐酸性、耐アルカリ性、耐酸化性などの耐薬品性が
優れているので、酸化剤、酸、アルカリなどによって膜
を薬洗することにより再生しうるし、さらに加熱殺菌や
ホルマリン、塩素など薬剤による殺菌も可能であシ、殺
菌法を自由に選択しうるので好ましい。As the material for the hollow fibers, materials commonly known as hollow fiber membrane materials such as polysulfone, polyacrylonitrile, cellulose such as cellulose acetate, polyamide, polycarbonate, and polyvinyl alcohol can be used. The polysulfone type has excellent heat resistance and chemical resistance such as acid resistance, alkali resistance, and oxidation resistance, so it can be regenerated by cleaning the membrane with oxidizing agents, acids, alkalis, etc., and it can also be heat sterilized. It is also possible to sterilize with chemicals such as formalin, chlorine, etc., which is preferable because the sterilization method can be freely selected.
上記中空糸束の一端を集束固定する接着剤は従来よシ用
いられているポリウレタン系、シリコーン系、エポキシ
系などの接着剤を用いることができる。特に耐熱性と耐
薬品性を要求される用途に用いる場合には中空糸はもち
ろん、接着剤も耐熱性及び耐薬品性を有するものでなけ
ればならない。As the adhesive for converging and fixing one end of the hollow fiber bundle, conventionally used adhesives such as polyurethane, silicone, and epoxy can be used. In particular, when used in applications that require heat resistance and chemical resistance, not only the hollow fiber but also the adhesive must have heat resistance and chemical resistance.
かかる用途にはイミダゾール系硬化エポキシ樹脂を用い
ることが好ましい。この樹脂はエポキシ主剤、そのエポ
キシ当量に対して25〜70モルチのアミン当量を有す
るポリアミン系硬化剤、およびエポキシ主剤に対して0
.5〜10重量饅のイミダゾール系硬化剤よシなり、か
つポリアミン系硬化剤/イミダゾール系硬化剤の重量比
が10o15o〜100/1である液状エポキシ系配合
物を中空糸の端部の間隙に充填し、まず0〜50℃で固
化させ、次いで60〜150℃にてキユアリングして中
空糸の端部を集束固定することができる。For such uses, it is preferable to use imidazole-based cured epoxy resins. This resin consists of an epoxy base resin, a polyamine curing agent having an amine equivalent of 25 to 70 moles relative to the epoxy equivalent, and a
.. A liquid epoxy compound consisting of 5 to 10 parts by weight of an imidazole curing agent and having a polyamine curing agent/imidazole curing agent weight ratio of 10 to 15 to 100/1 is filled into the gap at the end of the hollow fiber. The ends of the hollow fibers can be fixed together by first solidifying at 0 to 50°C and then curing at 60 to 150°C.
上記中空糸束を収容する筐体及び蓋体はステンレス鋼な
どの耐触性を有する金属や樹脂が用いられるが、一般に
樹脂を用いることが多い。かかるイθノ脂としてはポリ
プロピレン、ポリ4弗化エチレン、ポリ弗化ビニリデン
、ポリアセタール、ポリカーボネート、ポリスルホン、
ポリ−4−メチルペンテン−1などの耐熱性を有する樹
脂が好ましい。中でもポリスルホンは耐熱性、曲げ弾性
率が高いため特に好ましい。50℃以下の温度で処理す
る装置しこおいては塩化ビニル、ポリスチレン、ポリア
クリロニトリルなどの非耐熱性樹脂を用いてもよい。The casing and lid that house the hollow fiber bundle are made of contact-resistant metal such as stainless steel or resin, and resin is generally used in many cases. Such Iθ fats include polypropylene, polytetrafluoroethylene, polyvinylidene fluoride, polyacetal, polycarbonate, polysulfone,
Resins having heat resistance such as poly-4-methylpentene-1 are preferred. Among them, polysulfone is particularly preferred because it has high heat resistance and high flexural modulus. In an apparatus for processing at a temperature of 50° C. or lower, non-heat resistant resins such as vinyl chloride, polystyrene, polyacrylonitrile, etc. may be used.
またシールに用いるパツキンは工業用ゴム、例えばシリ
コンゴムなどが用いられる。Further, the gasket used for the seal is made of industrial rubber, such as silicone rubber.
本発明装置において原水を外圧または内圧全濾過、ある
いは外圧循環濾過する場合に原水にかけるf過圧はo、
1kg/cA以上、好ましくは11.5 kg/cn
1以上である。上限の圧力は高い捏造過速度はよくなる
が、中空糸が破壊しない範囲にとどめるのはもちろんで
あり、通常5にり10I以下、好ましくは3ky/cA
以下である。初期よシ高圧で濾過するとケークが密に滞
積するので却って全r過量が低下するので好ましくない
ケースが多い。したがって初期は低圧で濾過し、目詰り
するとともに徐々に濾過圧力を上げていくことが好まし
い。水道水を濾過する場合には装置を水道に直結するこ
とによシ水道圧を利用しポンプなどは全く使用しなくと
も高度に精製された純水が簡便に得られきわめて経済的
である。In the device of the present invention, when raw water is subjected to external pressure or internal pressure total filtration, or external pressure circulation filtration, the overpressure f applied to the raw water is o,
1 kg/cA or more, preferably 11.5 kg/cn
It is 1 or more. The upper limit pressure is good for high fabrication overspeed, but it is of course necessary to keep it within a range that does not destroy the hollow fiber, and is usually 5 to 10 I or less, preferably 3 ky/cA.
It is as follows. If filtration is performed at high pressure initially, the cake will accumulate densely, which will actually reduce the total amount of filtrate, which is often undesirable. Therefore, it is preferable to initially filter at a low pressure and gradually increase the filtration pressure as the filter becomes clogged. When filtering tap water, by directly connecting the device to the water supply, highly purified pure water can be easily obtained by utilizing the water pressure without using any pumps, which is extremely economical.
浄水の製造において装置に供給される原水としては原水
中のケーク(aoX以上の中空糸の膜面に滞積される沢
滓)の性状が非圧縮性に近いものがよい。ここにいう非
圧縮性ケークとはケーク形状が濾過圧によシ圧縮された
際変化し難いものをいい、このよりなケークの場合には
ケーク層内を比較的容易に水が透過することが出来る。The raw water to be supplied to the apparatus in the production of purified water is preferably one in which the cake (slag accumulated on the membrane surface of a hollow fiber of aoX or higher) in the raw water is close to incompressible. The term "incompressible cake" here refers to a cake whose shape does not change easily when it is compressed by filtration pressure, and in the case of this rigid cake, water can permeate through the cake layer relatively easily. I can do it.
たとえハ鉄コロイド、シリカなどの無機物や活性炭、イ
オン交換樹脂片など架橋ポリマー片などが比較的非圧縮
性ケークといえる。−1微生物より分泌された多糖類あ
るいは一般に蛋白質変性物などは圧縮するとゲル状ケー
クとなシ、ケーク層は水を殆んど透過させないので好ま
しくない。両者が混合している場合でも非圧縮性ケーク
が支配的である場合では、本発明の濾過対象としうる。Even inorganic materials such as iron colloids and silica, activated carbon, crosslinked polymer pieces such as ion exchange resin pieces, etc. can be said to be relatively incompressible cakes. -1 Polysaccharides or generally denatured proteins secreted by microorganisms form gel-like cakes when compressed, and the cake layer hardly allows water to pass through, which is not preferable. Even when both are mixed, if the incompressible cake is predominant, it can be filtered by the present invention.
ケーク濃度があまり高いとケークの滞積が早いため濃縮
水の排出や逆洗や薬洗などを頻繁に実施する必要がある
ので、好ましくは0.1 q6以下がよい。このような
原水としては超純水、純水、水道水、河川水、工業用水
、海水などがあげられる。本発明装置を超純水製造プロ
セスにおけるチェックフィルターとして用いれば、極め
て精製度の高い超純水を得ることができる。If the cake concentration is too high, the cake accumulates quickly and requires frequent discharge of concentrated water, backwashing, chemical washing, etc., so it is preferably 0.1 q6 or less. Examples of such raw water include ultrapure water, pure water, tap water, river water, industrial water, and seawater. If the device of the present invention is used as a check filter in an ultrapure water production process, ultrapure water with extremely high purity can be obtained.
以上の如く本発明の濾過装置は被処理液室と処理液室の
間に被処理液室よシ低圧の貫通孔を設けることによシ被
処理液が処理液側に絶対に洩れ込まないよう工夫した装
置であり、特に厳密な濾過精度が要求されるウィルスや
パイロジエンなどの除菌用フィルターあるいは超純水ラ
イン用フィルターとして有用である。また被処理液入口
と処理液出口を蓋体に設けたためラインに簡単に取シ付
けられ、かつ中空糸束の取付け、取外しのだめのスペー
スが小さくてすむ。さらに中空糸及び筐体。As described above, the filtration device of the present invention prevents the liquid to be processed from leaking into the processing liquid side by providing a through hole with low pressure between the liquid to be processed chamber and the liquid to be processed chamber. This is a well-devised device that is particularly useful as a sterilization filter for viruses and pyrogens, which requires particularly strict filtration accuracy, or as a filter for ultrapure water lines. Further, since the inlet of the liquid to be treated and the outlet of the treated liquid are provided in the lid, it can be easily attached to the line, and the space for attaching and removing the hollow fiber bundle is small. Furthermore, hollow fibers and casings.
蓋体の素材に耐熱性のポリスルホンを用いると耐薬品性
、耐熱性に優れているので滅菌又は殺菌が容易に行う′
ことができるという優れた効果を有している。Using heat-resistant polysulfone as the material for the lid has excellent chemical and heat resistance, making sterilization or sterilization easy.
It has the excellent effect of being able to
第1図〜第9図は本発明装置の一実施例を示す装置の断
面図であシ、第10図〜第15図は本発明装置に用いる
中空糸束の説明図であシ、第16図〜第17図は中空糸
束のシール部構造の拡大断面図である。
1・・・・・・筐体 2・・・・・・蓋体3・・・・・
・中空糸束 4・・・・・・キャップ体5・・・・・・
集束固定部 10・・・・・・環状溝13・・・・・・
沢液出口 14・・・・・・原水入口15・・・・・・
0リング 16・・・・・・洩出液出口特許出願人 株
式会社 り ラ し
代理人 弁理士本多 堅
図面のJ”4”J (内19に変更なし)第 1 図
倍2 図
拵 3 口
第 4 閃
筋 5 圀
第6 図
第7 図
第9 図
第 10 図 第11 間
第 13 図 第 14 図
第12 閉
薯 15 i
第16 聞
第17 図
手云”・シ1−オ、]i正書(自発)
昭和費年10月258
1、弗件〜妻示
埒巖叱Sビー17Gε1;号
2、発明の名称
E?AY?
倉敷市酒津1621爵地
(108)株式会社り ラ し
代表取締役 上 野 他 −1 to 9 are cross-sectional views of an apparatus showing one embodiment of the apparatus of the present invention, FIGS. 10 to 15 are explanatory views of a hollow fiber bundle used in the apparatus of the present invention, and 16. 17 are enlarged sectional views of the sealing structure of the hollow fiber bundle. 1... Housing 2... Lid body 3...
・Hollow fiber bundle 4...Cap body 5...
Focusing fixing part 10... Annular groove 13...
Sawa liquid outlet 14... Raw water inlet 15...
0 ring 16...Leaking liquid outlet Patent applicant Rira Co., Ltd. Agent Patent attorney Ken Honda Drawing J"4"J (no changes to 19) No. 1 Drawing 2 Drawing 3 Figure 7 Figure 9 Figure 10 Figure 11 Figure 13 Figure 14 Figure 12 Closure 15 i 16th Figure 17 Figure 1 i-author (spontaneous) Showa expense October 258 1. Input ~ Tsumaji Iwako Sbee 17Gε1; No. 2, Name of the invention E?AY? Kurashiki City Sakazu 1621 Estate (108) Rira Shi Co., Ltd. Representative Director Ueno et al. −
Claims (1)
中空糸の上端を接着剤で集束固定した中空糸束を、上端
に開口を有する筐体内に収容し、かつ該中空糸束の集束
固定部または該集束固定部に接続固定されたキャップ体
を、相互間隔をおいて配置された少くとも2つのパツキ
ンを介して、底壁に被処理液入口及び処理液出口と連通
ずる2つの開口を有する蓋体の一方の開口内に液密に挿
入し、さらに上記筐体を蓋体に液密に取着して、中空糸
束の集束固定部または該集束固定部に接続固定されたキ
ャップ体の挿入状態を保持するとともK、上記蓋体の側
壁に複数のパツキンの間に開口する洩出液出口を穿設し
たことを特徴とする濾過装置、。 2、 パツキンが中空糸束の集束固定部または該集束固
定部に接続固定されたキャップ体の外側に設けられた少
くとも2つの環状溝に収容されたOリングである特許請
求の範囲@1項記載の濾過装置。 3、 被処理液入口及び処理液出口が蓋体の側壁に直線
上に設けられてなる特許請求の範囲第1項記載の濾過装
置。[Claims] 1. A bundle of hollow fibers whose lower ends are substantially sealed and whose upper ends are open, the upper ends of which are collected and fixed with an adhesive, is housed in a casing having an opening at the upper end; and the convergence fixing part of the hollow fiber bundle or the cap body connected and fixed to the convergence fixing part is connected to the bottom wall through at least two gaskets arranged at a distance from each other, to the inlet of the liquid to be treated and the process liquid. The casing is fluid-tightly inserted into one opening of a lid body having two openings communicating with the outlet, and the housing is fluid-tightly attached to the lid body to form a convergence fixing part for the hollow fiber bundle or the convergence fixation part. A filtration device, characterized in that a cap body connected and fixed to the cap body is maintained in an inserted state, and a leakage liquid outlet opening between a plurality of gaskets is bored in a side wall of the lid body. 2. The packing is an O-ring accommodated in at least two annular grooves provided on the outside of a convergence fixing part of the hollow fiber bundle or a cap body connected and fixed to the convergence fixing part. The filtration device described. 3. The filtration device according to claim 1, wherein the inlet for the liquid to be treated and the outlet for the treated liquid are provided in a straight line on the side wall of the lid.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17681183A JPS6068006A (en) | 1983-09-24 | 1983-09-24 | filtration device |
CA000447361A CA1221645A (en) | 1983-02-28 | 1984-02-14 | Filtration apparatus using hollow fiber-membrane |
US06/584,118 US4547289A (en) | 1983-02-28 | 1984-02-27 | Filtration apparatus using hollow fiber membrane |
GB08405025A GB2135902B (en) | 1983-02-28 | 1984-02-27 | Membrane fibre filtration apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17681183A JPS6068006A (en) | 1983-09-24 | 1983-09-24 | filtration device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6068006A true JPS6068006A (en) | 1985-04-18 |
JPS6352524B2 JPS6352524B2 (en) | 1988-10-19 |
Family
ID=16020250
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17681183A Granted JPS6068006A (en) | 1983-02-28 | 1983-09-24 | filtration device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6068006A (en) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS621410A (en) * | 1985-06-26 | 1987-01-07 | Kitazawa Valve:Kk | Precision filter device |
JPS63315106A (en) * | 1988-04-29 | 1988-12-22 | Kuraray Co Ltd | filtration equipment |
JPH01218605A (en) * | 1988-02-26 | 1989-08-31 | Asahi Chem Ind Co Ltd | Hollow fiber type filtration module |
JPH01293023A (en) * | 1988-05-20 | 1989-11-27 | Nec Corp | Paging system for exchange maintenance attendant |
JPH0245131U (en) * | 1988-09-19 | 1990-03-28 | ||
JPH02144129A (en) * | 1988-11-26 | 1990-06-01 | Akzo Nv | Hollow fiber module |
JPH03500141A (en) * | 1987-07-28 | 1991-01-17 | ミンテック コーポレーション | filter cartridge |
JPH06254595A (en) * | 1993-03-01 | 1994-09-13 | Daicel Chem Ind Ltd | Method for purifying surface flow water |
JPH07227297A (en) * | 1994-02-21 | 1995-08-29 | Nippon Millipore Kk | Method and apparatus for inspecting microorganisms using hollow fiber |
JP2001000842A (en) * | 1998-05-22 | 2001-01-09 | Daicel Chem Ind Ltd | Module for enriching pathogenic protozoa and enrichment method |
JP2003506073A (en) * | 1999-08-06 | 2003-02-18 | フルード テクノロジーズ パブリック リミテッド カンパニー | Microbial detection |
JP2003536057A (en) * | 2000-06-09 | 2003-12-02 | ビヨ・メリウー | How to use filtration means to prepare analytical samples from very large samples |
EP1530996A2 (en) * | 1996-11-21 | 2005-05-18 | Fresenius Medical Care Deutschland GmbH | Hollow fiber membrane separation device |
JP2006255673A (en) * | 2005-03-18 | 2006-09-28 | Kurita Water Ind Ltd | Membrane evaluation method in membrane separator |
JP4703849B2 (en) * | 1998-05-15 | 2011-06-15 | ミリポア・コーポレイション | Nucleic acid purification method and apparatus |
JP2018171553A (en) * | 2017-03-31 | 2018-11-08 | ダイセン・メンブレン・システムズ株式会社 | Water treatment method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57122293A (en) * | 1980-08-28 | 1982-07-30 | Akzo Nv | Apparatus for transmitting heat and/or material through hollow fiber |
-
1983
- 1983-09-24 JP JP17681183A patent/JPS6068006A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57122293A (en) * | 1980-08-28 | 1982-07-30 | Akzo Nv | Apparatus for transmitting heat and/or material through hollow fiber |
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS621410A (en) * | 1985-06-26 | 1987-01-07 | Kitazawa Valve:Kk | Precision filter device |
JPH03500141A (en) * | 1987-07-28 | 1991-01-17 | ミンテック コーポレーション | filter cartridge |
JPH0477605B2 (en) * | 1987-07-28 | 1992-12-08 | Mintetsuku Corp | |
JPH01218605A (en) * | 1988-02-26 | 1989-08-31 | Asahi Chem Ind Co Ltd | Hollow fiber type filtration module |
JPS63315106A (en) * | 1988-04-29 | 1988-12-22 | Kuraray Co Ltd | filtration equipment |
JPH0417695B2 (en) * | 1988-04-29 | 1992-03-26 | Kuraray Co | |
JPH01293023A (en) * | 1988-05-20 | 1989-11-27 | Nec Corp | Paging system for exchange maintenance attendant |
JPH0245131U (en) * | 1988-09-19 | 1990-03-28 | ||
JPH0538823Y2 (en) * | 1988-09-19 | 1993-09-30 | ||
JPH02144129A (en) * | 1988-11-26 | 1990-06-01 | Akzo Nv | Hollow fiber module |
JPH06254595A (en) * | 1993-03-01 | 1994-09-13 | Daicel Chem Ind Ltd | Method for purifying surface flow water |
JPH07227297A (en) * | 1994-02-21 | 1995-08-29 | Nippon Millipore Kk | Method and apparatus for inspecting microorganisms using hollow fiber |
EP1530996A2 (en) * | 1996-11-21 | 2005-05-18 | Fresenius Medical Care Deutschland GmbH | Hollow fiber membrane separation device |
EP1530996B1 (en) * | 1996-11-21 | 2013-08-07 | Fresenius Medical Care Deutschland GmbH | Hollow fiber membrane separation device |
JP4703849B2 (en) * | 1998-05-15 | 2011-06-15 | ミリポア・コーポレイション | Nucleic acid purification method and apparatus |
JP2001000842A (en) * | 1998-05-22 | 2001-01-09 | Daicel Chem Ind Ltd | Module for enriching pathogenic protozoa and enrichment method |
JP2003506073A (en) * | 1999-08-06 | 2003-02-18 | フルード テクノロジーズ パブリック リミテッド カンパニー | Microbial detection |
JP4772242B2 (en) * | 1999-08-06 | 2011-09-14 | ミリポア・コーポレイション | Microbial detection |
JP2003536057A (en) * | 2000-06-09 | 2003-12-02 | ビヨ・メリウー | How to use filtration means to prepare analytical samples from very large samples |
JP4792590B2 (en) * | 2000-06-09 | 2011-10-12 | ビヨ・メリウー | Use of filtration means to prepare analytical samples from very large amounts of samples |
JP2006255673A (en) * | 2005-03-18 | 2006-09-28 | Kurita Water Ind Ltd | Membrane evaluation method in membrane separator |
JP2018171553A (en) * | 2017-03-31 | 2018-11-08 | ダイセン・メンブレン・システムズ株式会社 | Water treatment method |
Also Published As
Publication number | Publication date |
---|---|
JPS6352524B2 (en) | 1988-10-19 |
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