JPH0438446B2 - - Google Patents
Info
- Publication number
- JPH0438446B2 JPH0438446B2 JP59100572A JP10057284A JPH0438446B2 JP H0438446 B2 JPH0438446 B2 JP H0438446B2 JP 59100572 A JP59100572 A JP 59100572A JP 10057284 A JP10057284 A JP 10057284A JP H0438446 B2 JPH0438446 B2 JP H0438446B2
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- fiber filtration
- filtrate
- membrane
- membranes
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000001914 filtration Methods 0.000 claims description 84
- 239000012510 hollow fiber Substances 0.000 claims description 77
- 239000012528 membrane Substances 0.000 claims description 56
- 239000000706 filtrate Substances 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 239000000463 material Substances 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 239000008235 industrial water Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000007788 liquid Substances 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
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
- 239000008223 sterile water Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920006337 unsaturated polyester resin Polymers 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】
［技術分野］
本発明は、浄水器用の中空糸濾過モジユールに
関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a hollow fiber filtration module for a water purifier.
［従来技術］
中空糸濾過膜は、優れた濾過機能を有している
ため、従来より高純度の工業用水、飲料水、医療
用の無菌水等を製造するための浄水器に使用され
てきた。[Prior art] Hollow fiber filtration membranes have an excellent filtration function and have traditionally been used in water purifiers to produce high-purity industrial water, drinking water, sterile water for medical use, etc. .
これら浄水器に使用される中空糸濾過膜を具備
する濾過モジユールの構造としては、従来殆どの
ものが、筒状体内に中空糸濾過膜をＵ字型のある
いは一端を封鎖した糸状の形でそれぞれの開口端
を開口状態を保つたままポリウレタン等からなる
固定部材に固定してなる構造を有するものであつ
た。 Conventionally, most of the structures of filtration modules equipped with hollow fiber filtration membranes used in water purifiers include hollow fiber filtration membranes in a cylindrical body in a U-shape or in the form of a thread with one end closed. It had a structure in which the opening end of the opening was fixed to a fixing member made of polyurethane or the like while keeping it open.
中空糸濾過モジユールを使用して、大量の用水
を工業的規模で処理するには、中空糸濾過膜の本
数を増加させるかあるいは中空糸濾過膜の長さを
長くすることで対処されてきた。 In order to treat large amounts of water on an industrial scale using hollow fiber filtration modules, measures have been taken by increasing the number of hollow fiber filtration membranes or by increasing the length of the hollow fiber filtration membranes.
しかしながら、単位面積当りの中空糸濾過膜の
本数を増加させると、ある程度迄は設置本数に比
例して処理用水量は増加するが、中空糸濾過膜の
設置密度が高くなり過ぎると、中空糸濾過膜の束
の中央部への処理用水の通過抵抗が大きくなるた
め、設置本数に比例して処理用水量は増加させる
ことはできなくなる。一方、中空糸濾過膜の長さ
を長くすると、膜面積が増加するため、処理用水
量を増加させることができるが、この場合にも中
空糸濾過膜の内径と濾過膜の性能との関係によ
り、ある長さ以上では、中空糸濾過膜内部の流路
抵抗が律速となり、処理用水量を増加させること
ができなかつた。 However, if the number of hollow fiber filtration membranes per unit area is increased, the amount of water to be treated increases in proportion to the number of installed hollow fiber filtration membranes, but if the installation density of hollow fiber filtration membranes becomes too high, hollow fiber filtration Since the resistance to passage of treatment water to the center of the membrane bundle increases, the amount of treatment water cannot be increased in proportion to the number of membranes installed. On the other hand, if the length of the hollow fiber filtration membrane is increased, the membrane area increases and the amount of water to be treated can be increased. If the length exceeds a certain length, the flow path resistance inside the hollow fiber filtration membrane becomes rate-determining, and the amount of water to be treated cannot be increased.
しかしながら、時によつては、大量の用水をで
きるだけコンパクトな中空糸濾過モジユールを用
いて処理することを要請されることがあり、この
ような場合には、従来知られていた構造の中空糸
濾過モジユールは使用できなかつた。 However, sometimes it is required to treat a large amount of water using a hollow fiber filtration module that is as compact as possible, and in such cases, a hollow fiber filtration module with a conventionally known structure is could not be used.
［発明の目的］
本発明の目的は、上述した問題点を解決する全
く新たな構造を有する、工業的浄水器に使用する
のに適した中空糸濾過モジユールを提供すること
にある。[Object of the Invention] An object of the present invention is to provide a hollow fiber filtration module suitable for use in industrial water purifiers, which has a completely new structure that solves the above-mentioned problems.
本発明の他の目的は、中空糸濾過膜全体を効率
よく利用し、その結果コンパクトな構成の中空糸
濾過モジユールを提供することにある。 Another object of the present invention is to provide a hollow fiber filtration module that efficiently utilizes the entire hollow fiber filtration membrane and has a compact configuration as a result.
［発明の構成］
すなわち、本発明の中空糸濾過モジユールは、
多数の中空糸濾過膜をほぼ直線状に配列し、その
両端の開口端を開口状態を保つたまま固定部材を
介して環状部材の内面に集束固定した濾過部材
に、該濾過部材の一方の開口端に濾液を収集する
濾液集合室が付設され、該濾液集合室内の濾液を
他方の開口端からの濾液と合流させるための濾液
配管および多数の中空糸濾過膜の外周にあつて二
つの環状部材を結合する支持部材が配設されて構
成される。[Configuration of the invention] That is, the hollow fiber filtration module of the present invention has the following features:
A large number of hollow fiber filtration membranes are arranged in a substantially straight line, and one opening of the filtration member is fixed to the inner surface of an annular member through a fixing member while keeping both open ends open. A filtrate collection chamber for collecting filtrate is attached at one end, filtrate piping for merging the filtrate in the filtrate collection chamber with the filtrate from the other open end, and two annular members located around the outer periphery of the large number of hollow fiber filtration membranes. A support member is provided to connect the two.
［発明を実施するための好適な態様］
以下、本発明の中空糸濾過モジユールにつき図
面を参照しつつより詳細に説明する。[PREFERRED EMBODIMENTS FOR CARRYING OUT THE INVENTION] Hereinafter, the hollow fiber filtration module of the present invention will be described in more detail with reference to the drawings.
第１図は、本発明の中空糸濾過モジユールの一
態様例を示す一部欠截平面図模式図である。 FIG. 1 is a partially cutaway schematic plan view showing an example of one embodiment of the hollow fiber filtration module of the present invention.
本発明の中空糸濾過モジユールは、基本的には
環状部材１、固定部材２および中空糸濾過膜３と
からなる濾過部材と、濾液集合室４を形成する仕
切り部材５と、濾液配管６と、支持部材７とから
構成される。これらに加え、所望により他の部材
が付設されてもよい。 The hollow fiber filtration module of the present invention basically includes a filtration member consisting of an annular member 1, a fixing member 2, and a hollow fiber filtration membrane 3, a partition member 5 forming a filtrate collection chamber 4, a filtrate pipe 6, It is composed of a support member 7. In addition to these, other members may be attached as desired.
環状部材１は、浄水器内に中空糸濾過モジユー
ルを設置するに際して該モジユール全体を支持す
るための支持部材として機能するものであり、基
本的にはリング状の形状を有するが、矩形等の断
面形状のものでもよく、またその外周面の形状に
関しては、浄水器中の該モジユールの設置態様等
に合わせて種々の形状をとり得る。もう一方の環
状部材１′は、濾液集合室４を形成するための支
持部材として機能する。これら環状部材１，１′
の内面には、それぞれ中空糸濾過膜３を固定し、
かつこれを濾過膜として機能させるために浄化す
べき水を浄化された水との仕切り部材として機能
する固定部材２が接合される、固定部材２には、
多数の中空糸濾過膜３がそれぞれの開口端を開口
状態を保つたままほぼ直線状に集束して固定され
ている。固定部材２は、ポリウレタン、エポキシ
樹脂、不飽和ポリエステル樹脂、シリコン樹脂等
を用いるのがよい。 The annular member 1 functions as a support member for supporting the entire hollow fiber filtration module when it is installed in a water purifier, and basically has a ring shape, but may have a cross section such as a rectangle. The shape of the outer circumferential surface thereof may take various shapes depending on the manner in which the module is installed in the water purifier. The other annular member 1' functions as a support member for forming the filtrate collection chamber 4. These annular members 1, 1'
A hollow fiber filtration membrane 3 is fixed on the inner surface of each of the
The fixing member 2 is joined to the fixing member 2, which functions as a partition member between water to be purified and purified water in order to function as a filtration membrane.
A large number of hollow fiber filtration membranes 3 are bundled and fixed in a substantially straight line with each open end kept open. The fixing member 2 is preferably made of polyurethane, epoxy resin, unsaturated polyester resin, silicone resin, or the like.
本発明の中空糸濾過モジユールは、このような
環状部材１，１′、固定部材２および中空糸濾過
膜３とからなる濾過部材の一方の環状部材１′に
仕切り部材５が固着され、この仕切り部材５によ
り濾液を収集する濾液集合室４が形成される。そ
して、濾液集合室４内に収集された濾液を送液
し、もう一方の中空糸濾過膜３の開口端からの濾
液と合流させるための濾液配管６が、二つの固定
部材２内のそれぞれのほぼ中央部を通過して配設
されている。濾液配管６は、二つの環状部材１，
１′を一体化固定して中空糸濾過モジユールを形
成する接合部材としても機能している。濾液配管
６は複数個設けてもよい。支持部材７は、中空糸
濾過膜３の保護と不必要な乱れを防ぎ、あるいは
バブリングによる機能回復処理を行なう際に、気
泡を中空糸濾過膜３に効率的に接触させる機能を
発揮させることができる。 In the hollow fiber filtration module of the present invention, a partition member 5 is fixed to one annular member 1' of a filtration member consisting of such annular members 1, 1', a fixing member 2, and a hollow fiber filtration membrane 3. The member 5 forms a filtrate collection chamber 4 for collecting filtrate. A filtrate pipe 6 is connected to each of the two fixing members 2 for sending the filtrate collected into the filtrate collection chamber 4 and joining it with the filtrate from the open end of the other hollow fiber filtration membrane 3. It is placed almost through the center. The filtrate pipe 6 includes two annular members 1,
It also functions as a joining member that integrates and fixes 1' to form a hollow fiber filtration module. A plurality of filtrate pipes 6 may be provided. The support member 7 has the function of protecting the hollow fiber filtration membrane 3 and preventing unnecessary turbulence, or bringing air bubbles into efficient contact with the hollow fiber filtration membrane 3 when performing a function recovery process by bubbling. can.
支持部材７は、通常第１図のように円筒形状を
有するものを好適に用いることができるが、その
他複数本の円柱等種々の態様をとることができ
る。 The support member 7 can preferably have a cylindrical shape as shown in FIG. 1, but can also take various other shapes such as a plurality of cylinders.
支持部材７は、二つの環状部材１，１′と完全
に一体化させてもよく、あるいは環状部材１，
１′の外周部にスリーブ等で点接触させて中空糸
濾過膜３の外周部に配設してもよい。また、第１
図のように支持部材７を環状部材１，１′と一体
化させた場合には、給水口８を設ける必要があ
る。 The support member 7 may be completely integrated with the two annular members 1, 1' or alternatively the annular members 1, 1'
It may also be arranged on the outer periphery of the hollow fiber filtration membrane 3 by making point contact with the outer periphery of the hollow fiber filtration membrane 3 using a sleeve or the like. Also, the first
When the support member 7 is integrated with the annular members 1 and 1' as shown in the figure, it is necessary to provide a water supply port 8.
このような構造を有する本発明の中空糸濾過モ
ジユールは、特に固定部材２中に濾液配管６を設
置することにより、濾過液の集水口は濾液集合室
４が設けられていない中空糸濾過膜３の開口端面
にモジユール当り一箇所でよく、多本数の中空糸
濾過モジユールを組込んだ中空糸濾過モジユール
ユニツトの中空糸濾過モジユールとの接続部を半
分にすることができる。更に、一般に中空糸濾過
膜の場合、中空糸濾過膜の内径と濾過膜の透過性
能との関係により、長さが長くなる程中空糸濾過
膜が本来有する透過性能を現出できなくなる。す
なわち、通常の平膜では、透過膜の面積が例えば
２倍になれば、同一の操作条件下では透過量も２
倍になる。しかしながら、中空糸濾過膜の場合に
は、その形態（内径）と透過性能との関係によつ
て異るが、例えば膜面積が２倍になつても透過量
は２倍にならず低下する。この低下する度合は、
長さが長くなる程大きくなる。第１図の例のよう
に直線状の中空糸濾過膜３の両端を開口状態とす
れば、同じ長さで一端が封止された中空糸濾過膜
を使用したものに比べると、中空糸濾過膜の圧損
に寄与する長さは半分になり、それだけ単位膜面
積当りの透過量を増加させることができる。 In the hollow fiber filtration module of the present invention having such a structure, in particular, by installing the filtrate piping 6 in the fixing member 2, the filtrate collection port is connected to the hollow fiber filtration membrane 3 where the filtrate collection chamber 4 is not provided. Only one connection per module is required on the open end surface of the hollow fiber filtration module, and the number of connections between the hollow fiber filtration module and the hollow fiber filtration module of a hollow fiber filtration module unit incorporating a large number of hollow fiber filtration modules can be halved. Furthermore, in general, in the case of hollow fiber filtration membranes, due to the relationship between the inner diameter of the hollow fiber filtration membrane and the permeation performance of the filtration membrane, the longer the length, the less the hollow fiber filtration membrane can exhibit its inherent permeation performance. In other words, with a normal flat membrane, if the area of the permeable membrane doubles, the amount of permeation will also double under the same operating conditions.
Double. However, in the case of hollow fiber filtration membranes, for example, even if the membrane area doubles, the amount of permeation does not double but decreases, although it depends on the relationship between its form (inner diameter) and permeation performance. The degree of this decrease is
The longer the length, the larger it becomes. If both ends of the linear hollow fiber filtration membrane 3 are open as in the example shown in Fig. 1, the hollow fiber filtration will be more effective than when using a hollow fiber filtration membrane of the same length with one end sealed. The length that contributes to the pressure drop of the membrane is halved, and the amount of permeation per unit membrane area can be increased accordingly.
更に、直線状に配列した中空糸濾過膜３に適度
の緩みを持たれば、濾過部の中空糸濾過膜３相互
に対し適度な間隔をあけることもでき、被処理液
が中空糸濾過モジユールの中央部に位置する中空
糸濾過膜３まで流れやすくなり、結果として中空
糸濾過モジユールを構成する中空糸濾過膜３全体
を均一かつ効率よく使用することができる。 Furthermore, if the hollow fiber filtration membranes 3 arranged in a straight line have an appropriate amount of slack, it is possible to leave an appropriate distance between the hollow fiber filtration membranes 3 in the filtration section, so that the liquid to be treated can flow through the hollow fiber filtration module. It becomes easier to flow to the hollow fiber filtration membrane 3 located in the center, and as a result, the entire hollow fiber filtration membrane 3 constituting the hollow fiber filtration module can be used uniformly and efficiently.
したがつて、このような構造を有する本発明の
中空糸濾過モジユールは、構成する中空糸濾過膜
全体を効率よく利用し、その結果としてモジユー
ルユニツトの設置面積が最小限度ですむコンパク
トな中空糸濾過モジユールを提供することができ
る。 Therefore, the hollow fiber filtration module of the present invention having such a structure efficiently utilizes the entire constituent hollow fiber filtration membrane, resulting in a compact hollow fiber whose installation area is minimized. A filtration module can be provided.
本発明の中空糸濾過モジユールを構成する部材
としての環状部材、濾液配管、並びに所望により
付設される支持部材、中空糸サポート部材等は、
機械的強度および耐久性を有するような材料であ
ればどのような材料でも使用できるが、使用後焼
却処理が必要な場合には、焼却により有害ガスを
出さずに完全燃焼させることのできる炭化水素系
の樹脂からなるものであることが好ましく、ポリ
カーボネート、ポリスチレン、ABS樹脂等が特
に好ましい。 The annular member, filtrate piping, supporting member, hollow fiber support member, etc. that are included as members constituting the hollow fiber filtration module of the present invention are as follows:
Any material can be used as long as it has mechanical strength and durability, but if it is necessary to incinerate it after use, hydrocarbons that can be completely combusted without emitting harmful gases should be used. The material is preferably made of a type of resin, and polycarbonate, polystyrene, ABS resin, etc. are particularly preferred.
本発明の中空糸濾過モジユールに於ける中空糸
濾過膜３としては、種々のものが使用でき、例え
ばセルローズ系、ポリオレフイン系、ポリスルホ
ン系、ポリビニルアルコール系、PMMA系等の
各種材料からなる中空糸濾過膜が使用できる。し
かし耐久性に優れ、かつ濾過性能に優れたものと
しては、ポリオレフイン系の多孔質中空糸膜が挙
げられる。その中でも、微細なコロイド状物を濾
過するのに好適であり、濾過膜の目詰まりに対す
る機能回復操作として通常用いられる逆洗時にか
かる外力に対して耐えられるような膜が特に好ま
しく用いられ、このような中空糸膜の例として
は、例えばポリエチレン中空糸膜（ポリエチレン
中空糸EHF、商品名、三菱レイヨン(株)製）が挙
げられる。 Various materials can be used as the hollow fiber filtration membrane 3 in the hollow fiber filtration module of the present invention, such as hollow fiber filtration membranes made of various materials such as cellulose, polyolefin, polysulfone, polyvinyl alcohol, and PMMA. Membrane can be used. However, polyolefin porous hollow fiber membranes have excellent durability and filtration performance. Among these, membranes that are suitable for filtering fine colloidal substances and that can withstand external forces applied during backwashing, which is usually used as a function recovery operation for clogging of filtration membranes, are particularly preferred. Examples of such hollow fiber membranes include polyethylene hollow fiber membranes (polyethylene hollow fiber EHF, trade name, manufactured by Mitsubishi Rayon Co., Ltd.).
［本発明の効果］
このように本発明の中空糸濾過モジユールによ
れば、構成する中空糸濾過膜の利用効率が高く、
モジユールユニツトの構造が簡単であり、組立て
加工が容易な中空糸濾過モジユールを提供するこ
とができ、その結果として中空糸濾過モジユール
ユニツトのコンパクトが図れ、その設置面積の節
減が可能となり、更に構造面、組立て加工面で経
済的な工業性の高い浄水器を提供することができ
る。[Effects of the present invention] As described above, according to the hollow fiber filtration module of the present invention, the utilization efficiency of the hollow fiber filtration membrane is high,
It is possible to provide a hollow fiber filtration module that has a simple structure and is easy to assemble, and as a result, the hollow fiber filtration module unit can be made compact and its installation area can be reduced. It is possible to provide a highly industrial water purifier that is economical in terms of structure and assembly.
第１図は、本発明の中空糸濾過モジユールの一
態様例を示す一部欠截平面図模式図である。
１，１′……環状部材、２……固定部材、３…
…中空糸濾過膜、４……濾液集合室、５……仕切
り部材、６……濾液配管、７……支持部材、８…
…給水口。
FIG. 1 is a partially cutaway schematic plan view showing an example of one embodiment of the hollow fiber filtration module of the present invention. 1, 1'...Annular member, 2...Fixing member, 3...
... hollow fiber filtration membrane, 4 ... filtrate collection chamber, 5 ... partition member, 6 ... filtrate piping, 7 ... support member, 8 ...
...Water supply port.
Claims (1)
その両端の開口端を開口状態を保つたまま固定部
材を介して環状部材の内面に集束固定した濾過部
材に、該濾過部材の一方の開口端に濾液を収集す
る濾液集合室が付設され、該濾液集合室内の濾液
を他方の開口端からの濾液と合流させるための濾
液配管および多数の中空糸濾過膜の外周にあつて
二つの環状部材を結合する支持部材が配設されて
なる中空糸濾過モジユール。1 A large number of hollow fiber filtration membranes are arranged almost linearly,
A filtrate collecting chamber for collecting filtrate is attached to one open end of the filtration member, which is focused and fixed to the inner surface of the annular member via a fixing member while keeping both open ends open. A hollow fiber filtration system comprising a filtrate pipe for merging the filtrate in the filtrate collection chamber with the filtrate from the other open end, and a support member for connecting two annular members around the outer periphery of a large number of hollow fiber filtration membranes. Module.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10057284A JPS60244306A (en) | 1984-05-21 | 1984-05-21 | Hollow yarn filter module |
| EP85106215A EP0162446B2 (en) | 1984-05-21 | 1985-05-21 | Hollow-fiber filter module |
| US90/002761A US4720342B1 (en) | 1984-05-21 | 1985-05-21 | Hollow-fiber filter module with filtrate conduit |
| DE8585106215T DE3560858D1 (en) | 1984-05-21 | 1985-05-21 | Hollow-fiber filter module |
| US90/002762A US4781832B1 (en) | 1984-05-21 | 1987-06-05 | Hollow-fiber filter module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10057284A JPS60244306A (en) | 1984-05-21 | 1984-05-21 | Hollow yarn filter module |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60244306A JPS60244306A (en) | 1985-12-04 |
| JPH0438446B2 true JPH0438446B2 (en) | 1992-06-24 |
Family
ID=14277615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10057284A Granted JPS60244306A (en) | 1984-05-21 | 1984-05-21 | Hollow yarn filter module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60244306A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0657142B2 (en) * | 1988-03-01 | 1994-08-03 | 宇部興産株式会社 | Module for cell concentration and separation |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60206405A (en) * | 1984-03-31 | 1985-10-18 | Nippon Atom Ind Group Co Ltd | Hollow yarn membrane filter apparatus |
-
1984
- 1984-05-21 JP JP10057284A patent/JPS60244306A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60206405A (en) * | 1984-03-31 | 1985-10-18 | Nippon Atom Ind Group Co Ltd | Hollow yarn membrane filter apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60244306A (en) | 1985-12-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0162446B2 (en) | Hollow-fiber filter module | |
| JP2000157845A (en) | Hollow fiber membrane cartridge and its fixing structure | |
| US4990248A (en) | Reverse osmosis apparatus | |
| US5126043A (en) | Radial and axial flow filter device | |
| US5458774A (en) | Corrugated spiral membrane module | |
| KR850002034A (en) | Water purifier and hollow fiber membrane filtration modulus for water purifier | |
| JP2001269546A (en) | Rack-type filter | |
| JPH0810417Y2 (en) | Water purifier | |
| JPH01151906A (en) | Production of hollow yarn membrane module cartridge | |
| AU614296B2 (en) | Reverse osmosis apparatus | |
| JPH0438446B2 (en) | ||
| JPH0233867Y2 (en) | ||
| JPS60244305A (en) | Hollow yarn filter module | |
| JPH1057775A (en) | Hollow-fiber membrane module and hollow-fiber membrane module unit using the module | |
| JPH0470929B2 (en) | ||
| JPH0125613Y2 (en) | ||
| JPS6326164Y2 (en) | ||
| JPS60225612A (en) | Hollow yarn filter module | |
| JPS5832800Y2 (en) | Cylindrical hollow fiber module | |
| JPH10337449A (en) | Constricted filter element and hollow fiber membrane module | |
| JP3200190B2 (en) | Hollow fiber membrane module | |
| JP2607545Y2 (en) | Hollow fiber membrane module | |
| JPH0213068Y2 (en) | ||
| JP2620254B2 (en) | Hollow fiber membrane filtration module | |
| JPH02253831A (en) | Hollow yarn filtration module |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |