JPH08281078A - Floating hollow-fiber membrane module - Google Patents

Floating hollow-fiber membrane module

Info

Publication number
JPH08281078A
JPH08281078A JP11637795A JP11637795A JPH08281078A JP H08281078 A JPH08281078 A JP H08281078A JP 11637795 A JP11637795 A JP 11637795A JP 11637795 A JP11637795 A JP 11637795A JP H08281078 A JPH08281078 A JP H08281078A
Authority
JP
Japan
Prior art keywords
hollow fiber
fiber membrane
float
membrane module
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP11637795A
Other languages
Japanese (ja)
Other versions
JP3417139B2 (en
Inventor
Shinichi Yoshikawa
慎一 吉川
Naoki Okuma
直紀 大熊
Masato Onishi
真人 大西
Yutaka Okuno
裕 奥野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP11637795A priority Critical patent/JP3417139B2/en
Publication of JPH08281078A publication Critical patent/JPH08281078A/en
Application granted granted Critical
Publication of JP3417139B2 publication Critical patent/JP3417139B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE: To obtain a hollow-fiber membrane module with the sludge between the membranes of the module easily discharged. CONSTITUTION: Both ends of a hollow-fiber membrane 1 are supported at the two upper and lower parts or at one part. The filtered and cleaned water is collected from the supporting part in this hollow-fiber membrane module. The module consists of a water collecting part 2 formed at the lower supporting part of the membrane and a float 5 connected to the upper part 3 of the membrane 1 or to the membrane. A means for supplying or discharging air into or from the float is furnished.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は中空糸膜モジュールに係
わり、特に、中空糸膜モジュールを水中に浸漬して濾過
をなすのに好適であって大型の処理槽に用いるのに適し
た浮遊型中空糸膜モジュールに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hollow fiber membrane module, and more particularly to a floating type which is suitable for immersing a hollow fiber membrane module in water for filtration and is suitable for use in a large treatment tank. The present invention relates to a hollow fiber membrane module.

【0002】[0002]

【従来の技術】最近、水などの濾過に中空糸膜を使用し
た濾過器が多数用いられている。また、工業用水の濾過
に中空糸膜を何千〜何万本をひと束に束ねた後に端部を
接着材で固定して用いられている。この中空糸膜を何千
〜何万本をひと束に束ねたものは中空糸膜モジュールと
称されている。この中空糸膜モジュールは使い捨てか、
あるいは、汚れが一定量以上付着した段階において、清
浄水または薬液水による清浄やフラッシング処理を実施
するのが普通である。また、特開平5−220355号
公報に開示するように、微粒子や汚泥物質を含んだ液体
を加温した後に、中空糸膜モジュールで濾過することに
より、中空糸膜モジュールを長時間使用できるようにす
ることが提案されている。また、このような中空糸膜モ
ジュールを大容量の処理槽に使用する場合には、ハウジ
ング、その他の支持物によって中空糸膜の張りを一定に
保つ構成となっている。
2. Description of the Related Art Recently, many filters using hollow fiber membranes have been used for filtering water and the like. Further, it is used for filtering industrial water by bundling thousands to tens of thousands of hollow fiber membranes in a bundle and fixing the ends with an adhesive. A bundle of thousands to tens of thousands of hollow fiber membranes is called a hollow fiber membrane module. Is this hollow fiber membrane module disposable?
Alternatively, when a certain amount or more of dirt adheres, cleaning with clean water or chemical water or flushing treatment is usually performed. Further, as disclosed in JP-A-5-220355, a hollow fiber membrane module can be used for a long time by heating a liquid containing fine particles and a sludge substance and then filtering with a hollow fiber membrane module. It is suggested to do so. Further, when such a hollow fiber membrane module is used in a large-capacity treatment tank, the hollow fiber membrane tension is kept constant by a housing and other supports.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記従
来の構成によれば、清浄水または薬液水による清浄やフ
ラッシング処理を実施する場合には、清浄水または薬液
水を準備する必要があるとともに、使用した薬液水を処
理する必要があり工数、費用がかかる。また、加温した
液体を用いる場合には、専用の設備と処理をする必要が
あり、前記と同様に、工数、費用がかかる。また、中空
糸膜の張りを一定に保つ大容量の処理槽が大きい場合に
は、多数の中空糸膜の同士の間隔が狭く配置されている
とともに、張りが一定に保たれているために互いの間隔
が広がることがなく、濾過によって膜面に付着した汚泥
物質を中空糸膜間から排出することは困難である。さら
に、中空糸膜モジュールを水中に浸漬して使用している
場合は、中空糸膜の張りが一定に保たれているため水位
の変化に対応できないので水位の低下により中空糸膜が
水面上に露出する。このため、水位の人為的制御が不可
能な環境水中には浸漬して使用できないという問題があ
る。
However, according to the above-mentioned conventional configuration, when performing cleaning or flushing treatment with clean water or chemical liquid water, it is necessary to prepare clean water or chemical liquid water and to use it. It is necessary to treat the chemical liquid water, which requires man-hours and costs. Further, when a heated liquid is used, it is necessary to carry out special equipment and treatment, which requires man-hours and cost as in the above case. In addition, when a large-capacity treatment tank that keeps the tension of the hollow fiber membranes constant is large, a large number of hollow fiber membranes are arranged close to each other and the tension is kept constant. It is difficult to discharge the sludge substance adhering to the membrane surface from the space between the hollow fiber membranes by filtration without expanding the space between the membranes. Furthermore, when the hollow fiber membrane module is immersed in water and used, the tension of the hollow fiber membrane is kept constant, so it is not possible to respond to changes in the water level. Exposed. Therefore, there is a problem that it cannot be used by immersing it in environmental water where the water level cannot be artificially controlled.

【0004】本発明は上記従来の問題点に着目し、中空
糸膜束の膜面に付着し、糸膜間への挟雑物を簡単に排出
して濾過性能の低下を防止できる浮游型中空糸膜モジュ
ールを提供することを目的とする。また、中空糸膜モジ
ュールを水中に浸漬する大型の処理槽においても、中空
糸膜の張り、弛みの変化に対応して中空糸膜間の汚泥物
質が排出可能とするとともに、浸漬して使用した場合に
水位の変動に追従できる浮遊型中空糸膜モジュールの提
供を目的としている。
Focusing on the above-mentioned conventional problems, the present invention is a floating type hollow that can adhere to the membrane surface of a hollow fiber membrane bundle and easily discharge foreign matter between the membranes to prevent deterioration of filtration performance. An object is to provide a thread film module. Further, even in a large-sized treatment tank in which the hollow fiber membrane module is immersed in water, sludge substances between the hollow fiber membranes can be discharged in response to changes in the tension and looseness of the hollow fiber membrane, and the hollow fiber membrane was immersed and used. In this case, it is an object of the present invention to provide a floating hollow fiber membrane module that can follow fluctuations in water level.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、本発明の浮遊型中空糸膜モジュールは、中空糸膜を
束ねて構成される中空糸膜束の下端に濾過水の集水部を
設けるとともに、上端の支持部に浮子を連結した構成と
した。また、前記浮子に空気を給排する空気給排手段を
接続し、浮子の浮力調整による中空糸膜束の張りの調整
を可能とすることができる。
In order to achieve the above-mentioned object, a floating hollow fiber membrane module of the present invention comprises a hollow fiber membrane bundle formed by bundling hollow fiber membranes, and a filtered water collecting portion at the lower end of the bundle. And a float is connected to the support portion at the upper end. Further, an air supply / exhaust means for supplying / exhausting air to / from the float can be connected to enable adjustment of the tension of the hollow fiber membrane bundle by adjusting the buoyancy of the float.

【0006】[0006]

【作用】上記構成によれば、中空糸膜束の下方支持部に
集水部を設け、中空糸膜の上方支持部もしくは中空糸膜
に連結された浮子を設けているので、水位の上下動によ
りモジュール長が変化し、水位の変動に追従できるの
で、中空糸膜モジュールが空気中に露出することなく、
しかも、中空糸膜の張りが変化し中空糸膜間隔が広がる
ことにより膜間に介在している汚泥の排出が容易に行え
る。また、水位の変動がない場合でも浮子を上下動させ
ることにより、中空糸膜の張り、弛みを交互に与えるこ
とができ、中空糸膜間隔の汚泥の排出が行える。
According to the above construction, the water collecting portion is provided in the lower supporting portion of the hollow fiber membrane bundle, and the floating portion connected to the upper supporting portion of the hollow fiber membrane or the hollow fiber membrane is provided. By changing the module length, it is possible to follow the fluctuation of the water level, so the hollow fiber membrane module is not exposed to the air,
Moreover, since the tension of the hollow fiber membranes changes and the hollow fiber membrane spacing increases, the sludge interposed between the membranes can be easily discharged. Further, even if the water level does not change, the hollow fiber membrane can be tensioned and loosened alternately by moving the float up and down, and sludge can be discharged at intervals between the hollow fiber membranes.

【0007】[0007]

【実施例】以下に、本発明に係る浮遊型中空糸膜モジュ
ールの具体的実施例につき、図面を参照して詳細に説明
する。図1は本発明の浮遊型中空糸膜モジュールの第1
実施例の全体構成図を示す。図1において、中空糸膜1
は、一端部が集水部2に、他端が支持体3に固定されて
いる。支持体3は連結体4を介して浮子5に連結されて
いる。集水部2には、浄化された清浄水を集水する集水
配管6が付設されている。また、集水部2には、エアス
クラビング洗浄のための散気部を設けても良い。連結体
4は紐状、チェーンあるいは棒状により構成される。上
記構成において、集水部2、支持体3、および連結体4
は水中に沈み、浮子5は支持体3および連結体4を浮遊
させる浮力を有している。
EXAMPLES Hereinafter, specific examples of the floating hollow fiber membrane module according to the present invention will be described in detail with reference to the drawings. FIG. 1 shows the first embodiment of the floating hollow fiber membrane module of the present invention.
The whole block diagram of an Example is shown. In FIG. 1, the hollow fiber membrane 1
Has one end fixed to the water collecting part 2 and the other end fixed to the support 3. The support body 3 is connected to the float 5 via the connection body 4. The water collecting section 2 is provided with a water collecting pipe 6 for collecting purified water. Further, the water collecting section 2 may be provided with an air diffusing section for air scrubbing cleaning. The connecting body 4 is formed in a string shape, a chain or a bar shape. In the above structure, the water collecting portion 2, the support body 3, and the connection body 4
Is submerged in water, and the float 5 has a buoyancy force for floating the support 3 and the connecting body 4.

【0008】上記構成において、次に作動について説明
する。浮遊型中空糸膜モジュールが水中に浸漬されて使
用されることにより、水位変動にともなって浮子5が上
下動する。図1に示すように、水位が高い場合には、浮
子5によって中空糸膜1は張られた状態になり中空糸膜
の間隔(S)は狭くなり、水流あるいはエアスクラビン
グによって中空糸膜同士が容易に擦れ合い、膜面に付着
した汚泥の剥離を行う。図2に示すように、水位が低い
場合には、浮子5が下がり、中空糸膜1は弛んだ状態に
なり中空糸膜の間隔は広くなり、剥離後の中空糸膜間に
捕らえられている汚泥の排出が容易に行われる。また、
浮子5が上下動することにより、中空糸膜1が張った
り、緩んだりする息継ぎが行われて汚泥の排出が促進さ
れる。
Next, the operation of the above structure will be described. When the floating type hollow fiber membrane module is immersed in water for use, the float 5 moves up and down along with the fluctuation of the water level. As shown in FIG. 1, when the water level is high, the hollow fiber membranes 1 are stretched by the floats 5, the space (S) between the hollow fiber membranes is narrowed, and the hollow fiber membranes are separated from each other by water flow or air scrubbing. Easily rub against each other to remove sludge attached to the membrane surface. As shown in FIG. 2, when the water level is low, the floats 5 are lowered, the hollow fiber membranes 1 are in a slackened state, the intervals between the hollow fiber membranes are widened, and the hollow fiber membranes are trapped between the peeled hollow fiber membranes. Sludge is easily discharged. Also,
When the float 5 moves up and down, the hollow fiber membrane 1 is stretched or loosened to promote breathing, thereby promoting sludge discharge.

【0009】本発明の浮遊型中空糸膜モジュールを環境
水中に浸漬して使用し、造水施設の取水口として用いた
場合には取水時に前処理が行われ、水位の自然な変動に
より中空糸膜間に捕らえられている汚泥の排出が行われ
る。特に、海水淡水化施設の取水口として用いた場合に
は潮の干満により1日に2度大きく水位が変動するた
め、エネルギーを投入することなく汚泥の定期的な排出
が行われる。また、原水槽に浸漬した場合は機械的作用
を中空糸膜モジュールに与えることなく既存の原水ポン
プにより原水槽の水位を変えることによって、汚泥の排
出が行われる。
When the floating type hollow fiber membrane module of the present invention is used by being immersed in environmental water and used as an intake port of a fresh water facility, pretreatment is carried out at the time of intake of water, and the hollow fiber is caused by natural fluctuation of water level. The sludge trapped between the membranes is discharged. In particular, when it is used as an intake of a seawater desalination facility, the water level changes twice a day due to the ebb and flow of the tide, so sludge is regularly discharged without inputting energy. When immersed in a raw water tank, sludge is discharged by changing the water level in the raw water tank by an existing raw water pump without giving a mechanical action to the hollow fiber membrane module.

【0010】次に、図3は本発明の浮遊型中空糸膜モジ
ュールの第2実施例の全体構成図を示す。中空糸膜1
は、折り返して両端部が集水部2に固定されている。ま
た、中空糸膜1の折り返し位置には、複数もしくは単一
の支持体11を配設し、この支持体11には、1本ある
いは複数本つづ纏めて中空糸膜1を通して支持してい
る。支持体11の形状には、リング状、板状、あるい
は、櫛の形を用いている。複数もしくは単一の支持体1
1はそれぞれに連結体4が接続され、連結体4は浮子5
に連結されている。
Next, FIG. 3 shows the overall construction of the second embodiment of the floating hollow fiber membrane module of the present invention. Hollow fiber membrane 1
Is folded back and both ends are fixed to the water collecting part 2. A plurality of or a single support 11 is arranged at the folded position of the hollow fiber membrane 1, and one or a plurality of support bodies 11 are collectively supported by the support 11 through the hollow fiber membrane 1. The support 11 has a ring shape, a plate shape, or a comb shape. Multiple or single support 1
1 is connected to the connecting body 4, and the connecting body 4 is a float 5
It is connected to.

【0011】上記構成において、次に作動について説明
するが、浮子5にそれぞれの連結体4が接続されている
ため、水位変動にともなって浮子5が上下動したときの
自由度が増し、中空糸膜1が張ったり、緩んだりする息
継ぎが多く行われて汚泥の排出が増す。作用については
第1実施例と同様なため詳細の説明は省略する。
In the above structure, the operation will be described next. Since the respective connecting members 4 are connected to the float 5, the degree of freedom when the float 5 moves up and down due to the fluctuation of the water level increases, and the hollow fiber The membrane 1 is often stretched and loosened to increase sludge discharge. The operation is similar to that of the first embodiment, and thus detailed description will be omitted.

【0012】次に、図4は本発明の浮遊型中空糸膜モジ
ュールの第3実施例の全体構成図を示す。図4におい
て、浮子12には、撓み自在のチューブ13が接続さ
れ、チューブ13は電磁弁14を介してエアポンプ15
に接続されている。浮子12は伸縮自在な材料により構
成され、エアポンプ15からの空気量の変化により浮力
を変える。例えば、電磁弁14は2位置3ポートにより
構成され、第1ポートはエアポンプ15に、第2ポート
は浮子12に、および第3ポートは大気中に解放するよ
うに接続されている。また、1位置(A)ではエアポン
プ15からの空気を浮子12に、また、他の1位置
(B)では浮子12の空気を大気中に放出する構成とし
ている。
Next, FIG. 4 shows an overall configuration diagram of a third embodiment of the floating hollow fiber membrane module of the present invention. In FIG. 4, a flexible tube 13 is connected to the float 12, and the tube 13 is connected to an air pump 15 via a solenoid valve 14.
It is connected to the. The float 12 is made of a stretchable material, and changes its buoyancy by changing the amount of air from the air pump 15. For example, the solenoid valve 14 is constituted by a two-position three-port, the first port is connected to the air pump 15, the second port is connected to the float 12, and the third port is connected to the atmosphere. Further, the air from the air pump 15 is discharged to the float 12 at one position (A), and the air from the float 12 is discharged to the atmosphere at the other position (B).

【0013】上記構成において、次に作動について説明
する。エアポンプ15は、空気を電磁弁14、チューブ
13を介して浮子12に送る。浮子12は空気を受けて
膨らみ、浮子12の浮力が大きくなる。これに伴い、浮
子12は上昇し、連結体4を介して支持体3を引っ張り
上げて中空糸膜1は張られた状態となる。次に、電磁弁
14は1位置(A)より他の1位置(B)に切換えられ
る。これにより、浮子12の空気は電磁弁14を介して
大気中に放出され、浮子12は縮む。このため、浮子1
2の浮力が小さくなる。これに伴い、浮子12が沈むと
ともに、連結体4を介して支持体3も沈み、中空糸膜1
は弛んだ状態となる。このように、水位変動がない場所
に使用する場合でも、エアポンプ15および電磁弁14
を操作することにより、中空糸膜1の膜間隔を変化さ
せ、中空糸膜間に捕らえられている汚泥の排出が容易に
行われる。
Next, the operation of the above structure will be described. The air pump 15 sends air to the float 12 via the solenoid valve 14 and the tube 13. The float 12 receives air and swells, and the buoyancy of the float 12 increases. Along with this, the float 12 rises, the support 3 is pulled up via the connecting body 4, and the hollow fiber membrane 1 is in a tensioned state. Next, the solenoid valve 14 is switched from one position (A) to another one position (B). As a result, the air in the float 12 is released into the atmosphere via the solenoid valve 14, and the float 12 contracts. Therefore, the float 1
The buoyancy of 2 becomes small. Along with this, the float 12 sinks, and the support 3 also sinks via the connecting body 4, and the hollow fiber membrane 1
Becomes loose. As described above, even when the air pump 15 and the solenoid valve 14 are used in a place where the water level does not fluctuate.
By operating, the membrane spacing of the hollow fiber membranes 1 is changed, and the sludge trapped between the hollow fiber membranes can be easily discharged.

【0014】第5図にハウジングにより膜が固定され、
膜の張りが一定に保たれた従来の中空糸膜モジュールと
本発明のモジュールを河川水について、flux=0.
5[m/d]の定流量運転を行った時の操作圧力の経日
変化を示す。これに示すように従来のモジュールでは約
5か月でろ過圧力が140[kpa]を越えて、使用不
可能になったことに対して、本発明ではろ過圧力の上昇
が緩やかで約1年間の使用が可能であり、従来のモジュ
ールの2倍の膜寿命が得られた。
In FIG. 5, the membrane is fixed by the housing,
The conventional hollow fiber membrane module in which the membrane tension was kept constant and the module of the present invention were used for river water at flux = 0.
The change with time of the operating pressure when a constant flow rate operation of 5 [m / d] is performed is shown. As shown in the figure, in the conventional module, the filtration pressure exceeded 140 [kpa] in about 5 months and became unusable, whereas in the present invention, the increase in the filtration pressure was moderate and the filtration pressure was about 1 year. It can be used and has twice the membrane life of conventional modules.

【0015】[0015]

【発明の効果】以上説明したように、本発明によれば、
中空糸膜に連結された浮子を設け、水位の上下動、ある
いは、浮子自身の浮き沈みにより中空糸膜のモジュール
長が変化するので空気中に露出することなくなるととも
に、中空糸膜の張り、弛みが変化し中空糸膜間隔が広が
ったり、縮小することにより汚泥の排出が容易に行え
る。このため、中空糸膜のモジュールの清浄の工数の低
減できるとともに、簡単な構成、および自然の力により
行えるので費用も低減できる。また、中空糸膜モジュー
ルの使用期間が長くなるというという効果が得られる。
As described above, according to the present invention,
By providing a float connected to the hollow fiber membrane, the module length of the hollow fiber membrane changes due to the vertical movement of the water level, or the floating of the float itself, so that the hollow fiber membrane is not exposed and the tension and slack of the hollow fiber membrane are reduced. Sludge can be easily discharged by changing and expanding or reducing the space between hollow fiber membranes. Therefore, the number of steps for cleaning the hollow fiber membrane module can be reduced, and the cost can be reduced because the simple configuration and natural force can be used. Further, there is an effect that the usage period of the hollow fiber membrane module is extended.

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

【図1】本発明の浮遊型中空糸膜モジュールの第1実施
例の全体構成図を示す。
FIG. 1 shows an overall configuration diagram of a first embodiment of a floating hollow fiber membrane module of the present invention.

【図2】本発明の浮遊型中空糸膜モジュールの第1実施
例の作動を説明する図を示す。
FIG. 2 is a diagram for explaining the operation of the first embodiment of the floating hollow fiber membrane module of the present invention.

【図3】本発明の浮遊型中空糸膜モジュールの第2実施
例の全体構成図を示す。
FIG. 3 shows an overall configuration diagram of a second embodiment of the floating hollow fiber membrane module of the present invention.

【図4】本発明の浮遊型中空糸膜モジュールの第3実施
例の全体構成図を示す。
FIG. 4 shows an overall configuration diagram of a third embodiment of the floating hollow fiber membrane module of the present invention.

【図5】従来例モジュールと実施例モジュールのろ過圧
力の特性比較図である。
FIG. 5 is a characteristic comparison diagram of filtration pressures of a conventional example module and an example module.

【符号の説明】[Explanation of symbols]

1 中空糸膜、 2 集水部 3、11 支持体、 4 連結体、 5、12 浮子、 13 チューブ 14 電磁弁 15 エアポンプ、 DESCRIPTION OF SYMBOLS 1 Hollow fiber membrane, 2 Water collecting part 3,11 Support body, 4 Connection body, 5,12 Float, 13 Tube 14 Solenoid valve 15 Air pump,

───────────────────────────────────────────────────── フロントページの続き (72)発明者 奥野 裕 東京都千代田区内神田一丁目1番14号 日 立プラント建設株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hiroshi Okuno 1-14-1 Kanda, Chiyoda-ku, Tokyo Inside Hirit Plant Construction Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 中空糸膜を束ねて構成される中空糸膜束
の下端に濾過水の集水部を設けるとともに、上端の支持
部に浮子を連結したことを特徴とする浮遊型中空糸膜モ
ジュール。
1. A floating-type hollow fiber membrane, characterized in that a bundle of hollow fiber membranes formed by bundling hollow fiber membranes is provided with a collecting portion for filtered water, and a float is connected to a supporting portion at the upper end. module.
【請求項2】 前記浮子に空気を給排する空気給排手段
を接続し、浮子の浮力調整による中空糸膜束の張りの調
整を可能としたことを特徴とする請求項1記載の浮遊型
中空糸膜モジュール。
2. The floating type according to claim 1, wherein an air supply / exhaust means for supplying / exhausting air to / from the float is connected so that the tension of the hollow fiber membrane bundle can be adjusted by adjusting the buoyancy of the float. Hollow fiber membrane module.
JP11637795A 1995-04-18 1995-04-18 Floating type hollow fiber membrane module Expired - Fee Related JP3417139B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11637795A JP3417139B2 (en) 1995-04-18 1995-04-18 Floating type hollow fiber membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11637795A JP3417139B2 (en) 1995-04-18 1995-04-18 Floating type hollow fiber membrane module

Publications (2)

Publication Number Publication Date
JPH08281078A true JPH08281078A (en) 1996-10-29
JP3417139B2 JP3417139B2 (en) 2003-06-16

Family

ID=14685494

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11637795A Expired - Fee Related JP3417139B2 (en) 1995-04-18 1995-04-18 Floating type hollow fiber membrane module

Country Status (1)

Country Link
JP (1) JP3417139B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101524078B1 (en) * 2014-03-20 2015-05-29 서울시립대학교 산학협력단 Floating mambrane and filterling method using the same
JP2017070913A (en) * 2015-10-08 2017-04-13 日立造船株式会社 Infiltration water intake unit
WO2020129705A1 (en) * 2018-12-21 2020-06-25 国立大学法人高知大学 Wastewater treatment apparatus and wastewater treatment method
CN113274781A (en) * 2021-07-26 2021-08-20 山东润扬环保设备有限公司 Honeycomb body fiber filter

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101524078B1 (en) * 2014-03-20 2015-05-29 서울시립대학교 산학협력단 Floating mambrane and filterling method using the same
JP2017070913A (en) * 2015-10-08 2017-04-13 日立造船株式会社 Infiltration water intake unit
WO2020129705A1 (en) * 2018-12-21 2020-06-25 国立大学法人高知大学 Wastewater treatment apparatus and wastewater treatment method
JPWO2020129705A1 (en) * 2018-12-21 2021-12-23 国立大学法人高知大学 Wastewater treatment equipment and wastewater treatment method
CN113274781A (en) * 2021-07-26 2021-08-20 山东润扬环保设备有限公司 Honeycomb body fiber filter
CN113274781B (en) * 2021-07-26 2021-09-24 山东润扬环保设备有限公司 Honeycomb body fiber filter

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