JPS63302910A - Method for washing porous filter - Google Patents

Method for washing porous filter

Info

Publication number
JPS63302910A
JPS63302910A JP13344987A JP13344987A JPS63302910A JP S63302910 A JPS63302910 A JP S63302910A JP 13344987 A JP13344987 A JP 13344987A JP 13344987 A JP13344987 A JP 13344987A JP S63302910 A JPS63302910 A JP S63302910A
Authority
JP
Japan
Prior art keywords
filter
pressure
bubbles
porous filter
carbon dioxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP13344987A
Other languages
Japanese (ja)
Inventor
Kazuya Yamada
和矢 山田
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.)
Toshiba Corp
Nippon Atomic Industry Group Co Ltd
Original Assignee
Toshiba Corp
Nippon Atomic Industry Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toshiba Corp, Nippon Atomic Industry Group Co Ltd filed Critical Toshiba Corp
Priority to JP13344987A priority Critical patent/JPS63302910A/en
Publication of JPS63302910A publication Critical patent/JPS63302910A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To completely remove the fine particles clogging a porous filter by generating the bubbles of gaseous carbon dioxide on the surface of the filter and in the filter. CONSTITUTION:When filtration is carried out, a liq. contg. fine particles is supplied into the raw liq. storage 2a of a hollow yarn membrane container 2, and the liq. is filtered by a hollow yarn membrane filter 1. When the filter 1 is washed, the container 2 is filled with high-pressure carbonated water, a vacuum pump 19 is then driven to rapidly lower the pressure in the container 2, and a large amt. of the bubbles of gaseous carbon dioxide are generated in the water. The bubbles are also generated on the surface of the filter 1 and in the pores, and the deposited fine particles are released by the growing force of the bubbles. As a result, the fine particles clogging the inside of the filter 1 and which were incapable of being removed by the conventional washing method can be completely removed.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は微細粒子によって目詰りした多孔質フィルタの
洗浄方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to a method for cleaning a porous filter clogged with fine particles.

(従来の技術) 近年、食品工業、医薬品工業、原子カニ業などの分野で
は処理対象徴粒子を除去するために中空糸膜フィルタ、
セラミックフィルタ、焼結金属フィルタなどの多孔質フ
ィルタが広く用いられている。
(Prior art) In recent years, in the food industry, pharmaceutical industry, atomic crab industry and other fields, hollow fiber membrane filters are used to remove symbolic particles during processing.
Porous filters such as ceramic filters and sintered metal filters are widely used.

ところで、これらの多孔質フィルタには各種形状のもの
があり、運転方法もさまざまであるが、一様に、ろ適時
間の経過とともにフィルタ表面およびフィルタ内部に処
理対象の微粒子が捕捉、沈着されるので1次第にろ過性
能が低下し、またフィルタを透過する際の抵抗が増えて
、ろ過差圧が上昇し、その結果処理流量が低下するよう
になる。
By the way, these porous filters come in various shapes and operate in various ways, but they all uniformly capture and deposit particulates to be treated on the filter surface and inside the filter as time passes. Therefore, the filtration performance gradually decreases, and the resistance when passing through the filter increases, the filtration pressure difference increases, and as a result, the processing flow rate decreases.

従って、所定の処理容量が得られなくなった時にはフィ
ルタを洗浄して処理性能の回復が図られる。
Therefore, when a predetermined processing capacity cannot be obtained, the filter is cleaned to restore processing performance.

従来、フィルタの洗浄は透過液、清水、気体による洗浄
あるいはこれら流体をろ過処理時とは逆の方向に流すこ
とにより逆洗していた。しかし、フィルタ表面およびフ
ィルタ内部に捕捉、沈積した微粒子の種類によっては、
従来の洗浄方法では十分に処理性能が回復しない場合が
あった。そのような場合には、微粒子の種類に応じて薬
液を選定し、これで洗浄すればほとんどの場合、処理性
能は回復していたが、薬液による洗浄には薬液によるフ
ィルタ材料の変質、劣化の恐れがある上に、洗浄により
発生する廃液の処理が必要になるという問題があった。
Conventionally, filters have been washed by backwashing by washing with permeate, fresh water, or gas, or by flowing these fluids in the opposite direction to that during filtration. However, depending on the type of particulates trapped and deposited on the filter surface and inside the filter,
Conventional cleaning methods sometimes did not sufficiently restore processing performance. In such cases, cleaning with a chemical solution selected according to the type of particulates would restore treatment performance in most cases, but cleaning with a chemical solution may cause alteration or deterioration of the filter material. In addition to this, there was a problem in that it was necessary to dispose of waste liquid generated by cleaning.

(発明が解決しようとする問題点) 本発明は上記事情に鑑みてなされたもので、その目的は
、フィルタ表面およびフィルタ内部に目詰った微粒子を
効率よく除去するとともに洗浄により発生する廃液の処
理に付加的な処理装置を必要としない多孔質フィルタの
洗浄方法を提供することにある。
(Problems to be Solved by the Invention) The present invention has been made in view of the above circumstances, and its purpose is to efficiently remove particulates clogging the filter surface and inside the filter, and to treat waste liquid generated by cleaning. An object of the present invention is to provide a method for cleaning a porous filter that does not require an additional processing device.

〔発明の構成〕 (問題点を解決するための手段及び作用)上記目的を達
成するために、本願の第1番目の発明の多孔質フィルタ
の洗浄方法は、予め高圧で炭酸ガスを溶解させた高圧炭
酸水の中に多孔質フィルタを浸漬し、この浸漬中に該高
圧炭酸水を常圧あるいはそれ以下に減圧して、フィルタ
表面およびフィルタ内部で炭酸ガスの気泡を発生させ、
この気泡の発生により多孔質フィルタに目詰った微粒子
を除去することを特徴とするものである。
[Structure of the Invention] (Means and Effects for Solving the Problems) In order to achieve the above object, the method for cleaning a porous filter of the first invention of the present application involves dissolving carbon dioxide gas in advance under high pressure. A porous filter is immersed in high-pressure carbonated water, and during this immersion, the high-pressure carbonated water is reduced to normal pressure or lower to generate carbon dioxide gas bubbles on the filter surface and inside the filter,
This method is characterized in that the generation of bubbles removes fine particles clogging the porous filter.

さらに、本願の第2番目の発明の多孔質フィルタの洗浄
方法は、予め高圧で炭酸ガスを溶解させた高圧炭酸水を
、ろ過処理時とは逆の方向に多孔質フィルタを透過させ
、この際多孔質フィルタ収納容器内の圧力を常圧あるい
はそれ以下に減圧して、フィルタ表面およびフィルタ内
部で炭酸ガスの気泡を発生させ、この気泡の発生により
多孔質フィルタに目詰った微粒子を除去することを特徴
とするものである。
Furthermore, in the method for cleaning a porous filter according to the second invention of the present application, high-pressure carbonated water in which carbon dioxide gas has been dissolved in advance at high pressure is passed through the porous filter in the opposite direction to the filtration process. Reducing the pressure inside the porous filter storage container to normal pressure or lower to generate carbon dioxide gas bubbles on the filter surface and inside the filter, and removing particulates clogging the porous filter due to the generation of these bubbles. It is characterized by:

したがって、本発明の多孔質フィルタの洗浄方法による
と、高圧炭酸水の圧力を急激に低下させることにより水
中に炭酸ガスの気泡を多量に発生させ、この気泡の成長
力およびその上昇の際のせん断力によって、多孔質フィ
ルタの表面あるいは内部に付着した微粒子をはく離、除
去することができる。
Therefore, according to the porous filter cleaning method of the present invention, by rapidly reducing the pressure of high-pressure carbonated water, a large amount of carbon dioxide bubbles are generated in water, and the growth force of these bubbles and the shear when they rise are The force can peel off and remove fine particles attached to the surface or inside of the porous filter.

(実施例) 本発明の実施例を図面を参照して説明する。(Example) Embodiments of the present invention will be described with reference to the drawings.

図は本発明の一実施例の系統図である。同図において、
中空糸膜フィルタ1は、原液溜2aおよびろ液溜2bか
らなる中空糸膜収納容器2内に固定されている。中空糸
膜収納容器2の原液溜2aの下部には、弁5を備えた給
液配管12、弁7を備えた濃縮液排出配管17および弁
10を備えたスクラビング用空気配管15が接続されて
おり、また原液溜28の上部には弁8を備えたオーバー
フロー配管16および真空ポンプ19.弁21.配管2
0からなる排気系が接続されている。
The figure is a system diagram of an embodiment of the present invention. In the same figure,
The hollow fiber membrane filter 1 is fixed in a hollow fiber membrane storage container 2 consisting of a stock solution reservoir 2a and a filtrate reservoir 2b. A liquid supply pipe 12 equipped with a valve 5, a concentrated liquid discharge pipe 17 equipped with a valve 7, and a scrubbing air pipe 15 equipped with a valve 10 are connected to the lower part of the stock solution reservoir 2a of the hollow fiber membrane storage container 2. In addition, an overflow pipe 16 equipped with a valve 8 and a vacuum pump 19 are installed above the stock solution reservoir 28 . Valve 21. Piping 2
An exhaust system consisting of 0 is connected.

一方、中空糸膜収納容器2の図示しないシール部で原液
溜2aとは仕切られたろ液溜2bには、弁6を備えたろ
液吐出配管13、弁9を備えた空気加圧配管14および
高圧炭酸水貯蔵槽3.弁11.配Ir!18からなる高
圧炭酸水供給系が接続されている。また、中空糸膜フィ
ルタ1のろ過差圧を測定するために、給液配管12と、
ろ液吐出配管13の間には差圧計4が設置されている。
On the other hand, the filtrate reservoir 2b, which is separated from the stock solution reservoir 2a by a seal (not shown) of the hollow fiber membrane storage container 2, includes a filtrate discharge piping 13 equipped with a valve 6, an air pressurization piping 14 equipped with a valve 9, and a high pressure Carbonated water storage tank 3. Valve 11. Distribution! A high-pressure carbonated water supply system consisting of 18 units is connected. In addition, in order to measure the filtration differential pressure of the hollow fiber membrane filter 1, a liquid supply pipe 12,
A differential pressure gauge 4 is installed between the filtrate discharge pipes 13.

中空糸膜フィルタ1によるろ過処理においては、微粒子
を含む液は給液配管12を通って予め液で満たされてい
る中空糸膜収納容器2の原液溜2aに供給され、中空糸
膜フィルタ1でろ過されたろ液はろ液溜2b、ろ液吐出
配管13を通って吐出される。
In the filtration process using the hollow fiber membrane filter 1, a liquid containing fine particles is supplied through the liquid supply pipe 12 to the stock solution reservoir 2a of the hollow fiber membrane storage container 2, which is filled with liquid in advance, and is filtered by the hollow fiber membrane filter 1. The filtered filtrate is discharged through the filtrate reservoir 2b and the filtrate discharge pipe 13.

このとき給液中の微粒子はフィルタ表面あるいはフィル
タ細孔内部で捕捉されるため、ろ適時間の経過とともに
、フィルタを透過する際の抵抗が増えて、ろ過差圧が上
昇するので、処理流量が低下するようになる。このよう
な状態になると1本実施例では中空糸膜フィルタ1への
処理液の供給を止めて、中空糸膜フィルタ1を後記する
洗浄方法により処理することにより、処理容量の回復を
図るようにしている。
At this time, fine particles in the supplied liquid are captured on the filter surface or inside the filter pores, so as the filtration time passes, the resistance when passing through the filter increases and the filtration differential pressure increases, so the processing flow rate decreases. begins to decline. When such a state occurs, in this embodiment, the supply of processing liquid to the hollow fiber membrane filter 1 is stopped, and the hollow fiber membrane filter 1 is processed by the cleaning method described later, thereby recovering the processing capacity. ing.

ところで、通常の逆洗操作では、中空糸膜収納容器2の
ろ液溜2bに空気加圧配管14から加圧することにより
、該ろ液溜2b内のろ液をろ過処理時とは逆の方向に中
空糸膜フィルタ1を透過させるとともに、中空糸膜収納
容器2の原液溜2a内にスクラビング用空気配管15か
ら多数の気泡を噴出させて、該原液溜2a内の液体を撹
拌、振動させて、膜面に付着した微粒子を除去するよう
にしているが、この方法ではフィルタ表面およびフィル
タ内部に捕捉・沈積した微粒子の種類によっては十分に
これら微粒子を除去することはできなかった。
By the way, in a normal backwash operation, by pressurizing the filtrate reservoir 2b of the hollow fiber membrane storage container 2 from the air pressure piping 14, the filtrate in the filtrate reservoir 2b is moved in the opposite direction to that during filtration. The liquid is passed through the hollow fiber membrane filter 1, and a large number of bubbles are ejected from the scrubbing air pipe 15 into the stock solution reservoir 2a of the hollow fiber membrane storage container 2 to stir and vibrate the liquid in the stock solution reservoir 2a. Although this method attempts to remove particulates adhering to the membrane surface, it has not been possible to sufficiently remove these particulates depending on the type of particulates trapped and deposited on the filter surface and inside the filter.

次に、本実施例によるフィルタ洗浄方法について説明す
る。
Next, a filter cleaning method according to this embodiment will be explained.

中空糸膜フィルタ1への給液を止め、まず、弁5.6,
9,10.11を閉にし、弁7,8を開け、原液溜2b
内の液を排出する0次に弁7,8を閉じた後に、図示し
ない加圧ラインにより、中空糸膜収納容器2内の圧力を
高圧炭酸水貯蔵槽3内と同程度に加圧する1次に弁11
を開き、高圧炭酸水貯蔵槽3から弁11、配管18を経
て中空糸膜収納容器2のろ液溜2bp高圧炭酸水を注入
する。この際、中空糸膜収納容器2内の圧力が低下しな
いように注意しながら、弁8をわずかに開き、中空糸膜
収納容器2内を高圧炭酸水で満たした後、弁8,11を
閉じる1次に、真空ポンプ19を駆動し弁21を開く、
このとき中空糸膜収納容器2内の圧力が急激に低下する
ので、高圧で水に溶解していた炭酸ガスが放散され、水
中で多量の気泡を発生する。この気泡は中空糸膜フィル
タ1の表面および細孔内部においても、同様に発生し、
気泡の成長力により付着微粒子をはく離する0発生した
炭酸ガスは真空ポンプ19により吸引される。
Stop the liquid supply to the hollow fiber membrane filter 1, and first close the valves 5, 6,
Close valves 9, 10 and 11, open valves 7 and 8, and remove the stock solution reservoir 2b.
After the valves 7 and 8 are closed, the pressure inside the hollow fiber membrane storage container 2 is increased to the same level as the inside of the high-pressure carbonated water storage tank 3 using a pressure line (not shown). niben 11
is opened, and 2 bp of high-pressure carbonated water is injected from the high-pressure carbonated water storage tank 3 through the valve 11 and piping 18 into the filtrate reservoir of the hollow fiber membrane storage container 2. At this time, while being careful not to reduce the pressure inside the hollow fiber membrane storage container 2, open the valve 8 slightly, fill the inside of the hollow fiber membrane storage container 2 with high-pressure carbonated water, and then close the valves 8 and 11. 1st, drive the vacuum pump 19 and open the valve 21;
At this time, the pressure inside the hollow fiber membrane storage container 2 drops rapidly, and the carbon dioxide gas dissolved in the water at high pressure is dissipated, generating a large amount of bubbles in the water. These bubbles also occur on the surface of the hollow fiber membrane filter 1 and inside the pores,
The generated carbon dioxide gas, which peels off the adhered fine particles due to the growth force of the bubbles, is sucked by the vacuum pump 19.

中空糸膜収納容器2内で炭酸ガスの気泡の発生が終った
ら、弁21を閉じ、真空ポンプ19を停止し、次に弁7
,8を開けて、中空糸膜収納容器2内の液を排出する。
When the generation of carbon dioxide gas bubbles has finished within the hollow fiber membrane storage container 2, the valve 21 is closed, the vacuum pump 19 is stopped, and then the valve 7 is closed.
, 8 to drain the liquid inside the hollow fiber membrane storage container 2.

また、真空ポンプ19を停止した後、弁11,8を開け
て、高圧炭酸水をろ過処理時とは逆の方向に中空糸膜フ
ィルタ1を透過させれば、炭酸水の圧力が低下し透過中
に炭酸ガスの気泡が発生するので、洗浄効果がさらに増
進される。
In addition, if the valves 11 and 8 are opened after the vacuum pump 19 is stopped and the high-pressure carbonated water is allowed to pass through the hollow fiber membrane filter 1 in the opposite direction to that during filtration, the pressure of the carbonated water decreases and the water permeates. Since carbon dioxide gas bubbles are generated inside, the cleaning effect is further enhanced.

なお、本実施例では多孔質フィルタとして中空糸膜フィ
ルタを用いたが、セラミックフィルタ。
In this example, a hollow fiber membrane filter was used as the porous filter, but a ceramic filter was used instead.

焼結金属フィルタなど他の多孔質フィルタに関して全く
同様に実施することができる。
It can be implemented in exactly the same way for other porous filters, such as sintered metal filters.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明の洗浄方法によると、高圧
炭酸水の圧力を急激に低下させることにより水中に炭酸
ガスの気泡を多量に発生させ、この気泡の成長力および
その上昇の際のせん断力によって、多孔質フィルタの表
面あるいは内部に付着した微粒子をはく離、除去するも
のであるから。
As explained above, according to the cleaning method of the present invention, a large amount of carbon dioxide gas bubbles are generated in water by rapidly reducing the pressure of high-pressure carbonated water, and the growth force of these bubbles and the shear when they rise are This is because the force is used to peel off and remove fine particles attached to the surface or inside of the porous filter.

従来の洗浄法では除去できなかったフィルタ内部に目詰
った微粒子も完全に除去することができる。
It is also possible to completely remove particulates clogging the inside of the filter, which could not be removed using conventional cleaning methods.

また、使用する高圧炭酸水は、真空ポンプによる減圧操
作で、溶解していた炭酸ガスが全て放散されて最終的に
水のみとなるので、従来の薬液洗浄のような洗浄後の廃
液の処理の如き付加的な処理を全く必要としないという
すぐれた効果を奏する。
In addition, the high-pressure carbonated water used is depressurized by a vacuum pump, and all dissolved carbon dioxide gas is dissipated, leaving only water. This has an excellent effect in that it does not require any additional processing.

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

図は本発明の一実施例の系統図である。 1・・・中空糸膜フィルタ 2・・・中空糸膜収納容器  2a・・・原液溜2b・
・・ろ液溜     3・・・高圧炭酸水貯蔵槽4・・
・差圧計 5 、6 、7 、8 、9.10,11,
21−・・弁12.13,14,15,16,17,1
8.20・・・配管19・・・真空ポンプ
The figure is a system diagram of an embodiment of the present invention. 1... Hollow fiber membrane filter 2... Hollow fiber membrane storage container 2a... Stock solution reservoir 2b.
...Filtrate reservoir 3...High pressure carbonated water storage tank 4...
・Differential pressure gauge 5, 6, 7, 8, 9.10, 11,
21--Valve 12.13, 14, 15, 16, 17, 1
8.20...Piping 19...Vacuum pump

Claims (2)

【特許請求の範囲】[Claims] (1)予め高圧で炭酸ガスを溶解させた高圧炭酸水の中
に多孔質フィルタを浸漬し、この浸漬中に該高圧炭酸水
を常圧あるいはそれ以下に減圧して、フィルタ表面およ
びフィルタ内部で炭酸ガスの気泡を発生させ、この気泡
の発生により多孔質フィルタに目詰った微粒子を除去す
ることを特徴とする多孔質フィルタの洗浄方法。
(1) A porous filter is immersed in high-pressure carbonated water in which carbon dioxide gas has been dissolved at high pressure, and during this immersion, the high-pressure carbonated water is reduced to normal pressure or lower, so that the filter surface and inside the filter are A method for cleaning a porous filter, which comprises generating carbon dioxide gas bubbles and removing particulates clogging the porous filter by the generation of the bubbles.
(2)予め高圧で炭酸ガスを溶解させた高圧炭酸水を、
ろ過処理時とは逆の方向に多孔質フィルタを透過させ、
この際、多孔質フィルタ収納容器内の圧力を常圧あるい
はそれ以下に減圧して、フィルタ表面およびフィルタ内
部で炭酸ガスの気泡を発生させ、この気泡の発生により
多孔質フィルタに目詰った微粒子を除去することを特徴
とする多孔質フィルタの洗浄方法。
(2) High-pressure carbonated water in which carbon dioxide gas has been dissolved in advance at high pressure,
Pass through the porous filter in the opposite direction to the filtration process,
At this time, the pressure inside the porous filter storage container is reduced to normal pressure or lower to generate carbon dioxide gas bubbles on the filter surface and inside the filter, and the generation of these bubbles removes the particulates clogging the porous filter. A method of cleaning a porous filter, the method comprising: removing the porous filter;
JP13344987A 1987-05-30 1987-05-30 Method for washing porous filter Pending JPS63302910A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13344987A JPS63302910A (en) 1987-05-30 1987-05-30 Method for washing porous filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13344987A JPS63302910A (en) 1987-05-30 1987-05-30 Method for washing porous filter

Publications (1)

Publication Number Publication Date
JPS63302910A true JPS63302910A (en) 1988-12-09

Family

ID=15105034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13344987A Pending JPS63302910A (en) 1987-05-30 1987-05-30 Method for washing porous filter

Country Status (1)

Country Link
JP (1) JPS63302910A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
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JPH048334A (en) * 1990-04-25 1992-01-13 Haruo Miyata Cleaning method and its device for carpet and the like
JPH0441781A (en) * 1990-06-01 1992-02-12 Haruo Miyata Stain-resistant processing of carpet and device therefor
WO2009000693A1 (en) * 2007-06-28 2008-12-31 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method of treating water
US8236183B2 (en) 2004-07-02 2012-08-07 Pall Corporation Methods and systems for filtration
WO2015052840A1 (en) * 2013-10-11 2015-04-16 三菱電機株式会社 Water treatment device and hot-water supply device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JPH0441781A (en) * 1990-06-01 1992-02-12 Haruo Miyata Stain-resistant processing of carpet and device therefor
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WO2009000693A1 (en) * 2007-06-28 2008-12-31 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method of treating water
WO2015052840A1 (en) * 2013-10-11 2015-04-16 三菱電機株式会社 Water treatment device and hot-water supply device
JPWO2015052840A1 (en) * 2013-10-11 2017-03-09 三菱電機株式会社 Water treatment device, hot water supply device and heating device

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