JPH05285354A - Washing and regenerating method for filter membrane - Google Patents

Washing and regenerating method for filter membrane

Info

Publication number
JPH05285354A
JPH05285354A JP12128292A JP12128292A JPH05285354A JP H05285354 A JPH05285354 A JP H05285354A JP 12128292 A JP12128292 A JP 12128292A JP 12128292 A JP12128292 A JP 12128292A JP H05285354 A JPH05285354 A JP H05285354A
Authority
JP
Japan
Prior art keywords
membrane
cleaning
solid matter
pressure gas
ceramic filter
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
JP12128292A
Other languages
Japanese (ja)
Inventor
Kenzo Sugaya
謙三 菅谷
Minoru Tsuchiya
実 土屋
Hideyoshi Matsubara
秀吉 松原
Atsuo Baba
淳雄 馬場
Shigeyuki Fujimura
重幸 藤村
Toshiji Kashiide
敏次 樫出
Hiroyasu Takashima
宏泰 高島
Masayasu Nishino
方康 西野
Osamu Yamashita
修 山下
Kozo Sasaki
廣三 佐々木
Shigeru Miyoshi
茂 三好
Kimio Araki
公夫 荒木
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.)
Ishigaki Mechanical Industry Co Ltd
Original Assignee
Ishigaki Mechanical Industry 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 Ishigaki Mechanical Industry Co Ltd filed Critical Ishigaki Mechanical Industry Co Ltd
Priority to JP12128292A priority Critical patent/JPH05285354A/en
Publication of JPH05285354A publication Critical patent/JPH05285354A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To effectively remove solid material stuck on the membrane surfaced of a ceramic filter by combining a gaseous washing fluid with a liquid washing fluid and acting the combined washing fluid on the solid material stuck on the membrane surface of the ceramic filter. CONSTITUTION:A stop valve 7 is opened and both of high-pressure gas for washing and washing liquid are sent and allowed to act on solid material S stuck on the membrane surface 1a of a ceramic filter 1. In other words, the stuck solid material is peeled by the high-pressure gas and thereafter washed down by the liquid washing fluid. Therefore even the solid material is completely removed which is clogged on the membrane surface of a filter medium such as the ceramic filter and strongly stuck thereon.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、限外ろ過膜を用いた
ろ過装置におけるろ過膜の洗浄再生方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning and regenerating a filtration membrane in a filtration device using an ultrafiltration membrane.

【0002】[0002]

【従来の技術】この種、限外ろ過膜の洗浄再生方法に関
しては、種々提案されている。特開平3−188928
号では、ろ過膜を振動させて、付着物を剥離するように
している。また、特公昭55−37283号では、膜の
表面に気体および液体を流動させている。
2. Description of the Related Art Various methods for cleaning and regenerating an ultrafiltration membrane of this type have been proposed. JP-A-3-188928
In No. 6, the filtration membrane is vibrated to remove the deposits. In Japanese Patent Publication No. 55-37283, gas and liquid are made to flow on the surface of the film.

【0003】[0003]

【発明が解決しようとする課題】然しながら、上述の従
来技術では、膜を振動させたり、洗浄液やガスが膜の表
面を流動させるものであるので、膜の微細な通孔に詰ま
った固形物までも除去することは困難である。従って、
経時使用につれて、そのろ過効率が低下し、限度に達す
れば分解して再生するか交換しなければならない。
However, in the above-mentioned prior art, since the membrane is vibrated or the cleaning liquid or gas flows on the surface of the membrane, even solid matter clogged in the fine through-holes of the membrane can be obtained. Is also difficult to remove. Therefore,
As it ages, its filtration efficiency decreases, and if it reaches the limit, it must be decomposed and regenerated or replaced.

【0004】[0004]

【課題を解決するための手段】この発明は、上述のよう
な課題を解消したものであって、その要旨とするところ
は、膜面に付着した固形物に対して、洗浄液と洗浄ガス
とを作用させるようにしたものであり、洗浄液と洗浄ガ
スを固形物に作用させる具体的手法としては、例えば、
固形物の付着した膜をその裏面から高圧ガスでブローし
たのち、同じくその裏面から洗浄液を送って逆洗しても
よく、また、固形物の付着した膜表面に洗浄液を流し乍
ら、その裏面側から高圧ガスでブローしてもよく、ま
た、このブローする高圧ガスに合わせて洗浄液で逆洗し
てもよく、また、膜表面を流す洗浄液中にも高圧ガスを
合わせて流してもよい。また、洗浄液と高圧ガスを別途
に供給することなく、高圧下において洗浄液中に洗浄ガ
スを溶解させておき、膜面で洗浄ガスを遊離気化させて
固形物に作用させてもよい。さらに、膜面上の原液を真
空吸引して固形物を浮かせたのち、膜の裏面側から高圧
の洗浄ガスを吹き込むようにしてもよい。
The present invention has solved the above-mentioned problems, and its gist is to provide a cleaning liquid and a cleaning gas to a solid matter attached to a film surface. As a specific method of causing the cleaning liquid and the cleaning gas to act on the solid matter, for example,
After blowing the film with the solid matter on it from the back side with high-pressure gas, the cleaning solution may be sent from the back side to backwash it. Alternatively, the cleaning solution may be poured onto the surface of the film with the solid matter on the back side. The high-pressure gas may be blown from the side, the back-washing may be performed with the cleaning liquid in accordance with the high-pressure gas to be blown, and the high-pressure gas may be also flowed in the cleaning liquid flowing on the membrane surface. Alternatively, the cleaning gas may be dissolved in the cleaning liquid under high pressure without separately supplying the cleaning liquid and the high-pressure gas, and the cleaning gas may be liberated and vaporized on the membrane surface to act on the solid matter. Furthermore, the stock solution on the film surface may be vacuumed to float the solid matter, and then a high-pressure cleaning gas may be blown from the back surface side of the film.

【0005】[0005]

【作用】このように、この発明では膜上に生じた固形物
を除去するに当って、洗浄液と洗浄ガスとを併用するの
で、まず、洗浄ガスによって膜上の固形物に衝撃を与え
て剥離した上で、この剥離した固形物を洗い流すもので
あり、従って、目に詰まった固形物までも除去すること
ができるものである。例えば、洗浄ガスと洗浄液で逆洗
するときには、洗浄ガスで固形物を浮かせたのち、洗浄
液でこれを洗い流すことができるものであり、また、洗
浄ガスを過飽和に溶解した洗浄液を用いるときには、洗
浄液が固形物に接触して洗浄ガスが溶解液から遊離する
際、固形物に作用してろ過膜から剥離し、同時に洗浄液
によって洗い流すことができるものである。以下、図面
に基づいて、この発明を更に具体的に説明する。
As described above, according to the present invention, the cleaning liquid and the cleaning gas are used together to remove the solid matter generated on the film. Therefore, the cleaning gas first gives an impact to the solid matter on the film to remove it. In addition, the peeled solid matter is washed away, and therefore, even the solid matter clogged can be removed. For example, when backwashing with a cleaning gas and a cleaning liquid, the solid matter can be floated by the cleaning gas and then washed away with the cleaning liquid.When a cleaning liquid in which the cleaning gas is supersaturated is used, the cleaning liquid is When the cleaning gas is released from the solution by contacting with the solid matter, the cleaning gas acts on the solid matter and is separated from the filtration membrane, and at the same time, it can be washed away by the cleaning solution. Hereinafter, the present invention will be described more specifically with reference to the drawings.

【0006】[0006]

【実施例】図1〜図5は、この発明に係るろ過膜の洗浄
再生方法の概要のフローを示し、符号1はセラミックフ
ィルター、2はその収納容器、3は原液の供給ポンプ、
4は原液供給路に設けた開閉弁、5はろ液取出路に設け
た開閉弁、6は洗浄水の排出路に設けた開閉弁、7は洗
浄用の流体供給路に設けた開閉弁、8は原液中への空気
の供給路に設けた開閉弁、9はろ液受槽である。尚、セ
ラミックフィルター1は、収納容器2に多数並列して設
けられるが一本のみ代表して示している。
1 to 5 show an outline flow of a method for cleaning and regenerating a filtration membrane according to the present invention, in which reference numeral 1 is a ceramic filter, 2 is a storage container for the ceramic filter, 3 is a feed pump for the undiluted solution,
4 is an opening / closing valve provided in the stock solution supply passage, 5 is an opening / closing valve provided in the filtrate outlet passage, 6 is an opening / closing valve provided in the wash water discharge passage, 7 is an opening / closing valve provided in the cleaning fluid supply passage, 8 Is an on-off valve provided in the air supply path into the stock solution, and 9 is a filtrate receiving tank. Although a large number of ceramic filters 1 are provided in parallel in the storage container 2, only one ceramic filter 1 is shown as a representative.

【0007】このように構成したろ過装置では、原液ポ
ンプ3によって、セラミックフィルター1内に供給され
た原液は、セラミックフィルター1によってろ過されて
そのろ液はろ液受槽9に貯留され、濃縮された原液は収
納容器2に溜まる。そして、このような運転をしてセラ
ミックフィルター1の内面1aに固形物Sが溜まってろ
過性が低下したときには、開閉弁7を開いて洗浄用の高
圧ガスおよび洗浄液を送る(矢印イ)ことによってセラ
ミックフィルター1を逆洗してセラミックフィルター1
を再生することができる。このとき、逆洗排液は開閉弁
6を用いて外部に取り出す(矢印ロ)ものである。この
逆洗時にこの発明では、高圧ガスで固形物を剥離した上
で逆洗液で洗浄するので、膜の目に詰まった固形物迄も
除去することができる。
In the filtration device thus constructed, the stock solution supplied into the ceramic filter 1 by the stock solution pump 3 is filtered by the ceramic filter 1 and the filtrate is stored in the filtrate receiving tank 9 and concentrated. Collects in the storage container 2. Then, when the solid S is accumulated on the inner surface 1a of the ceramic filter 1 by such an operation and the filterability is deteriorated, the open / close valve 7 is opened to send the high pressure gas for cleaning and the cleaning liquid (arrow a). Backwash Ceramic Filter 1 and Ceramic Filter 1
Can be played. At this time, the backwash drainage is taken out to the outside using the open / close valve 6 (arrow B). In this invention, since the solid matter is peeled off with a high-pressure gas and then washed with the backwash solution during the backwashing, it is possible to remove even the solid matter clogging the membrane.

【0008】次に、図2として示すフローでは、上述の
洗浄液と高圧ガスの逆洗に加えて、開閉弁4および8を
開いて、高圧空気(矢印ハ)を含む原液(矢印ニ)で膜
表面を洗浄するようにしている。すなわち、逆洗によっ
て剥離した固形物を高圧空気を含む原液で洗い流すわけ
であり、セラミックフィルター1のろ過面を内外から洗
浄するので完全に再生することができる。
Next, in the flow shown in FIG. 2, in addition to the above-described backwashing of the cleaning liquid and the high-pressure gas, the on-off valves 4 and 8 are opened to form a membrane with the stock solution (arrow D) containing high-pressure air (arrow C). I try to clean the surface. That is, the solid matter separated by backwashing is washed away with a stock solution containing high-pressure air, and the filtration surface of the ceramic filter 1 is washed from inside and outside, so that it can be completely regenerated.

【0009】次に、図3に示すフローでは、弁4および
弁5を閉止して弁6を開いて収納容器2のろ液を真空ポ
ンプV吸引してこのろ液で膜を逆洗するようにしてい
る。この場合にも膜に付着した固形物には吸引負圧がか
かっている上でろ液による逆洗が行われるので、セラミ
ックフィルター1の内部に詰まった固形物迄も除去する
ことができる。また、この方式の場合、図4に示すよう
に、大型の開放型貯留槽9内に、多数のセラミックフィ
ルター1・・・・を設置してろ過装置を形成することができ
る。
Next, in the flow shown in FIG. 3, the valves 4 and 5 are closed and the valve 6 is opened to suck the filtrate in the storage container 2 by the vacuum pump V so that the membrane is backwashed with this filtrate. I have to. In this case as well, since the solid matter attached to the membrane is subjected to suction negative pressure and backwashed with the filtrate, even the solid matter clogging the inside of the ceramic filter 1 can be removed. Further, in the case of this system, as shown in FIG. 4, a large number of ceramic filters 1 ... Can be installed in a large open type storage tank 9 to form a filtration device.

【0010】さらに、この発明において、洗浄液と洗浄
ガスをセラミックフィルター1に付着した固形物に作用
させて除去するに当って、次のようにしてもよい。すな
わち、図1において、弁7から収納容器2に導入する逆
洗液中に高圧ガスを過飽和に溶解させ、この逆洗液が膜
面部分で圧力が低下するとき、溶解ガスを気化させるこ
とによって固形物を剥離することもできる。その状態を
図5に示す。図中、符号aは膜面に発生した気泡であ
り、膜面に付着した固形物Sを押し上げている。
Further, in the present invention, the cleaning liquid and the cleaning gas may be acted on the solid matter adhering to the ceramic filter 1 to be removed as follows. That is, in FIG. 1, the high-pressure gas is supersaturatedly dissolved in the backwash liquid introduced into the storage container 2 from the valve 7, and the dissolved gas is vaporized when the pressure of the backwash liquid drops at the membrane surface portion. The solid matter can also be peeled off. The state is shown in FIG. In the figure, reference numeral a is a bubble generated on the film surface, which pushes up the solid matter S attached to the film surface.

【0011】[0011]

【発明の効果】このように、この発明は、ろ過膜面に付
着した固形物に対して液体状の洗浄流体と気体状の洗浄
流体を作用させるようにしたのでろ過膜の微細通孔まで
詰まった固形物までも除去できるものであり、特に、セ
ラミック膜フィルターの如く、微細通路を有する支持体
表面上に形成された膜の洗浄に用いて卓効を奏する。
As described above, according to the present invention, since the liquid cleaning fluid and the gaseous cleaning fluid act on the solid matter attached to the surface of the filtration membrane, even the fine through holes of the filtration membrane are clogged. Even a solid matter can be removed, and it is particularly effective when used for cleaning a membrane formed on the surface of a support having fine passages such as a ceramic membrane filter.

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

【図1】この発明に係るろ過膜の洗浄再生方法の模式的
フローシートである。
FIG. 1 is a schematic flow sheet of a method for cleaning and regenerating a filtration membrane according to the present invention.

【図2】同じく、他の実施例を説明するための模式的フ
ローシートである。
FIG. 2 is likewise a schematic flow sheet for explaining another embodiment.

【図3】同じく、他の実施例を説明するための模式的フ
ローシートである。
FIG. 3 is likewise a schematic flow sheet for explaining another embodiment.

【図4】同じく、セラミックフィルターを内圧式に用い
た事例の模式的フローシートである。
FIG. 4 is likewise a schematic flow sheet of a case where a ceramic filter is used in an internal pressure system.

【図5】この発明に係るセラミックフィルターの一部の
縦断面図である。
FIG. 5 is a longitudinal sectional view of a part of the ceramic filter according to the present invention.

【符号の説明】[Explanation of symbols]

S 固形物 S solid

───────────────────────────────────────────────────── フロントページの続き (72)発明者 樫出 敏次 香川県坂出市林田町3594−2 (72)発明者 高島 宏泰 埼玉県川越市吉田新町2−16−11 (72)発明者 西野 方康 香川県善通寺市生野町2500−11 (72)発明者 山下 修 香川県高松市西宝町3−1−5 (72)発明者 佐々木 廣三 香川県観音寺市柞田町甲1590−24 (72)発明者 三好 茂 香川県坂出市青葉町3−25 (72)発明者 荒木 公夫 東京都八王子市台町1−2−15 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Toshiji Kashide 3594-2 Hayashida-cho, Sakaide-shi, Kagawa (72) Inventor Hiroyasu Takashima 2-16-11 Yoshida-shinmachi, Kawagoe-shi, Saitama (72) Inventor Nishinokata Kan 2500-11, Ikuno-cho, Zentsuji-shi, Kagawa Inventor Osamu Yamashita 3-1-5 Saiho-cho, Takamatsu-shi, Kagawa (72) Inventor Hirozo Sasaki 1590-24 Ko, Kata-cho, Kanonji-shi, Kagawa (72) Inventor Shigeru Miyoshi 3-25 Aoba-cho, Sakaide-shi, Kagawa (72) Inventor Kimio Araki 1-2-15, Taimachi, Hachioji-shi, Tokyo

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 膜ろ過装置において、膜面に付着した微
細な固形物Sを除去するに当り、微細な固形物Sに対し
て液体および気体の洗浄流体を作用させることを特長と
するろ過膜の洗浄再生方法。
1. A filtration membrane characterized in that a liquid and a gas cleaning fluid are applied to the fine solids (S) when removing the fine solids (S) attached to the membrane surface in the membrane filtration device. How to clean and recycle.
【請求項2】 請求項1において、固形物Sを除去する
に当り、膜をその裏面側から高圧ガスでブローしたの
ち、同じくその裏面側から洗浄液を透過させることを特
長とするろ過膜の洗浄再生方法。
2. The cleaning of a filtration membrane according to claim 1, wherein in removing the solid matter S, the membrane is blown from the back side with a high-pressure gas and then the washing solution is also permeated from the back side. How to play.
【請求項3】 請求項1において、固形物Sを除去する
に当り、膜面上に原液を流しつつ、膜をその裏面側から
高圧ガスおよび洗浄液でブローすることを特長とするろ
過膜の洗浄再生方法。
3. The cleaning of a filtration membrane according to claim 1, wherein in removing the solid matter S, the membrane is blown with a high-pressure gas and a washing solution from the back side of the membrane while flowing an undiluted solution onto the membrane surface. How to play.
【請求項4】 請求項1において、固形物Sを除去する
に当り、膜面上を原液に合わせて高圧ガスを流すことを
特長とするろ過膜の洗浄再生方法。
4. The method for cleaning and regenerating a filtration membrane according to claim 1, wherein in removing the solid matter S, a high-pressure gas is caused to flow along the surface of the membrane with the stock solution.
【請求項5】 請求項1において、微細な固形物Sに作
用させる洗浄流体は、高圧ガスを溶解した過飽和高圧流
体であり、かつ、膜の裏面から作用させることを特長と
するろ過膜の洗浄再生方法。
5. The cleaning of a filtration membrane according to claim 1, wherein the cleaning fluid that acts on the fine solid matter S is a supersaturated high-pressure fluid in which a high-pressure gas is dissolved, and that acts on the back surface of the membrane. How to play.
【請求項6】 請求項1において、膜面付着した固形物
Sを除去するに当り、膜面を真空吸引したのち、その裏
面から高圧ガスでブローすることを特長とするろ過膜の
再生洗浄方法。
6. The method for regenerating and cleaning a filtration membrane according to claim 1, wherein in removing the solid matter S adhering to the membrane surface, the membrane surface is vacuum-suctioned and then blown with high pressure gas from the back surface. ..
JP12128292A 1992-04-14 1992-04-14 Washing and regenerating method for filter membrane Pending JPH05285354A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12128292A JPH05285354A (en) 1992-04-14 1992-04-14 Washing and regenerating method for filter membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12128292A JPH05285354A (en) 1992-04-14 1992-04-14 Washing and regenerating method for filter membrane

Publications (1)

Publication Number Publication Date
JPH05285354A true JPH05285354A (en) 1993-11-02

Family

ID=14807400

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH05285354A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07251041A (en) * 1994-03-16 1995-10-03 Ngk Insulators Ltd Membrane separation apparatus and washing method therefor
JP2002011333A (en) * 2000-06-29 2002-01-15 Kuraray Co Ltd Method and apparatus for washing hollow fiber membrane module
JP2003265935A (en) * 2002-03-15 2003-09-24 Suido Kiko Kaisha Ltd Membrane filtration module cleaning method, membrane filtration apparatus, and chemical-used cleaning apparatus
JP2006088017A (en) * 2004-09-22 2006-04-06 Japan Organo Co Ltd Water treatment apparatus and its operating method
JP2007216102A (en) * 2006-02-14 2007-08-30 Mitsubishi Heavy Ind Ltd Filtering device, and membrane washing method of this filtering device
JP2011104548A (en) * 2009-11-19 2011-06-02 Atlas:Kk Liquid cleaning apparatus
WO2016117081A1 (en) * 2015-01-22 2016-07-28 株式会社クボタ Method for cleaning tubular filtration membrane
WO2016117082A1 (en) * 2015-01-22 2016-07-28 株式会社クボタ Water purification system

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Publication number Priority date Publication date Assignee Title
JPS4834783A (en) * 1971-09-06 1973-05-22
JPS5432179A (en) * 1977-08-15 1979-03-09 Ebara Infilco Co Ltd Controlling method for operation of fresh water making apparatus
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JPH07251041A (en) * 1994-03-16 1995-10-03 Ngk Insulators Ltd Membrane separation apparatus and washing method therefor
JP2002011333A (en) * 2000-06-29 2002-01-15 Kuraray Co Ltd Method and apparatus for washing hollow fiber membrane module
JP2003265935A (en) * 2002-03-15 2003-09-24 Suido Kiko Kaisha Ltd Membrane filtration module cleaning method, membrane filtration apparatus, and chemical-used cleaning apparatus
JP2006088017A (en) * 2004-09-22 2006-04-06 Japan Organo Co Ltd Water treatment apparatus and its operating method
JP2007216102A (en) * 2006-02-14 2007-08-30 Mitsubishi Heavy Ind Ltd Filtering device, and membrane washing method of this filtering device
JP2011104548A (en) * 2009-11-19 2011-06-02 Atlas:Kk Liquid cleaning apparatus
WO2016117081A1 (en) * 2015-01-22 2016-07-28 株式会社クボタ Method for cleaning tubular filtration membrane
WO2016117082A1 (en) * 2015-01-22 2016-07-28 株式会社クボタ Water purification system

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