JPH07124448A - Chemicals washing method for ceramic film - Google Patents

Chemicals washing method for ceramic film

Info

Publication number
JPH07124448A
JPH07124448A JP5275835A JP27583593A JPH07124448A JP H07124448 A JPH07124448 A JP H07124448A JP 5275835 A JP5275835 A JP 5275835A JP 27583593 A JP27583593 A JP 27583593A JP H07124448 A JPH07124448 A JP H07124448A
Authority
JP
Japan
Prior art keywords
membrane
ceramic
chemical
film
ceramic membrane
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
JP5275835A
Other languages
Japanese (ja)
Inventor
Katsuro Ishihara
勝郎 石原
Kanji Tokushima
幹治 徳島
Yoshihisa Narukami
善久 鳴上
Ichiro Nagai
一郎 永井
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP5275835A priority Critical patent/JPH07124448A/en
Publication of JPH07124448A publication Critical patent/JPH07124448A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a chemicals washing method for a ceramic film, by which a washing effect is high, and also, a washing operation can be executed easily. CONSTITUTION:Liquid chemicals 12 which are led into a treating vessel 1 is sucked and filtered by a ceramic film 4, or liquid chemicals 13 are fed forcibly into the inside of the film 4. Accordingly, since chemicals washing can be executed not only from the outside of the film but also from the inside, a high washing effect is obtained.

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、浄水処理、下水処理、
廃水処理などにおいて使用される浸漬型膜分離装置のセ
ラミック膜の薬品洗浄方法に関する。
BACKGROUND OF THE INVENTION The present invention relates to water purification treatment, sewage treatment,
The present invention relates to a chemical cleaning method for a ceramic membrane of an immersion type membrane separator used in wastewater treatment and the like.

【0002】[0002]

【従来の技術】従来、浄水処理、下水処理、廃水処理な
どにおいて固液分離のために使用されている浸漬型膜分
離装置には、たとえば図2に示したようなものがある。
浸漬型膜分離装置は、処理槽1内の被処理水2に浸漬し
て複数の膜モジュール3を設けており、各膜モジュール
3の内部に複数のセラミック膜4を適当間隔で並列に配
置するとともに、セラミック膜4の内側に形成された膜
透過液流路に接続する集水管5を設けている。集水管5
には通水弁6を介して吸引ポンプ7が接続されていて、
この吸引ポンプ7によって集水管5を通して膜透過液流
路に負圧をかけることで、セラミック膜4により被処理
水2を固液分離し、膜透過液たる処理水8を取り出して
処理水槽9に貯留している。
2. Description of the Related Art Conventionally, there is an immersion type membrane separation apparatus as shown in FIG. 2 which is used for solid-liquid separation in water purification, sewage treatment, wastewater treatment and the like.
The immersion type membrane separation device is provided with a plurality of membrane modules 3 by being immersed in the water to be treated 2 in the treatment tank 1, and a plurality of ceramic membranes 4 are arranged in parallel inside each membrane module 3 at appropriate intervals. At the same time, a water collecting pipe 5 is provided which is connected to the membrane permeate liquid passage formed inside the ceramic membrane 4. Water collection pipe 5
Is connected to a suction pump 7 via a water passage valve 6,
By applying a negative pressure to the membrane permeate flow path through the water collection pipe 5 by this suction pump 7, the water to be treated 2 is separated into solid and liquid by the ceramic membrane 4, and the treated water 8 as the membrane permeate is taken out to the treated water tank 9. It is stored.

【0003】そして、膜の目づまりを防止するために、
定期的に、塩酸や次亜塩素酸ナトリウムなどの薬品によ
ってセラミック膜4の洗浄を行っている。すなわち、処
理槽1または薬品洗浄槽に、約1000ppmの塩酸溶
液および有効塩素濃度約1000ppmの次亜塩素酸ナ
トリウム溶液をそれぞれ導入し、セラミック膜4を塩酸
溶液中に2時間以上、次亜塩素酸ナトリウム溶液中に1
6時間以上浸漬することにより、膜面に付着したケーキ
層やゲル層を除去している。
In order to prevent clogging of the film,
The ceramic film 4 is regularly cleaned with a chemical such as hydrochloric acid or sodium hypochlorite. That is, a hydrochloric acid solution having a concentration of about 1000 ppm and a sodium hypochlorite solution having an effective chlorine concentration of about 1000 ppm were introduced into the treatment tank 1 or the chemical cleaning tank, and the ceramic membrane 4 was placed in the hydrochloric acid solution for 2 hours or more and the hypochlorous acid 1 in sodium solution
The cake layer and gel layer attached to the film surface are removed by immersing for 6 hours or more.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記の
ような従来の洗浄方法は、セラミック膜を薬品溶液に浸
漬するだけであるため、膜の外側は薬品に接触するもの
の膜の内側までは薬品は浸透しにくく、洗浄が十分でな
かった。また、塩酸と次亜塩素酸ナトリウムの2種類の
薬品を使用するため、洗浄操作が複雑であった。
However, in the conventional cleaning method as described above, since the ceramic membrane is only immersed in the chemical solution, the outer side of the membrane is in contact with the chemical but the inner side of the membrane is not exposed to the chemical. Difficult to penetrate and was not washed sufficiently. Further, since two kinds of chemicals, hydrochloric acid and sodium hypochlorite, are used, the cleaning operation is complicated.

【0005】本発明は上記問題を解決するもので、洗浄
効果が高くかつ洗浄操作が容易なセラミック膜の薬品洗
浄方法を提供することを目的とするものである。
The present invention solves the above problems, and an object of the present invention is to provide a chemical cleaning method for a ceramic membrane, which has a high cleaning effect and is easy to clean.

【0006】[0006]

【課題を解決するための手段】上記問題を解決するため
に本発明は、浸漬型膜分離装置のセラミック膜の薬品洗
浄方法であって、処理槽内に導入した薬液をセラミック
膜により吸引濾過するか、あるいはセラミック膜の内側
に薬液を圧入する少なくともいずれかの工程を行うこと
により、薬液によって膜の表面および内部を洗浄するこ
とを特徴とする。
In order to solve the above problems, the present invention relates to a method for cleaning chemicals in a ceramic membrane of an immersion type membrane separator, in which a chemical introduced into a treatment tank is suction-filtered by the ceramic membrane. Alternatively, the surface and the inside of the film are washed with the chemical liquid by performing at least one of the steps of press-fitting the chemical liquid into the inside of the ceramic membrane.

【0007】また本発明は、薬液が500〜3000p
pmの有効塩素濃度を有することを特徴とする。さらに
本発明は、セラミック膜の下方に設置した散気手段より
空気を曝気しながら洗浄を行うことを特徴とする。
In the present invention, the chemical solution is 500 to 3000 p
It is characterized by having an effective chlorine concentration of pm. Further, the present invention is characterized in that cleaning is performed while aerating air from an air diffusing means installed below the ceramic membrane.

【0008】[0008]

【作用】上記の構成により、膜の外側から内側に向け
て、あるいは膜の内側から外側へ向けて圧送される薬液
によって、膜の表面および内部を効果的に洗浄すること
ができる。また、セラミック膜の下方に設置した散気手
段より空気を曝気しながら洗浄を行うことによって、洗
浄効果が上昇する。
With the above structure, the surface and the inside of the membrane can be effectively cleaned by the chemical solution that is pumped from the outside to the inside of the membrane or from the inside to the outside of the membrane. Further, the cleaning effect is enhanced by performing the cleaning while aerating the air from the air diffuser installed below the ceramic film.

【0009】[0009]

【実施例】以下、本発明の一実施例を図1を参照しなが
ら説明する。図1における浸漬型膜分離装置は、上で図
2を用いて説明した従来の膜分離装置とほぼ同じなの
で、同一の構成および同一の作用を有する部材に同じ符
号を付してその説明を省略する。ここで、本発明の膜分
離装置が従来の膜分離装置と異なるのは、処理水8の管
路を通水弁6の上流側で分岐させ、逆洗弁10と逆洗ポ
ンプ11を介装して処理水槽9に連結して、処理水槽9
内の処理水8を膜モジュール3のセラミック膜4の内側
に圧送できる構成とした点である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. Since the submerged membrane separation apparatus in FIG. 1 is almost the same as the conventional membrane separation apparatus described with reference to FIG. 2 above, members having the same configuration and the same action are denoted by the same reference numerals and the description thereof is omitted. To do. Here, the membrane separation device of the present invention is different from the conventional membrane separation device in that the pipeline of the treated water 8 is branched on the upstream side of the water valve 6 and the backwash valve 10 and the backwash pump 11 are installed. And connect to the treated water tank 9,
The point is that the treated water 8 therein can be pressure-fed to the inside of the ceramic membrane 4 of the membrane module 3.

【0010】上記構成において、固液分離を行うとき
は、逆洗弁10を閉じて通水弁6を開き、吸引ポンプ7
を作用させてセラミック膜4の内側の透過液流路を負圧
とすることにより、セラミック膜4によって被処理水2
を固液分離する。膜透過した処理水8は、処理水槽9に
貯留する。
In the above structure, when solid-liquid separation is performed, the backwash valve 10 is closed, the water passage valve 6 is opened, and the suction pump 7
By making the permeated liquid flow path inside the ceramic membrane 4 to have a negative pressure,
Solid-liquid separation. The treated water 8 that has permeated the membrane is stored in the treated water tank 9.

【0011】そして、定期的にセラミック膜4を洗浄す
るに際しては、処理槽1内の被処理水2に次亜塩素酸ナ
トリウムを添加して槽内に有効塩素濃度約1000pp
mの次亜塩素酸ナトリウム溶液12を調製し、この溶液
12を上記と同様にしてセラミック膜4により吸引濾過
する浸漬洗浄を行う。これにより、セラミック膜4に付
着したケーキ層やゲル層などは、膜の外側から内側へ向
けて圧送される次亜塩素酸ナトリウム溶液12の作用に
より除去される。
When the ceramic membrane 4 is to be washed regularly, sodium hypochlorite is added to the water 2 to be treated in the treatment tank 1 so that the effective chlorine concentration in the tank is about 1000 pp.
A sodium hypochlorite solution 12 of m is prepared, and the solution 12 is subjected to immersion cleaning by suction filtration through the ceramic membrane 4 in the same manner as above. As a result, the cake layer, gel layer, and the like attached to the ceramic film 4 are removed by the action of the sodium hypochlorite solution 12 that is pressure-fed from the outside to the inside of the film.

【0012】また、処理水槽9内の処理水8に次亜塩素
酸ナトリウムを添加して槽内に有効塩素濃度約1000
ppmの次亜塩素酸ナトリウム溶液13を調製し、通水
弁6を閉じるとともに逆洗弁10を開き、槽9内の溶液
13を逆洗ポンプ11によりセラミック膜4の内側へ圧
送する逆洗操作を、上記の浸漬洗浄と並行して30分か
ら60分に1回程度行う。これにより、膜の内側から外
側へ向けて圧送される次亜塩素酸ナトリウム溶液13に
よってセラミック膜4の内側も洗浄できるので、洗浄効
果が上がる。
Further, sodium hypochlorite is added to the treated water 8 in the treated water tank 9 to obtain an effective chlorine concentration of about 1000 in the tank.
A backwash operation in which a ppm sodium hypochlorite solution 13 is prepared, the water flow valve 6 is closed and the backwash valve 10 is opened, and the solution 13 in the tank 9 is pressure-fed to the inside of the ceramic membrane 4 by the backwash pump 11. Is performed about once every 30 to 60 minutes in parallel with the above immersion cleaning. As a result, the inside of the ceramic film 4 can be cleaned by the sodium hypochlorite solution 13 that is pressure-fed from the inside to the outside of the film, so that the cleaning effect is improved.

【0013】上記の方法によれば、次亜塩素酸ナトリウ
ム溶液1種類を用いてセラミック膜4を効果的に洗浄で
きるので、洗浄操作が簡単になる。このときの次亜塩素
酸ナトリウム溶液の濃度は、有効塩素濃度約500〜3
000ppm、好ましくは約1000ppmとすればよ
い。
According to the above method, the ceramic membrane 4 can be effectively cleaned using one type of sodium hypochlorite solution, so that the cleaning operation is simplified. At this time, the concentration of the sodium hypochlorite solution is about 500 to 3 available chlorine.
It may be 000 ppm, preferably about 1000 ppm.

【0014】また、図示したように、セラミック膜4の
下方に槽外のブロワ14に接続して散気手段15を設置
し、この散気手段15より空気を曝気すれば、曝気空気
の気泡により形成される上昇液流によってセラミック膜
4の膜面が洗浄されるので、洗浄効果が上昇する。
Further, as shown in the figure, if the air diffuser 15 is installed below the ceramic membrane 4 and connected to the blower 14 outside the tank, and air is aerated from the air diffuser 15, air bubbles will be generated by the aerated air. Since the film surface of the ceramic film 4 is cleaned by the rising liquid flow that is formed, the cleaning effect is increased.

【0015】以下に、上記本発明の方法によるセラミッ
ク膜の薬品洗浄試験結果を示す。この試験においては、
下水処理場膜分離装置のセラミック膜を薬液(Naclo- 1
000PPM)により一昼夜洗浄した。曝気・逆洗の条件は上
記と同じであり、吸引は薬品洗浄終了前の4時間のみ行
った。薬品洗浄前および薬品洗浄後に、セラミック膜の
純水透過量(m3/m2d)を測定した。結果は表1に示した
通りであり、薬品洗浄前の汚染したセラミック膜の純水
透過量は2.2(m3/m2d)であったが、薬品洗浄後に1
9.2(m3/m2d)まで回復した。なお、新品のセラミッ
ク膜の純水透過量は19〜20(m3/m2d)である。
The chemical cleaning test results of the ceramic film according to the method of the present invention will be shown below. In this test,
Chemical solution (Naclo-1
(000 PPM) and washed overnight. The conditions of aeration and backwash were the same as above, and suction was performed only for 4 hours before the completion of chemical cleaning. The pure water permeation amount (m 3 / m 2 d) of the ceramic membrane was measured before and after chemical cleaning. The results are shown in Table 1. The pure water permeation amount of the contaminated ceramic membrane before chemical cleaning was 2.2 (m 3 / m 2 d), but it was 1 after chemical cleaning.
It recovered to 9.2 (m 3 / m 2 d). The pure water permeation amount of the new ceramic membrane is 19 to 20 (m 3 / m 2 d).

【0016】[0016]

【表1】 [Table 1]

【0017】[0017]

【発明の効果】以上のように本発明によれば、処理槽内
に導入した薬液をセラミック膜により吸引濾過するか、
あるいはセラミック膜の内側に薬液を圧入することによ
り、膜の外側だけでなく膜の内側からも膜付着物を洗浄
除去できるので、薬液に浸漬するだけの従来の洗浄方法
に比べて高い洗浄効果が得られる。このとき、1種類の
薬液、好ましくは次亜塩素酸ナトリウム溶液によって洗
浄できるので、洗浄操作が簡単になる。また、セラミッ
ク膜の下方より空気を曝気しながら洗浄を行うことによ
って、さらに高い洗浄効果が得られる。
As described above, according to the present invention, the chemical introduced into the processing tank is suction-filtered by a ceramic membrane,
Alternatively, by pressing the chemical solution into the inside of the ceramic membrane, it is possible to wash and remove the film deposits not only from the outside of the membrane but also from the inside of the membrane, so a higher cleaning effect than the conventional cleaning method of just immersing in the chemical solution is achieved. can get. At this time, the washing operation can be simplified because the washing can be performed with one kind of chemical solution, preferably sodium hypochlorite solution. Further, by performing cleaning while aerating the air from below the ceramic film, a higher cleaning effect can be obtained.

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

【図1】本発明の洗浄方法が行われる一実施例の膜分離
装置の全体構成を示した説明図である。
FIG. 1 is an explanatory diagram showing an overall configuration of a membrane separation device of an embodiment in which a cleaning method of the present invention is performed.

【図2】従来例の膜分離装置の構成を示した説明図であ
る。
FIG. 2 is an explanatory diagram showing a configuration of a conventional membrane separation device.

【符号の説明】[Explanation of symbols]

1 処理槽 4 セラミック膜 12,13 次亜塩素酸ナトリウム溶液(薬液) 15 散気手段 1 Treatment tank 4 Ceramic membrane 12,13 Sodium hypochlorite solution (chemical solution) 15 Aeration means

───────────────────────────────────────────────────── フロントページの続き (72)発明者 永井 一郎 大阪府大阪市西淀川区西島2丁目1番地6 号 株式会社クボタ新淀川工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Ichiro Nagai 2-6-6 Nishijima, Nishiyodogawa-ku, Osaka-shi, Osaka Kubota Shin-Yodogawa factory

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 浸漬型膜分離装置のセラミック膜の薬品
洗浄方法であって、処理槽内に導入した薬液をセラミッ
ク膜により吸引濾過するか、あるいはセラミック膜の内
側に薬液を圧入する少なくともいずれかの工程を行うこ
とにより、薬液によって膜の表面および内部を洗浄する
ことを特徴とするセラミック膜の薬品洗浄方法。
1. A chemical cleaning method for a ceramic membrane of an immersion type membrane separator, which comprises sucking and filtering a chemical solution introduced into a treatment tank through a ceramic membrane, or at least inserting a chemical solution inside the ceramic membrane. A chemical cleaning method for a ceramic film, characterized in that the surface and the inside of the film are cleaned with a chemical solution by performing the step of.
【請求項2】 薬液が500〜3000ppmの有効塩
素濃度を有することを特徴とする請求項1記載のセラミ
ック膜の薬品洗浄方法。
2. The chemical cleaning method for a ceramic membrane according to claim 1, wherein the chemical solution has an effective chlorine concentration of 500 to 3000 ppm.
【請求項3】 セラミック膜の下方に設置した散気手段
より空気を曝気しながら洗浄を行うことを特徴とする請
求項1または請求項2のいずれかに記載のセラミック膜
の薬品洗浄方法。
3. The chemical cleaning method for a ceramic film according to claim 1, wherein the cleaning is performed while aerating air from an air diffusing unit installed below the ceramic film.
JP5275835A 1993-11-05 1993-11-05 Chemicals washing method for ceramic film Pending JPH07124448A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5275835A JPH07124448A (en) 1993-11-05 1993-11-05 Chemicals washing method for ceramic film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5275835A JPH07124448A (en) 1993-11-05 1993-11-05 Chemicals washing method for ceramic film

Publications (1)

Publication Number Publication Date
JPH07124448A true JPH07124448A (en) 1995-05-16

Family

ID=17561099

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5275835A Pending JPH07124448A (en) 1993-11-05 1993-11-05 Chemicals washing method for ceramic film

Country Status (1)

Country Link
JP (1) JPH07124448A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012147534A1 (en) * 2011-04-25 2012-11-01 日本碍子株式会社 Method for washing ceramic filter
CN110026089A (en) * 2019-05-23 2019-07-19 广西碧清源环保投资有限公司 A kind of cleaning device and cleaning method of earthenware slab membrane module

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04131182A (en) * 1990-09-20 1992-05-01 Ebara Infilco Co Ltd Biological treating device for organic polluted water
JPH0670825U (en) * 1993-03-17 1994-10-04 石垣機工株式会社 Undiluted liquid filtration device with internal pressure type filtration membrane
JPH07116482A (en) * 1993-10-28 1995-05-09 Kurita Water Ind Ltd Submerged type membrane separation device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04131182A (en) * 1990-09-20 1992-05-01 Ebara Infilco Co Ltd Biological treating device for organic polluted water
JPH0670825U (en) * 1993-03-17 1994-10-04 石垣機工株式会社 Undiluted liquid filtration device with internal pressure type filtration membrane
JPH07116482A (en) * 1993-10-28 1995-05-09 Kurita Water Ind Ltd Submerged type membrane separation device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012147534A1 (en) * 2011-04-25 2012-11-01 日本碍子株式会社 Method for washing ceramic filter
CN103501879A (en) * 2011-04-25 2014-01-08 日本碍子株式会社 Method for washing ceramic filter
JP6060074B2 (en) * 2011-04-25 2017-01-11 日本碍子株式会社 Cleaning method of ceramic filter
US10166512B2 (en) 2011-04-25 2019-01-01 Ngk Insulators, Ltd. Method for cleaning ceramic filter
CN110026089A (en) * 2019-05-23 2019-07-19 广西碧清源环保投资有限公司 A kind of cleaning device and cleaning method of earthenware slab membrane module

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