JPH04161232A - Cleaning of membrane module - Google Patents
Cleaning of membrane moduleInfo
- Publication number
- JPH04161232A JPH04161232A JP2288202A JP28820290A JPH04161232A JP H04161232 A JPH04161232 A JP H04161232A JP 2288202 A JP2288202 A JP 2288202A JP 28820290 A JP28820290 A JP 28820290A JP H04161232 A JPH04161232 A JP H04161232A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- membrane module
- tank
- membrane
- tubular 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.)
- Pending
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 69
- 238000004140 cleaning Methods 0.000 title claims abstract description 53
- 239000000126 substance Substances 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 238000000926 separation method Methods 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 15
- 230000000813 microbial effect Effects 0.000 claims description 3
- 239000012466 permeate Substances 0.000 claims 2
- 238000005406 washing Methods 0.000 claims 1
- 239000003599 detergent Substances 0.000 abstract 2
- 239000000243 solution Substances 0.000 description 18
- 239000000919 ceramic Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、浸漬型の膜モジュールを洗浄液で洗浄する膜
モジュールの洗浄方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a membrane module cleaning method for cleaning a submerged membrane module with a cleaning liquid.
従来の技術
近年では、複数のセラミックチューブ膜を並列に配設し
てなる膜モジュールを槽内に浸漬し、セラミックチュー
ブ膜内を吸引状態として、汚水をろ過処理のみ、または
微生物処理およびろ過処理等することか既に実用化され
ている。この膜モジュールの各セラミックチューブ膜表
面には、ろ過処理に伴いケーキ層が付着するため、第4
図に示すように、定期的に膜モジュール1を洗浄液とし
ての薬液2(例えは希塩酸等の酸、もしくはアルカリ溶
液等)に浸けてケーキ層3を溶解させながら洗浄してい
た。Conventional technology In recent years, a membrane module consisting of a plurality of ceramic tube membranes arranged in parallel is immersed in a tank, and the inside of the ceramic tube membrane is in a suction state to process wastewater for only filtration treatment, or for microbial treatment and filtration treatment. It has already been put into practical use. Because a cake layer adheres to the surface of each ceramic tube membrane of this membrane module during the filtration process, the fourth
As shown in the figure, the membrane module 1 was periodically immersed in a chemical solution 2 (for example, an acid such as dilute hydrochloric acid, or an alkaline solution) as a cleaning solution to dissolve the cake layer 3 while cleaning.
発明か解決しようとする課題
しかしなから、上記従来の膜モジュールの洗浄方法では
、単に膜モジュール1を薬液2に浸けるだけであるため
、第5図に示すように、セラミックチューブ膜4か互い
に近接状態で配置されている膜モジュールlの内部箇所
では、薬液2か膜表面の汚染物(ケーキ層3)等で消費
されてしまい、膜内面まで行き渡らず洗浄効果か少ない
という問題があった。However, in the conventional membrane module cleaning method described above, the membrane module 1 is simply immersed in the chemical solution 2, so as shown in FIG. In the interior of the membrane module 1, which is placed in this state, the chemical solution 2 is consumed by contaminants (cake layer 3) on the membrane surface, etc., and does not reach the inner surface of the membrane, resulting in a problem that the cleaning effect is low.
本発明は上記問題を解決するもので、膜モジュールの内
部まで効果的に洗浄できる膜モジュールの洗浄方法を提
供することを目的とするものである。The present invention solves the above problems, and aims to provide a membrane module cleaning method that can effectively clean the inside of the membrane module.
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、膜モジュールに配
設された複数のチューブ状膜の内部もしくは外部に洗浄
液を供給して、チューブ状膜の内部から外部へもしくは
外部から内部へ洗浄液を通過させるものである。Means for Solving the Problems In order to solve the above problems, the present invention supplies a cleaning liquid to the inside or outside of a plurality of tubular membranes arranged in a membrane module, and cleans the tubular membranes from the inside to the outside. This allows cleaning liquid to pass from the outside to the inside.
作用
上記構成により、チューブ状膜表面に付着物かあっても
、洗浄液は膜の表面および内部を強制的に通過させられ
るので、洗浄液か次第に膜内部に行き渡り、膜表面の付
着物は効果的に除去される。Effect With the above structure, even if there is any deposit on the surface of the tubular membrane, the cleaning liquid is forced to pass through the surface and inside of the membrane, so the cleaning solution gradually spreads inside the membrane and effectively removes the deposit on the membrane surface. removed.
実施例 以下、本発明の一実施例を図面に基つき説明する。Example An embodiment of the present invention will be described below with reference to the drawings.
第1図において、11は膜洗浄用の薬液12か貯留され
た洗浄槽て、この洗浄槽11には、洗浄される膜モジュ
ール13か浸けられている。膜モジュール13は、ポン
プ14を介して、洗浄槽ll内に配置されたフィルター
15か接続され、膜モジュール13において複数列に並
設された各セラミックチューブ膜16(第2図参照)の
内部には、フィルター15によってろ過された薬液12
が供給されるようになっている。In FIG. 1, reference numeral 11 denotes a cleaning tank in which a chemical solution 12 for membrane cleaning is stored, and a membrane module 13 to be cleaned is immersed in this cleaning tank 11. The membrane module 13 is connected to a filter 15 arranged in a cleaning tank 11 through a pump 14, and is connected to the inside of each ceramic tube membrane 16 (see FIG. 2) arranged in a plurality of rows in the membrane module 13. is the chemical solution 12 filtered by the filter 15
is being supplied.
上記構成において、膜モジュール13を洗浄する場合に
は、ポンプ14を駆動させることにより、清浄な薬液1
2かセラミックチューブ膜16の内部から外部(第3図
におけるa方向)へ通過して流れ、このろ過使用時とは
逆の方向への薬液12の流れによって、セラミックチュ
ーブ膜16の表面に付着したケーキ層17は効果的に除
去される。In the above configuration, when cleaning the membrane module 13, the pump 14 is driven to clean the chemical solution 1.
2 flows from the inside of the ceramic tube membrane 16 to the outside (direction a in FIG. 3), and due to the flow of the chemical solution 12 in the opposite direction to that during filtration, it adheres to the surface of the ceramic tube membrane 16. Cake layer 17 is effectively removed.
なお、ケーキ層17を含有した洗浄槽11内の薬液12
はフィルター15によってろ過されて清浄とされ、再度
洗浄液として用いられるか、フィルター15を設けずに
、汚れた洗浄液を交換してもよい。Note that the chemical solution 12 in the cleaning tank 11 containing the cake layer 17
may be filtered by the filter 15 to be cleaned and used again as a cleaning solution, or the dirty cleaning solution may be replaced without providing the filter 15.
また、上記実施例のように膜モジュール13を薬液洗浄
槽11に浸漬して薬液洗浄してもよいし、膜分離槽をい
くつかに分室できる方式の場合は、分室できる膜浸漬槽
(洗浄槽)を他とはバルブや堰等で切離し、1室だけを
この方式で薬液洗浄してもよい。In addition, as in the above embodiment, the membrane module 13 may be immersed in the chemical cleaning tank 11 for chemical cleaning, or in the case of a system in which the membrane separation tank can be divided into several compartments, the membrane immersion tank (cleaning tank ) may be separated from the others by a valve or dam, and only one chamber may be cleaned with a chemical solution using this method.
また、上記実施例では、薬液をセラミックチューブ膜の
内部から外部へ通過させる場合を述べたが、逆に薬液を
セラミックチューブ膜の外部から内部(第3図における
b方向)へ通過させてもよい。Furthermore, in the above embodiment, the case where the chemical solution is passed from the inside of the ceramic tube membrane to the outside has been described, but it is also possible to pass the chemical solution from the outside of the ceramic tube membrane to the inside (direction b in FIG. 3). .
発明の効果
以上のように、本発明によれば、洗浄液をチューブ状膜
の内部から外部へ、またはその逆方向に流すことにより
、チューブ状膜の表面に付着したケーキ層を効果的に除
去でき、膜モジュールを内部まで良好にかつ能率的に洗
浄することかできる。Effects of the Invention As described above, according to the present invention, the cake layer attached to the surface of the tubular membrane can be effectively removed by flowing the cleaning liquid from the inside to the outside of the tubular membrane or in the opposite direction. , it is possible to clean the membrane module well and efficiently to the inside.
第1図は本発明の一実施例に係る膜モジュールの洗浄方
法に用いる洗浄装置の構成図、第2図は同洗浄方法の作
用を説明する膜モジュールの概略断面図、第3図は同洗
浄方法における膜モジュールおよび薬液の流れの作用を
説明する図、第4図は従来の膜モジュールの洗浄方法に
用いる洗浄装置の構成図、第5図は同従来の洗浄方法の
作用を説明する膜モジュールの概略断面図である。
11・・・洗浄槽、12・・・薬液(洗浄液)、13・
・・膜モジュール、14・・・ポンプ、15・・・フィ
ルター、16・・・セラミックチューブ膜、17・・・
ケーキ層(付着物)、a、b・・・薬液の流れ方向。FIG. 1 is a configuration diagram of a cleaning device used in a membrane module cleaning method according to an embodiment of the present invention, FIG. 2 is a schematic sectional view of a membrane module for explaining the action of the same cleaning method, and FIG. 3 is a same cleaning method. Figure 4 is a block diagram of a cleaning device used in the conventional membrane module cleaning method, and Figure 5 is a diagram illustrating the membrane module and the effect of the flow of the chemical solution in the method. FIG. 11...Cleaning tank, 12...Chemical solution (cleaning liquid), 13.
... Membrane module, 14... Pump, 15... Filter, 16... Ceramic tube membrane, 17...
Cake layer (deposit), a, b...flow direction of the chemical solution.
Claims (1)
前記槽内より取り出され、薬液洗浄槽に浸漬された浸漬
型の膜モジュールの薬液洗浄液による洗浄方法であって
、膜モジュールに配設された複数のチューブ状膜の内部
に洗浄液を供給して、チューブ状膜の内部から外部へ、
すなわち透過液の流れとは逆方向に洗浄液を通過させ、
チューブ状膜表面の付着物を洗浄液の流れにより除去す
ることを特徴とする膜モジュールの洗浄方法。 2、微生物槽または膜分離槽内に浸漬された、もしくは
前記槽内より取り出され、薬液洗浄槽に浸漬された浸漬
型の膜モジュールの薬液洗浄液による洗浄方法であって
、膜モジュールに配設された複数のチューブ状膜の外部
に洗浄液を供給して、チューブ状膜の外部から内部へ、
すなわち透過液の流れと同方向に洗浄液を通過させ、チ
ューブ状膜表面の付着物を洗浄液の流れにより除去する
ことを特徴とする膜モジュールの洗浄方法。[Scope of Claims] 1. A method for cleaning a submerged membrane module immersed in a microbial tank or a membrane separation tank, or taken out from the tank and immersed in a chemical cleaning tank, using a chemical cleaning solution, comprising: A cleaning solution is supplied to the inside of the plurality of tubular membranes arranged in the membrane module, and from the inside of the tubular membrane to the outside,
In other words, the cleaning solution is passed in the opposite direction to the flow of the permeate,
A method for cleaning a membrane module, characterized in that deposits on the surface of a tubular membrane are removed by a flow of cleaning liquid. 2. A method for cleaning a submerged membrane module immersed in a microbial tank or a membrane separation tank, or taken out from the tank and immersed in a chemical cleaning tank, using a chemical cleaning solution, the method comprising: A cleaning solution is supplied to the outside of the plurality of tubular membranes, and the washing liquid is supplied to the outside of the tubular membranes from the outside to the inside.
That is, a method for cleaning a membrane module, which comprises passing a cleaning liquid in the same direction as the flow of the permeate, and removing deposits on the surface of the tubular membrane by the flow of the cleaning liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2288202A JPH04161232A (en) | 1990-10-25 | 1990-10-25 | Cleaning of membrane module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2288202A JPH04161232A (en) | 1990-10-25 | 1990-10-25 | Cleaning of membrane module |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04161232A true JPH04161232A (en) | 1992-06-04 |
Family
ID=17727140
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2288202A Pending JPH04161232A (en) | 1990-10-25 | 1990-10-25 | Cleaning of membrane module |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04161232A (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50153778A (en) * | 1974-06-03 | 1975-12-11 | ||
JPS5317581A (en) * | 1976-07-31 | 1978-02-17 | Toshiba Machine Co Ltd | Method and apparatus for cleaning semipermeable membrane |
JPS58104612A (en) * | 1981-07-06 | 1983-06-22 | Japan Organo Co Ltd | Method for backwashing ultrafiltration membrane apparatus used in treatment of sweet water |
JPS61129094A (en) * | 1984-11-26 | 1986-06-17 | Nitto Electric Ind Co Ltd | Apparatus for treating membrane |
-
1990
- 1990-10-25 JP JP2288202A patent/JPH04161232A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50153778A (en) * | 1974-06-03 | 1975-12-11 | ||
JPS5317581A (en) * | 1976-07-31 | 1978-02-17 | Toshiba Machine Co Ltd | Method and apparatus for cleaning semipermeable membrane |
JPS58104612A (en) * | 1981-07-06 | 1983-06-22 | Japan Organo Co Ltd | Method for backwashing ultrafiltration membrane apparatus used in treatment of sweet water |
JPS61129094A (en) * | 1984-11-26 | 1986-06-17 | Nitto Electric Ind Co Ltd | Apparatus for treating membrane |
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