JPH06226065A - Membrane washing method - Google Patents
Membrane washing methodInfo
- Publication number
- JPH06226065A JPH06226065A JP3605293A JP3605293A JPH06226065A JP H06226065 A JPH06226065 A JP H06226065A JP 3605293 A JP3605293 A JP 3605293A JP 3605293 A JP3605293 A JP 3605293A JP H06226065 A JPH06226065 A JP H06226065A
- Authority
- JP
- Japan
- Prior art keywords
- water
- membrane
- washing
- valve
- cleaning
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
(57)【要約】
【目的】 水処理装置の固液分離膜の洗浄を行うに際
し,処理水の使用を最少限の量により,かつ効率良く行
うことを目的とする。
【構成】 分離膜を空気による洗浄と水による逆洗洗浄
を同時に行うことにより,濁質等を完全に剥離し,その
剥離分を完全に系外に原水を使用して押し出すことがで
きるように構成する。
(57) [Summary] [Purpose] The purpose is to efficiently use the treated water with a minimum amount when cleaning the solid-liquid separation membrane of the water treatment device. [Structure] The separation membrane can be completely exfoliated by simultaneously performing air washing and back washing with water so that the exfoliated portion can be completely pushed out of the system using raw water. Constitute.
Description
【0001】[0001]
【産業上の利用分野】この発明は,水処理装置の固液分
離装置に係り,特にマイクロフィルタ膜,ウルトラフィ
ルタ膜の洗浄方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid-liquid separation device for a water treatment device, and more particularly to a method for cleaning a microfilter membrane and an ultrafilter membrane.
【0002】[0002]
【従来の技術】従来は,膜表面を空気によるバブリング
等で洗浄する方法,又,水による逆流洗浄を行い,その
後,ドレンにて濁質を系外に排出していた。2. Description of the Related Art Conventionally, a method of washing the surface of a membrane by bubbling with air or the like, or backwashing with water, and then draining turbidity out of the system.
【0003】しかし本方法では,膜表面に付着した濁質
等を剥離させることが不十分であり,又,ドレンでは,
系外に完全に濁質等を排出することが困難である。又,
処理水を用いて系外へ排出する方法では水回収率が下が
るという欠点がある。However, according to this method, it is insufficient to remove the turbidity or the like adhering to the film surface, and with the drain,
It is difficult to completely discharge suspended matter out of the system. or,
The method of discharging treated water to the outside of the system has a drawback that the water recovery rate is lowered.
【0004】[0004]
【発明が解決しようとする課題】本発明は,膜の洗浄を
処理水の使用を最少限量で,効率良く行うため,空気洗
浄と処理水の逆流洗浄を同時に行い,発生した洗浄排水
を原水で系外へ押し出す様にしたもので,膜が長期安定
処理を維持する洗浄方法を提供するにある。SUMMARY OF THE INVENTION According to the present invention, in order to efficiently wash a membrane with a minimum amount of treated water and efficiently perform backwashing with air and backwashing with treated water, the generated washing wastewater is treated with raw water. It is designed to be pushed out of the system, and it is to provide a cleaning method that keeps the membrane stable for a long period of time.
【0005】[0005]
【課題を解決するための手段】本発明は,空気による洗
浄と水による逆流洗浄を同時に行うことにより,濁質等
を完全に剥離し,それを完全に系外に原水を使用して押
し出すものとし,洗浄に使用する処理水を最少限量で,
効率良い洗浄方法として構成したものである。According to the present invention, the washing with air and the backwashing with water are carried out at the same time to completely remove turbidity and push it out of the system by using raw water. The minimum amount of treated water used for cleaning is
This is configured as an efficient cleaning method.
【0006】[0006]
【実 施 例】実施例を図1に基づき説明する。ろ過工
程では,原水は,供給ポンプ1により,供給弁10を通
り膜モジュール2に供給される。原水は膜モジュール内
で固液分離され,膜透過した処理水は処理水弁6を通り
原水槽8に集められる。また膜で透過しなかった水は,
循環水弁を通り返送される。[Example] An example will be described with reference to FIG. In the filtration step, raw water is supplied to the membrane module 2 by the supply pump 1 through the supply valve 10. The raw water is solid-liquid separated in the membrane module, and the treated water that has permeated the membrane passes through the treated water valve 6 and is collected in the raw water tank 8. Water that did not permeate through the membrane
Returned through the circulating water valve.
【0007】洗浄時は,まず供給ポンプ停止し,供給水
弁,処理水弁を閉じ,洗浄水弁5を開ける。その後,空
気洗浄弁3,逆洗水弁7を開け,空気洗浄ブロワ9,逆
洗ポンプ11を運転し,膜表面の濁質等を剥離する。次
に,剥離した濁質等を膜モジュール内から系外に排出す
るため,空気洗浄弁,逆洗水弁を閉じ,空気洗浄ブロ
ワ,逆洗水ポンプを停止し,供給水弁を開け,供給水ポ
ンプを運転して原水を膜モジュール内に供給し,モジュ
ール内の洗浄排水を洗浄排水弁より系外へ排出する。洗
浄終了後は,ろ過工程に復帰する。At the time of cleaning, first, the supply pump is stopped, the supply water valve and the treated water valve are closed, and the cleaning water valve 5 is opened. After that, the air washing valve 3 and the back washing water valve 7 are opened, and the air washing blower 9 and the back washing pump 11 are operated to remove turbidity and the like on the membrane surface. Next, in order to discharge the separated suspended matters from the inside of the membrane module to the outside of the system, close the air washing valve and the backwash water valve, stop the air washing blower and the backwash water pump, open the supply water valve, and supply. The water pump is operated to supply raw water into the membrane module, and the cleaning drainage inside the module is discharged from the system through the cleaning drain valve. After washing, return to the filtration process.
【0008】逆流水洗浄は連続ではなく空気洗浄中に断
続に行い,さらに処理水の使用を低減することができ
る。なお,図2に弁の開閉状態を説明するタイムチャー
トを示す。[0008] The backwash water washing is not continuous but is performed intermittently during the air washing, and the use of treated water can be further reduced. Note that FIG. 2 shows a time chart for explaining the open / closed state of the valve.
【0009】[0009]
【発明の効果】膜の性能を長期に維持でき,洗浄に使用
する処理水が最少限となり,水回収率が高くなる。The performance of the membrane can be maintained for a long period of time, the treated water used for cleaning is minimized, and the water recovery rate is increased.
【図1】本発明のシステム構成を示す。FIG. 1 shows a system configuration of the present invention.
【図2】運転時の弁開閉状態を示すタイムチャート。FIG. 2 is a time chart showing a valve opening / closing state during operation.
1 供給ポンプ 2 膜モジュール 3 空気洗浄自動弁 4 循環水用自動弁 5 洗浄排水自動弁 6 処理水自動弁 7 逆洗水自動弁 8 処理水タンク 9 洗浄ブロワ 10 供給水自動弁 11 逆洗ポンプ 1 Supply pump 2 Membrane module 3 Air cleaning automatic valve 4 Circulating water automatic valve 5 Cleaning drainage automatic valve 6 Treated water automatic valve 7 Backwash water automatic valve 8 Treated water tank 9 Washing blower 10 Supply water automatic valve 11 Backwash pump
Claims (1)
タ膜,ウルトラフィルタ膜の膜面の洗浄方法において,
膜表面を空気で洗浄し,同時に膜裏面から洗浄水を逆流
させて濁質を剥離させ,その後,原水を流入させて系外
に排出することにより膜面を洗浄する方法。1. A method for cleaning a membrane surface of a microfilter membrane for solid-liquid separation and an ultrafilter membrane of a water treatment device, comprising:
A method of washing the membrane surface by washing the membrane surface with air, and at the same time flowing back washing water from the membrane back surface to separate suspended substances, and then introducing raw water and discharging it out of the system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3605293A JPH06226065A (en) | 1993-02-01 | 1993-02-01 | Membrane washing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3605293A JPH06226065A (en) | 1993-02-01 | 1993-02-01 | Membrane washing method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06226065A true JPH06226065A (en) | 1994-08-16 |
Family
ID=12458951
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3605293A Pending JPH06226065A (en) | 1993-02-01 | 1993-02-01 | Membrane washing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06226065A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003082449A1 (en) * | 2002-04-03 | 2003-10-09 | Bucher-Guyer Ag | Cross-flow filtration system and operation method therefor |
| WO2003084650A1 (en) * | 2002-04-10 | 2003-10-16 | Bucher-Guyer Ag | Cross-flow filtration installation |
| KR100407180B1 (en) * | 2001-03-21 | 2003-11-28 | 주식회사 알고에스앤엠 | Method for cleaninging in the spiral membrane and thereof apparatus |
-
1993
- 1993-02-01 JP JP3605293A patent/JPH06226065A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100407180B1 (en) * | 2001-03-21 | 2003-11-28 | 주식회사 알고에스앤엠 | Method for cleaninging in the spiral membrane and thereof apparatus |
| WO2003082449A1 (en) * | 2002-04-03 | 2003-10-09 | Bucher-Guyer Ag | Cross-flow filtration system and operation method therefor |
| WO2003084650A1 (en) * | 2002-04-10 | 2003-10-16 | Bucher-Guyer Ag | Cross-flow filtration installation |
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