JPH08229362A - Method for cleaning membrane with liquid chemical in immersion-type membrane filter and device therefor - Google Patents

Method for cleaning membrane with liquid chemical in immersion-type membrane filter and device therefor

Info

Publication number
JPH08229362A
JPH08229362A JP3886595A JP3886595A JPH08229362A JP H08229362 A JPH08229362 A JP H08229362A JP 3886595 A JP3886595 A JP 3886595A JP 3886595 A JP3886595 A JP 3886595A JP H08229362 A JPH08229362 A JP H08229362A
Authority
JP
Japan
Prior art keywords
membrane
cleaning
chemical
immersion
chemical liquid
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.)
Granted
Application number
JP3886595A
Other languages
Japanese (ja)
Other versions
JP3488535B2 (en
Inventor
Genzo Ozawa
源三 小澤
Tatsuhiko Suzuki
辰彦 鈴木
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.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP03886595A priority Critical patent/JP3488535B2/en
Publication of JPH08229362A publication Critical patent/JPH08229362A/en
Application granted granted Critical
Publication of JP3488535B2 publication Critical patent/JP3488535B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE: To eliminate the need for equipment to move a membrane, etc., to shorten the cleaning time and to clean the membrane with a small amt. of liq. chemical. CONSTITUTION: A membrane 4a dipped in an immersion tank 3 storing raw water is cleaned with a liq. chemical. In this case, the chemical is supplied to the membrane 4a from the treated water side to clean the membrane 4a. The raw water is filtered by the membrane 4a dipped in the tank 3 in this immersion-type membrane filter. A device 1 for cleaning the membrane 4a with the chemical is provided with a means 10 to supply the cleaning chemical to the membrane 4a from the treated water side of the membrane 4a.

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、浸漬槽内に浸漬した膜
により原水を濾過する浸漬型膜濾過装置に係り、その浸
漬槽内の膜を薬液により洗浄する膜の薬液洗浄方法及び
薬液洗浄装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an immersion type membrane filtration device for filtering raw water with a membrane immersed in an immersion tank, and a method for cleaning a membrane in the immersion tank with a chemical solution and a chemical solution cleaning. Regarding the device.

【0002】[0002]

【従来の技術】従来、原水が貯留された浸漬槽内に膜
(膜モジュールともいう)を浸漬して膜の濾過作用で原
水を浄化する浸漬型の膜濾過装置がある。この膜濾過装
置において、膜濾過を継続すると、濁質等により膜に目
詰まりが生じ濾過効率が低下するので、一定時間使用し
たら膜を洗浄するようにしている。
2. Description of the Related Art Conventionally, there is an immersion type membrane filtration device in which a membrane (also referred to as a membrane module) is immersed in an immersion tank in which raw water is stored to purify the raw water by a filtering action of the membrane. In this membrane filtration device, when the membrane filtration is continued, the membrane is clogged with turbidity or the like to lower the filtration efficiency. Therefore, the membrane is washed after a certain period of use.

【0003】この洗浄方法としては、処理水を膜の処理
水側から原水側に逆流させて洗浄する逆洗浄を行った
り、浸漬槽内の膜の下方に設けたエアーノズルからの気
泡により膜の表面を洗浄するものなどがある。
As this cleaning method, backwashing is carried out in which the treated water is backwashed from the treated water side of the membrane to the raw water side, or the membrane is formed by air bubbles from an air nozzle provided below the membrane in the dipping tank. There are things such as cleaning the surface.

【0004】さらに、一定期間使用すると、濁質等が膜
内部まで入り込み、上記洗浄による効果が著しく低下す
るので、洗浄用の薬液を使用して膜を洗浄することにな
る。この場合、膜を装置から取り外して、洗浄用の薬液
が貯留された薬液洗浄槽内に浸漬させて膜の薬液洗浄を
行っていた。
Further, when it is used for a certain period of time, suspended matters and the like enter the inside of the membrane and the effect of the above-mentioned cleaning is remarkably reduced, so that the membrane is cleaned using a cleaning chemical solution. In this case, the membrane is removed from the apparatus and immersed in the chemical cleaning tank in which the cleaning chemical is stored to clean the membrane with the chemical.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、従来の
薬液洗浄では、次のような問題点がある。膜を膜濾過装
置から取り外して薬液洗浄槽内に浸漬するので、クレー
ン等、膜の移動および取り外し・取り付けのための設備
が必要となる。また、取り外し・取り付け作業に時間が
かかるので、膜濾過装置の可動率が低下する。さらに、
膜を薬液洗浄槽内に浸漬して洗浄するので、洗浄用の薬
液が多量に必要となりコスト高となる。
However, the conventional chemical cleaning has the following problems. Since the membrane is removed from the membrane filtration device and immersed in the chemical cleaning tank, equipment such as a crane for moving and removing / attaching the membrane is required. In addition, since it takes time to remove and attach the work, the mobility of the membrane filtration device is lowered. further,
Since the membrane is immersed in the chemical cleaning bath for cleaning, a large amount of cleaning chemical is required, resulting in high cost.

【0006】本発明は、上記問題点に鑑みてなされたも
ので、膜の移動等の設備を不要とし、洗浄時間を短縮で
きると共に、少量の薬液で洗浄が行える膜の薬液洗浄方
法及び薬液洗浄装置を提供することにある。
The present invention has been made in view of the above-mentioned problems, and eliminates the need for equipment such as movement of the membrane, shortens the cleaning time, and can clean the membrane with a small amount of chemical liquid. To provide a device.

【0007】[0007]

【課題を解決するための手段】本発明は上記課題を解決
するため、次のように構成した。原水が貯溜された浸漬
槽内に浸漬した膜の薬液洗浄方法において、前記膜に洗
浄用の薬液をその膜の処理水側から供給して洗浄する膜
の薬液洗浄方法とした。この洗浄において、洗浄用の薬
液を膜に浸透させた後、供給する薬液を少量に切り換え
て原水側に流してもよい。
Means for Solving the Problems In order to solve the above-mentioned problems, the present invention is configured as follows. In the method for cleaning a membrane with a membrane immersed in a dipping tank in which raw water is stored, a membrane cleaning solution is supplied by supplying a membrane cleaning solution from the treated water side of the membrane. In this cleaning, the cleaning chemical may be permeated through the membrane, and then the supplied chemical may be switched to a small amount and flowed to the raw water side.

【0008】また、浸漬槽内に浸漬した膜により原水を
濾過する浸漬型膜濾過装置において、前記膜に洗浄用の
薬液を該膜の処理水側から供給する薬液供給手段を備え
たことを特徴とする膜の薬液洗浄装置とした。前記薬液
供給手段は、多量の洗浄用の薬液を供給する多量薬液供
給手段と、少量の洗浄用の薬液を供給する少量薬液供給
手段とから構成するのがよい。
Further, in the immersion type membrane filtration device for filtering raw water with a membrane immersed in an immersion tank, a chemical solution supply means for supplying a chemical solution for cleaning to the membrane from the treated water side of the membrane is provided. The film was used as a chemical cleaning device for the film. It is preferable that the chemical liquid supply unit includes a large chemical liquid supply unit that supplies a large amount of cleaning chemical liquid and a small amount chemical liquid supply unit that supplies a small amount of cleaning chemical liquid.

【0009】[0009]

【作用】本発明によれば、次のように作用する。薬液供
給手段により洗浄用の薬液が膜の処理水側から膜に供給
され、薬液が膜に浸透する。これにより膜が洗浄される
ことになる。また、多量薬液供給手段と少量薬液供給手
段を備えたものにおいては、薬液が膜に浸透した後、供
給する薬液を少量に切り換えて原水側に流して洗浄す
る。これにより、原水側に流出する薬液を少量におさえ
ることができると共に、洗浄効果を向上させることがで
きる。
According to the present invention, the following operations are performed. The chemical liquid for cleaning is supplied to the membrane from the treated water side of the membrane by the chemical liquid supply means, and the chemical liquid permeates the membrane. This will wash the membrane. Further, in the case of having a large amount chemical liquid supply means and a small amount chemical liquid supply means, after the chemical liquid permeates the membrane, the chemical liquid to be supplied is switched to a small amount and flowed to the raw water side for washing. As a result, the chemical liquid flowing out to the raw water side can be kept small and the cleaning effect can be improved.

【0010】[0010]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1から図4に、本実施例の薬液洗浄装置1が付
設された浸漬型膜濾過装置2を示す。
Embodiments of the present invention will be described below with reference to the drawings. 1 to 4 show an immersion type membrane filtration device 2 provided with a chemical liquid cleaning device 1 of this embodiment.

【0011】前記浸漬型膜濾過装置2は、原水が貯留さ
れる浸漬槽3と、この浸漬槽3内の原水中に浸漬された
膜モジュール4とを備えて概略構成されている。この膜
モジュール4は、中空糸膜4a(以下、膜4aと記す)
を多数集積したもので、横置とし上下に2基配置してい
る。個々の膜4aは両端部を夫々連結すると共に、両端
部で内側内を連通してある。この膜4aは原水が膜4a
の外側(原水側)から膜4aの内側(処理水側)に透過
して透過水(処理水)となる。
The submerged membrane filtration device 2 is roughly constructed by including a submerged tank 3 in which raw water is stored, and a membrane module 4 submerged in the raw water in the submerged tank 3. This membrane module 4 is a hollow fiber membrane 4a (hereinafter referred to as membrane 4a).
A large number of these are integrated, and they are placed side by side and two are arranged above and below. Each of the membranes 4a has both ends connected to each other, and both ends communicate with each other inside. This membrane 4a is a raw water membrane 4a.
Permeate from the outside (raw water side) to the inside (treated water side) of the membrane 4a to become permeated water (treated water).

【0012】前記膜モジュール4の両端部には、夫々配
管5,6を接続してあり、一方の配管6には開閉弁V1
を介装している。各配管5,6は、配管6に設けた開閉
弁V1よりも膜モジュール4側で、開閉弁V4を介して
接続している。配管6は開閉弁V1から更に延長されて
透過水路となっている。
Pipes 5 and 6 are connected to both ends of the membrane module 4, and the open / close valve V1 is connected to one pipe 6.
Is intervening. The pipes 5 and 6 are connected to each other on the membrane module 4 side of the on-off valve V1 provided on the pipe 6 via the on-off valve V4. The pipe 6 is further extended from the on-off valve V1 to form a permeate channel.

【0013】前記薬液洗浄装置1は、膜4aに洗浄用の
薬液を膜4aの内側から供給する薬液供給手段10から
なり、この薬液供給手段10には多量の薬液を供給する
大容量のポンプP1(多量薬液手段)と、少量の薬液を
供給する少容量のポンプP2(多量薬液手段)とを備え
ている。また、前記配管5の先端を二股に分岐して、一
方の分岐路には開閉弁V2を介装してエアー抜き排水路
とし、他方の分岐路には開閉弁V3を介装して薬液排水
路としている。
The chemical liquid cleaning apparatus 1 comprises a chemical liquid supply means 10 for supplying a cleaning chemical liquid to the membrane 4a from the inside of the membrane 4a, and a large capacity pump P1 for supplying a large amount of chemical liquid to the chemical liquid supply means 10. It is provided with (a large amount liquid medicine means) and a small capacity pump P2 (a large amount liquid medicine means) for supplying a small amount of liquid medicine. Further, the tip of the pipe 5 is bifurcated, and an opening / closing valve V2 is provided in one branch passage to form an air drainage passage, and an opening / closing valve V3 is provided in the other branch passage to drain chemical liquid. It is a road.

【0014】また、開閉弁V1よりも膜モジュール4側
の配管6には、配管7を接続してあり、この配管7には
逆洗水用のポンプP3及び開閉弁V5を直列に介装して
ある。さらに、膜4aを洗浄するための薬液を貯留する
薬品タンク8が設けられており、この薬品タンク8から
配管7に向けて配管9を設けている。この配管9にはポ
ンプP1を直列に介装していると共に、このポンプP1
と並列にポンプP2を接続してある。これらのポンプP
1,P2と配管7との間には開閉弁V6を介装してい
る。
A pipe 7 is connected to a pipe 6 on the membrane module 4 side of the on-off valve V1, and a pump P3 for backwash water and an on-off valve V5 are connected in series to this pipe 7. There is. Further, a chemical tank 8 for storing a chemical liquid for cleaning the membrane 4a is provided, and a pipe 9 is provided from the chemical tank 8 toward the pipe 7. A pump P1 is installed in series in the pipe 9, and the pump P1
A pump P2 is connected in parallel with. These pumps P
An on-off valve V6 is interposed between the pipes 1 and P2 and the pipe 7.

【0015】次に、浸漬型膜濾過装置2の作動と膜4a
の洗浄方法および薬液洗浄方法について説明する。
Next, the operation of the submerged membrane filtration device 2 and the membrane 4a.
The cleaning method and the chemical cleaning method will be described.

【0016】先ず、図4(a),(b)を参照して、本
実施例の浸漬型膜濾過装置2により通常の濾過工程を行
う場合を示す。
First, referring to FIGS. 4 (a) and 4 (b), a case where a normal filtration step is performed by the immersion type membrane filtration device 2 of the present embodiment will be described.

【0017】すなわち、前記ポンプP1,P2,P3を
停止状態とし、開閉弁V2,V3,V5,V6を閉状態
にすると共に、開閉弁V1,V4を開状態にする。透過
水路に設けた図示しない吸引ポンプを作動すると、原水
が膜4aの外側から膜4aを介して膜4aの内側に透過
し、濾過される。膜4aの内側内の透過水は透過水路を
介して図示しない透過水槽に貯溜されることになる。
That is, the pumps P1, P2, P3 are stopped, the opening / closing valves V2, V3, V5, V6 are closed, and the opening / closing valves V1, V4 are opened. When a suction pump (not shown) provided in the permeate channel is operated, raw water permeates from the outside of the membrane 4a through the membrane 4a to the inside of the membrane 4a and is filtered. The permeated water inside the membrane 4a is stored in a permeated water tank (not shown) through the permeated water passage.

【0018】このように、濾過工程が所定時間(例え
ば、濾過時間が30〜60分)経ったら、膜4aの目詰
まりを解消すべく、逆洗浄工程を所定時間(たとえば3
0〜60秒間)行う。
In this way, after the filtration step has passed a predetermined time (for example, a filtration time of 30 to 60 minutes), the back washing step is performed for a predetermined time (for example, 3 times) in order to eliminate clogging of the membrane 4a.
(0 to 60 seconds).

【0019】すなわち、前記ポンプP1,P2を停止状
態にすると共に、ポンプP3を駆動状態とし、開閉弁V
1,V2,V3,V6を閉状態にすると共に、開閉弁V
4,V5を開状態にする。これにより、逆洗水がポンプ
P3によって膜4aの内側内に圧送され、膜4aの内側
から外側に向けて流出して膜4aの目詰まりを解消す
る。逆洗水は前記した透過水槽からの透過水を使用する
のが通常であるが、別の逆洗用水槽からの水を使用して
もよい。
That is, the pumps P1 and P2 are stopped, the pump P3 is driven, and the on-off valve V
1, V2, V3, V6 are closed and the on-off valve V
Open V4 and V5. As a result, the backwash water is pumped into the inside of the membrane 4a by the pump P3, flows out from the inside of the membrane 4a toward the outside, and the clogging of the membrane 4a is eliminated. As the backwash water, the permeated water from the above-mentioned permeated water tank is usually used, but water from another backwash water tank may be used.

【0020】また、配管内にエアーが溜まる場合がある
ので、エアー抜き工程を設けてある。これは、前記ポン
プP1,P2を停止状態にすると共に、ポンプP3を駆
動状態とし、開閉弁V1,V3,V4,V6を閉状態に
すると共に、開閉弁V2,V5を開状態にする。これに
より、透過水槽からの透過水が循環し、配管内のエアー
が除去されることになる。
Further, since air may accumulate in the pipe, an air venting process is provided. This puts the pumps P1 and P2 into the stopped state, puts the pump P3 into the driven state, closes the on-off valves V1, V3, V4 and V6, and opens the on-off valves V2 and V5. Thereby, the permeated water from the permeated water tank circulates and the air in the pipe is removed.

【0021】前記浸漬型膜濾過装置2により長期間(た
とえば一ヶ月〜数カ月)濾過を行うと、逆洗浄しても膜
4aの目詰まりを解消することができなくなるので、洗
浄用の薬液を用いた薬液洗浄工程を行う。この薬液洗浄
工程を図1から図3を用いて説明する。
If filtration is carried out for a long time (for example, one month to several months) by the immersion type membrane filtration device 2, the clogging of the membrane 4a cannot be eliminated even by back washing, so that a cleaning chemical solution is used. The chemical cleaning step that was performed previously is performed. This chemical cleaning step will be described with reference to FIGS.

【0022】先ず、ポンプP2,P3を停止状態とし、
開閉弁V1,V2,V3,V4,V5を閉状態にすると
共に、開閉弁V6を開状態にする。ポンプP1を駆動す
ると、図1(a)に示すように、薬液タンク8内の薬液
が配管9,6を通って膜4aの内側内に供給される。供
給された薬液は、膜4aの内側から膜4a内部に浸透し
て、膜4a内部に詰まった濁質等を溶解することにな
る。
First, the pumps P2 and P3 are stopped,
The on-off valves V1, V2, V3, V4 and V5 are closed, and the on-off valve V6 is opened. When the pump P1 is driven, as shown in FIG. 1A, the chemical liquid in the chemical liquid tank 8 is supplied into the inside of the membrane 4a through the pipes 9 and 6. The supplied chemical solution permeates from the inside of the film 4a into the inside of the film 4a, and dissolves suspended substances and the like that are clogged inside the film 4a.

【0023】次に、ポンプP1,P3を停止状態とし、
ポンプP2を駆動すると、図2に示すように、薬液が膜
モジュール4の膜4aの内部に押し込まれ、図2(b)
に示すように、薬液が膜4aの内側から膜4aの内部を
介して外側に向けて流出する。この際、膜4aの内部に
侵入した濁質等がほぼ完全に除去される。
Next, the pumps P1 and P3 are stopped,
When the pump P2 is driven, the chemical liquid is pushed into the inside of the membrane 4a of the membrane module 4 as shown in FIG.
As shown in, the chemical solution flows out from the inside of the film 4a to the outside through the inside of the film 4a. At this time, turbid substances and the like that have entered the inside of the film 4a are almost completely removed.

【0024】前記ポンプP2が一定時間駆動されたら、
ポンプP2,P3を停止状態とし、ポンプP1を駆動す
ると共に、開閉弁V3を開状態にする。これにより、図
3(a)に示すように、薬液タンク8に貯留された別の
薬液が膜モジュール4の膜内に圧送されると共に、開閉
弁V3を介して外部に排出され薬液の入れ替えが行われ
る。
When the pump P2 is driven for a certain time,
The pumps P2 and P3 are stopped, the pump P1 is driven, and the on-off valve V3 is opened. As a result, as shown in FIG. 3A, another chemical solution stored in the chemical solution tank 8 is pressure-fed into the membrane of the membrane module 4 and is discharged to the outside through the on-off valve V3 to replace the chemical solution. Done.

【0025】このように薬液洗浄工程が終わったら、通
常の濾過工程に移行する。しかし、膜4aの内側内には
薬液が充填されたままであるので、通常の濾過工程の初
期段階においては透過水に薬液が混入するので、濾過工
程の初期の透過水を透過水槽には入れないで、他のタン
クに入れる。
When the chemical cleaning step is completed in this way, the process proceeds to the normal filtration step. However, since the inside of the membrane 4a is still filled with the chemical liquid, the permeated water mixes with the permeated water in the initial stage of the normal filtration process, so the permeated water in the initial stage of the filtration process cannot be put into the permeated water tank. Then put it in another tank.

【0026】なお、薬液は膜の種類や目詰まり物質の種
類に応じて適宜の種類が使用されるが、水酸化ナトリウ
ム溶液、塩酸溶液、次亜塩素ナトリウム溶液等が使用さ
れる。また、1種類の薬液を用いても、複数種類の薬液
を2段に分けて使用するようにしてもよい。この場合に
は、初めにアルカリ系の薬液を入れ、次に酸系の薬液を
入れるようにすることが好ましい。
An appropriate type of chemical solution is used depending on the type of membrane and the type of clogging substance, and sodium hydroxide solution, hydrochloric acid solution, sodium hypochlorite solution, etc. are used. Further, one kind of chemical solution may be used, or plural kinds of chemical solutions may be divided into two stages and used. In this case, it is preferable that the alkaline chemical solution is first introduced, and then the acid chemical solution is introduced.

【0027】本実施例の膜4aの薬液洗浄装置及び薬液
洗浄方法によれば、薬液を膜モジュール4の膜4aの内
側に洗浄用の薬液を充填させ、充填された薬液を膜4a
の内側から膜4aの外側に向かって流出させて膜4aを
洗浄するようにしているので、適宜の薬液を用いれば膜
4aの目詰まりをほぼ完全に洗浄することができる。し
かも、使用できる状態で設置された膜4aに薬液を充填
して洗浄するだけであるので、膜モジュール4を取り外
したりする必要がなく、浸漬型膜濾過装置2の停止期間
を最小限とすることができる。
According to the chemical cleaning device and the chemical cleaning method for the membrane 4a of the present embodiment, the chemical is filled inside the membrane 4a of the membrane module 4 with the chemical for cleaning, and the filled chemical is filled in the membrane 4a.
Since the membrane 4a is washed out by flowing out from the inside to the outside of the membrane 4a, the clogging of the membrane 4a can be almost completely washed by using an appropriate chemical solution. Moreover, it is not necessary to remove the membrane module 4 since the membrane 4a installed in a ready-to-use state is only filled with the chemical liquid and washed, and the period of suspension of the submerged membrane filtration device 2 is minimized. You can

【0028】なお、図5に示すように、上記実施例と同
様な水路を並列に複数(図中では7組)設けるようにし
てもよい。
As shown in FIG. 5, a plurality of water channels (seven sets in the figure) may be provided in parallel as in the above embodiment.

【0029】本発明は上記実施例に限るものではなく、
例えば、中空糸膜に変えて平膜やスパイラル膜および管
状膜等を使用してもよい。また、薬液供給手段が流量を
変えられる1台のポンプであってもよく、一定量の定量
ポンプと流量制御弁を組合わせたものでもよい。さら
に、一台のポンプで薬液を供給するだけでもよく、その
薬液を膜を介して循環させるようにしてもよい。
The present invention is not limited to the above embodiment,
For example, a flat membrane, a spiral membrane, a tubular membrane, or the like may be used instead of the hollow fiber membrane. Further, the chemical liquid supply means may be a single pump whose flow rate can be changed, or may be a combination of a fixed amount of metering pump and a flow rate control valve. Further, the chemical solution may be supplied by only one pump, or the chemical solution may be circulated through the membrane.

【0030】[0030]

【発明の効果】本発明は、以上のように構成したので、
次のような効果がある。膜に洗浄用の薬液をその膜の処
理水側から供給して洗浄するので、膜を浸漬槽内に浸漬
した状態で洗浄することができる。よって、クレーン
等、膜の移動および取り外し・取り付けのための設備が
不要となる。また、取り外し・取り付け作業の時間が不
要となるので、装置の可動率が向上する。さらに、洗浄
用の薬液は膜に供給する量となるので、膜を薬液洗浄槽
内に浸漬して洗浄するのに比して、薬液が少量ですみ、
低コストにできる。
Since the present invention is constructed as described above,
It has the following effects. Since the cleaning chemical is supplied to the membrane from the treated water side of the membrane for cleaning, the membrane can be cleaned while being immersed in the immersion tank. Therefore, equipment for moving and removing / attaching the membrane, such as a crane, becomes unnecessary. In addition, since the time required for the removal / attachment work is unnecessary, the mobility of the device is improved. Furthermore, since the amount of chemical used for cleaning is the amount supplied to the membrane, a small amount of chemical is required compared to dipping the membrane in the chemical cleaning tank for cleaning.
Can be low cost.

【0031】また、薬液が膜に浸透した後、供給する薬
液を少量に切り換えて原水側に流して洗浄するので、原
水側に流出する薬液を少量におさえることができると共
に、洗浄効果を向上させることができる。
Further, after the chemical solution has penetrated into the membrane, the chemical solution to be supplied is switched to a small quantity to flow to the raw water side for cleaning, so that the chemical solution flowing out to the raw water side can be suppressed to a small quantity and the cleaning effect is improved. be able to.

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

【図1】本発明の実施例の膜の薬液洗浄装置及びこれを
用いた薬洗工程の一工程を示す図である。
FIG. 1 is a diagram showing one step of a chemical cleaning device for a membrane and a chemical cleaning process using the same according to an embodiment of the present invention.

【図2】図1の膜の薬液洗浄装置を用いた薬洗工程の一
工程を示す図である。
FIG. 2 is a diagram showing one process of a chemical cleaning process using the chemical cleaning device for the membrane of FIG.

【図3】図1の膜の薬液洗浄装置を用いた薬洗工程の一
工程を示す図である。
FIG. 3 is a diagram showing one process of a chemical cleaning process using the chemical cleaning device for the membrane of FIG.

【図4】図1の膜の薬液洗浄装置が付設された膜濾過装
置による通常の濾過工程を示す図である。
FIG. 4 is a diagram showing a normal filtration process by a membrane filtration device provided with the membrane chemical cleaning device of FIG. 1.

【図5】本発明の他の実施例の膜の薬液洗浄装置を示す
図である。
FIG. 5 is a diagram showing a chemical cleaning device for a membrane according to another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:薬液洗浄装置 2:浸漬型膜濾過装置 3:浸漬槽 4:膜モジュール 4a:中空糸膜(膜) 5,6:配管 10:薬液供給手段 V1,V2,V3,V4,V5,V6 開閉弁 P1:ポンプ(多量薬液手段) P2:ポンプ(少量薬液手段) P3:ポンプ 1: Chemical solution cleaning device 2: Immersion type membrane filtration device 3: Immersion tank 4: Membrane module 4a: Hollow fiber membrane (membrane) 5,6: Piping 10: Chemical solution supply means V1, V2, V3, V4, V5, V6 Open / close Valve P1: Pump (Means for large amount of liquid medicine) P2: Pump (Means for small amount of liquid medicine) P3: Pump

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 原水が貯溜された浸漬槽内に浸漬した膜
の薬液洗浄方法において、前記膜に洗浄用の薬液を該膜
の処理水側から供給して洗浄することを特徴とする浸漬
型膜濾過装置における膜の薬液洗浄方法。
1. A method for cleaning a membrane immersed in an immersion tank in which raw water is stored, wherein the membrane is supplied with a cleaning solution from the treated water side of the membrane for cleaning. A method of cleaning a membrane with a chemical solution in a membrane filtration device.
【請求項2】 前記膜の洗浄において、洗浄用の薬液を
膜に浸透させた後、供給する薬液を少量に切り換えて原
水側に流すことを特徴とする請求項1記載の浸漬型膜濾
過装置における膜の洗浄方法。
2. The immersion type membrane filtration device according to claim 1, wherein, in cleaning the membrane, after the cleaning chemical is permeated into the membrane, the supplied chemical is switched to a small amount and flowed to the raw water side. Method for cleaning membrane in.
【請求項3】 浸漬槽内に浸漬した膜により原水を濾過
する浸漬型膜濾過装置において、前記膜に洗浄用の薬液
を該膜の処理水側から供給する薬液供給手段を備えたこ
とを特徴とする浸漬型膜濾過装置における膜の薬液洗浄
装置。
3. An immersion-type membrane filtration device for filtering raw water with a membrane immersed in an immersion tank, comprising a chemical solution supply means for supplying a cleaning chemical solution to the membrane from the treated water side of the membrane. A chemical cleaning device for a membrane in an immersion type membrane filtration device.
【請求項4】 前記薬液供給手段が、多量の洗浄用の薬
液を供給する多量薬液供給手段と、少量の洗浄用の薬液
を供給する少量薬液供給手段とからなることを特徴とす
る請求項3記載の浸漬型膜濾過装置における膜の薬液洗
浄装置。
4. The chemical liquid supply means comprises a large chemical liquid supply means for supplying a large amount of cleaning chemical liquid and a small chemical liquid supply means for supplying a small amount of cleaning chemical liquid. A membrane chemical cleaning device in the immersion type membrane filtration device described.
JP03886595A 1995-02-27 1995-02-27 Chemical solution cleaning method for membrane in immersion type membrane filtration device and chemical solution cleaning device Expired - Fee Related JP3488535B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03886595A JP3488535B2 (en) 1995-02-27 1995-02-27 Chemical solution cleaning method for membrane in immersion type membrane filtration device and chemical solution cleaning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03886595A JP3488535B2 (en) 1995-02-27 1995-02-27 Chemical solution cleaning method for membrane in immersion type membrane filtration device and chemical solution cleaning device

Publications (2)

Publication Number Publication Date
JPH08229362A true JPH08229362A (en) 1996-09-10
JP3488535B2 JP3488535B2 (en) 2004-01-19

Family

ID=12537108

Family Applications (1)

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

Country Link
JP (1) JP3488535B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001070763A (en) * 1999-09-08 2001-03-21 Asahi Kasei Corp Membrane washing method
WO2001008789A3 (en) * 1999-07-29 2001-08-16 Zenon Environmental Inc Maintenance cleaning for membranes
US6303035B1 (en) 1999-07-30 2001-10-16 Zenon Environmental Inc. Immersed membrane filtration process
JP2002177746A (en) * 2000-12-15 2002-06-25 Maezawa Ind Inc Method for cleaning membrane module and membrane filter
US6547968B1 (en) 1999-07-30 2003-04-15 Zenon Environmental Inc. Pulsed backwash for immersed membranes
JP2005211847A (en) * 2004-01-30 2005-08-11 Tsukishima Kikai Co Ltd Filtering device
JP2009039677A (en) * 2007-08-10 2009-02-26 Toray Ind Inc Cleaning method of immersion type membrane module and immersion type membrane filtering apparatus
KR101447954B1 (en) * 2007-07-18 2014-10-13 주식회사 퓨어엔비텍 A membrane module cassette train with a vertical type manifold and the cleaning method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001008789A3 (en) * 1999-07-29 2001-08-16 Zenon Environmental Inc Maintenance cleaning for membranes
US6303035B1 (en) 1999-07-30 2001-10-16 Zenon Environmental Inc. Immersed membrane filtration process
US6547968B1 (en) 1999-07-30 2003-04-15 Zenon Environmental Inc. Pulsed backwash for immersed membranes
JP2001070763A (en) * 1999-09-08 2001-03-21 Asahi Kasei Corp Membrane washing method
JP2002177746A (en) * 2000-12-15 2002-06-25 Maezawa Ind Inc Method for cleaning membrane module and membrane filter
JP2005211847A (en) * 2004-01-30 2005-08-11 Tsukishima Kikai Co Ltd Filtering device
KR101447954B1 (en) * 2007-07-18 2014-10-13 주식회사 퓨어엔비텍 A membrane module cassette train with a vertical type manifold and the cleaning method
JP2009039677A (en) * 2007-08-10 2009-02-26 Toray Ind Inc Cleaning method of immersion type membrane module and immersion type membrane filtering apparatus

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