JP3341428B2 - Operating method of immersion membrane device - Google Patents

Operating method of immersion membrane device

Info

Publication number
JP3341428B2
JP3341428B2 JP34595793A JP34595793A JP3341428B2 JP 3341428 B2 JP3341428 B2 JP 3341428B2 JP 34595793 A JP34595793 A JP 34595793A JP 34595793 A JP34595793 A JP 34595793A JP 3341428 B2 JP3341428 B2 JP 3341428B2
Authority
JP
Japan
Prior art keywords
membrane
filtration
air diffuser
air
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.)
Expired - Fee Related
Application number
JP34595793A
Other languages
Japanese (ja)
Other versions
JPH07185271A (en
Inventor
和夫 今井
繁樹 沢田
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP34595793A priority Critical patent/JP3341428B2/en
Publication of JPH07185271A publication Critical patent/JPH07185271A/en
Application granted granted Critical
Publication of JP3341428B2 publication Critical patent/JP3341428B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

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、平膜を複数枚積層し
た積層体や、中空糸膜を平面状、或いはすだれ状にした
膜エレメントを複数枚積層した積層体や、管状膜を複数
本並行に接続したものを膜ユニットとして用いた浸漬膜
装置の運転方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a laminated body in which a plurality of flat membranes are laminated, a laminated body in which a plurality of hollow fiber membranes are formed in a planar or interdigital shape, and a plurality of tubular membranes. The present invention relates to a method for operating an immersion membrane apparatus using a parallel connection as a membrane unit.

【0002】[0002]

【従来の技術】処理槽の液中に上述した膜ユニットを浸
漬し、膜ユニットの内部を吸引して膜を透過した濾過処
理水を得る浸漬膜装置は従来から公知である。又、膜の
下部に散気装置を設け濾過ケークを剥離させることも公
知である。
2. Description of the Related Art An immersion membrane apparatus in which the above-mentioned membrane unit is immersed in a liquid in a treatment tank, and the inside of the membrane unit is suctioned to obtain filtered water permeated through the membrane is conventionally known. It is also known to provide an air diffuser below the membrane to remove the filter cake.

【0003】[0003]

【発明が解決しようとする課題】この浸漬膜装置を運転
して膜濾過を行うと、膜面には濃度分極層、ゲル層、ケ
ーク層などの非濾過物質が付着する。そして、非濾過物
質の厚さが増すと濾過抵抗が増大し、濾過圧力が高まっ
て濾過効率は著しく低下する。このため膜ユニットの下
方に散気装置を設け、一定時間膜濾過運転を行ったら、
又は膜濾過運転中に一定濾過圧力になったら、運転を中
止して逆洗を行うが、この逆洗の前後に散気装置を作動
し、膜ユニットの下面全体に下から気泡を浴びせ、膜の
間を上向する気泡と、上向水流の剪断力で膜面に付着し
た非濾過物質を剥離する必要がある。この場合、膜ユニ
ットの回りに槽内の液が下向流して循環する対流スペー
スを保つことが必要で、処理槽内への膜の充填率がその
対流スペース分だけ減少することになる。
When this immersion membrane device is operated to perform membrane filtration, non-filtration substances such as a concentration polarization layer, a gel layer and a cake layer adhere to the membrane surface. As the thickness of the non-filtration material increases, the filtration resistance increases, the filtration pressure increases, and the filtration efficiency decreases significantly. For this reason, if an air diffuser is provided below the membrane unit and the membrane filtration operation is performed for a certain time,
Or, when the filtration pressure reaches a certain level during the membrane filtration operation, the operation is stopped and backwashing is performed.However, before and after this backwashing, the air diffuser is operated, and the entire lower surface of the membrane unit is exposed to air bubbles from below, and the membrane is washed. It is necessary to peel off the non-filtration substance adhering to the membrane surface due to the upward bubbles and the shear force of the upward water flow. In this case, it is necessary to maintain a convection space in which the liquid in the tank flows downward and circulates around the membrane unit, and the filling rate of the membrane in the processing tank is reduced by the convection space.

【0004】[0004]

【課題を解決するための手段】そこで本発明は、処理槽
の液中に複数の膜ユニットを、液中の仕切板で隔てゝ槽
内液中に配置すると共に、その個々の膜ユニットの下方
に個々に散気装置を設け、膜を透過した濾過処理水を得
る浸漬膜装置において、請求項1は、膜濾過運転を中止
し、逆洗を行う前後に上記散気装置を交互に作動するこ
とを特徴とし、請求項2は、膜濾過運転中に、上記散気
装置を交互に作動することを特徴とする。
SUMMARY OF THE INVENTION Accordingly, the present invention provides a method for disposing a plurality of membrane units in a liquid in a processing tank, separated by a partition plate in the liquid, in the liquid in the tank, and below the individual membrane units. In the immersion membrane device which obtains the filtration treatment water permeated through the membrane, the membrane diffusion operation is stopped, and the air diffusion device is alternately operated before and after performing the backwash. According to a second aspect of the present invention, the air diffuser is operated alternately during the membrane filtration operation.

【0005】[0005]

【実施例】図示の各実施例において、10は処理槽で、
処理槽の液中には膜ユニット11が浸漬してあり、ポン
プ12を接続した吸引管13が膜ユニットの内部を吸引
し、処理槽内の原液中、膜ユニット11を透過したもの
を濾過処理水として採水する。膜ユニットは、前述した
ように平膜の複数枚の積層体、又は中空糸膜を平面状、
或いはすだれ状にした膜エレメントの複数枚の積層体、
又は管状膜を複数本並行に接続したものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In each of the illustrated embodiments, reference numeral 10 denotes a processing tank.
The membrane unit 11 is immersed in the liquid in the processing tank, and the suction pipe 13 connected to the pump 12 sucks the inside of the membrane unit, and the undiluted solution in the processing tank that has passed through the membrane unit 11 is filtered. Collect water as water. The membrane unit is formed by stacking a plurality of flat membranes or hollow fiber membranes as described above,
Alternatively, a plurality of laminated bodies of interleaved membrane elements,
Alternatively, a plurality of tubular membranes are connected in parallel.

【0006】図1の実施例では、処理槽10内に2つの
膜ユニット11A,11Bを上端が液面下の仕切板14
で隔てゝ隣接状に配置してあり、各膜ユニット11A,
11Bの下方には個々に散気装置15A,15Bが設け
てある。散気装置15A,15Bは共通のブロワー16
に分岐管17で接続し、管に設けた開閉弁18A,18
Bで個々に作動できるようになっている。膜濾過運転を
中止し、逆洗を行う前後に開閉弁18A,18Bを交互
に開閉し、例えば散気装置15Aから15分間、気泡を
膜ユニット11Aに浴びせ、次の15分は散気装置15
Bから気泡を膜ユニット11Bに浴びせ、これを繰返
す。これにより散気装置15Aから浮上する気泡によっ
て膜ユニット11Aの膜の間には上向流が生じ、気泡と
上向水流により膜ユニット11Aの膜面に付着した非濾
過物質は膜面から剥離し、同時に膜ユニット11Bの膜
間には下向流が生じ、この下向水流によって膜面に付着
した非濾過物質が剥離される。散気装置15Bが作動し
ているときは上記とは逆で膜ユニット11Bの膜面に付
着した非濾過物質は気泡と上向水流により膜面から剥離
し、膜ユニット11Aの膜面に付着した非濾過物質は膜
間に生じた下向水流で膜面から剥離する。尚、散気は膜
の運転を中止して行っても、膜の運転中に行ってもよ
い。
In the embodiment shown in FIG. 1, two membrane units 11A and 11B are placed in a processing tank 10 by a partition plate 14 whose upper end is below the liquid level.
Are disposed adjacent to each other, and each of the membrane units 11A,
Air diffusers 15A and 15B are individually provided below 11B. A diffuser 15A, 15B is a common blower 16
To the opening and closing valves 18A, 18 provided on the pipes.
B can be operated individually. The membrane filtration operation is stopped, and the opening / closing valves 18A and 18B are alternately opened and closed before and after the backwash. For example, the air bubbles are exposed to the membrane unit 11A for 15 minutes from the air diffuser 15A, and the air diffuser 15 is used for the next 15 minutes.
From B, air bubbles are poured into the membrane unit 11B, and this is repeated. As a result, bubbles rising from the air diffuser 15A cause an upward flow between the membranes of the membrane unit 11A, and the non-filtration substances attached to the membrane surface of the membrane unit 11A due to the bubbles and the upward water flow are separated from the membrane surface. At the same time, a downward flow is generated between the membranes of the membrane unit 11B, and the non-filtration substance attached to the membrane surface is separated by the downward flow. When the air diffuser 15B is operating, the non-filtration substance adhered to the membrane surface of the membrane unit 11B is peeled off from the membrane surface by bubbles and upward water flow, and adheres to the membrane surface of the membrane unit 11A. The non-filtered material is separated from the membrane surface by the downward water flow generated between the membranes. The air diffusion may be performed after the operation of the membrane is stopped, or may be performed during the operation of the membrane.

【0007】図2の実施例では、処理槽10内に4つの
膜ユニット11A,11B,11C,11Dを三枚の仕
切板14A,14B,14Cで隔てゝ隣接状に配置して
あり、各膜ユニットの下方には個々に散気装置15A,
15B,15C,15Dが設けてある。4つの散気装置
は共通のブロワー16に分岐管17で接続し、分岐管に
設けた4つの開閉弁18A,18B,18C,18Dで
4つの散気装置を個々に作動することができる。膜濾過
運転を行っている間、或いは運転を中止し、逆洗の前後
に開閉弁を操作し、例えば散気装置15A,15B,1
5C,15Dの順に15分間宛作動させたり、或いは1
5Aと15C、15Bと15Dを15分間宛交互に作動
させる。作動している散気装置の上の膜ユニットの膜間
には気泡による上向流が生じ、気泡と上向水流が膜面に
付着した非濾過物質を剥離し、作動していない散気装置
の上の膜ユニットの膜間には下向流が生じ、この下向水
流が膜面に付着した非濾過物質を膜面から剥離する。
In the embodiment shown in FIG. 2, four membrane units 11A, 11B, 11C and 11D are arranged in a processing tank 10 so as to be separated from each other by three partition plates 14A, 14B and 14C. Below the unit are individually air diffusers 15A,
15B, 15C and 15D are provided. The four air diffusers are connected to a common blower 16 by a branch pipe 17, and the four air diffusers can be individually operated by four on-off valves 18A, 18B, 18C, 18D provided in the branch pipe. While the membrane filtration operation is being performed, or the operation is stopped, the on-off valve is operated before and after the backwash, and for example, the air diffusers 15A, 15B, 1
Operate for 15 minutes in the order of 5C, 15D, or 1
5A and 15C, 15B and 15D are alternately operated for 15 minutes. An upward flow due to air bubbles is generated between the membranes of the membrane units above the operating air diffuser, and the air bubbles and the upward water flow separate the non-filtration substance adhering to the membrane surface, and the air diffuser is not operated. A downward flow is generated between the membranes of the membrane units above the membrane unit, and this downward water flow separates the non-filtration substance adhering to the membrane surface from the membrane surface.

【0008】[0008]

【発明の効果】以上で明らかなように、散気装置を交互
に作動することで、作動している散気装置の上の膜ユニ
ットの膜間には気泡による上向流が生じ、気泡と上向水
流とにより膜面に付着した非濾過物質を剥離する。そし
て、作動を中止している散気装置の上の膜ユニットの膜
間には下向流が生じ、この下向水流が膜面に付着した非
濾過物質を剥離する。従って、下向流を生じさせる対流
スペースを膜ユニットの間に保つ必要が無くなるので、
処理槽への膜充填率が高まる。又、同じ数の膜ユニット
を充填する場合、使用する処理槽の大きさは大幅に小型
化する。
As is apparent from the above, by alternately operating the air diffusers, an upward flow of air bubbles is generated between the membranes of the membrane units above the operating air diffusers, and the air bubbles and the air bubbles are generated. The non-filtration substance adhering to the membrane surface is removed by the upward water flow. Then, a downward flow is generated between the membranes of the membrane units above the air diffuser whose operation has been stopped, and this downward water flow separates the non-filtration substance adhering to the membrane surface. Therefore, there is no need to maintain a convection space for generating the downward flow between the membrane units,
The film filling rate in the processing tank increases. Further, when filling the same number of membrane units, the size of the processing tank used is greatly reduced.

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

【図1】本発明の浸漬膜装置の第1実施例の断面図であ
る。
FIG. 1 is a sectional view of a first embodiment of an immersion film apparatus according to the present invention.

【図2】本発明の浸漬膜装置の他の1実施例の断面図で
ある。
FIG. 2 is a sectional view of another embodiment of the immersion film apparatus of the present invention.

【符号の説明】[Explanation of symbols]

10 処理槽 11A 膜ユニット 11B 膜ユニット 11C 膜ユニット 11D 膜ユニット 12 ポンプ 13 吸引管 14 仕切板 14A 仕切板 14B 仕切板 14C 仕切板 15A 散気装置 15B 散気装置 15C 散気装置 15D 散気装置 16 ブロワー 17 分岐管 18A 開閉弁 18B 開閉弁 18C 開閉弁 18D 開閉弁 DESCRIPTION OF SYMBOLS 10 Processing tank 11A Membrane unit 11B Membrane unit 11C Membrane unit 11D Membrane unit 12 Pump 13 Suction tube 14 Divider 14A Divider 14B Divider 14C Divider 15A Air diffuser 15B Air diffuser 15C Air diffuser 15D Air diffuser 16 17 Branch pipe 18A On-off valve 18B On-off valve 18C On-off valve 18D On-off valve

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 処理槽の液中に複数の膜ユニットを、液
中の仕切板で隔てゝ配置すると共に、その個々の膜ユニ
ットの下方に個々に散気装置を設け、膜を透過した濾過
処理水を得る浸漬膜装置の運転方法において、膜濾過運
転を中止し、逆洗を行う前後に上記散気装置を交互に作
動することを特徴とする浸漬膜装置の運転方法。
1. A plurality of membrane units are arranged in a liquid in a processing tank, separated by a partition plate in the liquid, and an air diffuser is individually provided below each of the membrane units to provide filtration through the membrane. A method for operating a submerged membrane apparatus for obtaining treated water, wherein the membrane filtration operation is stopped and the air diffuser is alternately operated before and after performing backwashing.
【請求項2】 処理槽の液中に複数の膜ユニットを、液
中の仕切板で隔てゝ配置すると共に、その個々の膜ユニ
ットの下方に個々に散気装置を設け、膜を透過した濾過
処理水を得る浸漬膜装置の運転方法において、膜濾過運
転中に上記散気装置を交互に作動することを特徴とする
浸漬膜装置の運転方法。
2. A plurality of membrane units are arranged in a liquid in a processing tank, separated by a partition plate in the liquid, and an air diffuser is individually provided below each of the membrane units to perform filtration through the membrane. A method for operating a submerged membrane apparatus for obtaining treated water, wherein the air diffuser is operated alternately during a membrane filtration operation.
JP34595793A 1993-12-24 1993-12-24 Operating method of immersion membrane device Expired - Fee Related JP3341428B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34595793A JP3341428B2 (en) 1993-12-24 1993-12-24 Operating method of immersion membrane device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34595793A JP3341428B2 (en) 1993-12-24 1993-12-24 Operating method of immersion membrane device

Publications (2)

Publication Number Publication Date
JPH07185271A JPH07185271A (en) 1995-07-25
JP3341428B2 true JP3341428B2 (en) 2002-11-05

Family

ID=18380157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34595793A Expired - Fee Related JP3341428B2 (en) 1993-12-24 1993-12-24 Operating method of immersion membrane device

Country Status (1)

Country Link
JP (1) JP3341428B2 (en)

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