JPH0839061A - Immersion type membrane separator - Google Patents

Immersion type membrane separator

Info

Publication number
JPH0839061A
JPH0839061A JP19718694A JP19718694A JPH0839061A JP H0839061 A JPH0839061 A JP H0839061A JP 19718694 A JP19718694 A JP 19718694A JP 19718694 A JP19718694 A JP 19718694A JP H0839061 A JPH0839061 A JP H0839061A
Authority
JP
Japan
Prior art keywords
water
membrane
pipe
membrane element
chemical
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
JP19718694A
Other languages
Japanese (ja)
Other versions
JP3575072B2 (en
Inventor
Katsumi Ishiguro
克己 石黒
Kunihiro Iwasaki
邦博 岩崎
Shigeki Sawada
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 JP19718694A priority Critical patent/JP3575072B2/en
Publication of JPH0839061A publication Critical patent/JPH0839061A/en
Application granted granted Critical
Publication of JP3575072B2 publication Critical patent/JP3575072B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To enhance the effect of chemical washing by distributing a chemical soln. over the entire surface of a membrane. CONSTITUTION:Four water passing ports are provided to the respective membrane elements 2 of an immersion type membrane separator and the upper and lower right water passing ports among them are connected to the first and second take-out pipes 26a, 26b on a suction pipe side through first and third water passages 21, 23 and the upper and lower left water passing ports among them are connected to first and second water or chemical soln. supply pipes 32a, 32b through second and fourth water passages 22, 24 and opening and closing valves 27a, 27b, 27c, 27e, 27f are provided to the take-out pipes and the supply pipes to select the water passing ports. The flow direction of water or a chemical soln. at the time of the introduction of water or the chemical soln. into the transmission chambers of the respective membrane elements can be changed over by valve changeover operation.

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、逆浸透膜、限外濾過
膜、精密濾過膜、その他高分子状膜、無機(アルミナセ
ラミックなど)の膜と、膜を透過した水が入る透過室と
を備えた膜エレメントを複数液中に浸漬し、膜分離処理
を行う浸漬型膜分離装置に関するものである。
BACKGROUND OF THE INVENTION The present invention relates to a reverse osmosis membrane, an ultrafiltration membrane, a microfiltration membrane, a polymer membrane, an inorganic (alumina ceramic, etc.) membrane, and a permeation chamber in which water permeated through the membrane enters. The present invention relates to an immersion type membrane separation device that performs a membrane separation treatment by immersing a membrane element having the above in a plurality of liquids.

【0002】[0002]

【従来の技術】浸漬型膜分離装置は、膜エレメントを浸
漬した浸漬槽内の水深に基づく水頭差と、吸引ポンプの
吸引力により低エネルギで膜分離を行い、透過水を得る
ことができる。この様な浸漬型膜分離装置では間欠停
止、バブリング、エアーリフト上向流などにより膜面の
ケーキ、ゲル層を剥離させて透過流束を維持させるが、
長期の運転ではその付着が不可逆となり薬品洗浄が必要
となる。そこで、本願出願人は特願平5−291516
号により、膜エレメントの対向する隅角部に接続口を設
け、一方の接続口に吸引ポンプの取出管を、他方の接続
口に水や薬液を供給する供給管を接続し、少量の薬液に
より洗浄するように構成した浸漬型膜分離装置を提案し
た。
2. Description of the Related Art Immersion type membrane separators are capable of obtaining permeated water by performing membrane separation with low energy due to the water head difference based on the water depth in the immersion tank in which the membrane element is immersed and the suction force of the suction pump. In such an immersion type membrane separation device, the permeation flux is maintained by peeling the cake and gel layer on the membrane surface by intermittent stoppage, bubbling, air lift upward flow, etc.
Adhesion becomes irreversible during long-term operation, requiring chemical cleaning. Therefore, the applicant of the present application filed Japanese Patent Application No. 5-291516.
The connection port is provided at the opposite corner of the membrane element, the extraction pipe of the suction pump is connected to one of the connection ports, and the supply pipe for supplying water or the chemical liquid is connected to the other connection port. We proposed an immersion type membrane separation device configured to be washed.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、前記浸
漬型膜分離装置では、膜の全面に均一に薬液を分布させ
ることが困難であり、薬液の入口となる接続口と出口と
なる接続口を直線で結ぶ近傍のみが薬品洗浄され、未洗
浄範囲が広かった。したがって、次第に薬品洗浄の効果
が低下し、膜性能を維持できないという問題点があっ
た。そこで、本発明は、膜の全面に薬液を分布させ、薬
品洗浄の効果を向上せしめた浸漬型膜分離装置を提供す
ることを目的とする。
However, in the above-mentioned immersion type membrane separation device, it is difficult to evenly distribute the chemical liquid over the entire surface of the membrane, and the connection port serving as the chemical liquid inlet and the connection port serving as the outlet are straight lines. Only the area connected with was washed with chemicals, and the unwashed area was wide. Therefore, there is a problem that the effect of chemical cleaning gradually decreases and the membrane performance cannot be maintained. Therefore, an object of the present invention is to provide a submerged membrane separation device in which a chemical solution is distributed over the entire surface of the membrane to improve the effect of chemical cleaning.

【0004】[0004]

【課題を解決するための手段】本発明は上記目的を達成
するために提案されたもので、請求項1に記載のもの
は、膜透過水が入る透過室を備えた膜エレメントを複数
並べて液中に浸漬し、膜分離装置を行う浸漬型膜分離装
置において、各膜エレメントに3個以上の通水口を設
け、これら通水口の1以上に吸引ポンプ側の取出管を、
残りの通水口に水や薬液の供給管を接続し、前記管には
弁を設けて連通する通水口を選択可能とし、弁の切換操
作によって、各膜エレメントの透過室内に水や薬液を導
入する際の流れ方向を切換可能にしたものである。ま
た、請求項2に記載のものは、スペーサの両側に膜を配
置して対向する端縁に集水管を設け、スペーサの透過流
路を集水管に連通して膜エレメントを構成し、この膜エ
レメントを複数並べて液中に浸漬し、膜分離を行う浸漬
型膜分離装置において、各膜エレメントの一方の集水管
を吸水ポンプ側の取出管に接続し、他方の集水管を水や
薬液の供給管に接続したものである。
DISCLOSURE OF THE INVENTION The present invention has been proposed in order to achieve the above object. According to a first aspect of the present invention, a plurality of membrane elements having permeation chambers for receiving permeated water are arranged in a liquid. In a submerged membrane separation device which is immersed in the inside to perform a membrane separation device, each membrane element is provided with three or more water passage ports, and at least one of these water passage ports is connected to a suction pipe on the suction pump side.
A water or chemical solution supply pipe is connected to the remaining water passage port, and a valve is provided on the pipe to select the water passage port that communicates with the pipe.By switching the valve, water or chemical liquid is introduced into the permeation chamber of each membrane element. The flow direction when switching is made switchable. According to the second aspect of the present invention, membranes are arranged on both sides of the spacer, water collecting pipes are provided at opposite edges, and a permeation flow path of the spacer is connected to the water collecting pipe to form a membrane element. In an immersion-type membrane separation device that performs membrane separation by arranging multiple elements side by side in the liquid, connect one water collection pipe of each membrane element to the extraction pipe on the water absorption pump side, and supply the other water collection pipe to water or chemical liquid. It is connected to a pipe.

【0005】[0005]

【作用】請求項1に記載の浸漬型膜分離装置では、供給
管の弁と取出管の弁を適宜に切り換えると、膜エレメン
トの透過室内に導入される位置と排出される位置が変化
し、これにより透過室内の洗浄液の流れる流域が切り換
わる。したがって、この洗浄液の流域の切り換えにより
膜面の全面にわたって洗浄液を流すことができる。ま
た、請求項2に記載のものでは、一方の集水管が膜間の
透過流路の一側と線状に連通しているので、この一方の
集水管から洗浄液を供給すると、膜間の透過流路内には
洗浄液が当初から広がりをもって流れ込み、また、他方
の集水管が透過流路の他側と線状に連通しているので、
透過流路内の洗浄液はそのまま広がりをもったまま他方
の集水管から排出される。したがって、膜面の全面にわ
たって洗浄することができる。
In the submerged membrane separation apparatus according to the first aspect, when the valve of the feed pipe and the valve of the take-out pipe are appropriately switched, the position of introduction into the permeation chamber of the membrane element and the position of discharge are changed, As a result, the flow region of the cleaning liquid in the permeation chamber is switched. Therefore, the cleaning liquid can be flowed over the entire surface of the membrane by switching the flow region of the cleaning liquid. Further, according to the second aspect, since one of the water collecting pipes linearly communicates with one side of the permeation passage between the membranes, when the cleaning liquid is supplied from the one of the water collecting pipes, the permeation between the membranes is performed. From the beginning, the cleaning liquid spreads in the flow channel with a spread, and since the other water collection pipe is in linear communication with the other side of the permeation flow channel,
The cleaning liquid in the permeation channel is discharged from the other water collecting pipe while spreading as it is. Therefore, the entire surface of the film can be cleaned.

【0006】[0006]

【実施例】以下、本発明の実施例を図面にもとづいて説
明する。膜ユニット1を構成する1枚宛の膜エレメント
2は、平らで四角の、トリコット編地等からなるネット
状の流路スペーサ3の両面に同大の平膜4,4を重ね、
その四周縁部を熱、接着、高周波溶着などによりシール
して一体に構成し、二枚の平膜の間にシール5で囲まれ
た透過室6を形成する。なお、膜エレメント2は多孔質
部材のスペーサの表裏両面に直接製膜したものでもよ
い。そして、各膜エレメント2にはシール5で囲まれた
透過室6内の各コーナには通水口7が設けてある。即
ち、本実施例では膜エレメント2のコーナに合計4つの
通水口7a,7b,7c,7dを開設する。
Embodiments of the present invention will be described below with reference to the drawings. The single membrane element 2 that constitutes the membrane unit 1 has flat and square flat membranes 4 and 4 on both sides of a flat, square, net-shaped flow path spacer 3 made of tricot knitted fabric.
The four peripheral edges are sealed by heat, adhesion, high-frequency welding or the like to be integrally formed, and a permeation chamber 6 surrounded by the seal 5 is formed between two flat membranes. The membrane element 2 may be one in which the spacers of the porous member are directly formed on both the front and back surfaces. A water passage 7 is provided at each corner in the permeation chamber 6 surrounded by the seal 5 in each membrane element 2. That is, in this embodiment, a total of four water passages 7a, 7b, 7c, 7d are provided at the corners of the membrane element 2.

【0007】8は膜エレメント2の通水口7を有する各
コーナに配置し、隣接する二枚の膜エレメント2の間に
所定の通水間隔を保つ弾性のガスケットであり、膜エレ
メント2のコーナに対応した直角な二辺を有する三角形
又は四角形で、通水口7に連通する同大の開口9を有す
る。
Numeral 8 is an elastic gasket which is arranged at each corner having the water passage port 7 of the membrane element 2 and maintains a predetermined water passage distance between two adjacent membrane elements 2, and at the corner of the membrane element 2. It is a triangle or a quadrangle having two corresponding right-angled sides, and has an opening 9 of the same size that communicates with the water passage 7.

【0008】10と11は、ガスケットで通水間隔12
を保って並べて重ねた複数枚の膜エレメント2の一列を
対向して挟圧する端板であり、大きさは膜エレメント2
と同大である。そして、各端板10,11には、膜エレ
メント2の通水口7と連通する貫通孔13が開設してあ
る。
Numerals 10 and 11 are gaskets and a water passage interval 12
It is an end plate that sandwiches a row of a plurality of membrane elements 2 that are arranged side by side while maintaining the same, and has a size of the membrane elements 2.
Is the same size as. A through hole 13 that communicates with the water passage 7 of the membrane element 2 is formed in each of the end plates 10 and 11.

【0009】端板の貫通孔13は、相対向した部分が膜
エレメント2の通水口7やガスケットの開口9と同大の
大径部14であり、残部は締付ボルト15が通る小径部
16になっている。そして、大径部14の奥に外面に開
口した接続口17が設けてある。したがって、本実施例
では膜エレメント2の各通水口7aに連通する接続口1
7a、各通水口7bに連通する接続口17b、各通水口
7cに連通する接続口17c、各通水口7dに連通する
接続口17dがそれぞれ独立して開口している。
The through hole 13 of the end plate has a large diameter portion 14 having the same size as the water passage 7 of the membrane element 2 and the opening 9 of the gasket, and the remaining portion has a small diameter portion 16 through which the tightening bolt 15 passes. It has become. Then, a connection port 17 opened to the outer surface is provided at the back of the large diameter portion 14. Therefore, in the present embodiment, the connection port 1 communicating with each water passage port 7a of the membrane element 2 is connected.
7a, a connection port 17b communicating with each water communication port 7b, a connection port 17c communicating with each water communication port 7c, and a connection port 17d communicating with each water communication port 7d are independently opened.

【0010】膜ユニット1に組み立てるには、所定の枚
数の膜エレメント2をガスケット8を介して一列に並べ
て重ね(膜エレメント2の通水口7とガスケットの開口
9を連通させる)、連通している全部の膜エレメント2
の通水口7と、全部のガスケット8の開口9に一連にボ
ルト15を貫通し、ボルト15の各端部に貫通孔13を
嵌めて両端板10,11で膜エレメント2を挟み、ボル
ト15の各端部に螺合したナット18を端板10,11
に対して締め付け、膜エレメント2とガスケット8を挟
圧して一体にする。
In order to assemble the membrane unit 1, a predetermined number of membrane elements 2 are lined up in a row with the gasket 8 in between (the water passage 7 of the membrane element 2 and the opening 9 of the gasket are communicated) and are communicated with each other. All membrane elements 2
The bolts 15 are passed through the water passage 7 and the openings 9 of all the gaskets 8 in series, the through holes 13 are fitted to the respective ends of the bolts 15, and the membrane element 2 is sandwiched between the end plates 10 and 11, and the bolts 15 A nut 18 screwed to each end is provided with end plates 10 and 11
Then, the membrane element 2 and the gasket 8 are pressed together to be integrated.

【0011】なお、ボルト15の各端部の、貫通孔13
の小径部16内に位置する部分にはOリング19を嵌め
てシールする。これにより端板10,11の貫通孔13
の大径部14と、ガスケット8の開口8と、膜エレメン
ト2の通水口7とが一連に連なり、個々の膜エレメント
2の透過室6を連通させる第1,第2水路21,22が
上部に、下部には第3,第4水路23,24がそれぞれ
平行に形成される。
The through hole 13 at each end of the bolt 15 is provided.
An O-ring 19 is fitted and sealed in a portion located inside the small diameter portion 16. Thereby, the through holes 13 of the end plates 10 and 11
The large diameter portion 14, the opening 8 of the gasket 8 and the water passage 7 of the membrane element 2 are connected in series, and the first and second water channels 21 and 22 for communicating the permeation chamber 6 of each membrane element 2 In addition, third and fourth water channels 23 and 24 are formed in parallel in the lower portion.

【0012】上記した構成からなる膜ユニット1を浸漬
槽25の液中に浸漬して上になった第1水路21の端板
10にある接続口17aに第1取出管26aを、下にな
った第3水路23の端板10にある接続口17cに第2
取出管26bを接続し、第1開閉弁27aを途中に有す
る第1取出管26aの下流側と、第2開閉弁27bを途
中に有する第2取出管26bの下流側を合流して主取出
管26cとして途中に吸引ポンプ28を設ける。主取出
管26cは吸引ポンプ28の下流で二つに分岐し、第3
開閉弁27cを途中に有する分岐管の一方29aは起立
して、水面が浸漬槽25と同じか、それよりも上位の透
過水の貯槽30に上から開口し、第4開閉弁27dを途
中に有する分岐管29bの他方は真っ直ぐに延びて排水
槽31に開口する。
When the membrane unit 1 having the above-mentioned structure is immersed in the liquid in the dipping tank 25, the first outlet pipe 26a is connected to the connection port 17a of the end plate 10 of the first water channel 21 which is located above. 2nd to the connection port 17c in the end plate 10 of the third water channel 23
The extraction pipe 26b is connected, and the downstream side of the first extraction pipe 26a having the first opening / closing valve 27a in the middle and the downstream side of the second extraction pipe 26b having the second opening / closing valve 27b in the middle are joined to form the main extraction pipe. A suction pump 28 is provided on the way as 26c. The main extraction pipe 26c is branched into two downstream of the suction pump 28,
One of the branch pipes 29a having the opening / closing valve 27c in the middle is erected, and the water surface is the same as that of the immersion tank 25 or is opened from above to the storage tank 30 of the permeated water higher than it, and the fourth opening / closing valve 27d is inserted in the middle. The other one of the branch pipes 29 b that they have extends straight and opens into the drainage tank 31.

【0013】また、浸漬して上になった第2水路22の
端板11にある接続口17bに第1供給管32aを、下
になった第4水路24の端板11にある接続口17dに
第2供給管32bを接続し、第5開閉弁27eを途中に
有する第1供給管32aの上流側と第6開閉弁27fを
途中に有する第2供給管32bの上流側とを合流して主
供給管32cとし、この主供給管32cの上流端を前記
貯槽30の液中に上から突入してストレーナに接続す
る。なお、取出管26或は供給管32を接続しない端板
10,11の接続口17は栓で閉じる。
Further, the first supply pipe 32a is connected to the connection port 17b in the end plate 11 of the second water channel 22 which is soaked up, and the connection port 17d in the end plate 11 of the fourth water channel 24 is down. The second supply pipe 32b is connected to the upstream side of the first supply pipe 32a having the fifth opening / closing valve 27e in the middle and the upstream side of the second supply pipe 32b having the sixth opening / closing valve 27f in the middle. The main supply pipe 32c is used, and the upstream end of the main supply pipe 32c is projected into the liquid in the storage tank 30 from above and connected to the strainer. The connection ports 17 of the end plates 10 and 11 to which the take-out pipe 26 or the supply pipe 32 is not connected are closed with plugs.

【0014】そして、薬液槽33内の薬液を薬液ポンプ
34で注入する薬注管35を主供給管32cの途中に接
続する。また、浸漬槽25には上部に原水の供給管36
を設け、底には排泥管37を設ける。
Then, a chemical injection pipe 35 for injecting the chemical liquid in the chemical liquid tank 33 with a chemical liquid pump 34 is connected in the middle of the main supply pipe 32c. In addition, the dipping tank 25 has a raw water supply pipe 36 at the top.
And a sludge discharge pipe 37 is provided at the bottom.

【0015】透過水を採水するには第1,第2,第3開
閉弁27a,27b,27cを開き、第4,第5,第6
開閉弁27d,27e,27fを閉じて、吸引ポンプ2
8を運転する。これにより、浸漬槽25内の液のうち、
吸引ポンプ28の吸引と水頭差で膜を透過した透過水は
各膜エレメント2の透過室6から第1,第3水路21,
23に集まり、第1,第2取出管26a,26b,主取
出管26cおよび分岐管29aを介して貯槽30に入
る。
To collect the permeated water, the first, second and third on-off valves 27a, 27b and 27c are opened and the fourth, fifth and sixth valves are opened.
The on-off valves 27d, 27e, 27f are closed, and the suction pump 2
Drive 8 As a result, of the liquid in the immersion tank 25,
The permeated water that has permeated the membrane due to the suction of the suction pump 28 and the head difference from the permeation chamber 6 of each membrane element 2 into the first and third water channels 21,
23, and enters the storage tank 30 through the first and second take-out pipes 26a and 26b, the main take-out pipe 26c and the branch pipe 29a.

【0016】透過水の採水工程を行ない、膜4の外面に
ある程度ケークが付着したら、第3開閉弁27cを閉
じ、第4開閉弁27dを開き、第1,第2,第5,第6
開閉弁27a,27b,27e,27fを適宜選択して
開閉するとともに吸引ポンプ28と薬液ポンプ34を運
転し、これにより各膜エレメント2の透過室6内を流れ
る水や薬液の流れ方向を切り換えて洗浄する。
When the cake of the permeate is collected on the outer surface of the membrane 4 to some extent, the third opening / closing valve 27c is closed, the fourth opening / closing valve 27d is opened, and the first, second, fifth and sixth parts are opened.
The on-off valves 27a, 27b, 27e, 27f are appropriately selected to be opened and closed, and the suction pump 28 and the chemical liquid pump 34 are operated to switch the flow directions of water and the chemical liquid flowing through the permeation chamber 6 of each membrane element 2. To wash.

【0017】例えば、第1開閉弁27aと第6開閉弁2
7fを閉じ、第2開閉弁27bと第5開閉弁27eを開
いた状態(第1ステップ)で洗浄すると、膜ユニット1
の透過室6を満たしている透過水は吸引ポンプ28で引
かれて第3水路23を通って第2取出管26bから分岐
管29bを流れて排水槽31に入ると同時に、貯槽30
内の透過水が浸漬槽25との水頭差、及び吸引ポンプ2
8の吸引で置換水の主供給管32c,第1供給管32a
内を膜ユニット1の第2水路22に向かって流れ、薬注
管35で注入される薬液と合流し、所定濃度の洗浄液に
なって膜4に過剰な圧力を付加することなく第2水路2
2から各膜エレメント2の通水口7bを通り透過室6に
入る。
For example, the first on-off valve 27a and the sixth on-off valve 2
When 7f is closed and the second opening / closing valve 27b and the fifth opening / closing valve 27e are opened (first step), the membrane unit 1 is washed.
The permeated water filling the permeation chamber 6 is drawn by the suction pump 28, flows through the third water passage 23 and the branch pipe 29b from the second extraction pipe 26b into the drainage tank 31, and at the same time the storage tank 30
The permeated water inside is the head difference from the immersion tank 25, and the suction pump 2
The main supply pipe 32c of the replacement water and the first supply pipe 32a by suction of 8
It flows through the inside toward the second water channel 22 of the membrane unit 1 and merges with the chemical liquid injected through the chemical injection pipe 35 to become a cleaning liquid having a predetermined concentration, and the second water channel 2 without applying excessive pressure to the membrane 4.
2 enters the permeation chamber 6 through the water passage 7b of each membrane element 2.

【0018】この様にして、洗浄液が透過室6内の透過
水と置換した後に、暫く吸引ポンプ28と薬液ポンプ3
4の運転を継続すると、各膜エレメント2の透過室6内
では上方の通水口7bから流入した洗浄液が対角に位置
する下方の通水口7cから吸引されて排出されるので、
主として図5(A)一点鎖線で示す範囲内が洗浄液の水
流によって強力に洗浄される。なお、この場合、膜4の
内面側の洗浄効果が顕著である。
In this way, after the cleaning liquid is replaced with the permeated water in the permeation chamber 6, the suction pump 28 and the chemical liquid pump 3 are briefly held.
When the operation of No. 4 is continued, in the permeation chamber 6 of each membrane element 2, the cleaning liquid flowing from the upper water passage 7b is sucked and discharged from the diagonally lower water passage 7c.
Mainly within the range indicated by the alternate long and short dash line in FIG. In this case, the cleaning effect on the inner surface side of the film 4 is remarkable.

【0019】そして、吸引ポンプ28と薬液ポンプ34
の運転を停止し、第3開閉弁27c以外に第4開閉弁2
7dも閉じ、貯槽30と浸漬槽25との水頭差で洗浄液
を第2水路22から各膜エレメント2の透過室6に送り
込むと、透過室6内の洗浄液が膜4の内面から外面に透
過し、これにより外面に付着しているケークを剥離する
ことができる。この場合、洗浄液は図5(A)一点鎖線
で示す範囲よりも広い範囲で透過する。なお、洗浄液は
透過水とは逆方向に膜を透過するため、ケークは比較的
容易に膜の外面から剥がれ、除去される。除去されたケ
ークは排泥管37の弁を開いて浸漬槽25から排出す
る。
Then, the suction pump 28 and the chemical liquid pump 34
Operation of the fourth on-off valve 2 is stopped in addition to the third on-off valve 27c.
When 7d is also closed and the cleaning liquid is sent from the second water channel 22 to the permeation chamber 6 of each membrane element 2 due to the water head difference between the storage tank 30 and the immersion tank 25, the cleaning liquid in the permeation chamber 6 permeates from the inner surface to the outer surface of the membrane 4. As a result, the cake adhering to the outer surface can be peeled off. In this case, the cleaning liquid permeates in a wider range than the range shown by the one-dot chain line in FIG. Since the cleaning liquid permeates the membrane in the direction opposite to the permeated water, the cake is easily peeled off from the outer surface of the membrane. The removed cake is discharged from the dipping tank 25 by opening the valve of the mud discharge pipe 37.

【0020】第1ステップが終了して次の第2ステップ
では第1開閉弁27aを開いて第2開閉弁27bを閉
じ、また、第5開閉弁27eを閉じて第6開閉弁27f
を開き、この状態で前記と同様の操作で再度洗浄を行な
う。この様にすると、各エレメントの透過室6内では下
方の通水口7dから流入した洗浄液が対角に位置する上
方の通水口7aから吸引されて第1水路21から排出さ
れるので、主として図5(B)一点鎖線で示す範囲内が
洗浄液の水流によって強力に洗浄される。
In the next second step after the completion of the first step, the first on-off valve 27a is opened and the second on-off valve 27b is closed, and the fifth on-off valve 27e is closed to the sixth on-off valve 27f.
Open and wash again in this state by the same operation as above. In this way, in the permeation chamber 6 of each element, the cleaning liquid flowing in from the lower water passage 7d is sucked from the diagonally upper water passage 7a and discharged from the first water passage 21. (B) The area shown by the alternate long and short dash line is strongly washed by the water flow of the washing liquid.

【0021】したがって、先の第1ステップの洗浄と本
第2ステップの洗浄を行なうと、膜面のほぼ全域にわた
って強力な洗浄を行なうことが可能となり、洗浄残しに
起因する膜性能の低下を防止することができる。
Therefore, if the above first step cleaning and the second step cleaning are performed, it becomes possible to perform strong cleaning over almost the entire surface of the film, and prevent deterioration of the film performance due to residual cleaning. can do.

【0022】前記した実施例では第1ステップでは透過
室6の左上から右下に洗浄液を流して洗浄し(図5
(A))、この後の第2ステップでは第1ステップの流
れに交叉させる様にして左下から右上に洗浄液を流して
膜のほぼ全域を強力洗浄したが、本発明における洗浄液
の流れの方向はこれに限定されるものではなく、開閉弁
を適宜に選択して開閉することにより様々な洗浄態様を
採ることができる。
In the above-described embodiment, in the first step, the cleaning liquid is flowed from the upper left to the lower right of the permeation chamber 6 for cleaning (see FIG. 5).
(A)) In the subsequent second step, the cleaning liquid is flowed from the lower left to the upper right so as to intersect with the flow of the first step to strongly clean almost the entire area of the membrane. The present invention is not limited to this, and various cleaning modes can be adopted by appropriately selecting and opening / closing the open / close valve.

【0023】例えば、第1ステップでは第1開閉弁27
a,第5開閉弁27e,第6開閉弁27fを開いて第2
開閉弁27bを閉じて洗浄すると、図6(A)で示すよ
うに、各膜エレメント2の透過室6内では一側上下に開
口した通水口7b,7dから流入した洗浄液が他側上方
に位置する通水口7aから吸引されて第1水路21から
排出され、同図中一点鎖線で示す範囲が主として強力洗
浄される。そして、次の第2ステップでは第2開閉弁2
7b,第5開閉弁27e,第6開閉弁27fを開いて第
1開閉弁27aを閉じて洗浄する。この様にして洗浄す
ると、図6(B)で示すように、透過室6内では一側上
下に開口した通水口7b,7dから流入した洗浄液が他
側下方に位置する通水口7cから吸引されて第3水路2
3から排出され、同図中一点鎖線で示す範囲が主として
強力洗浄される。したがって、第1ステップと第2ステ
ップの洗浄を切り換えることにより膜のほぼ全面を強力
洗浄することができる。
For example, in the first step, the first opening / closing valve 27
a, the fifth opening / closing valve 27e, and the sixth opening / closing valve 27f are opened to the second
When the on-off valve 27b is closed and washed, as shown in FIG. 6 (A), in the permeation chamber 6 of each membrane element 2, the washing liquid flowing from the water passages 7b and 7d opened on one side is located above the other side. The water is sucked from the water passage 7a and discharged from the first water passage 21, and the range indicated by the alternate long and short dash line in the figure is mainly washed intensively. Then, in the next second step, the second opening / closing valve 2
7b, the 5th on-off valve 27e, and the 6th on-off valve 27f are opened, and the 1st on-off valve 27a is closed and it wash | cleans. When the cleaning is performed in this manner, as shown in FIG. 6B, the cleaning liquid flowing in from the water passages 7b and 7d opened on one side in the permeation chamber 6 is sucked from the water passage 7c located below the other side. 3rd waterway 2
3 is discharged, and the range indicated by the alternate long and short dash line in FIG. Therefore, by switching the cleaning between the first step and the second step, almost the entire surface of the film can be strongly cleaned.

【0024】なお、前記した第1ステップと第2ステッ
プの洗浄は連続して行なってもよい1回目の洗浄では第
1ステップのみを行ない、一定期間稼働した後に2回目
の洗浄として第2ステップの洗浄を行なうようにしても
よい。
The above-mentioned cleaning of the first step and the second step may be carried out continuously. In the first cleaning, only the first step is carried out, and after a certain period of operation, the second cleaning is carried out as the second cleaning. You may make it wash.

【0025】また、前記した実施例では膜エレメント2
に4つの通水口7a,7b,7c,7dを設け、2つの
通水口7a,7cの接続口17a,17cに吸引ポンプ
28側の取出管26a,26bを、残りの2つの通水口
7b,7dの接続口17b,17dに供給管32a,3
2bを接続し、各管に設けた開閉弁27a,27b,2
7e,27fの切換により連通する接続口17、即ち通
水口を選択可能として透過室6内に導入する洗浄液の流
れ方向を切り換えるようにしたが、本発明における通水
口7の数は3個以上であればよく、また、透過室6内の
洗浄液の流れを切り換える弁の機構も前記実施例に限定
されるものではなく適宜設計変更することができる。
Further, in the above-mentioned embodiment, the membrane element 2
Is provided with four water passages 7a, 7b, 7c, 7d, and the connection pipes 17a, 17c of the two water passages 7a, 7c are connected to the extraction pipes 26a, 26b on the suction pump 28 side and the remaining two water passages 7b, 7d. Supply pipes 32a, 3 to the connection ports 17b, 17d of
Open / close valves 27a, 27b, 2 provided on each pipe by connecting 2b
The connection port 17 communicating with each other by switching between 7e and 27f, that is, the water passage port is selectable so that the flow direction of the cleaning liquid introduced into the permeation chamber 6 is switched, but the number of the water passage ports 7 in the present invention is three or more. The valve mechanism for switching the flow of the cleaning liquid in the permeation chamber 6 is not limited to the above embodiment, and the design can be changed as appropriate.

【0026】そして、前記第1実施例では、互いに対角
に位置する一方の通水口7から洗浄液を導入して取出管
側の他方の通水口7から吸引等によって回収して洗浄
し、第2実施例では、2つの通水口7から洗浄液を導入
し、これらの対角に位置する1つの通水口7から回収し
て洗浄したが、互いに対角に位置する通水口7について
順に導入、回収するようにしてもよい。
In the first embodiment, the cleaning liquid is introduced from one of the water passages 7 located diagonally to each other, and is collected and washed by suction from the other water passage 7 on the side of the discharge pipe. In the embodiment, the cleaning liquid is introduced from the two water passages 7 and is collected and washed from one water passage 7 located diagonally to these, but the water passages 7 diagonally located to each other are sequentially introduced and collected. You may do it.

【0027】また、図7に示すように、膜エレメント
2′は、平らで四角のスペーサ38の両面に同大の平膜
4,4を重ね、左右の対向する端縁はそのまま開放して
おき、他の端縁、即ち本実施例では上縁と下縁を熱、接
着、高周波溶着などによりシールして一体に構成し、二
枚の平膜4,4の間に透過流路(透過室)39を形成
し、対向する端縁、即ち本実施例では左右の端縁に集水
管40a,40bを設けて該集水管40a,40bに透
過流路39を連通したものである。この様な構成からな
る膜エレメント2を複数枚並べて膜ユニット1として浸
漬槽25の液中に浸漬したならば、一方の集水管40a
に前記主供給管32cを、他方の集水管40bを前記主
取出管26cを接続する。なお、各集水管40a,40
bを供給管や取出管に直接接続してもよいが、一方の集
水管40a群に連通する第5水路を設けるとともに、他
方の集水管40b群に連通する第6水路を設け、第5水
路を供給管32に、第6水路を取出管26に接続しても
よい。
Further, as shown in FIG. 7, in the membrane element 2 ', flat membranes 4 and 4 of the same size are superposed on both surfaces of a flat and square spacer 38, and the left and right opposite edges are left open. , The other edge, that is, the upper edge and the lower edge in this embodiment are sealed by heat, adhesion, high-frequency welding, or the like to be integrally formed, and the permeation channel (permeation chamber) is formed between the two flat membranes 4 and 4. ) 39 is formed, and water collecting pipes 40a, 40b are provided at the opposite edges, that is, the left and right edges in this embodiment, and the permeation flow path 39 is communicated with the water collecting pipes 40a, 40b. If a plurality of membrane elements 2 having such a configuration are arranged and immersed as the membrane unit 1 in the liquid in the dipping tank 25, one water collecting pipe 40a
To the main supply pipe 32c and the other water collecting pipe 40b to the main take-out pipe 26c. In addition, each water collection pipe 40a, 40
Although b may be directly connected to the supply pipe or the take-out pipe, a fifth water channel communicating with one of the water collecting pipes 40a group is provided, and a sixth water channel communicating with the other water collecting pipe 40b group is also provided. May be connected to the supply pipe 32 and the sixth water channel may be connected to the extraction pipe 26.

【0028】透過水を採水するには膜ユニット1と吸引
ポンプ28との間の開閉弁、貯槽30への分岐管の途中
の開閉弁を開き、主供給管32cの途中の開閉弁を閉じ
て、吸引ポンプ28を運転する。これにより、浸漬槽2
5内の液のうち、吸引ポンプ28の吸引と水頭差で膜を
透過した透過水は各膜エレメント2の透過流路39から
他方の集水管40bに集まり、主取出管26cおよび分
岐管を介して貯槽30に入る。
To collect permeated water, the on-off valve between the membrane unit 1 and the suction pump 28, the on-off valve in the middle of the branch pipe to the storage tank 30 are opened, and the on-off valve in the middle of the main supply pipe 32c is closed. Then, the suction pump 28 is operated. As a result, the immersion tank 2
Of the liquid in 5, the permeated water that has permeated the membrane due to the suction of the suction pump 28 and the head difference collects from the permeation flow channel 39 of each membrane element 2 to the other water collection pipe 40b, and passes through the main extraction pipe 26c and the branch pipe. Enter the storage tank 30.

【0029】透過水の採水工程を行ない、膜の外面にあ
る程度ケークが付着したら、貯槽30への分岐管の開閉
弁を閉じ、主供給管32cの開閉弁を開き、吸引ポンプ
28と薬液ポンプ34を運転し、これにより各膜エレメ
ント2の透過流路内に一方の集水管40aから水や薬液
などの洗浄液を導入し、他方の集水管40bからこの洗
浄液を回収して洗浄する。
After the permeated water sampling step is performed and the cake has adhered to the outer surface of the membrane to some extent, the on / off valve of the branch pipe to the storage tank 30 is closed, the on / off valve of the main supply pipe 32c is opened, and the suction pump 28 and the chemical liquid pump are opened. 34 is operated, whereby a cleaning liquid such as water or a chemical liquid is introduced into the permeation flow path of each membrane element 2 from one water collecting pipe 40a, and this cleaning liquid is collected and cleaned from the other water collecting pipe 40b.

【0030】この様にして洗浄すると、本実施例におけ
る膜エレメント2は、一方の集水管40aに透過室6の
一側が連通して他側が他方の集水管40bに連通してい
るので、一方の集水管40aから透過流路39内に導入
された洗浄液が膜面の全域に均等に流れて他方の集水管
40bに回収され、これにより膜面の全域を確実に洗浄
することができる。
When the membrane element 2 in this embodiment is washed in this way, one side of the permeation chamber 6 is in communication with one of the water collection pipes 40a and the other side is in communication with the other water collection pipe 40b. The cleaning liquid introduced from the water collection pipe 40a into the permeation flow channel 39 uniformly flows over the entire area of the membrane surface and is collected in the other water collection tube 40b, whereby the entire area of the membrane surface can be reliably cleaned.

【0031】なお、前記した各実施例では、薬液槽33
の薬液を所定濃度の洗浄液にしたり、透過室6内の洗浄
液を置換するのに貯槽30の透過水を使用したが、貯槽
30とは別に、浸漬槽25よりも上位に清水槽を設け、
置換水の供給管を清水槽の清水中に上から突入させ、薬
液の希釈、置換を清水で行なってもよい。
In each of the above-described embodiments, the chemical liquid tank 33
Although the permeated water of the storage tank 30 was used to replace the cleaning liquid having a predetermined concentration with the cleaning liquid having a predetermined concentration or to replace the cleaning liquid in the permeation chamber 6, a fresh water tank is provided above the immersion tank 25 in addition to the storage tank 30.
The supply pipe of the replacement water may be rushed into the fresh water of the fresh water tank from above to dilute or replace the chemical liquid with the fresh water.

【0032】[0032]

【発明の効果】以上説明したように本発明によれば、膜
エレメントの透過水側の流路に特別な手段を施すことな
く膜面の全域にわたって均一に洗浄液を分布させて洗浄
することができる。したがって、薬品洗浄の効果を毎回
期待することができ、膜性能を長期間維持することがで
きる。
As described above, according to the present invention, the cleaning liquid can be uniformly distributed and cleaned over the entire area of the membrane surface without providing any special means in the permeate side flow passage of the membrane element. . Therefore, the effect of chemical cleaning can be expected every time, and the membrane performance can be maintained for a long time.

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

【図1】本発明の第1実施例のフローシートである。FIG. 1 is a flow sheet of a first embodiment of the present invention.

【図2】膜エレメントの一部を剥離した斜視図である。FIG. 2 is a perspective view in which a part of a membrane element is peeled off.

【図3】膜エレメントにガスケットを重ねた正面図であ
る。
FIG. 3 is a front view of a gasket overlaid on a membrane element.

【図4】膜ユニットの組立状態の一部の拡大断面図であ
る。
FIG. 4 is an enlarged sectional view of a part of the assembled state of the membrane unit.

【図5】洗浄範囲を示す膜の正面図であり、(A)は洗
浄液を左上の通水口から右下の通水口に通した状態の主
洗浄範囲を示し、(B)は左下の通水口から右上の通水
口に通した状態の主洗浄範囲を示す。
FIG. 5 is a front view of a membrane showing a cleaning range, (A) shows a main cleaning range in which a cleaning liquid is passed from an upper left water passage to a lower right water passage, and (B) is a lower left water passage. Shows the main cleaning range with the water passing through the upper right through to the water inlet.

【図6】洗浄範囲を示す膜の正面図であり、(A)は洗
浄液を左側の両通水口から右上の通水口に通した状態の
主洗浄範囲を示し、(B)は左側の両通水口から右下の
通水口に通した状態の主洗浄範囲を示す。
FIG. 6 is a front view of a membrane showing a cleaning range, (A) shows a main cleaning range in which a cleaning liquid is passed from both left water passages to an upper right water passage, and (B) is a left both passages. The main cleaning range is shown from the water inlet to the lower right water inlet.

【図7】膜の左右の端縁に集水管を設けた膜エレメント
の正面図である。
FIG. 7 is a front view of a membrane element provided with water collecting pipes on the left and right edges of the membrane.

【図8】図7に示す膜エレメントの集水管部分の拡大断
面図である。
8 is an enlarged sectional view of a water collecting pipe portion of the membrane element shown in FIG.

【符号の説明】[Explanation of symbols]

1 膜ユニット 2 膜エレメント 3 流路スペーサ 4 膜 6 透過室 7 通水口 10,11 端板 17 接続口 21 第1水路 22 第2水路 23 第3水路 24 第4水路 25 浸漬槽 26 取出管 27 開閉弁 28 吸引ポンプ 29 分岐管 30 貯槽 31 排水槽 32 供給管 33 薬液槽 34 薬液ポンプ 35 薬液管 38 スペーサ 39 透過流路 40 集水管 1 Membrane Unit 2 Membrane Element 3 Channel Spacer 4 Membrane 6 Permeate Chamber 7 Water Port 10, 11 End Plate 17 Connection Port 21 First Channel 22 Second Channel 23 Third Channel 24 Fourth Channel 25 Immersion Tank 26 Ejection Tube 27 Opening / Closing Valve 28 Suction pump 29 Branch pipe 30 Storage tank 31 Drainage tank 32 Supply pipe 33 Chemical liquid tank 34 Chemical liquid pump 35 Chemical liquid pipe 38 Spacer 39 Permeable flow passage 40 Water collection pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 膜透過水が入る透過室を備えた膜エレメ
ントを複数並べて液中に浸漬し、膜分離装置を行う浸漬
型膜分離装置において、 各膜エレメントに3個以上の通水口を設け、これら通水
口の1以上に吸引ポンプ側の取出管を、残りの通水口に
水や薬液の供給管を接続し、前記管には弁を設けて連通
する通水口を選択可能とし、弁の切換操作によって、各
膜エレメントの透過室内に水や薬液を導入する際の流れ
方向を切換可能にしたことを特徴とする浸漬型膜分離装
置。
1. A submerged membrane separation apparatus in which a plurality of membrane elements each having a permeation chamber for receiving permeated water are arranged and immersed in a liquid to perform a membrane separation apparatus. Each membrane element is provided with three or more water passage ports. , A suction pump side extraction pipe is connected to one or more of these water passages, and a water or chemical solution supply pipe is connected to the remaining water passages, and a valve is provided in the pipes so that the water passages communicating with each other can be selected. An immersion type membrane separation device characterized in that the flow direction when introducing water or a chemical solution into the permeation chamber of each membrane element can be switched by a switching operation.
【請求項2】 スペーサの両側に膜を配置して対向する
端縁に集水管を設け、スペーサの透過流路を集水管に連
通して膜エレメントを構成し、この膜エレメントを複数
並べて液中に浸漬し、膜分離を行う浸漬型膜分離装置に
おいて、 各膜エレメントの一方の集水管を吸水ポンプ側の取出管
に接続し、他方の集水管を水や薬液の供給管に接続した
ことを特徴とする浸漬型膜分離装置。
2. Membranes are arranged on both sides of the spacer, water collecting pipes are provided at opposite edges, and a permeation channel of the spacer is connected to the water collecting pipe to form a membrane element. In a submerged membrane separation device that performs membrane separation by immersing in one of the membrane elements, one of the water collection pipes of each membrane element should be connected to the extraction pipe on the water absorption pump side, and the other water collection pipe should be connected to the water or chemical supply pipe. Characteristic immersion type membrane separation device.
JP19718694A 1994-08-01 1994-08-01 Immersion type membrane separation device Expired - Fee Related JP3575072B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11207332A (en) * 1998-01-28 1999-08-03 Maezawa Ind Inc Immersion type membrane filtering device of siphon suction system
WO2009069294A1 (en) 2007-11-28 2009-06-04 Kubota Corporation Dipping type film-separating apparatus, and film cartridge
WO2011092804A1 (en) * 2010-01-26 2011-08-04 阿波製紙株式会社 Filtration device
JP2015192937A (en) * 2014-03-31 2015-11-05 三機工業株式会社 Immersion type membrane separation unit and operational method thereof
JP2019166424A (en) * 2018-03-22 2019-10-03 株式会社クボタ Wastewater treatment device and wastewater treatment method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11207332A (en) * 1998-01-28 1999-08-03 Maezawa Ind Inc Immersion type membrane filtering device of siphon suction system
WO2009069294A1 (en) 2007-11-28 2009-06-04 Kubota Corporation Dipping type film-separating apparatus, and film cartridge
CN101878062A (en) * 2007-11-28 2010-11-03 株式会社久保田 Dipping type film-separating apparatus, and film cartridge
US9878290B2 (en) 2007-11-28 2018-01-30 Kubota Corporation Submerged membrane separator and membrane cartridge
WO2011092804A1 (en) * 2010-01-26 2011-08-04 阿波製紙株式会社 Filtration device
JP5244913B2 (en) * 2010-01-26 2013-07-24 阿波製紙株式会社 Filtration device
US8778183B2 (en) 2010-01-26 2014-07-15 Awa Paper Mfg. Co., Ltd. Filtering apparatus
JP2015192937A (en) * 2014-03-31 2015-11-05 三機工業株式会社 Immersion type membrane separation unit and operational method thereof
JP2019166424A (en) * 2018-03-22 2019-10-03 株式会社クボタ Wastewater treatment device and wastewater treatment method

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