JPH07116482A - Submerged type membrane separation device - Google Patents

Submerged type membrane separation device

Info

Publication number
JPH07116482A
JPH07116482A JP29151693A JP29151693A JPH07116482A JP H07116482 A JPH07116482 A JP H07116482A JP 29151693 A JP29151693 A JP 29151693A JP 29151693 A JP29151693 A JP 29151693A JP H07116482 A JPH07116482 A JP H07116482A
Authority
JP
Japan
Prior art keywords
membrane
water
liquid
chamber
permeation
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
JP29151693A
Other languages
Japanese (ja)
Other versions
JP3401874B2 (en
Inventor
Shigeki Sawada
繁樹 沢田
Katsumi Ishiguro
克己 石黒
Kazuo Imai
和夫 今井
Kunihiro Iwasaki
邦博 岩崎
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 JP29151693A priority Critical patent/JP3401874B2/en
Publication of JPH07116482A publication Critical patent/JPH07116482A/en
Application granted granted Critical
Publication of JP3401874B2 publication Critical patent/JP3401874B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To perform effective washing by a method wherein washing liquid is introduced into a permeation chamber of a membrane unit, without imparting excessive pressure to a membrane, to replace permeation water, in the chamber, having permeated the membrane with the washing liquid, and the washing liquid is made to permeate the membrane in a direction opposite to the direction of the flow of the water so that gel-like cake attached to the outer surface of the membrane is separated and removed. CONSTITUTION:In a submerged type membrane separation device wherein a membrane unit 10 provided with membranes and a permeation chamber 11, into which water having permeated the membranes flow in, is submerged in a liquid to perform a membrane separation process, a plurality of connection ports 23 in communication with the permeation chamber 11 are formed in the unit 10, and a takeout pipe 2 including a suction pump P1 is connected to one of the ports 23 and a feed pipe 5 for water or chemical liquid is connected to other one of the ports 23 so that the water or chemical is introduced through the feed pipe 5 into the permeation chamber by operating the suction pump to replace the liquid in the chamber with the water or chemical liquid.

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、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)膜などの膜と、膜を透過した水が入る透
過室とを備えた膜ユニットを液中に浸漬し、膜分離処理
を行う浸漬型膜分離装置に関する。
BACKGROUND OF THE INVENTION The present invention relates to a reverse osmosis membrane, an ultrafiltration membrane, a microfiltration membrane, a membrane such as a polymer membrane, an inorganic (alumina ceramic etc.) membrane, and a water permeation membrane that permeates the membrane. The present invention relates to an immersion type membrane separation device that performs a membrane separation treatment by immersing a membrane unit having a chamber in a liquid.

【0002】[0002]

【従来の技術】浸漬型膜分離装置は、膜ユニットを浸漬
した浸漬槽内の水深に基づく水頭差を利用し、吸引ポン
プ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。本特許出願人は特願平5−15941号、平
成5年9月28日付特許出願で多数枚の平膜による膜ユ
ニットを提案し、浸漬槽を洗浄するなど槽内の液を抜き
出す際、透過室に残存する透過水の重量ないし水圧で膜
が破損するのを有効に防止した。膜ユニットによって、
透過水の膜分離工程を行うと、膜の外面にはゲル状物の
ケークが付着し、次第に透過が阻害されるので、ケーク
が或る程度、付着したらケークを剥離除去する洗浄を行
うことが必要である。
2. Description of the Related Art Immersion type membrane separators are capable of obtaining permeated water by utilizing a water head difference based on the water depth in an immersion tank in which a membrane unit is immersed and performing a membrane separation with a low energy by a suction pump. The applicant of the present patent proposed in Japanese Patent Application No. Hei 5-15941, a patent application dated September 28, 1993, a membrane unit consisting of a number of flat membranes, and permeated when the liquid in the tank was extracted by washing the dipping tank. The membrane was effectively prevented from being damaged by the weight or water pressure of the permeated water remaining in the chamber. By the membrane unit,
When the permeation process of the permeated water is carried out, the cake of gel-like substance adheres to the outer surface of the membrane, and the permeation of the cake is gradually obstructed. is necessary.

【0003】[0003]

【発明が解決しようとする課題】ケークの除去は、加圧
水等により薬液を透過室に注入し、薬液を透過水とは逆
に膜に透過させる逆洗が最も効果的であるが、そうする
と余剰の圧力が膜に作用し、膜の破損が頻繁に生じる。
このため浸漬槽の液に薬剤を添加して洗浄する方法を採
らざるを得ない。しかし、この方法では多量の薬液を必
要とし、廃液処理の負担を高める。又、浸漬槽を耐薬品
性にする必要があった。
The most effective method for removing the cake is backwashing in which the chemical solution is injected into the permeation chamber by pressurized water or the like, and the chemical solution is permeated through the membrane in the opposite direction to the permeation water. Pressure acts on the membrane causing frequent breakage of the membrane.
For this reason, there is no choice but to adopt a method of adding a chemical to the liquid in the dipping tank and washing the liquid. However, this method requires a large amount of chemical liquid and increases the burden of waste liquid treatment. Further, it is necessary to make the dipping tank chemically resistant.

【0004】[0004]

【課題を解決するための手段】本発明は上記に鑑み開発
されたもので、液中に浸漬した膜ユニットに透過室と連
通する複数の接続口を設け、上記接続口の一つに吸引ポ
ンプを有する透過水の取出管を接続し、接続口の他の一
つに水や薬液の供給管を接続し、吸引ポンプの運転によ
り供給管を通じ透過室内に水や薬液を導入して室内の液
と置換できるようにしたことを特徴とする。
The present invention was developed in view of the above, and a plurality of connection ports communicating with a permeation chamber are provided in a membrane unit immersed in a liquid, and one of the connection ports is a suction pump. The permeated water extraction pipe is connected, and the water or chemical liquid supply pipe is connected to the other one of the connection ports, and water or the chemical liquid is introduced into the permeation chamber through the supply pipe by operating the suction pump. It is characterized in that it can be replaced with.

【0005】[0005]

【実施例】図4〜7は、本出願人が平成5年9月28日
付特許出願で提案した平膜による膜ユニット10を示
し、膜ユニットを構成する1枚宛の平膜エレメント11
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12の両面に同大の平膜13,13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14して一体に構成し、二枚の平膜13,13の間
にシール14で囲まれた透過室11´を形成する。尚、
平膜エレメント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、各平膜エレメントに
はシール14で囲まれた透過室11´内の一対角方向の
コーナに通水口15,15が設けてある。16は平膜エ
レメントの通水口15を有するコーナに配置し、隣接す
る二枚の平膜エレメントの間に所定の通水間隔18を保
つ弾性のガスケットで、平膜エレメントのコーナに対応
した直角な二辺を有する三角形又は四角形で、通水口1
5に連通する同大の開口17を有する。
Examples FIGS. 4 to 7 show a membrane unit 10 made of a flat membrane proposed by the applicant in the patent application dated September 28, 1993, and a flat membrane element 11 for one sheet constituting the membrane unit is shown.
Is a flat, square, net-shaped flow path spacer 12 made of tricot knitted fabric, and flat membranes 13, 13 of the same size are superposed on both surfaces, and the four peripheral edges are sealed 14 by heat, adhesion, high-frequency welding, or the like. To form an integral body and form a permeation chamber 11 ′ surrounded by a seal 14 between the two flat membranes 13, 13. still,
The flat sheet membrane element may be formed by directly forming a film on both the front and back surfaces of the spacer of the porous member. Each flat sheet membrane element is provided with water passages 15 and 15 at diagonal corners in the permeation chamber 11 ′ surrounded by the seal 14. Reference numeral 16 denotes an elastic gasket which is arranged at a corner having a water passage port 15 of the flat sheet membrane element and maintains a predetermined water passage interval 18 between two adjacent flat sheet membrane elements, and which is a right angle corresponding to the corner of the flat sheet membrane element. Triangular or quadrangular with two sides, water passage 1
5 has an opening 17 of the same size communicating with 5.

【0006】19と20は、ガスケット16で通水間隔
を保って並べ重ねた複数枚の平膜エレメントの一列を対
向して挟圧する端板で、大きさは膜エレメントと同大で
ある。各端板には、平膜エレメントの通水口15,15
と連通する貫通孔21が同じ一対角方向に開設してあ
る。端板19と20の貫通孔は、相対向した部分が平膜
エレメントの通水口15や、ガスケット16の開口17
と同大の大径部22であり、残部は締付けボルト25が
通る小径部24になっている。そして、大径部22の奥
に外面に開口した接続口23が設けてある。
Reference numerals 19 and 20 denote end plates for sandwiching and opposing a row of a plurality of flat sheet membrane elements arranged side by side with a gasket 16 at a water-passing interval and having the same size as the membrane element. Each end plate has a water inlet 15, 15 for the flat sheet membrane element.
A through hole 21 communicating with is opened in the same diagonal direction. The through holes of the end plates 19 and 20 are such that the portions facing each other are the water passage port 15 of the flat sheet membrane element and the opening 17 of the gasket 16.
And a large-diameter portion 22 of the same size as the above, and the remaining portion is a small-diameter portion 24 through which the tightening bolt 25 passes. Further, a connection port 23 opened to the outer surface is provided at the back of the large diameter portion 22.

【0007】膜ユニットに組立てるには、所定の枚数の
膜エレメント11をガスケット16を介して一列に並べ
重ね(平膜エレメントの通水口15とガスケットの開口
17は連通させる)、連通している全部の平膜エレメン
トの通水口15と、全部のガスケットの開口17に一連
にボルト25を貫通し、ボルト25の各端部に貫通孔2
1を嵌めて端板19と20で平膜エレメント11…、ガ
スケット16を挟み、ボルトの各端部にねじ込んだナッ
ト26を端板19,20に対し締付け、平膜エレメント
とガスケットを挟圧して一体にする。尚、ボルト25の
各端部の、貫通孔の小径部23内に位置する部分にはO
リング27を嵌めてシールを行う。これにより端板の貫
通孔の大径部22と、ガスケットの開口17と、膜エレ
メントの通水孔15とが一連に連なり、個々の平膜エレ
メントの透過室11´を連通させる水路28,29が一
対角方向に2つ生じる。
In order to assemble the membrane unit, a predetermined number of membrane elements 11 are lined up in a row through the gasket 16 (the water inlet 15 of the flat membrane element and the opening 17 of the gasket communicate with each other) and all communicate with each other. The bolts 25 pass through the water inlet 15 of the flat membrane element and the openings 17 of all the gaskets in series, and the through holes 2 are formed at the respective ends of the bolts 25.
1 is fitted and the flat plate element 11 and the gasket 16 are sandwiched between the end plates 19 and 20, and the nut 26 screwed into each end of the bolt is tightened to the end plates 19 and 20, and the flat film element and the gasket are sandwiched. Make one. It should be noted that at each end of the bolt 25, a portion located in the small diameter portion 23 of the through hole is
The ring 27 is fitted and sealed. As a result, the large-diameter portion 22 of the through hole of the end plate, the opening 17 of the gasket, and the water passage hole 15 of the membrane element are connected in series, and the water passages 28 and 29 for connecting the permeation chambers 11 'of the individual flat sheet membrane elements are connected. Occurs in two diagonal directions.

【0008】図1は上記膜ユニットを、どちらか一方の
水路が上、他方が下となるように浸漬槽1の液中に浸漬
し、上になった水路28の端板19,20にある接続口
23の一方に吸引ポンプPを途中に有する透過水の取出
管2を連結して他方の接続口は栓で閉じる。取出管は吸
引ポンプの下流で二つに分岐し、分岐管一方2aは起ち
上り、水面が浸漬槽1と同じか、それよりも上位の透過
水の貯槽3に上から開口し、分岐管の他方2bは真っ直
ぐに延びて排水槽4に開口する。分岐管2a,2bには
開閉弁V1 ,V2 を途中に設ける。膜ユニットの下にな
った水路29の端板19,20にある接続口23の一方
には前記貯槽3の液中に上から突入し、置換水の供給管
5を連結し、他方の接続口23は栓で閉じる。そして、
薬液槽6内の薬液をポンプP2 で注入する薬注管7を供
給管5の途中に接続する。尚、供給管5には、薬注管の
接続点よりも水路29側に開閉弁V3 を設け、浸漬槽1
には原水の供給管と、底に排泥管8を設ける。
FIG. 1 shows that the above membrane unit is immersed in the liquid of the dipping tank 1 so that one of the water channels is on the top and the other is on the bottom plate, and the end plates 19 and 20 of the water channel 28 are on the upper side. The permeate extraction pipe 2 having a suction pump P in the middle is connected to one of the connection ports 23, and the other connection port is closed with a plug. The take-out pipe branches into two downstream of the suction pump, and one of the branch pipes 2a rises, and the water surface is the same as that of the immersion tank 1 or opens to the permeate storage tank 3 above it from above, The other 2b extends straight and opens into the drainage tank 4. Branch pipe 2a, the 2b provided in the middle of the on-off valve V 1, V 2. One of the connection ports 23 in the end plates 19 and 20 of the water channel 29 below the membrane unit projects into the liquid in the storage tank 3 from above, connects the replacement water supply pipe 5, and connects the other connection port. 23 is closed with a stopper. And
A chemical injection pipe 7 for injecting the chemical liquid in the chemical liquid tank 6 with a pump P 2 is connected in the middle of the supply pipe 5. The supply pipe 5 is provided with an opening / closing valve V 3 on the water channel 29 side of the connection point of the chemical injection pipe, and the immersion tank 1
Is provided with a raw water supply pipe and a mud discharge pipe 8 at the bottom.

【0009】透過水を採水するには開閉弁V1 を開、V
2 ,V3 を閉にし、吸引ポンプP1を運転する。これに
より、浸漬槽内の液のうち、ポンプの吸引と、水頭差で
膜を透過した透過水は透過室から管2,2aを流れ、貯
槽3に入る。
To collect permeated water, open the on-off valve V 1 ,
2 and V 3 are closed and the suction pump P 1 is operated. As a result, of the liquid in the immersion tank, the permeated water that has permeated the membrane due to the suction of the pump and the water head difference flows from the permeation chamber to the pipes 2 and 2a and enters the storage tank 3.

【0010】透過水の採水工程を行い、膜の外面に或る
程度ケークが付着したら、開閉弁V1 を閉、V2 ,V3
を開にして、吸引ポンプP1 と薬液用ポンプP2 を運転
して洗浄を行う。これにより膜ユニットの透過室を満た
している透過水は吸引ポンプで引かれ、管2,2bを流
れて排水槽4に入ると同時に、貯槽3内の透過水が浸漬
槽1との水頭差、及び吸引ポンプの吸引で置換水の供給
管5内を膜ユニットに向かって流れ、薬注管7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に過剰
な圧力を付加することなく透過室に入る。こうして、洗
浄液が透過室内の透過水と置換したら、吸引ポンプP1
と、薬液用ポンプP2 の運転を停め、開閉弁V1 以外に
2 も閉にし、貯槽3と浸漬槽1との水頭差で洗浄液を
透過室に送り込み、透過室内の洗浄液を膜の内面から外
面に透過させ、外面に付着するケークを剥離する。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容易
に膜の外面から剥れ、除去される。除去されたケークは
排泥管8の弁を開いて浸漬槽から排出する。
The permeated water sampling step is performed, and when a certain amount of cake adheres to the outer surface of the membrane, the on-off valve V 1 is closed and V 2 and V 3 are closed.
Is opened, and the suction pump P 1 and the chemical solution pump P 2 are operated for cleaning. As a result, the permeated water that fills the permeation chamber of the membrane unit is drawn by the suction pump, flows through the pipes 2 and 2b and enters the drainage tank 4, and at the same time, the permeated water in the storage tank 3 has a head difference from the immersion tank 1, And flowing by suction of the suction pump toward the membrane unit in the replacement water supply pipe 5 to merge with the chemical liquid injected in the chemical injection pipe 7 to become a cleaning liquid having a predetermined concentration and to apply excessive pressure to the membrane. Instead, enter the permeation chamber. In this way, when the cleaning liquid replaces the permeated water in the permeation chamber, the suction pump P 1
Then, the operation of the chemical liquid pump P 2 is stopped, V 2 is closed in addition to the on-off valve V 1 , and the cleaning liquid is sent to the permeation chamber by the water head difference between the storage tank 3 and the immersion tank 1, and the cleaning liquid in the permeation chamber is transferred to the inner surface of the membrane. To the outer surface and peel off the cake adhering to the outer surface. Since the cleaning liquid permeates the membrane in the direction opposite to the permeated water, the cake easily peels off from the outer surface of the membrane and is removed. The removed cake is discharged from the dipping tank by opening the valve of the mud discharge pipe 8.

【0011】洗浄が終ったら開閉弁V1 を閉、V2 ,V
3 を開にし、吸引ポンプP1 を運転し、透過室内の洗浄
液を排水槽4に吸引して入れ、同時に貯槽内の透過水を
吸引ポンプの吸引と、貯槽と浸漬槽の水頭差で供給管5
から透過室に入れ、透過室内の洗浄液を透過水で置換す
る。透過室内が透過水で置換したら、開閉弁V1 を開
き、V2 ,V3 を閉じ、透過水の採水工程を再開する。
When the cleaning is completed, the on-off valve V 1 is closed and V 2 , V
3 is opened, the suction pump P 1 is operated, the cleaning liquid in the permeate chamber is sucked into the drainage tank 4, and at the same time, the permeated water in the storage tank is sucked by the suction pump and the supply pipe is supplied by the head difference between the storage tank and the immersion tank. 5
To the permeate chamber, and the permeate replaces the cleaning liquid in the permeate chamber. After the permeate chamber is replaced with the permeate, the on-off valve V 1 is opened, V 2 and V 3 are closed, and the permeate water sampling process is restarted.

【0012】この実施例では、薬液槽6の薬液を所定濃
度の洗浄液にしたり、透過室内の洗浄液を置換するのに
貯槽3の透過水を使用したが、図2の実施例のように貯
槽とは別に、浸漬槽よりも上位に清水槽9を設け、置換
水の供給管5を清水槽の清水中に上から突入させ、薬液
の稀釈、置換を清水で行ってもよい。又、図3の実施例
のように水路28に吸引ポンプを有する二本の取出管
2,2´を連結し、一方の取出管2は貯槽3に上から開
口させ、他方の取出管2´は排水槽4に上から開口さ
せ、透過水の採水工程は取出管2の吸引ポンプP1 を運
転し、透過室内の液を置換するときは取出管2´の吸引
ポンプP3 を運転するようにしてもよい。
In this embodiment, the chemical liquid in the chemical liquid tank 6 is used as a cleaning liquid having a predetermined concentration, and the permeated water in the storage tank 3 is used to replace the cleaning liquid in the permeation chamber. However, as in the embodiment of FIG. Separately, a fresh water tank 9 may be provided above the dipping tank, and the replacement water supply pipe 5 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. Further, as in the embodiment of FIG. 3, two outlet pipes 2 and 2'having suction pumps are connected to the water channel 28, one of the outlet pipes 2 is opened to the storage tank 3 from above, and the other outlet pipe 2 '. causes the opening from above the drainage tank 4, water sampling step of permeate operated suction pump P 1 of the take-out tube 2, when replacing the transmission chamber of the liquid to drive the suction pump P 3 of the take-out tube 2 ' You may do it.

【0013】膜ユニットの膜は図示した平膜に限定され
ず、中空糸形膜、管形膜その他何でもよい。又、膜ユニ
ットへの透過水の取出管の接続位置と、置換水の供給管
の接続位置は、図示の実施例では対向し、これにより水
や薬液の短絡を防止できるが、必ずしも対向する位置に
設けなくてもよい。更に、薬液槽6の薬液はポンプP
2 、薬注管7で供給管5に供給し、貯槽3からの透過水
や、清水槽9からの清水に合流させて透過室に供給した
が、図2に示すように合流させずに薬注管7を膜ユニッ
トの接続口に接続して直接透過室に供給し、透過室内で
供給管5から供給された透過水や清水と混合し、洗浄液
に希釈してもよい。又、薬液はポンプP2 で供給する以
外に、弁を有する薬注管によって落差で供給してもよ
い。
The membrane of the membrane unit is not limited to the illustrated flat membrane, and may be a hollow fiber membrane, a tubular membrane or any other membrane. Further, the connection position of the permeated water extraction pipe to the membrane unit and the connection position of the replacement water supply pipe are opposed to each other in the illustrated embodiment, which can prevent a short circuit of water or a chemical solution, but are not necessarily opposed to each other. Need not be provided. Further, the chemical liquid in the chemical liquid tank 6 is pump P
2. It was supplied to the supply pipe 5 by the chemical injection pipe 7 and was combined with the permeated water from the storage tank 3 and the fresh water from the fresh water tank 9 to be supplied to the permeation chamber. However, as shown in FIG. The injection pipe 7 may be directly connected to the connection port of the membrane unit to be directly supplied to the permeation chamber, and may be mixed with permeated water or fresh water supplied from the supply pipe 5 in the permeation chamber to be diluted with the cleaning liquid. Further, the chemical liquid may be supplied by a drop with a chemical injection pipe having a valve, instead of being supplied by the pump P 2 .

【0014】[0014]

【発明の効果】以上で明らかなように、本発明によれ
ば、洗浄の際は膜に過剰な圧力を加えることなく透過室
内の透過水を洗浄液に置換し、この洗浄液を膜の内面か
ら外面に透過させる。これにより膜の外面に付着したゲ
ル状のケークを膜を逆方向に透過する洗浄液が剥離する
ため、洗浄液の化学作用と相俟ち非常に優れた洗浄効果
が得られる。
As is apparent from the above, according to the present invention, the permeated water in the permeation chamber is replaced with the cleaning liquid without applying excessive pressure to the membrane during cleaning, and the cleaning liquid is changed from the inner surface to the outer surface of the membrane. To penetrate. As a result, the cleaning liquid that permeates the film in the reverse direction is peeled off from the gel cake attached to the outer surface of the film, so that a very excellent cleaning effect can be obtained in combination with the chemical action of the cleaning liquid.

【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】本発明の第2実施例のフローシートである。FIG. 2 is a flow sheet of a second embodiment of the present invention.

【図3】本発明の第3実施例のフローシートである。FIG. 3 is a flow sheet of a third embodiment of the present invention.

【図4】平膜による膜ユニットの一例の斜視図である。FIG. 4 is a perspective view of an example of a flat membrane unit.

【図5】膜ユニットを構成する平膜エレメントの一部を
剥離した斜視図である。
FIG. 5 is a perspective view in which a part of a flat sheet membrane element that constitutes a membrane unit is peeled off.

【図6】膜エレメントにガスケットを重ねた正面図であ
る。
FIG. 6 is a front view of a gasket overlaid on a membrane element.

【図7】平膜ユニットの組立状態の一部の拡大断面図で
ある。
FIG. 7 is an enlarged cross-sectional view of a part of an assembled state of the flat sheet membrane unit.

【符号の説明】[Explanation of symbols]

1 浸漬槽 2 取出管 3 貯槽 4 排水槽 5 供給管 6 薬液槽 7 薬注管 8 排泥管 9 清水槽 10 膜ユニット 11´ 透過室 13 膜 23 接続口 P1 吸引ポンプ1 Immersion tank 2 Extraction pipe 3 Storage tank 4 Drainage tank 5 Supply pipe 6 Chemical liquid tank 7 Chemical injection pipe 8 Mud pipe 9 Fresh water tank 10 Membrane unit 11 'Permeation chamber 13 Membrane 23 Connection port P 1 Suction pump

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岩崎 邦博 東京都新宿区西新宿3丁目4番7号 栗田 工業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Kunihiro Iwasaki 3-4-7 Nishishinjuku, Shinjuku-ku, Tokyo Kurita Industry Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 膜と、膜を透過した水が入る透過室とを
備えた膜ユニットを液中に浸漬し、膜分離処理を行う浸
漬型膜分離装置において、前記膜ユニットに透過室と連
通する複数の接続口を設け、上記接続口の一つに吸引ポ
ンプを有する透過水の取出管を接続し、接続口の他の一
つに水や薬液の供給管を接続し、吸引ポンプの運転によ
り供給管を通じ透過室内に水や薬液を導入して室内の液
と置換できるよう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 for immersing a membrane unit, which comprises a membrane and a permeation chamber into which water permeated through the membrane, in a liquid to perform membrane separation treatment, wherein the membrane unit communicates with the permeation chamber. Operation of the suction pump by providing a plurality of connection ports, connecting the permeate extraction pipe with a suction pump to one of the connection ports, and connecting the water or chemical supply pipe to the other one of the connection ports. The immersion type membrane separation device is characterized in that water or a chemical solution is introduced into the permeation chamber through the supply pipe to replace the liquid in the chamber.
JP29151693A 1993-10-28 1993-10-28 Immersion type membrane separation device Expired - Lifetime JP3401874B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29151693A JP3401874B2 (en) 1993-10-28 1993-10-28 Immersion type membrane separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29151693A JP3401874B2 (en) 1993-10-28 1993-10-28 Immersion type membrane separation device

Publications (2)

Publication Number Publication Date
JPH07116482A true JPH07116482A (en) 1995-05-09
JP3401874B2 JP3401874B2 (en) 2003-04-28

Family

ID=17769909

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29151693A Expired - Lifetime JP3401874B2 (en) 1993-10-28 1993-10-28 Immersion type membrane separation device

Country Status (1)

Country Link
JP (1) JP3401874B2 (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07124448A (en) * 1993-11-05 1995-05-16 Kubota Corp Chemicals washing method for ceramic film
FR2741280A1 (en) * 1995-11-22 1997-05-23 Omnium Traitement Valorisa METHOD OF CLEANING A IMMERING MEMBRANE TYPE FILTRATION FACILITY
WO2001008789A3 (en) * 1999-07-29 2001-08-16 Zenon Environmental Inc Maintenance cleaning for membranes
JP2001259378A (en) * 2000-03-21 2001-09-25 Sti:Kk Separation membrane module
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
JP2005161264A (en) * 2003-12-04 2005-06-23 National Institute Of Advanced Industrial & Technology Separation membrane module
US7025885B2 (en) 1998-11-23 2006-04-11 Zenon Environmental Inc. Water filtration using immersed membranes
US7063788B2 (en) 1995-08-11 2006-06-20 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
NL1028484C2 (en) * 2005-03-08 2006-09-11 Kiwa Water Res Treating a wastewater stream from a bioreactor comprises immersing a membrane filtration unit in the wastewater stream
JP2008238141A (en) * 2007-03-29 2008-10-09 Kubota Corp Water collection device
WO2010073574A1 (en) * 2008-12-25 2010-07-01 株式会社クボタ Membrane unit and membrane module
US7776214B2 (en) 2005-02-23 2010-08-17 Gs Yuasa Corporation Membrane element
CN103894072A (en) * 2012-12-27 2014-07-02 第一毛织株式会社 Separation membrane cleaning system and separation membrane cleaning method using the same
KR101447954B1 (en) * 2007-07-18 2014-10-13 주식회사 퓨어엔비텍 A membrane module cassette train with a vertical type manifold and the cleaning method
KR20150126576A (en) * 2015-10-23 2015-11-12 롯데케미칼 주식회사 Cleaning system of separation membrane and method using the same

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07124448A (en) * 1993-11-05 1995-05-16 Kubota Corp Chemicals washing method for ceramic film
US7063788B2 (en) 1995-08-11 2006-06-20 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
FR2741280A1 (en) * 1995-11-22 1997-05-23 Omnium Traitement Valorisa METHOD OF CLEANING A IMMERING MEMBRANE TYPE FILTRATION FACILITY
WO1997018887A1 (en) * 1995-11-22 1997-05-29 Otv Omnium De Traitements Et De Valorisation Method for cleaning an immersed-membrane filtration apparatus
US7025885B2 (en) 1998-11-23 2006-04-11 Zenon Environmental Inc. Water filtration using immersed membranes
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
JP2001259378A (en) * 2000-03-21 2001-09-25 Sti:Kk Separation membrane module
JP2005161264A (en) * 2003-12-04 2005-06-23 National Institute Of Advanced Industrial & Technology Separation membrane module
US7776214B2 (en) 2005-02-23 2010-08-17 Gs Yuasa Corporation Membrane element
NL1028484C2 (en) * 2005-03-08 2006-09-11 Kiwa Water Res Treating a wastewater stream from a bioreactor comprises immersing a membrane filtration unit in the wastewater stream
JP2008238141A (en) * 2007-03-29 2008-10-09 Kubota Corp Water collection 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
WO2010073574A1 (en) * 2008-12-25 2010-07-01 株式会社クボタ Membrane unit and membrane module
CN103894072A (en) * 2012-12-27 2014-07-02 第一毛织株式会社 Separation membrane cleaning system and separation membrane cleaning method using the same
US20140183132A1 (en) * 2012-12-27 2014-07-03 Cheil Industries Inc. Separation membrane cleaning system and separation membrane cleaning method using the same
KR20150126576A (en) * 2015-10-23 2015-11-12 롯데케미칼 주식회사 Cleaning system of separation membrane and method using the same

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