JPH0999223A - Membrane separation device by hollow tubular membrane - Google Patents
Membrane separation device by hollow tubular membraneInfo
- Publication number
- JPH0999223A JPH0999223A JP7282371A JP28237195A JPH0999223A JP H0999223 A JPH0999223 A JP H0999223A JP 7282371 A JP7282371 A JP 7282371A JP 28237195 A JP28237195 A JP 28237195A JP H0999223 A JPH0999223 A JP H0999223A
- Authority
- JP
- Japan
- Prior art keywords
- water
- raw water
- membrane
- hollow tubular
- water tank
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、外筒の内部に収容
された内圧型又は外圧型の中空管状膜によって原水をエ
アリフトで上向流させながら膜分離し、膜を透過した透
過水を採水する中空管状膜による膜分離装置に関するも
のである。TECHNICAL FIELD The present invention relates to an internal pressure type or external pressure type hollow tubular membrane housed inside an outer cylinder to separate raw water by an air lift while performing membrane separation and collect permeated water that has passed through the membrane. The present invention relates to a membrane separation device using a hollow tubular membrane that is watered.
【0002】[0002]
【従来の技術】図4は、従来のエアリフト循環方式の浸
漬型膜分離装置を示すもので、原水が供給される処理槽
1の水中にエアリフト筒2を立設し、エアリフト筒2の
上端に透過水の取出口7を有する複数枚の平膜エレメン
ト3を前後方向に流路間隔6を保って一列に立て並べた
膜モジュール4を配置してある。2. Description of the Related Art FIG. 4 shows a conventional air-lift circulation type submerged membrane separator, in which an air-lift cylinder 2 is erected in the water of a treatment tank 1 to which raw water is supplied, and the air-lift cylinder 2 is provided at the upper end of the air-lift cylinder 2. A membrane module 4 is arranged in which a plurality of flat sheet membrane elements 3 having permeated water outlets 7 are arranged in a row in the front-rear direction with a flow path interval 6 maintained.
【0003】エアリフト筒2は、断面形状が四角形で、
上端から下端まで断面積は一定である。散気装置5から
散気することによって、エアリフト筒2内の膜モジュー
ル4を構成する平膜エレメント3の相対向した膜面の流
路間隔6にはエアリフトによるクロスフロー上昇流が生
じ、膜面にゲル状の付着物が生成するのを防止しながら
膜を透過する透過水を平膜エレメント3の内部に得、こ
の透過水を各平膜エレメント3の取出口7に接続したヘ
ッダー管8を介してポンプPで吸引して採水する。The air lift cylinder 2 has a rectangular cross section,
The cross-sectional area is constant from the upper end to the lower end. By diffusing air from the air diffusing device 5, a cross flow upward flow due to an air lift is generated in the flow path interval 6 between the opposed membrane surfaces of the flat sheet membrane element 3 constituting the membrane module 4 in the air lift cylinder 2, and the membrane surface The permeated water that permeates the membrane is obtained inside the flat sheet membrane elements 3 while preventing the formation of gel-like deposits on the inside of the flat sheet membrane elements 3, and the permeated water is connected to the outlets 7 of the flat sheet membrane elements 3 through the header pipes 8. Water is drawn by sucking with the pump P via the.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上記従
来装置を設置するには、処理槽を構築してその内部にエ
アリフト筒を立設し、エアリフト筒上に膜モジュールを
支持し、槽底にはエアリフト筒内に気泡を浮上させる散
気装置を配置して槽外のブロアなどと配管で接続すると
共に、膜モジュールを構成する平膜エレメントの一枚宛
をヘッダー管に接続し、ヘッダー管とポンプを配管で接
続することが必要であり、設置に非常に手数が掛かる。However, in order to install the above-mentioned conventional apparatus, a processing tank is constructed, an air lift tube is erected inside the processing tank, the membrane module is supported on the air lift tube, and the tank bottom is installed. An air diffuser that floats air bubbles inside the air lift cylinder is installed and connected to a blower outside the tank by piping, and one flat membrane element that constitutes the membrane module is connected to the header pipe, and the header pipe and pump Need to be connected by piping, which is very troublesome to install.
【0005】さらに、装置の規模を増大し、原水の処理
能力を向上するための膜の充填率を高めるには、前後方
向に一列に立て並べて膜モジュールを構成する平膜エレ
メントの枚数を増加するほか、処理槽や、エアリフト筒
を前後方向に長く改造することが必要で、非常に手数が
掛かると共に、完成するまでの工期も長く、コストも非
常に嵩む。Further, in order to increase the scale of the apparatus and increase the filling rate of the membrane for improving the treatment capacity of raw water, the number of flat membrane elements constituting the membrane module by arranging them in a row in the front-rear direction is increased. In addition, it is necessary to remodel the processing tank and the air lift cylinder in the front-rear direction, which is very time-consuming and requires a long construction period until completion, resulting in a very high cost.
【0006】また、平膜エレメントは、強度上の問題か
ら平膜の大きさに限度があり、充填率を高めるためには
平膜エレメントを上下方向に多段にする必要があるが、
多段にすると設置構造、配管構造が非常に複雑になる。
さらに、浸漬型膜分離装置では定期的に膜モジュールを
槽外に取り出し、洗浄したり、取り換えたりする必要が
あるが、上述のような複雑な構造であるため膜モジュー
ルに対する平膜エレメントの取り外し、取り付けが困難
で、非常に手数が掛かる。Further, the flat sheet membrane element has a limitation in the size of the flat sheet membrane due to the problem of strength, and it is necessary to make the flat sheet membrane element in multiple stages in the vertical direction in order to increase the filling rate.
If the number of stages is increased, the installation structure and piping structure will become very complicated.
Further, in the immersion type membrane separation device, it is necessary to periodically take out the membrane module from the tank and wash or replace it, but since the membrane structure is complicated as described above, removal of the flat membrane element from the membrane module, It is difficult to install and very troublesome.
【0007】[0007]
【課題を解決するための手段】本発明は、上述した問題
点を解消するために開発されたもので、内部に原水を貯
留する水槽と、該水槽の下部に連結され、内部に原水供
給室を形成すると共に、上面の一部に開口を有する横型
の下部缶胴と、該下部缶胴の内部にその長手方向に設け
られ、原水供給室内にガスを供給する散気管と、上記下
部缶胴の上面の開口に対して着脱可能に立設された外筒
の内部に多数本の中空管状膜を収容し、中空管状膜によ
り内部が透過水集水室と、上下に開放した原水流路部と
に仕切られ、原水流路部の下端を原水供給室に連通させ
た膜エレメントと、上記外筒の上部に設けられると共に
水槽の上部に連結され、原水流路部を通過した濃縮水を
外筒から水槽内へ循環させる横型の上部缶胴とからな
り、水槽から原水供給室へ供給された原水を散気管から
供給されるガスで膜エレメントの原水流路部中を中空管
状膜に沿って上向流させ、原水流路部中を通過して上に
出た水を上部缶胴内を経て水槽内に循環し、中空管状膜
を透過した透過水を透過水集水室から外に採水するよう
にしたことを特徴とする中空管状膜による膜分離装置で
ある。The present invention was developed in order to solve the above-mentioned problems, and is a water tank for storing raw water therein, and a raw water supply chamber connected to the lower portion of the water tank. And a horizontal lower can body having an opening in a part of the upper surface thereof, an air diffuser provided inside the lower can body in the longitudinal direction thereof to supply gas into the raw water supply chamber, and the lower can body. A large number of hollow tubular membranes are housed inside an outer cylinder that is detachably erected with respect to the opening on the upper surface of the And a membrane element in which the lower end of the raw water flow passage communicates with the raw water supply chamber, and the concentrated water that has been passed through the raw water flow passage is connected to the upper part of the water tank and the upper part of the outer cylinder. It consists of a horizontal upper can body that circulates from the cylinder into the water tank. The raw water supplied to the chamber is made to flow upward along the hollow tubular membrane in the raw water flow passage of the membrane element by the gas supplied from the diffuser pipe, and the water that has passed through the raw water flow passage and comes out above is discharged. A membrane separation device using a hollow tubular membrane, wherein permeated water that has passed through the hollow tubular membrane and is circulated through the upper can body is collected from the permeated water collection chamber to the outside.
【0008】[0008]
【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図示の実施形態において、20は
内部に原水を貯留する水槽、10は水槽20の下部に連
結され、上面の一部に開口11を有する円筒形の横型下
部缶胴、12は下部缶胴10の内部下周にサポート部に
よって支持され、缶胴の長手方向に設けられた散気管、
13は下部缶胴10の端部に設けてある鍔に対し取り付
けて下部缶胴10の端部を塞ぎ、下部缶胴10の内部を
原水供給室10’に形成する端板であり、端板13の下
部には散気管12との連通口15が設けてあり、連通口
15にはブロアなどからの給気管を接続する。Embodiments of the present invention will be described below with reference to the drawings. In the illustrated embodiment, 20 is a water tank for storing raw water therein, 10 is a cylindrical horizontal lower can body connected to the lower part of the water tank 20 and has an opening 11 in a part of its upper surface, and 12 is a lower can body. An air diffuser, which is supported by the support section on the inner lower circumference and is provided in the longitudinal direction of the can body.
Reference numeral 13 denotes an end plate that is attached to a flange provided at the end of the lower can body 10 to close the end of the lower can body 10 and form the inside of the lower can body 10 in the raw water supply chamber 10 ′. A communication port 15 for communicating with the air diffuser 12 is provided in the lower part of 13, and an air supply pipe from a blower or the like is connected to the communication port 15.
【0009】この端板13は例えば四角形にし、四角の
一辺で接床して円筒形の下部缶胴10を水平状態に安定
に支持できるようにする。下部缶胴10の他方の鍔には
水槽20の下部に形成された原水供給口14が連結され
ている。この原水供給口14の鍔は、端板13と同様に
四角形にし、四角の一辺で接床して円筒形の下部缶胴1
0を水平状態に安定に支持する。The end plate 13 is, for example, a quadrangle, and is brought into contact with the floor at one side of the quadrangle so that the lower cylindrical can body 10 can be stably supported in a horizontal state. A raw water supply port 14 formed at the bottom of the water tank 20 is connected to the other flange of the lower can body 10. The brim of the raw water supply port 14 has a quadrangular shape similar to the end plate 13, and has a cylindrical lower can body 1 which comes into contact with the floor at one side of a square.
0 is supported stably in a horizontal state.
【0010】下部缶胴10の上面の一部に設けた開口1
1の回りにはフランジを設け、フランジ上に外筒16の
下端のフランジを載せて取り付け、開口11上に外筒1
6を着脱可能に立設する。なお、下部缶胴10、外筒1
6は、塩化ビニル、ポリプロピレンなどのブロー成形に
より製作する。An opening 1 provided in a part of the upper surface of the lower can body 10.
1. A flange is provided around 1, and the flange at the lower end of the outer cylinder 16 is mounted on the flange and mounted, and the outer cylinder 1 is placed on the opening 11.
6 is detachably set up. The lower can body 10 and the outer cylinder 1
6 is manufactured by blow molding of vinyl chloride, polypropylene or the like.
【0011】21は外筒16の内部に多数本の中空管状
膜22を収容した膜エレメントである。そして、この膜
エレメント21を内部に挿入配置する外筒16上には、
循環口17及び連設口28を有する横型の上部缶胴29
を設ける。上部缶胴29の循環口17には、水槽20の
上部に形成された濃縮水導入口33を連結する。一方、
上部缶胴29の連設口28には、盲板34を取付けて密
閉する。なお、水槽20は、原水の水位が膜エレメント
21の透過水集水室24内の水位よりも上方に位置する
深さ乃至高さとする。Reference numeral 21 is a membrane element in which a large number of hollow tubular membranes 22 are housed inside the outer cylinder 16. Then, on the outer cylinder 16 in which the membrane element 21 is inserted and arranged,
Horizontal upper can body 29 having a circulation port 17 and a continuous port 28
Is provided. The concentrated water introduction port 33 formed in the upper portion of the water tank 20 is connected to the circulation port 17 of the upper can body 29. on the other hand,
A blind plate 34 is attached to the connection port 28 of the upper can body 29 to seal it. The water tank 20 has a depth or height such that the water level of the raw water is located above the water level in the permeate collection chamber 24 of the membrane element 21.
【0012】図1,2に示した実施形態で使用する膜エ
レメント21の中空管状膜22は、原水を膜の中空部に
通水し、膜を透過した透過水を中空管状膜22の外に得
る内圧型で、この場合、多数本の中空管状膜22は上端
を膜エレメント21の多孔円盤状上管板25に貫通し、
下端を同様の下管板26に貫通して上下方向に配列し、
原水は1本宛の中空管状膜22の中空部中を下から上に
流れる。従って、1本宛の中空管状膜22の中空部が原
水流路部23になり、上下の管板25,26で閉じられ
た外筒16の内部(中空管状膜22の周りの空間)が透
過水集水室24になる。そして、上管板25と下管板2
6の中心に、透過水集水室24に連通した透過水の取出
口27が上下に突設してある。The hollow tubular membrane 22 of the membrane element 21 used in the embodiment shown in FIGS. 1 and 2 allows raw water to pass through the hollow portion of the membrane, and permeate that has permeated through the membrane to the outside of the hollow tubular membrane 22. In this case, a large number of hollow tubular membranes 22 penetrate the upper end of the perforated disc-shaped upper tube sheet 25 of the membrane element 21 in this case,
The lower end penetrates the same lower tube sheet 26 and is arranged vertically.
Raw water flows from the bottom to the top in the hollow portion of the hollow tubular membrane 22 addressed to one. Therefore, the hollow portion of the hollow tubular membrane 22 addressed to one becomes the raw water flow path portion 23, and the inside of the outer cylinder 16 (the space around the hollow tubular membrane 22) closed by the upper and lower tube plates 25 and 26 permeates. It becomes the water collection room 24. Then, the upper tube sheet 25 and the lower tube sheet 2
At the center of 6, a permeated water outlet 27 that communicates with the permeated water collection chamber 24 is vertically provided.
【0013】このように本実施形態では内圧型の中空管
状膜22を採用したが、これに限るものではなく、外側
から膜を通過した透過水を中空管状膜の中空部に得る外
圧型を採用することもでき、その場合には中空管状膜の
内側を上下の管板25で閉塞することになる。As described above, in this embodiment, the internal pressure type hollow tubular membrane 22 is adopted. However, the present invention is not limited to this, and an external pressure type that obtains permeated water that has passed through the membrane from the outside in the hollow portion of the hollow tubular membrane is used. Alternatively, the inner side of the hollow tubular membrane is closed by the upper and lower tube sheets 25.
【0014】図1,2の実施形態では、下部缶胴10の
内部上周に沿って、散気管12と同様に長手方向に透過
水取出管18がサポート部により吊り下げた状態で設け
てあり、端板13の上部にはこの取出管18との連通口
19が設けてある。そして、透過水取出口18には下部
缶胴10の上面に設けられた開口11の中心に向かって
上向きに突出する分岐口30が突設してある。従って、
内圧型の中空管状膜22を使用した膜エレメント21の
下管板26から下向きに突出する透過水の取出口27を
上記分岐口30に嵌合して接続することにより膜エレメ
ント21を外筒16の内部に挿入した状態で支持するこ
とができる。そして、膜エレメント21の上管板25か
ら上向きに突出する取出口27には排気管31を接続す
る。排気管31は外筒16の上端から上に突出した部分
に開閉弁32を有する。In the embodiment shown in FIGS. 1 and 2, the permeated water extraction pipe 18 is provided in the longitudinal direction along the upper inner circumference of the lower can body 10 in the same manner as the diffuser pipe 12 in a state of being suspended by a support portion. At the upper part of the end plate 13, there is provided a communication port 19 with the extraction pipe 18. The permeated water outlet 18 is provided with a branch port 30 projecting upward toward the center of the opening 11 provided on the upper surface of the lower can body 10. Therefore,
The permeated water outlet 27 projecting downward from the lower tube sheet 26 of the membrane element 21 using the internal pressure type hollow tubular membrane 22 is fitted and connected to the branch port 30 to connect the membrane element 21 to the outer cylinder 16 It can be supported in a state of being inserted inside. An exhaust pipe 31 is connected to the outlet 27 that projects upward from the upper tube plate 25 of the membrane element 21. The exhaust pipe 31 has an opening / closing valve 32 in a portion protruding upward from the upper end of the outer cylinder 16.
【0015】透過水を採水するには、水槽20の原水供
給口14に下部缶胴10を連結すると共に、水槽20の
濃縮水導入口33に上部缶胴29を連結し、散気管12
と連通した端板13の連通口15にはブロアなどからの
給気管を接続し、透過水取出管18と連通した端板13
の連通口19には吸引ポンプからの吸引管を接続し、排
気管31の開閉弁32を閉にし、吸引ポンプ、ブロアを
運転する。その際、水槽20の原水供給口14から下部
缶胴10の原水供給室10’内への原水の供給は、原水
供給ポンプを設けなくても水槽20内の原水と透過水集
水室24内の透過水との水位差Lによって行われ、この
水位差Lが膜透過の推進力にもなる。To collect permeated water, the lower can body 10 is connected to the raw water supply port 14 of the water tank 20, the upper can body 29 is connected to the concentrated water inlet port 33 of the water tank 20, and the diffuser pipe 12 is connected.
An air supply pipe from a blower or the like is connected to the communication port 15 of the end plate 13 that communicates with the end plate 13 that communicates with the permeated water extraction pipe 18.
A suction pipe from a suction pump is connected to the communication port 19 of 1, the opening / closing valve 32 of the exhaust pipe 31 is closed, and the suction pump and the blower are operated. At that time, the raw water is supplied from the raw water supply port 14 of the water tank 20 into the raw water supply chamber 10 ′ of the lower can body 10 in the raw water inside the water tank 20 and the permeated water collection chamber 24 without providing a raw water supply pump. The water level difference L from the permeated water is also the driving force for the membrane permeation.
【0016】下部缶胴10内の原水供給室10’には原
水と、散気管12からの気泡が供給され、気泡のエアリ
フト作用で原水は膜エレメント21の1本宛の中空管状
膜22の中空部中を膜の内周に接して高速で上向流す
る。膜エレメント21の内部の透過水集水室24には、
吸引ポンプによる負圧が透過水取出管18、分岐口3
0、透過水取出口27を経て作用するため、中空管状膜
22中を膜に接して上向流する原水中の膜を透過できる
透過水はその吸引力で膜を透過して集水室24に集ま
り、透過水取出口27、分岐口30、透過水取出管1
8、連通口19、吸引管を経て採水される。Raw water and air bubbles from the air diffuser 12 are supplied to the raw water supply chamber 10 'in the lower can body 10, and the air lift action of the air bubbles causes the raw water to be hollow in the hollow tubular membrane 22 addressed to one of the membrane elements 21. Upward flow at a high speed in contact with the inner circumference of the membrane. In the permeate collection chamber 24 inside the membrane element 21,
Negative pressure by suction pump is permeated water extraction pipe 18, branch port 3
0, since it acts through the permeated water outlet 27, the permeated water that can pass through the membrane in the raw water flowing upward in contact with the membrane in the hollow tubular membrane 22 permeates the membrane by its suction force and is collected in the water collection chamber 24. Permeate outlet 27, branch port 30, permeate outlet pipe 1
Water is collected through 8, the communication port 19, and the suction pipe.
【0017】一方、中空管状膜22を透過しなかった濃
縮水は、中空管状膜22の中空部の上端から膜エレメン
ト21上の上部缶胴29の内部に流出し、上部缶胴29
の循環口17及び濃縮水導入口33を経て、水槽20内
に流入し、水槽20内の原水と混合し、再び原水供給口
14から原水供給室10’内に供給され、エアリフト作
用で膜エレメントの中空管状膜中を上向流して循環す
る。また、原水をエアリフト作用で上向流させた気泡は
上部缶胴29の循環口17から放出される。On the other hand, the concentrated water that has not permeated the hollow tubular membrane 22 flows out from the upper end of the hollow portion of the hollow tubular membrane 22 into the upper can body 29 on the membrane element 21, and the upper can body 29.
Through the circulation port 17 and the concentrated water introduction port 33 of the water, flows into the water tank 20, is mixed with the raw water in the water tank 20, and is again supplied from the raw water supply port 14 into the raw water supply chamber 10 ′, by the air lift action. And circulates upward in the hollow tubular membrane. Further, the bubbles obtained by upwardly flowing the raw water by the air lift action are discharged from the circulation port 17 of the upper can body 29.
【0018】このように外筒16内に膜エレメント21
を挿入し、この膜エレメント21は多数本の中空管状膜
22を有することにより外筒16内を透過水集水室24
と原水流路部23とに仕切り、膜を透過し透過水集水室
24に集まった透過水を透過水取出管18を経て採水す
るようにしたので、外筒16に開口部を形成することな
く、透過水を採水することができる。As described above, the membrane element 21 is provided in the outer cylinder 16.
This membrane element 21 has a large number of hollow tubular membranes 22 so that the permeated water collection chamber 24
Since the permeated water that has passed through the membrane and is collected in the permeated water collecting chamber 24 is sampled through the permeated water extraction pipe 18, the opening is formed in the outer cylinder 16. Permeate can be collected without
【0019】また、原水供給室10’内の散気管12に
よってもたらされるエアリフト上向流のほぼ全長に中空
管状膜22を配置することができ、膜エレメント21の
充填密度を高めることができる。Further, the hollow tubular membrane 22 can be arranged over almost the entire length of the upward flow of the air lift provided by the air diffusing pipe 12 in the raw water supply chamber 10 ', and the packing density of the membrane element 21 can be increased.
【0020】原水が接触して流れる中空管状膜22の内
周面が汚れ、透過水の採水効率が低下したら透過水取出
管18に洗浄液をポンプで圧送して膜エレメント21の
透過水集水室24に供給し、中空管状膜22の内周面に
付着した汚れを膜を外から内に透過する洗浄液で除去す
る。それには集水室24内の透過水を吸引して全量排出
し、排気管31の開閉弁32を開いて集水室24内の空
気を排気し、図示していないが、原水供給口14及び濃
縮水導入口33に設けた開閉弁を閉じて水槽20と遮断
した後、原水供給室10’及び外筒16の内部の原水を
原水供給口14に設けた排水弁(図示せず)を開けるこ
とにより排水し、排気管31の開閉弁32を閉じ、その
後、端板13の連通口19に洗浄液タンク、ポンプから
の洗浄液供給管を接続し、洗浄液を膜エレメント21の
透過水の集水室24に供給し、洗浄液を中空管状膜22
に外周から内周に透過させる。中空管状膜22の内周に
透過した洗浄廃液は、除去された汚れを伴って中空管状
膜22中を下降して原水供給室10’に排出されるので
原水供給口14、排出弁(図示せず)から排出する。洗
浄が終ったら、膜エレメント21の集水室24に残る洗
浄液を透過水取出管18を経て外に排出し、透過水の採
水運転を再開する。When the inner peripheral surface of the hollow tubular membrane 22 flowing in contact with the raw water becomes dirty and the efficiency of collecting the permeated water decreases, the cleaning liquid is pumped to the permeated water extraction pipe 18 by a pump to collect the permeated water in the membrane element 21. The cleaning liquid supplied to the chamber 24 and attached to the inner peripheral surface of the hollow tubular membrane 22 is removed by a cleaning liquid that permeates the membrane from the outside to the inside. For this, the permeated water in the water collection chamber 24 is sucked and discharged in its entirety, the open / close valve 32 of the exhaust pipe 31 is opened to exhaust the air in the water collection chamber 24, and the raw water supply port 14 and After closing the on-off valve provided at the concentrated water inlet 33 to shut off the water tank 20, the raw water inside the raw water supply chamber 10 'and the outer cylinder 16 is opened at the drain valve (not shown) provided at the raw water supply port 14. Drainage is performed, the on-off valve 32 of the exhaust pipe 31 is closed, and then the cleaning liquid tank and the cleaning liquid supply pipe from the pump are connected to the communication port 19 of the end plate 13 to collect the cleaning liquid in the permeate collection chamber of the membrane element 21. 24, and the cleaning liquid is supplied to the hollow tubular membrane 22.
Permeate from the outer circumference to the inner circumference. The cleaning waste liquid that has permeated the inner periphery of the hollow tubular membrane 22 descends in the hollow tubular membrane 22 along with the removed stains and is discharged to the raw water supply chamber 10 ′. Therefore, the raw water supply port 14 and the discharge valve (not shown). Discharge). When the cleaning is completed, the cleaning liquid remaining in the water collecting chamber 24 of the membrane element 21 is discharged to the outside through the permeated water extraction pipe 18, and the permeated water sampling operation is restarted.
【0021】図3は、図1,2に示した下部缶胴10を
2つ左右に並べ、その相対向した端部の鍔同士をボル
ト、ナットなどで接合して一体にし、これにより各下部
缶胴10,10内の散気管12,12と、透過水取出管
18,18の相対向した端部同士を突き合わせて連通
し、端板13を右の下部缶胴10の右端部に取付けた状
態を示す。各下部缶胴10,10の上面の開口11,1
1には外筒16,16を立設し、外筒16,16の内部
には透過水取出管18,18に設けた上向きの分岐口3
0,30で膜エレメント21,21を支持してある。さ
らに、外筒16,16の上部に2つ左右に並べて上部缶
胴29,29を設け、その相対向した端部のフランジを
ボルト、ナットなどで接合して一体にする。こうするこ
とによって一連の原水供給室10’,10’に原水供給
口14から原水を供給し、一連の散気管12,12に連
通口15から圧力空気を供給し、各膜エレメント21,
21で原水から膜分離した透過水を一連の透過水取出管
18,18を通じ吸引して採水でき、膜の設置面積を簡
単に2倍に高めることができる。勿論、下部缶胴10を
3台、或いは4台等、一連に接合して膜の設置面積を3
倍、或いは4倍等に高めることもできる。即ち、膜エレ
メント21の高密度配置により、集積度を高めることが
できるものである。In FIG. 3, two lower can bodies 10 shown in FIGS. 1 and 2 are arranged on the left and right sides, and flanges at opposite ends thereof are joined together by bolts, nuts, etc., so that each lower portion can be integrated. The air diffusers 12 and 12 in the can bodies 10 and 10 and the permeated water extraction pipes 18 and 18 facing each other are brought into contact with each other to communicate with each other, and the end plate 13 is attached to the right end of the lower can body 10 on the right. Indicates the status. Opening 11,1 on the upper surface of each lower can body 10,10
1, outer cylinders 16 and 16 are provided upright, and inside the outer cylinders 16 and 16, upward branch ports 3 provided in permeate extraction pipes 18 and 18 are provided.
The membrane elements 21 and 21 are supported by 0 and 30. Further, two upper can barrels 29, 29 are provided side by side on the upper portions of the outer cylinders 16, 16 and flanges of the opposite end portions thereof are joined together by bolts, nuts and the like. By doing this, raw water is supplied from the raw water supply port 14 to the series of raw water supply chambers 10 ', 10', and pressurized air is supplied from the communication port 15 to the series of diffuser pipes 12, 12 to generate each membrane element 21,
The permeated water that has been membrane-separated from the raw water in 21 can be sucked through the series of permeated water extraction pipes 18, 18 to collect water, and the installation area of the membrane can be easily doubled. Of course, three or four lower can bodies 10 are joined in series to reduce the film installation area to three.
It can be increased to double or quadruple. That is, the high integration of the membrane elements 21 can increase the degree of integration.
【0022】この実施形態の場合は、複数連結する下部
缶胴10,10及び上部缶胴29,29の間にそれぞれ
開閉弁(図示せず)を設け、これを適宜閉じて他系列と
縁切りすることにより、他系列の運転を阻害することな
く薬品洗浄を行うことができる。In the case of this embodiment, an on-off valve (not shown) is provided between each of the lower can bodies 10 and 10 and the upper can bodies 29, 29 which are connected to each other, and the on-off valves (not shown) are appropriately closed to cut off from other series. As a result, chemical cleaning can be performed without disturbing the operation of other series.
【0023】図1,2の実施形態では、膜エレメント2
1で原水から膜分離した透過水を、膜エレメント21の
下管板26から下向きに突出する取出口27、分岐口3
0、下部缶胴10内の上周に沿って設けた透過水取出管
18を通じ吸引して採水したが、これに限るものではな
く、上管板25から上向きに突出する取出口27を経て
採水することもできる。この場合には、下管板26から
の取出口27をプラグで塞いで透過水取出管18の上向
きの分岐口30に嵌合し、こうして膜エレメント21を
外筒16の内部に挿入支持する。膜エレメント21の上
管板26から突出する取出口27には上部管胴29の連
設口28を貫通するL形の採水管を取付け、吸引ポンプ
からの吸引管をこの採水管に接続する。洗浄の際に膜エ
レメント21の集水室24内の空気を排気するため、上
管板25には中空管状膜22を避けて集水室24と連通
した接続口を設け、この接続口に開閉弁32を有する排
気管31を接続する。In the embodiment of FIGS. 1 and 2, the membrane element 2
The permeated water that has been membrane-separated from the raw water in 1 is an outlet 27 that projects downward from the lower tube plate 26 of the membrane element 21, and a branch port 3
0, the water was drawn by suction through the permeated water withdrawal pipe 18 provided along the upper circumference in the lower can body 10, but the present invention is not limited to this, and the water is taken out from the upper pipe sheet 25 through the takeout port 27 protruding upward. You can also collect water. In this case, the outlet 27 from the lower tube sheet 26 is closed with a plug and fitted into the upward branch port 30 of the permeated water outlet pipe 18, and thus the membrane element 21 is inserted and supported inside the outer cylinder 16. An L-shaped water sampling pipe penetrating the continuous port 28 of the upper tube body 29 is attached to the outlet 27 projecting from the upper tube plate 26 of the membrane element 21, and the suction pipe from the suction pump is connected to this water sampling pipe. In order to exhaust the air in the water collecting chamber 24 of the membrane element 21 at the time of cleaning, the upper tube plate 25 is provided with a connection port that communicates with the water collecting chamber 24 while avoiding the hollow tubular membrane 22, and the connection port is opened and closed. An exhaust pipe 31 having a valve 32 is connected.
【0024】透過水の採水運転、洗浄は前述の実施形態
と同じで、透過水は採水管から吸引して採水できる。
又、洗浄液は採水管から膜エレメント21の集水室24
に供給して行う。このような実施形態でも複数の下部缶
胴10を一連に結合し、個々の上部缶胴29を貫通した
採水管から透過水を採水することができる。The permeated water sampling operation and washing are the same as those in the above-described embodiment, and the permeated water can be sampled by suctioning from the water sampling pipe.
In addition, the cleaning liquid flows from the water sampling pipe to the water collection chamber 24 of the membrane element 21.
To supply. Also in such an embodiment, a plurality of lower can bodies 10 can be connected in series, and permeated water can be collected from the water collecting pipes that penetrate the individual upper can bodies 29.
【0025】下部缶胴10上には、図示のように膜エレ
メント21とほぼ同じ高さの外筒16と、濃縮水の循環
口17を有し、外筒16上にフランジ接合で接続される
上部缶胴29とが設けられているが、上部缶胴29を取
外し、膜エレメント21を外筒16の中に収容したり、
保守点検や、交換のために外筒16の外に取出したりす
ることができるので作業性が良い。On the lower can body 10, as shown in the drawing, an outer cylinder 16 having substantially the same height as the membrane element 21 and a concentrated water circulation port 17 are provided, and are connected to the outer cylinder 16 by flange joining. Although the upper can body 29 is provided, the upper can body 29 is removed to house the membrane element 21 in the outer cylinder 16,
Workability is good because it can be taken out of the outer cylinder 16 for maintenance and inspection or replacement.
【0026】[0026]
【発明の効果】以上述べたように、本発明によれば、複
雑な構造の処理槽を構築することなく、水槽に下部缶胴
及び上部缶胴を連結し、横置した下部缶胴の上面の開口
上に外筒を立設し、外筒の内部に内圧型又は外圧型の中
空管状膜を有する膜エレメントを挿入支持することで簡
単に膜分離装置を組立てることができる。As described above, according to the present invention, the upper surface of the lower can body which is placed horizontally by connecting the lower can body and the upper can body to the water tank without constructing a treatment tank having a complicated structure. A membrane separation device can be easily assembled by erection of an outer cylinder on the opening of, and inserting and supporting a membrane element having an internal pressure type or external pressure type hollow tubular membrane inside the outer cylinder.
【0027】このように外筒内に膜エレメントを挿入
し、膜エレメントに多数本の中空管状膜を収容すること
により外筒内を透過水集水室と原水流路部とに仕切り、
膜を透過し透過水集水室に集まった透過水を透過水取出
管を経て採水するので、外筒に開口部を形成することな
く、透過水を採水することができる。By thus inserting the membrane element into the outer cylinder and accommodating a large number of hollow tubular membranes in the membrane element, the outer cylinder is partitioned into a permeate collection chamber and a raw water flow passage portion,
Since the permeated water that permeates the membrane and collects in the permeated water collection chamber is sampled through the permeated water extraction pipe, the permeated water can be collected without forming an opening in the outer cylinder.
【0028】また、散気管によるエアリフト上向流のほ
ぼ全長に中空管状膜を配置することができるので、膜エ
レメントの充填密度を高めることができる。Further, since the hollow tubular membrane can be arranged over almost the entire length of the upward flow of the air lift by the air diffuser, the packing density of the membrane element can be increased.
【0029】さらに、上部缶胴を取外し、膜エレメント
を外筒の中に収容したり、保守点検や、交換のために外
筒の外に取出したりすることができるので作業性が良
い。Further, since the upper can body can be removed and the membrane element can be housed in the outer cylinder, or can be taken out of the outer cylinder for maintenance and inspection or replacement, workability is good.
【0030】そして、規模を大きくして膜の充填率をよ
り高めるには、複数の横型缶胴を一連に結合することで
膜の設置面積を簡単に2以上の整数倍にすることも可能
である。この場合、複数連結する各下部缶胴及び各上部
缶胴の間にそれぞれ開閉弁を設けることにより、他系列
の運転を阻害することなく薬品洗浄を行うことができ
る。In order to increase the scale and increase the filling rate of the membrane, it is possible to easily increase the installation area of the membrane to an integral multiple of 2 or more by connecting a plurality of horizontal can bodies in series. is there. In this case, by providing an opening / closing valve between each lower can body and each upper can body that are connected in plurality, chemical cleaning can be performed without disturbing the operation of other series.
【図1】本発明の膜分離装置の第1実施形態の縦断側面
図である。FIG. 1 is a vertical side view of a first embodiment of a membrane separation device of the present invention.
【図2】図1のII−II線での断面図である。FIG. 2 is a sectional view taken along line II-II in FIG.
【図3】図1の横型缶胴を複数、一連に結合した場合の
側面図である。FIG. 3 is a side view when a plurality of horizontal can bodies shown in FIG. 1 are connected in series.
【図4】従来の膜分離装置を示し、(A)はその概略正
面図、(B)はその概略側面図である。FIG. 4 shows a conventional membrane separation device, (A) is a schematic front view thereof, and (B) is a schematic side view thereof.
10 下部缶胴 10’ 原水供給室 11 開口 12 散気管 13 端板 14 原水供給口 16 外筒 17 循環口 18 透過水取出管 19 連通口 20 水槽 21 膜エレメント 22 中空管状膜 23 原水流路部 24 透過水集水室 25 上管板 26 下管板 27 取出口 28 連設口 29 上部缶胴 30 分岐口 31 排気管 32 開閉弁 33 濃縮水導入口 34 盲板 10 Lower Can Body 10 'Raw Water Supply Chamber 11 Opening 12 Diffuser Pipe 13 End Plate 14 Raw Water Supply Port 16 Outer Cylinder 17 Circulation Port 18 Permeate Extraction Pipe 19 Communication Port 20 Water Tank 21 Membrane Element 22 Hollow Tubular Membrane 23 Raw Water Flow Channel 24 Permeate collection chamber 25 Upper tube plate 26 Lower tube plate 27 Outlet port 28 Connection port 29 Upper can body 30 Branch port 31 Exhaust pipe 32 Open / close valve 33 Concentrated water inlet port 34 Blind plate
Claims (1)
と共に、上面の一部に開口を有する横型の下部缶胴と、 該下部缶胴の内部にその長手方向に設けられ、原水供給
室内にガスを供給する散気管と、 上記下部缶胴の上面の開口に対して着脱可能に立設され
た外筒の内部に多数本の中空管状膜を収容し、中空管状
膜により内部が透過水集水室と、上下に開放した原水流
路部とに仕切られ、原水流路部の下端を原水供給室に連
通させた膜エレメントと、 上記外筒の上部に設けられると共に水槽の上部に連結さ
れ、原水流路部を通過した濃縮水を外筒から水槽内へ循
環させる横型の上部缶胴とからなり、 水槽から原水供給室へ供給された原水を散気管から供給
されるガスで膜エレメントの原水流路部中を中空管状膜
に沿って上向流させ、原水流路部中を通過して上に出た
水を上部缶胴内を経て水槽内に循環し、中空管状膜を透
過した透過水を透過水集水室から外に採水するようにし
たことを特徴とする中空管状膜による膜分離装置。1. A water tank for storing raw water therein, a horizontal lower can body connected to a lower portion of the water tank to form a raw water supply chamber therein, and having an opening in a part of an upper surface thereof, and the lower can. A large number of hollow tubes are provided inside the body in the longitudinal direction thereof to supply gas into the raw water supply chamber, and an outer cylinder detachably installed to the opening on the upper surface of the lower can body. A tubular membrane is housed, and the inside is separated by a hollow tubular membrane into a permeate collection chamber and a raw water flow channel that is open vertically, and a membrane element that connects the lower end of the raw water flow channel to the raw water supply chamber, It is provided on the upper part of the outer cylinder and is connected to the upper part of the water tank.It consists of a horizontal upper can body that circulates the concentrated water that has passed through the raw water flow passage part from the outer cylinder into the water tank, and supplies it from the water tank to the raw water supply chamber. The raw water flow path of the membrane element with the gas supplied from the diffused raw water The water flows upwards along the hollow tubular membrane, and the water that passes through the raw water flow path and goes up is circulated in the water tank through the upper can body, and the permeated water that permeates the hollow tubular membrane permeates. A membrane separation device using a hollow tubular membrane, wherein water is collected from a water collection chamber to the outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28237195A JP3562066B2 (en) | 1995-10-05 | 1995-10-05 | Membrane separation device with hollow tubular membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28237195A JP3562066B2 (en) | 1995-10-05 | 1995-10-05 | Membrane separation device with hollow tubular membrane |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0999223A true JPH0999223A (en) | 1997-04-15 |
JP3562066B2 JP3562066B2 (en) | 2004-09-08 |
Family
ID=17651541
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28237195A Expired - Fee Related JP3562066B2 (en) | 1995-10-05 | 1995-10-05 | Membrane separation device with hollow tubular membrane |
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Cited By (9)
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---|---|---|---|---|
JP2002052315A (en) * | 2000-08-10 | 2002-02-19 | Yuasa Corp | Tubular membrane element and submerged filter system using the same |
JP2002052316A (en) * | 2000-08-10 | 2002-02-19 | Yuasa Corp | Tubular membrane element and submerged filter system using the same |
NL1020159C2 (en) * | 2002-03-12 | 2003-09-16 | Waterleiding Mij Overijssel N | Water purification device with vertical capillary tube membrane module, has two water supply pipes for carrying out purification in opposite directions |
JP2004351247A (en) * | 2003-05-27 | 2004-12-16 | Yanmar Co Ltd | Portable type sewage treatment unit and construction method of this portable type sewage treatment unit |
JP2010125360A (en) * | 2008-11-26 | 2010-06-10 | Daiki Ataka Engineering Co Ltd | Membrane separation apparatus |
WO2014103565A1 (en) * | 2012-12-28 | 2014-07-03 | 住友重機械工業株式会社 | Water treatment system |
US9873088B2 (en) | 2011-05-17 | 2018-01-23 | Natrix Separations Inc. | Layered tubular membranes for chromatography, and methods of use thereof |
CN110655148A (en) * | 2018-06-29 | 2020-01-07 | 中石化石油工程设计有限公司 | Oil field produced water film filtering device with internal circulation surface cross flow form |
US10800808B2 (en) | 2008-09-02 | 2020-10-13 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
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CN106834086B (en) * | 2017-02-23 | 2019-03-08 | 浙江兰博生物科技股份有限公司 | A kind of separation of fermentative broth device |
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JPH0670825U (en) * | 1993-03-17 | 1994-10-04 | 石垣機工株式会社 | Undiluted liquid filtration device with internal pressure type filtration membrane |
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JPH04300634A (en) * | 1991-03-29 | 1992-10-23 | Kubota Corp | Immersion-type membrane module |
JPH0670825U (en) * | 1993-03-17 | 1994-10-04 | 石垣機工株式会社 | Undiluted liquid filtration device with internal pressure type filtration membrane |
JP3536466B2 (en) * | 1995-08-09 | 2004-06-07 | 栗田工業株式会社 | Membrane separation device with hollow tubular membrane |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002052316A (en) * | 2000-08-10 | 2002-02-19 | Yuasa Corp | Tubular membrane element and submerged filter system using the same |
JP2002052315A (en) * | 2000-08-10 | 2002-02-19 | Yuasa Corp | Tubular membrane element and submerged filter system using the same |
NL1020159C2 (en) * | 2002-03-12 | 2003-09-16 | Waterleiding Mij Overijssel N | Water purification device with vertical capillary tube membrane module, has two water supply pipes for carrying out purification in opposite directions |
JP2004351247A (en) * | 2003-05-27 | 2004-12-16 | Yanmar Co Ltd | Portable type sewage treatment unit and construction method of this portable type sewage treatment unit |
US11884701B2 (en) | 2008-09-02 | 2024-01-30 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
US10981949B2 (en) | 2008-09-02 | 2021-04-20 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
US10800808B2 (en) | 2008-09-02 | 2020-10-13 | Merck Millipore Ltd. | Chromatography membranes, devices containing them, and methods of use thereof |
JP2010125360A (en) * | 2008-11-26 | 2010-06-10 | Daiki Ataka Engineering Co Ltd | Membrane separation apparatus |
US10874990B2 (en) | 2011-05-17 | 2020-12-29 | Merck Millipore Ltd. | Layered tubular membranes for chromatography, and methods of use thereof |
US9873088B2 (en) | 2011-05-17 | 2018-01-23 | Natrix Separations Inc. | Layered tubular membranes for chromatography, and methods of use thereof |
US10195567B2 (en) | 2011-05-17 | 2019-02-05 | Natrix Separations Inc. | Layered tubular membranes for chromatography, and methods of use thereof |
JPWO2014103565A1 (en) * | 2012-12-28 | 2017-01-12 | 住友重機械工業株式会社 | Water treatment system |
WO2014103565A1 (en) * | 2012-12-28 | 2014-07-03 | 住友重機械工業株式会社 | Water treatment system |
CN110655148A (en) * | 2018-06-29 | 2020-01-07 | 中石化石油工程设计有限公司 | Oil field produced water film filtering device with internal circulation surface cross flow form |
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