JP3258561B2 - Membrane separation device - Google Patents

Membrane separation device

Info

Publication number
JP3258561B2
JP3258561B2 JP12444996A JP12444996A JP3258561B2 JP 3258561 B2 JP3258561 B2 JP 3258561B2 JP 12444996 A JP12444996 A JP 12444996A JP 12444996 A JP12444996 A JP 12444996A JP 3258561 B2 JP3258561 B2 JP 3258561B2
Authority
JP
Japan
Prior art keywords
water
membrane separation
membrane
tank
treated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP12444996A
Other languages
Japanese (ja)
Other versions
JPH09299952A (en
Inventor
八郎 佐藤
良人 北井
和之 本田
正修 岩橋
勝己 浜田
真一 古瀬
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP12444996A priority Critical patent/JP3258561B2/en
Publication of JPH09299952A publication Critical patent/JPH09299952A/en
Application granted granted Critical
Publication of JP3258561B2 publication Critical patent/JP3258561B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、濾過膜板を取り付
け可能な取付部を多数並設した膜分離装置に関し、具体
的には、例えば浄化槽に用いられる膜分離装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane separation device having a large number of attachment portions to which a filtration membrane plate can be attached, and more specifically, to a membrane separation device used for a septic tank, for example.

【0002】[0002]

【従来の技術】従来、この種の膜分離装置としては、濾
過膜板を取り付け可能な取付部を多数並設し、その取付
部の全てに濾過膜板を設けて構成してある膜分離装置が
知られている。
2. Description of the Related Art Conventionally, as this kind of membrane separation device, a large number of attachment portions to which a filtration membrane plate can be attached are arranged in parallel, and a filtration membrane plate is provided on all of the attachment portions. It has been known.

【0003】[0003]

【発明が解決しようとする課題】ところで、上記膜分離
装置が浄化槽に用いられるような場合には、膜分離装置
に濾過膜板を並設できる枚数は、取付部の数に規定さ
れ、前記膜分離装置ごとに所定量に限られるので、その
水処理に必要とされる濾過膜板の枚数と、前記膜分離装
置に並設可能な濾過膜板の枚数とが一致しない場合が多
い。つまり、前記膜分離装置は予め製造してあるものを
適用し、その膜分離装置に設けた取付部の数は、例え
ば、50個、60個、………と10個単位にするなど、
製造効率の良い枚数に設定され、水処理の必要に合わせ
て膜分離装置を製造するような個別対応は、製造効率の
面で不利であるとして行われていない。しかし、上述し
た従来の膜分離装置を用いれば、水処理(濾過膜板によ
る固液分離処理)に必要とされる濾過膜板の枚数は処理
すべき水質、量によって規定され、設定変更することは
出来ないので、前記膜分離装置に設ける濾過膜板の枚数
を設定変更せざるを得ない。そこで、このような設定変
更を余儀なくされる場合には、必要とされる濾過膜板の
枚数よりも多数の取付部を設けた膜分離装置を用意して
おき、前記膜分離装置に並設する濾過膜板の一部を膜濾
過処理を行わない整流板に取り替えて水処理を行う濾過
膜板を減少させて必要とされる濾過膜板の設定枚数を実
現することが考えられている。例えば、52枚の濾過膜
板を必要とする水処理を行う場合、取付部を60個設け
た膜分離装置に52枚の濾過膜板を設けるとともに、8
枚の整流板を設けておくわけである。しかし、このよう
な整流板は管理の都合上一か所にまとめて並設するべき
ものであると考えられていた。ところが、このように整
流板を一か所にまとめて並設してある前記膜分離装置を
水処理室に内装して水処理を行った場合には、水処理室
内の濾過膜板の配設位置では水処理が順調に行われるも
のの、整流板をまとめて並設してある位置では水処理が
順調に行われない虞れがあるという指摘が成されている
(特に整流板の枚数が取付部の総数に対して大きな割合
にならざるを得ない場合には、この傾向が強いと考えら
れる)。なぜなら、整流板は水処理を行わないので、固
液分離された固形分の付着状況や、固液分離圧による濾
過膜板の周囲の水流の変化等で、濾過膜板の周囲と整流
板の周囲とで被処理水の流れが異なり、水の循環が不均
一になり、前記整流板の周囲の被処理水が滞留して処理
されにくくなることが考えられるためである。
In the case where the above-mentioned membrane separation device is used in a septic tank, the number of filter membrane plates that can be installed in the membrane separation device is determined by the number of mounting portions. Since the amount is limited to a predetermined amount for each separation device, the number of filtration membrane plates required for the water treatment often does not match the number of filtration membrane plates that can be juxtaposed in the membrane separation device. That is, the membrane separation device is manufactured in advance, and the number of attachment portions provided in the membrane separation device is, for example, 50, 60,...
The number of sheets is set to a value with high production efficiency, and individual measures such as manufacturing a membrane separation apparatus according to the need for water treatment are not performed because they are disadvantageous in terms of production efficiency. However, if the above-mentioned conventional membrane separation device is used, the number of filtration membrane plates required for water treatment (solid-liquid separation treatment by filtration membrane plates) is determined by the quality and quantity of water to be treated, and the setting may be changed. Therefore, the number of filtration membrane plates provided in the membrane separation device must be changed. Therefore, when such a setting change is inevitable, a membrane separation device provided with a larger number of mounting portions than the required number of filtration membrane plates is prepared and installed in parallel with the membrane separation device. It has been considered that a part of the filtration membrane plate is replaced with a rectifying plate that does not perform the membrane filtration treatment to reduce the number of filtration membrane plates that perform the water treatment to realize the required number of filtration membrane plates. For example, when performing water treatment requiring 52 filtration membrane plates, 52 filtration membrane plates are provided in a membrane separation device provided with 60 mounting portions, and 8
That is, a plurality of straightening plates are provided. However, it was considered that such a current plate should be arranged in one place and juxtaposed for convenience of management. However, in the case where the above-mentioned membrane separation device in which the straightening plates are collectively arranged in one place is installed in a water treatment chamber to perform water treatment, the arrangement of the filtration membrane plate in the water treatment chamber is performed. It has been pointed out that although the water treatment is performed smoothly in the position, the water treatment may not be performed smoothly in the position where the flow straightening plates are collectively arranged side by side. This tendency is likely to be strong if it must be a large percentage of the total number of copies.) Because the rectifying plate does not perform water treatment, the surroundings of the rectifying plate and the surroundings of the rectifying plate may be changed due to the adhesion of solids separated by solid-liquid separation and the change of water flow around the filtering membrane plate due to the solid-liquid separation pressure. This is because the flow of the water to be treated differs from the surrounding area, the water circulation becomes uneven, and the water to be treated around the rectifying plate stays and becomes difficult to be treated.

【0004】従って、本発明の目的は、上記実情に鑑
み、水処理に必要とされる濾過膜板の枚数と、前記膜分
離装置に並設可能な濾過膜板の枚数とが一致しない場合
にも、前記膜分離装置に設ける濾過膜板の枚数を水処理
に必要な枚数に一致させ、かつ、水処理に不都合を生じ
させにくい構成の膜分離装置を提供することにある。
[0004] Accordingly, an object of the present invention is to provide, in view of the above circumstances, a case where the number of filtration membrane plates required for water treatment does not match the number of filtration membrane plates that can be juxtaposed in the membrane separation device. Another object of the present invention is to provide a membrane separation apparatus having a configuration in which the number of filtration membrane plates provided in the membrane separation apparatus is equal to the number required for water treatment, and in which there is little inconvenience in water treatment.

【0005】[0005]

【課題を解決するための手段】この目的を達成するため
の本発明の特徴構成は、各請求項記載の通りであり、さ
らに、図面を参照して詳述すれば、濾過膜板1を取り付
け可能な取付部2を多数並設した膜分離装置において、
膜濾過処理を行わない整流板5を前記取付部2に設ける
とともに、その整流板2を並設した取付部2の並設方向
の両端側に分散配設してあることにあり、前記整流板5
を、鉄材を露出状態に設けてなる板状体から形成してあ
ってもよい。
The features of the present invention for achieving the object are as described in the claims. Further, referring to the drawings, the filter membrane plate 1 is mounted. In a membrane separation device having a large number of possible mounting portions 2 arranged side by side,
A rectifying plate 5 that does not perform a membrane filtration process is provided on the mounting portion 2, and the rectifying plate 2 is dispersed and disposed on both ends in the direction in which the mounting portions 2 are juxtaposed. 5
May be formed from a plate-like body in which an iron material is provided in an exposed state.

【0006】尚、特徴構成を説明するために、図面を参
照して符号を記すが、該記入により本発明は添付図面の
構成に限定されるものではない。
Incidentally, in order to explain the characteristic configuration, reference numerals are described with reference to the drawings, but the present invention is not limited to the configuration shown in the accompanying drawings.

【0007】〔作用効果〕つまり、上述の膜分離装置は
濾過膜板を取り付け可能な取付部を多数並設してあるも
のであるから、その取付部に濾過膜板を取り付けておく
ことで、処理すべき被処理水の収容されてなる水処理室
にその膜分離装置を収容することで、水処理をおこなう
ことができる。ここで、前記水処理室に必要とされる濾
過膜板の数が、膜分離装置に規定される枚数と一致しな
い状況があったと仮定すると、前記取付部に膜濾過処理
を行わない整流板を設けてあることで、その他の取付部
に濾過膜板を設ければ、前記膜分離装置に設けた濾過膜
板の数を水処理室に必要とされる濾過膜板の数に一致さ
せることができ、その水処理に適した膜分離装置を提供
することが出来る。ところで、前記整流板が一か所にま
とめて設けてあれば、先述の水処理に係わる不都合の生
じるおそれがあるものの、整流板は並設した取付部の並
設方向の両端側に分散配設してあるので、前記水処理を
行わない整流板は、固液分離された固形分の付着状況
や、固液分離圧による濾過膜板の周囲の水流の差異等に
係わらず、前記取付部の並設方向でバランス良く被処理
水を循環させることができるようになる。また、被処理
水の循環のバランスという点では、前記膜分離装置の取
付部の並設方向における両端は、被処理水が最も乱れや
すい位置でもあるので、被処理水の循環流が安定しにく
い位置では、水処理を行わずに単に整流だけすることに
なるので、主に循環流の安定した位置で水処理を行うこ
とが出来るように設定することにもなって、水の循環が
不均一になることに起因する被処理水に処理ムラを発生
しにくくできる。
[Effects] In other words, since the above-mentioned membrane separation device has a large number of mounting portions to which a filtration membrane plate can be mounted, the filtration membrane plate is mounted on the mounting portion. Water treatment can be performed by housing the membrane separation device in a water treatment chamber containing the water to be treated. Here, assuming that the number of filtration membrane plates required for the water treatment chamber does not match the number specified for the membrane separation device, assuming that a rectifying plate that does not perform the membrane filtration process is attached to the mounting portion. By being provided, if a filtration membrane plate is provided in the other mounting portion, the number of filtration membrane plates provided in the membrane separation device can be matched with the number of filtration membrane plates required in the water treatment chamber. And a membrane separation device suitable for the water treatment can be provided. By the way, if the rectifying plates are provided in one place, there is a possibility that the inconvenience relating to the above-described water treatment may occur.However, the rectifying plates are distributed and arranged at both ends in the juxtaposing direction of the juxtaposed mounting portions. Therefore, the rectifying plate that does not perform the water treatment, regardless of the adhesion state of the solid-liquid separated solid, the difference in water flow around the filtration membrane plate due to the solid-liquid separation pressure, etc. The water to be treated can be circulated in a balanced manner in the juxtaposed direction. Further, in terms of the balance of the circulation of the water to be treated, since both ends of the mounting portion of the membrane separation device in the juxtaposition direction are also positions where the water to be treated is most likely to be disturbed, the circulation flow of the water to be treated is difficult to stabilize. In the position, the water is simply rectified without performing the water treatment, so it is also set so that the water treatment can be performed mainly in a position where the circulation flow is stable, and the water circulation is uneven. It is possible to reduce the occurrence of processing unevenness in the water to be treated due to the above.

【0008】そのため、例えば、このような膜分離装置
で、取付部を50個設けたものを、その膜分離装置を幅
方向に1台、長手方向に二台並設して収容可能な水処理
室を備えた浄化槽に適用する場合には、必要となる濾過
膜板が80枚という場合であっても、各膜分離装置にお
ける両端側の各5個の取付部に整流板を取り付けること
で、前記水処理室内における前記濾過膜板に対する被処
理水の循環のバランスは良好に保てるとともに、通常浄
化槽に設ける膜分離装置においては被処理水の循環流は
下から上に向かうのであるが、被処理水が前記膜分離装
置の並設した濾過膜板の下方に流入する際のデッドスペ
ースとなりがちな端部では膜分離しない状態になり、被
処理水の生物処理を良好に保ちながらの前記濾過膜板に
よる固液分離が安定して行える。
[0008] Therefore, for example, a water treatment apparatus capable of accommodating one such membrane separation apparatus provided with 50 mounting portions, one in the width direction and two in the longitudinal direction. When applied to a septic tank provided with a chamber, even if the required filtration membrane plate is 80 sheets, by attaching a rectifying plate to each of the five mounting portions at both ends of each membrane separation device, The balance of the circulation of the water to be treated with respect to the filtration membrane plate in the water treatment chamber can be kept good, and the circulating flow of the water to be treated goes from the bottom to the top in the membrane separation device usually provided in the septic tank. At the end which tends to become a dead space when water flows below the juxtaposed filtration membrane plates of the membrane separation device, membrane separation does not occur, and the filtration membrane while maintaining good biological treatment of the water to be treated. Solid-liquid separation by plate is cheap And it can be performed by.

【0009】[0009]

【発明の実施の形態】以下に本発明の実施の形態を、活
性汚泥を固液分離処理する浄化槽の膜分離室において膜
分離装置を使用する場合を例に、図面に基づいて説明す
る。図1〜3に浄化槽を示す。この浄化槽は、円筒状の
浄化槽本体Xの両端を鑑部X1,X2を設けて内部に密
閉空間を形成するとともに、内部の密閉空間に仕切り壁
を設けて区分けして、上流側から、流量調整槽N、脱窒
素槽E1、膜分離槽E2、放流ポンプ槽Tをそれぞれ水
処理室として設けてあり、前記各槽の上部には、メンテ
ナンス等に用いるマンホールHを設けてある。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings, taking as an example a case where a membrane separation device is used in a membrane separation chamber of a septic tank for performing a solid-liquid separation process on activated sludge. The septic tank is shown in FIGS. This septic tank is provided with observing parts X1 and X2 at both ends of a cylindrical septic tank main body X to form an enclosed space inside, and a partition wall is provided inside the enclosed space to divide the septic tank. A tank N, a denitrification tank E1, a membrane separation tank E2, and a discharge pump tank T are respectively provided as water treatment chambers, and a manhole H used for maintenance and the like is provided above each of the tanks.

【0010】前記流量調整槽Nは、前記浄化槽本体Xの
一方の鏡部X1に設けてなる流入口Iから浄化槽内に流
入した被処理水の原水を受けて、その被処理水中の夾雑
物を濾過するパンチングスクリーンFを設けるととも
に、前記パンチングスクリーンFに気泡供給する散気装
置Cを設けて、前記夾雑物を濾別しながら破砕、細分化
可能に構成するとともに、濾別された被処理水を一時貯
留する水処理室内に、被処理水を脱窒素槽E1に移送す
る第一ポンプP1を設け、被処理水が大量に流入した場
合や、長期にわたって被処理水の流入が無い場合にも、
被処理水を定常的に脱窒素槽E1に移送して、後続の各
水処理室での水処理に支障をきたさないようにしてあ
る。
The flow rate adjusting tank N receives raw water to be treated flowing into the purification tank from an inlet I provided in one mirror portion X1 of the purification tank main body X, and removes impurities in the treatment water. In addition to providing a punching screen F for filtration, a diffusing device C for supplying air bubbles to the punching screen F is provided so that the impurities can be crushed and fragmented while being filtered, and the filtered treated water to be treated is provided. A first pump P1 for transferring the water to be treated to the denitrification tank E1 is provided in the water treatment chamber where the water to be treated is temporarily stored, even when the water to be treated flows in a large amount or when there is no inflow of the water to be treated for a long time. ,
The water to be treated is constantly transferred to the denitrification tank E1 so as not to hinder the water treatment in each of the subsequent water treatment chambers.

【0011】前記脱窒素槽E1は、前記流量調整槽Nに
隣接する水処理室に、前記流量調整槽Nからの被処理水
を流入させる流入管A1を、前記第一ポンプP1に接続
して設け、被処理水の流入路を構成してある。また、第
二ポンプP2を内装し、その第二ポンプP2に移送管A
2を設け、被処理水を前記膜分離槽E2へ移送する構成
にしてある。また、槽内の被処理水を攪拌循環させる攪
拌ポンプP3を内装してあり、槽内の被処理水の混合を
図り、BOD負荷の高い被処理水と、硝化済の被処理水
とを混合し、高度な脱窒処理を行える構成にしてある。
The denitrification tank E1 is connected to an inflow pipe A1 through which water to be treated from the flow rate adjusting tank N flows into the water treatment chamber adjacent to the flow rate adjusting tank N, to the first pump P1. To form an inflow passage for the water to be treated. In addition, a second pump P2 is provided therein, and the second pump P2 is provided with a transfer pipe A.
2 is provided to transfer the water to be treated to the membrane separation tank E2. In addition, a stirring pump P3 for stirring and circulating the water to be treated in the tank is provided to mix the water to be treated in the tank and mix the water to be treated with a high BOD load with the nitrified water to be treated. In addition, it is configured to perform advanced denitrification processing.

【0012】前記膜分離槽E2は、前記脱窒素槽E1と
の間を仕切る隔壁に、前記流入路を設けるとともに、前
記脱窒素槽E1から過剰に流入した被処理水を前記脱窒
素槽E1に返送する返送口A4を設けて、被処理水の返
送路を構成してある。そして、前記膜分離槽E2には、
本発明の膜分離装置Mを前記浄化槽本体Xの長手方向に
2台並べて内装してある。
In the membrane separation tank E2, the inflow path is provided in a partition separating the denitrification tank E1, and the water to be treated excessively flowing from the denitrification tank E1 is supplied to the denitrification tank E1. A return port A4 for returning is provided to form a return path for the water to be treated. And, in the membrane separation tank E2,
Two membrane separation devices M according to the present invention are installed side by side in the longitudinal direction of the septic tank main body X.

【0013】前記膜分離装置Mは、多数の平板状の濾過
膜板1(図4(イ)参照)を直立状態で取付可能な50
対の取付部2、2………を設けてある濾過膜板保持枠3
を設け、前記取付部2に濾過膜板1を立設することによ
り、多数の濾過膜板1を平行に並設可能に構成してあ
る。前記取付部2、2………の両端側の各5対には、そ
れぞれ前記濾過膜板1とほぼ同形状でかつ濾過機能を有
しない整流板5(図4(ロ)参照)を取り付けるととも
に、前記取付部2、2………の中央側の各40対には、
前記濾過膜板1を取り付けてあり(図1参照)、前記各
膜分離装置に濾過膜板1の40枚分の膜分離機能を持た
せ、膜分離槽E2に濾過膜板1の80枚分の水処理能力
を付与してある。また、前記濾過膜板保持枠3の下部に
は、前記濾過膜板保持枠3を支持する一組の脚部4を設
け、前記脚部4の間にその濾過膜板1に気泡を供給し
て、その膜面に汚泥等の付着しすぎるのを防止し、か
つ、前記膜分離槽E2内に循環流を形成しながら被処理
水に酸素を供給する散気装置Dを内装してある。また、
前記膜分離装置Mのそれぞれの濾過膜板1には取水管6
を連設するとともに、前記取水管6からの濾過水を合流
させて膜分離槽E2外へ導く集水管7を接続してあり、
前記膜分離槽E2の水面よりも下方で前記膜分離槽E2
に隣接する放流ポンプ槽Tに連通接続してある。
The membrane separation device M is capable of mounting a large number of flat filtration membrane plates 1 (see FIG. 4A) upright.
A filter membrane plate holding frame 3 provided with a pair of mounting portions 2, 2,...
And the filter membrane plates 1 are erected on the mounting portion 2 so that many filter membrane plates 1 can be arranged in parallel. A rectifying plate 5 (see FIG. 4 (b)) having substantially the same shape as the filtration membrane plate 1 and having no filtering function is attached to each of the five pairs at both ends of the mounting portions 2, 2,. , Each of the 40 pairs on the central side of the mounting portions 2, 2,...
The filtration membrane plate 1 is attached (see FIG. 1), each membrane separation device is provided with a membrane separation function for 40 filtration membrane plates 1, and the membrane separation tank E2 is provided with 80 filtration membrane plates. Water treatment capacity. Further, a set of legs 4 for supporting the filtration membrane plate holding frame 3 is provided below the filtration membrane plate holding frame 3, and air bubbles are supplied to the filtration membrane plate 1 between the leg portions 4. Further, an air diffuser D for supplying oxygen to the water to be treated while preventing a sludge or the like from adhering excessively to the membrane surface and forming a circulating flow in the membrane separation tank E2 is provided therein. Also,
Each filtration membrane plate 1 of the membrane separation device M has an intake pipe 6
And a water collecting pipe 7 for joining filtered water from the water intake pipe 6 and guiding the filtered water to the outside of the membrane separation tank E2.
The membrane separation tank E2 is located below the water surface of the membrane separation tank E2.
Is connected to a discharge pump tank T adjacent to the tank.

【0014】前記放流ポンプ槽Tは、消毒槽Q1と、貯
留槽Q2とからなり、前記消毒槽Q1は、前記膜分離槽
E2と、前記放流ポンプ槽Tとを仕切る隔壁に処理水受
け容器を設け、その壁面に小孔を設けて構成してあり、
前記消毒槽Q1に流入した濾過水は、消毒されたのち貯
留槽Q2に流入する。前記貯留槽Q2は、放流ポンプP
4を内装してあり、一旦貯留槽Q2に貯留された処理水
を前記放流ポンプP1で汲み上げ、排出管A5を介して
放流口Zから浄化槽外へ放流可能に構成してある。これ
により、消毒済の処理水が前記貯留槽Tからほぼ定量的
に浄化槽外に放流される。
The discharge pump tank T comprises a disinfecting tank Q1 and a storage tank Q2. The disinfecting tank Q1 has a treated water receiving container on a partition separating the membrane separation tank E2 and the discharge pump tank T. It is configured by providing a small hole in the wall surface,
The filtered water that has flowed into the disinfection tank Q1 flows into the storage tank Q2 after being disinfected. The storage tank Q2 is provided with a discharge pump P
4, and the treated water once stored in the storage tank Q2 is pumped up by the discharge pump P1 and can be discharged from the discharge port Z to the outside of the purification tank via the discharge pipe A5. Thereby, the disinfected treated water is almost quantitatively discharged from the storage tank T to the outside of the purification tank.

【0015】[0015]

【実施例】上述の実施の形態における浄化槽を定常運転
したところ、被処理水は、図2中矢印のように循環し
て、すべての濾過膜板に対してほぼ均一な気泡供給が可
能となるとともに、ほぼ均一な被処理水供給が行われ、
バランス良く固液分離処理が行われる状況が実現出来
た。
EXAMPLE When the septic tank in the above-described embodiment was operated in a steady state, the water to be treated circulated as indicated by the arrow in FIG. 2 so that substantially uniform air bubbles could be supplied to all the filtration membrane plates. At the same time, the water to be treated is supplied almost uniformly,
The situation where the solid-liquid separation treatment was performed in a well-balanced manner was realized.

【0016】〔別実施形態〕以下に別実施形態を説明す
る。前記整流板は、鉄材から構成してあってもよく、鉄
材から構成することによって、その比重の大きさから、
前記整流板のがたつきを減少させることが出来、かつ、
被処理水中への前記鉄材の溶出に伴い、三価の鉄イオン
が被処理水中のリン成分を沈殿除去させる機能を発揮
し、整流作用のみならず、被処理水の生物処理を補助す
る働きを示すので好都合である。尚、前記リン成分の沈
殿除去については、整流板を鉄材を露出状態に設けてな
る板状体から形成してあれば、十分に機能を発揮出来る
ものである。
[Other Embodiment] Another embodiment will be described below. The current plate may be made of an iron material, and by being made of an iron material, from the magnitude of its specific gravity,
Rattling of the current plate can be reduced, and
With the elution of the iron material into the water to be treated, trivalent iron ions exert a function of precipitating and removing the phosphorus component in the water to be treated, and not only a rectifying action, but also a function of assisting biological treatment of the water to be treated. It is convenient because it is shown. As for the removal of the precipitate of the phosphorus component, the function can be sufficiently exhibited if the rectifying plate is formed from a plate-like body in which an iron material is provided in an exposed state.

【0017】尚、例えば、浄化槽に必要とされる濾過膜
板の枚数が、120枚である場合には、浄化槽本体とし
て前記膜分離装置を3台並設可能な膜分離槽を設け、そ
の膜分離槽に3台の膜分離装置に各40枚の濾過膜板及
び10枚の整流板を設けてあるものを内装して120枚
分の水処理能力を付与することになり、同様に、前記整
流板は前記膜分離装置の両端側に5枚づつ配設すればよ
く、さらに、浄化槽に必要とされる濾過膜板の枚数が種
々に変更になる場合でも、整流板は各膜分離装置の両端
側に分散配置してあればよいものとする。
For example, when the number of filtration membrane plates required for the septic tank is 120, a membrane separation tank capable of arranging three membrane separation devices in parallel as a septic tank main body is provided. Separation tanks equipped with three membrane separators each having 40 filtration membrane plates and 10 rectifying plates are installed, and water treatment capacity for 120 sheets is provided. The rectifying plates may be disposed at each end of the membrane separation device in units of five. Further, even when the number of filtration membrane plates required for the septic tank is variously changed, the rectification plates are provided for each of the membrane separation devices. What is necessary is to disperse and arrange on both ends.

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

【図1】浄化槽の縦断側面図FIG. 1 is a vertical side view of a septic tank.

【図2】本発明の膜分離装置を備えてなる水処理層の被
処理水の循環を示す図
FIG. 2 is a diagram showing circulation of water to be treated in a water treatment layer provided with the membrane separation device of the present invention.

【図3】膜分離装置に対する濾過膜板の配設状態を示す
平面図
FIG. 3 is a plan view showing a state in which a filtration membrane plate is provided in the membrane separation device.

【図4】濾過膜板と整流板とに対比図FIG. 4 is a comparison diagram of a filtration membrane plate and a rectifying plate.

【符号の説明】 1 濾過膜板 2 取付部 4 整流板[Description of Signs] 1 Filtration membrane plate 2 Mounting part 4 Rectifier plate

フロントページの続き (72)発明者 岩橋 正修 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (72)発明者 浜田 勝己 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (72)発明者 古瀬 真一 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (56)参考文献 特開 平9−220448(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 61/00 - 65/10 C02F 1/44 Continued on the front page (72) Inventor Masaharu Iwahashi 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside the Kubota Shiga Plant (72) Katsumi Hamada, 2nd Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture In the Kubota Shiga Plant (72) Inventor Shinichi Furuse 2 in Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture In the Kubota Shiga Plant (56) References JP-A-9-220448 (JP, A) (58) Field (Int.Cl. 7 , DB name) B01D 61/00-65/10 C02F 1/44

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 濾過膜板を取り付け可能な取付部を多数
並設した膜分離装置であって、膜濾過処理を行わない整
流板を前記取付部に設けるとともに、その整流板を並設
した取付部の並設方向の両端側に分散配設してある膜分
離装置。
1. A membrane separation device in which a number of mounting portions to which a filtration membrane plate can be mounted are arranged in parallel, wherein a rectifying plate not performing a membrane filtration process is provided in the mounting portion, and the rectifying plates are arranged in parallel. Membrane separation devices distributed on both ends in the direction of juxtaposition of the sections.
【請求項2】 前記整流板を、鉄材を露出状態に設けて
なる板状体から形成してある請求項1に記載の膜分離装
置。
2. The membrane separation device according to claim 1, wherein the rectifying plate is formed from a plate-like body in which an iron material is provided in an exposed state.
JP12444996A 1996-05-20 1996-05-20 Membrane separation device Expired - Fee Related JP3258561B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12444996A JP3258561B2 (en) 1996-05-20 1996-05-20 Membrane separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12444996A JP3258561B2 (en) 1996-05-20 1996-05-20 Membrane separation device

Publications (2)

Publication Number Publication Date
JPH09299952A JPH09299952A (en) 1997-11-25
JP3258561B2 true JP3258561B2 (en) 2002-02-18

Family

ID=14885802

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12444996A Expired - Fee Related JP3258561B2 (en) 1996-05-20 1996-05-20 Membrane separation device

Country Status (1)

Country Link
JP (1) JP3258561B2 (en)

Also Published As

Publication number Publication date
JPH09299952A (en) 1997-11-25

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