JP2000237551A - Immersion type flat membrane separation device and its controlling method - Google Patents

Immersion type flat membrane separation device and its controlling method

Info

Publication number
JP2000237551A
JP2000237551A JP11037233A JP3723399A JP2000237551A JP 2000237551 A JP2000237551 A JP 2000237551A JP 11037233 A JP11037233 A JP 11037233A JP 3723399 A JP3723399 A JP 3723399A JP 2000237551 A JP2000237551 A JP 2000237551A
Authority
JP
Japan
Prior art keywords
membrane
filtration
type flat
water
immersion type
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
JP11037233A
Other languages
Japanese (ja)
Other versions
JP3815645B2 (en
Inventor
Naoki Okuma
那夫紀 大熊
Masato Onishi
真人 大西
Toshio Yamadera
利夫 山寺
Yutaka Okuno
裕 奥野
Yukio Murai
行男 村井
Hiroki Ando
尋樹 安藤
Shiro Tanshu
紫朗 丹宗
Nobuo Hayashi
信夫 林
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.)
Hitachi Plant Technologies Ltd
Yuasa Corp
Original Assignee
Hitachi Plant Technologies Ltd
Yuasa Corp
Yuasa Battery 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 Hitachi Plant Technologies Ltd, Yuasa Corp, Yuasa Battery Corp filed Critical Hitachi Plant Technologies Ltd
Priority to JP03723399A priority Critical patent/JP3815645B2/en
Publication of JP2000237551A publication Critical patent/JP2000237551A/en
Application granted granted Critical
Publication of JP3815645B2 publication Critical patent/JP3815645B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an immersion type flat membrane separation device capable of continuing filtering over a long period of time while efficiently removing a cake on the membrane surface without damage to the membrane. SOLUTION: A separation body unit A is constituted by fitting a filter membrane 12 on the both surfaces of a water permeable material 16 by interposing a spacer 14, fitting membrane end fixing materials 20 and 22 in the parallel direction of its upper and lower ends respectively and also forming a hollow part at the upper part membrane end fixing materials 20, and a water collecting part is constituted by fixing the left and right end parts of a plurality of these separation body units with each other at membrane joining and fixing parts 24 and 26 and fixing a water collecting pipe 24a allowing the hollow part of the upper part membrane end fixing material to communicate with the upper part of the joining and fixing part.

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、浸漬型平膜分離装
置およびその制御方法に係り、特に精密ろ過膜や限外ろ
過膜による廃水中の懸濁物を効率良く分離し得る浸漬型
膜分離装置およびその制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an immersion type flat membrane separation apparatus and a control method thereof, and more particularly to an immersion type membrane separation apparatus capable of efficiently separating suspended matter in wastewater by a microfiltration membrane or an ultrafiltration membrane. The present invention relates to an apparatus and a control method thereof.

【0002】[0002]

【従来の技術】最近、膜分離は、技術発展に伴い薬品や
食品の製造ラインの固液分離だけでなく、用水の製造、
排水からの有機物の回収、上水,中水及びし尿の固液分
離に広く適用され、更には下水や産業排水処理にまで適
用されようとしている。排水処理に適用できるランニン
グコストの安価な方法として、原液槽にろ過膜を浸漬し
ながら、全量ろ過する浸漬方式が開発されている。この
方式は、膜面上に原液の流れを与えない代わりに、液循
環方式よりも低い膜間差圧でろ過することによって、膜
面へのケーキの蓄積を抑制してろ過する方式で、低動力
の運転が可能であり、また構造がシンプルであるためメ
ンテナンスが容易という利点がある。この浸漬方式にお
いて、ろ過するため膜間に差圧を生じさせるには、加圧
方式よりも目詰まりの少ないこと、ろ過膜を原液槽に浸
漬するだけでよいことから吸引方式が多く用いられてい
る。そして、この吸引方式では、膜面上に付着するケー
キは、膜の下部に設けた散気管又は散気板から空気を供
給しながらバブリングして剥離、除去される。
2. Description of the Related Art Recently, with the development of technology, not only solid-liquid separation of pharmaceutical and food production lines, but also water production,
It is widely applied to the recovery of organic matter from wastewater, solid-liquid separation of clean water, sewage and human waste, and even to sewage and industrial wastewater treatment. As an inexpensive running cost method applicable to wastewater treatment, an immersion method has been developed in which a filtration membrane is immersed in a stock solution tank and the total amount is filtered. In this method, instead of not providing the flow of the undiluted solution on the membrane surface, filtration is performed with a lower transmembrane pressure than in the liquid circulation system, thereby suppressing the accumulation of cake on the membrane surface and performing filtration. There is an advantage that it can be driven by power and its maintenance is easy because of its simple structure. In this immersion method, in order to generate a pressure difference between the membranes for filtration, a suction method is often used because there is less clogging than in the pressure method, and it is only necessary to immerse the filtration membrane in a stock solution tank. I have. In this suction method, the cake adhering to the film surface is separated and removed by bubbling while supplying air from a diffuser tube or a diffuser plate provided below the film.

【0003】使用される膜の形状としては、管状膜,中
空糸膜及び平膜がある。これらのうち管状膜は膜面積を
大きく確保できないため大量処理には不向きである。ま
た、中空糸膜は、容積効率が高いが、特開平4−265
128号公報などで示されているように、中空糸膜の束
の内部に懸濁物が付着又は固着するためにろ過抵抗が高
くなり、これらの懸濁物をエアバブリングによって除去
することは困難である。
[0003] The shape of the membrane used includes a tubular membrane, a hollow fiber membrane and a flat membrane. Of these, the tubular membrane is not suitable for large-scale processing because a large membrane area cannot be secured. Further, the hollow fiber membrane has a high volumetric efficiency,
As shown in Japanese Patent Publication No. 128 and the like, filtration resistance increases due to suspension adhered or fixed inside the bundle of hollow fiber membranes, and it is difficult to remove these suspensions by air bubbling. It is.

【0004】これに対して平膜は、中空糸膜のように局
部的に懸濁物が付着しないため、エアバブリングによる
膜面の洗浄が容易であり、また、管状膜より容積効率が
高い。このような観点から懸濁物濃度の高い液をろ過す
る場合の浸漬型のろ過方式は、平膜の適用が望ましい。
[0004] On the other hand, a flat membrane does not adhere locally to a suspension unlike a hollow fiber membrane, so that the membrane surface can be easily cleaned by air bubbling and has a higher volumetric efficiency than a tubular membrane. From such a viewpoint, it is desirable to apply a flat membrane to the immersion-type filtration system for filtering a liquid having a high suspension concentration.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、平膜を
使用した場合、ろ過膜の下方からのエアバブリングによ
る膜面上のケーキの除去や剥離が充分でないときがあ
り、これを補うために多くの膜面積を必要とし、コスト
の上昇につながるなどの問題がある。これに対処する方
法として、特開平6−327949号公報に開示されて
いるように複数枚のろ過膜を分離槽内に浸漬、立設し、
膜間にひも状の可撓性の洗浄体を設けたものがある。こ
れは、下方からのエアバブリングによって、可撓性の洗
浄体が膜面に接触して付着物を剥離するものであるが、
接触状態が不均一のため効率的でない。また、ろ過を停
止してエアバブリングを継続していると、膜上部にエア
溜まりが生じ、ろ過膜が膨れて隣接するろ過膜同士がこ
すれ合い膜表面を損傷することがある。このようにエア
バブリングによる洗浄には、未だ改善されるべき問題が
残されている。
However, when a flat membrane is used, there is a case where the removal or peeling of the cake on the membrane surface by air bubbling from below the filtration membrane is not sufficient. There is a problem that a film area is required, which leads to an increase in cost. As a method for coping with this, a plurality of filtration membranes are immersed in a separation tank and erected, as disclosed in JP-A-6-327949.
In some cases, a string-shaped flexible cleaning body is provided between the membranes. In this method, the flexible cleaning body comes into contact with the membrane surface to peel off extraneous matter by air bubbling from below.
Inefficient due to uneven contact. In addition, when the filtration is stopped and the air bubbling is continued, air accumulation occurs at the upper part of the membrane, the filtration membrane swells, and the adjacent filtration membranes may rub against each other to damage the membrane surface. Thus, cleaning by air bubbling still has a problem to be improved.

【0006】本発明はこのような事情に鑑みてなされた
もので、従来技術の問題点を解消し、効率よく膜面上の
ケーキを除去しながら、ろ過膜の損傷もなく、長時間ろ
過を継続することのできる浸漬型平膜分離装置およびそ
の制御方法を提供することを目的とする。
[0006] The present invention has been made in view of such circumstances, and solves the problems of the prior art, while efficiently removing the cake on the membrane surface, without long-term filtration without damage to the filtration membrane. It is an object of the present invention to provide an immersion type flat membrane separation apparatus that can be continued and a control method thereof.

【0007】[0007]

【課題を解決するための手段】本発明は、前記目的を達
成するために、本発明に係る請求項1の浸漬型平膜分離
装置では、通水材の両面にろ過膜を添設し、その上下端
の水平方向に膜端固定材をそれぞれ装着して分離体ユニ
ットを構成し、これら複数枚の分離体ユニットを間隔を
もって並設し、それらの分離体ユニットの左右端部を膜
接合固定材で固定するとともに、該膜接合固定材に吸引
管を配設し、該吸引管を前記通水材の通水路に連通させ
ている。
According to the present invention, in order to achieve the above object, in the immersion type flat membrane separation apparatus according to claim 1 of the present invention, filtration membranes are provided on both surfaces of a water-permeable material, Separator units are constructed by attaching the membrane end fixing materials horizontally at the upper and lower ends, and a plurality of these separator units are arranged side by side at intervals, and the left and right ends of these separator units are fixed by membrane bonding. In addition to the fixing with a material, a suction pipe is provided in the membrane bonding fixing material, and the suction pipe is communicated with a water passage of the water-permeable material.

【0008】この発明の浸漬型平膜分離装置によれば、
原液槽内の排水がろ過膜全体から通水材内に吸引され、
ろ過膜によって浄化され、その処理水は通水材の通水
路,吸引管を経て外部へ排出され、空気も処理水ととも
に外部へ排出されるため、膜上部に空気が溜まることな
く、したがって、膜上部が膨らむことによるろ過膜同士
の接触がなくなり、ろ過膜の損傷を防止できる。
According to the immersion type flat membrane separation device of the present invention,
The wastewater in the stock solution tank is sucked from the entire filtration membrane into the water-permeable material,
The treated water is purified by the filtration membrane, and the treated water is discharged to the outside through the water passage of the water-permeable material and the suction pipe. The air is also discharged to the outside together with the treated water. The contact between the filtration membranes due to the swelling of the upper part is eliminated, and damage to the filtration membranes can be prevented.

【0009】また、本発明に係る請求項2の浸漬型平膜
分離装置では、請求項1において、前記上下の膜端固定
材に各分離体ユニットの間隔を維持する膜間保持材をそ
れぞれ1つ以上設けている。この発明の浸漬型平膜分離
装置によれば、膜間の間隔が保持されるので、ろ過膜同
士の接触がなくなり、ろ過膜の損傷を防止できる。
Further, in the immersion type flat membrane separation apparatus according to claim 2 of the present invention, in the first aspect, each of the upper and lower membrane end fixing members is provided with one inter-membrane holding member for maintaining a distance between the respective separator units. More than one. ADVANTAGE OF THE INVENTION According to the immersion type flat membrane separation apparatus of this invention, since the space | interval between membranes is maintained, there is no contact between filtration membranes and damage of filtration membranes can be prevented.

【0010】また、本発明に係る請求項3の浸漬型平膜
分離装置では、請求項1または2において、前記分離体
ユニットの通水路に連通するドレンパイプを備えてい
る。この発明の浸漬型平膜分離装置によれば、装置を水
面上に引き上げる際に、通水材内に滞留している処理水
による膜下部の膨れを防止し、それによってろ過膜同士
の接触がなくなり、ろ過膜の損傷を防止できる。
Further, in the immersion type flat membrane separation device according to claim 3 of the present invention, in claim 1 or 2, a drain pipe communicating with a water passage of the separator unit is provided. ADVANTAGE OF THE INVENTION According to the immersion type flat membrane separation apparatus of this invention, when raising an apparatus on a water surface, the swelling of the lower part of a membrane by the treatment water staying in a water-permeable material is prevented, and thereby contact between filtration membranes is prevented. And damage to the filtration membrane can be prevented.

【0011】また、本発明に係る請求項4の浸漬型平膜
分離装置では、請求項1,2または3において、前記分
離体ユニットの下方に散気管を配設するとともに、該散
気管に連通させた空気導入管を前記膜接合固定材に沿っ
て設置している。この発明の浸漬型平膜分離装置によれ
ば、分離体ユニットを原水槽から取り出す際に、散気管
および空気導入管も一体に取り出すことができ、作業性
が向上する。
According to a fourth aspect of the present invention, there is provided the immersion type flat membrane separation device according to the first, second or third aspect, further comprising an air diffuser disposed below the separator unit and communicating with the air diffuser. The air introduction pipe thus set is installed along the membrane bonding fixing material. According to the immersion type flat membrane separation device of the present invention, when the separator unit is taken out of the raw water tank, the diffuser tube and the air introduction tube can also be taken out integrally, and workability is improved.

【0012】また、本発明に係る請求項5の浸漬型平膜
分離装置の制御方法では、請求項1,2,3または4の
装置において、ろ過停止状態において、所定時間以内に
一時的に短時間ろ過することを特徴としている。この発
明の浸漬型平膜分離装置によれば、長時間のろ過停止状
態においても、膜上部が膨れる虞れがなく、したがって
ろ過膜同士の接触がなくなり、ろ過膜の損傷を防止でき
る。
According to a fifth aspect of the present invention, there is provided the method for controlling a submerged flat membrane separation device according to the first, second, third, or fourth aspect, wherein the filtration is temporarily stopped within a predetermined time when the filtration is stopped. It is characterized by filtering over time. ADVANTAGE OF THE INVENTION According to the immersion type flat membrane separation apparatus of this invention, even if filtration is stopped for a long time, there is no possibility that the upper part of a membrane may swell. Therefore, there is no contact between filtration membranes, and damage to the filtration membrane can be prevented.

【0013】[0013]

【発明の実施の形態】以下添付図面に従って本発明の浸
漬型平膜分離装置およびその制御方法の好ましい実施の
形態について詳説する。図1は、本発明に係る浸漬型平
膜分離装置の一実施の形態を示している。この浸漬型平
膜分離装置10では、ろ過膜12がスペーサ14を介し
て通水材16を覆っている。スペーサ14は不織布等の
通気性のある材料によって形成されている。この場合、
ろ過膜12とスペーサ14は一体構造でもよい。通水材
16は、図2に示したように、断面が波状をした基材1
6aの両面に多孔板16bを添設したもので、基材16
aと多孔板16bとによって、高さ方向へ延びる複数本
の独立した通水路18を画成している。また、この通水
材16は多孔体でもよい。ろ過膜12の上下端には水平
方向に膜端固定材20,22がそれぞれ設けられてお
り、上部膜端固定材20は図2に示したように、中空に
なっている。この上部膜端固定材20の中空部20aは
後述する吸引管に連通されている。この実施の形態で
は、下部の膜端固定材22は中空ではない。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of a submerged flat membrane separation apparatus and a control method thereof according to the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows an embodiment of a submerged flat membrane separation apparatus according to the present invention. In the immersion type flat membrane separation device 10, the filtration membrane 12 covers the water-permeable material 16 via the spacer 14. The spacer 14 is formed of a breathable material such as a nonwoven fabric. in this case,
The filtration membrane 12 and the spacer 14 may have an integral structure. As shown in FIG. 2, the water-permeable material 16 is a base material 1 having a corrugated cross section.
6a, a perforated plate 16b is attached to both sides of the base material 16a.
a and the perforated plate 16b define a plurality of independent water passages 18 extending in the height direction. Further, the water-permeable material 16 may be a porous body. At the upper and lower ends of the filtration membrane 12, membrane end fixing materials 20 and 22 are provided in the horizontal direction, respectively, and the upper membrane end fixing material 20 is hollow as shown in FIG. The hollow portion 20a of the upper membrane end fixing member 20 is communicated with a suction tube described later. In this embodiment, the lower end fixing member 22 is not hollow.

【0014】このように形成されたろ過膜12、スペー
サ14、通水材16、膜端固定材20、22等によって
構成された分離体ユニットAは、複数組が互いに併置さ
れ、それらの左右側端に膜接合固定材24、26が配設
されている。膜接合固定材24、26は、集水管24
a、26aを有しており、該集水管24a、26aは上
部膜端固定材20の中空部20aに連通している。この
集水管24a、26aの上端には吸引管28、30が形
成されている。また、各分離体ユニットAの上下部の膜
端固定材20、22には、櫛歯状をした膜間保持材3
2、34がそれぞれ少なくとも1個以上設けられ、その
膜間保持材32,34の歯が各分離体ユニットA,Aの
間に介在され、膜間隔を均一に保持している 上記した浸漬型平膜分離装置10では、該装置10を原
液槽内に浸漬し、吸引管28、30を真空ポンプ等の吸
引ホースに接続して、集水管24a、26aの流体を吸
引し、かつ分離体ユニットAの下方から空気を散気しな
がらろ過を行う。すると、ろ過膜12の両面間には差圧
が発生し、その差圧によって原液槽内の排水がろ過膜1
2,スペーサ14,多孔板16bの通孔16cを経て通
水路18に吸引され、該通水路18から上部膜端固定材
20の中空部20aを経て膜接合固定材24、26の集
水管24a、26aに吸引され、吸引管28,30を経
て外部に排出される。
A plurality of sets of the separation unit A composed of the filtration membrane 12, the spacer 14, the water-permeable material 16, the membrane end fixing materials 20, 22 and the like thus formed are juxtaposed with each other, and the left and right sides thereof are arranged. Membrane bonding fixing materials 24 and 26 are provided at the ends. The membrane bonding fixing members 24, 26
a, 26a, and the water collecting pipes 24a, 26a communicate with the hollow portion 20a of the upper membrane end fixing material 20. Suction pipes 28 and 30 are formed at the upper ends of the water collecting pipes 24a and 26a. The upper and lower membrane edge fixing members 20 and 22 of each of the separator units A are provided with a comb-shaped inter-membrane holding member 3.
2 and 34 are provided at least one each, and the teeth of the inter-membrane holding members 32 and 34 are interposed between the separator units A and A, and the inter-membrane spacing is uniformly maintained. In the membrane separation device 10, the device 10 is immersed in a stock solution tank, and the suction pipes 28 and 30 are connected to a suction hose such as a vacuum pump to suck the fluid of the water collection pipes 24a and 26a, and the separation unit A Filter while aerating air from underneath. Then, a pressure difference is generated between both surfaces of the filtration membrane 12, and the pressure difference causes the drainage in the stock solution tank to flow through the filtration membrane 1.
2, the water is sucked into the water passage 18 through the spacer 14 and the through hole 16c of the perforated plate 16b, and from the water passage 18 through the hollow portion 20a of the upper membrane end fixing material 20, the water collecting pipe 24a of the membrane bonding fixing material 24, 26; It is sucked by 26a and discharged to the outside via suction pipes 28 and 30.

【0015】したがって、上記した浸漬型平膜分離装置
では、ろ過膜12の全面から排水が吸引され、かつ膜間
に空気が均一に供給できるため、長期間膜性能を維持す
ることができる。また、上部の膜端固定材20の中空部
20aに空気が溜まると、その空気は膜接合固定材2
4、26の集水管24a、26aに吸引されるので、ろ
過膜12の上部を膨らませることはなく、ろ過膜12同
士がこすれ合うことによるろ過膜12の損傷は生じな
い。しかし、ろ過を停止した場合、停止時間とともに、
ろ過膜12内上部に空気が溜まる。ろ過停止が所定時
間、例えば6時間以上になる場合には空気溜まり量が多
くなり、ろ過膜12が膨れることもあるため、6時間以
内に一時的に短時間、例えば1分間以上吸引ろ過を行う
ことで、ろ過膜12の膨れを防止し、ろ過膜12の損傷
を未然に防ぐことができる。
Therefore, in the above-mentioned immersion type flat membrane separation apparatus, since the drainage is sucked from the entire surface of the filtration membrane 12 and the air can be uniformly supplied between the membranes, the membrane performance can be maintained for a long period of time. When air accumulates in the hollow portion 20a of the upper membrane end fixing material 20, the air is transferred to the membrane bonding fixing material 2
Since the suction is performed by the water collecting pipes 24a and 26a of the fourth and fourth water collection tubes 24, the upper portion of the filtration membrane 12 does not swell, and the filtration membrane 12 is not damaged due to the rubbing between the filtration membranes 12. However, if you stop filtration, along with the downtime,
Air accumulates in the upper part of the filtration membrane 12. If the filtration is stopped for a predetermined time, for example, 6 hours or more, the amount of air accumulation increases, and the filtration membrane 12 may swell. Therefore, suction filtration is temporarily performed within 6 hours for a short time, for example, 1 minute or more. Thus, the swelling of the filtration membrane 12 can be prevented, and damage to the filtration membrane 12 can be prevented.

【0016】図3は、本発明の他の実施の形態を示すも
ので、下部に中空の膜端固定材22を設け、膜接合固定
材24、26に集水管24b,26bを各分離体ユニッ
トAにわたって配設し、その集水管24b,26bにド
レンパイプ36、38を設け、上記膜端固定材22の中
空部を集水管24b,26bに連通している。また、ド
レンパイプ36、38には、キャップ40,42をそれ
ぞれ装着し、ドレンパイプ36,38を閉塞しておく。
そして、装置10を水面上に引き上げる際に、キャップ
40,42を外し、ドレンパイプ36,38を開成し
て、分離体ユニットAから処理水を排出させて、処理水
によるろ過膜12の膨れを防止する。なお、上記キャッ
プ40,42に替えて、ドレンパイプ36,38に逆止
弁(図示せず)を介在させて、分離体ユニットA内が原
液槽の圧力以下の場合には、ドレンパイプ36,38を
閉塞し、分離体ユニットA内が原液槽の圧力よりも大き
くなった場合には、ドレンパイプ36,38を開成する
ようにしてもよい。この場合には、キャップ40,42
を取り外す等の手間を必要とせず、装置を原液槽から引
き上げる際に、ドレンパイプ36,38は自動的に開放
される。
FIG. 3 shows another embodiment of the present invention, in which a hollow membrane end fixing member 22 is provided at a lower portion, and water collecting pipes 24b, 26b are provided on membrane bonding fixing members 24, 26, respectively. A, drain pipes 36, 38 are provided in the water collecting pipes 24b, 26b, and the hollow portion of the membrane end fixing member 22 communicates with the water collecting pipes 24b, 26b. Caps 40 and 42 are attached to the drain pipes 36 and 38, respectively, and the drain pipes 36 and 38 are closed.
Then, when the apparatus 10 is lifted above the water surface, the caps 40 and 42 are removed, the drain pipes 36 and 38 are opened, and the treated water is discharged from the separator unit A to prevent the swelling of the filtration membrane 12 due to the treated water. To prevent. It should be noted that, in place of the caps 40 and 42, a check valve (not shown) is interposed between the drain pipes 36 and 38, and when the pressure inside the separator unit A is lower than the pressure of the stock solution tank, the drain pipes 36 and 38 When the pressure in the separator unit A becomes higher than the pressure of the stock solution tank, the drain pipes 36 and 38 may be opened. In this case, the caps 40, 42
The drain pipes 36 and 38 are automatically opened when the apparatus is pulled up from the stock solution tank, without the need for removing the device.

【0017】なお、この実施の形態では、通水材16と
ろ過膜12を点接着で一体化したことにより、ろ過膜1
2における応力集中を分散化し、信頼性を向上してい
る。図4は、本発明のさらに他の実施の形態を示すもの
で、各分離体ユニットAの下方に、各ろ過膜12に沿っ
て散気管44をそれぞれ配設するとともに、膜接合固定
材24、26内に空気導入管46,48を集水管24
a、26aの吸引管28、30とは独立して設置してい
る。この空気導入管46,48は、その下端に各分離体
ユニットAに渡って設置される枝管46a,48aを備
え、該枝管46a,48aを各散気管44に連通させて
いる。これにより、各分離体ユニットAのろ過膜12に
確実に空気を供給することができる。
In this embodiment, the water-permeable material 16 and the filtration membrane 12 are integrated by point bonding, so that the filtration membrane 1
2, the stress concentration is dispersed and the reliability is improved. FIG. 4 shows still another embodiment of the present invention, in which a diffuser 44 is provided along each filtration membrane 12 below each separator unit A, and a membrane bonding fixing material 24, The air introduction pipes 46 and 48 are provided in the water collection pipe 24.
a, 26a are installed independently of the suction pipes 28, 30. The air introduction pipes 46 and 48 are provided at their lower ends with branch pipes 46a and 48a installed over the respective separator units A, and communicate the branch pipes 46a and 48a to the respective diffuser pipes 44. Thereby, air can be reliably supplied to the filtration membrane 12 of each separation unit A.

【0018】図5は、本発明のさらに他の実施の形態を
示すもので、図4に示した分離体ユニットA,Aを垂直
方向に重ねて配設し、上下分離体ユニットA,Aの吸引
管28,28、30,30を互いに接続するとともに、
下段の分離体ユニットAの下方に散気管44を配設し、
該散気管44の端部に連通させた空気導入管46,48
を膜接合固定材24、26内に配設させ、それらを上段
の分離体ユニットAの上面から外方へ延設させている。
FIG. 5 shows still another embodiment of the present invention, in which the separator units A, A shown in FIG. While connecting the suction pipes 28, 28, 30, 30 to each other,
A diffuser 44 is provided below the lower separator unit A,
Air introduction pipes 46 and 48 communicated with the end of the air diffusion pipe 44.
Are disposed in the membrane bonding fixing members 24 and 26, and they are extended outward from the upper surface of the upper separation unit A.

【0019】なお、上記各実施の形態における分離体ユ
ニットAでは、通水路18を上下方向に形成している
(図2参照)が、図6に示したように、水平方向に形成
してもよい。この場合には、原液槽内の排水がろ過膜1
2、通水材16の多孔板16bの孔を経て水平に配置さ
れた通水路18に吸引され、該通水路18から膜接合固
定材24、26内に配設された吸引管28、30を経て
外部に排出される。この場合、吸引管28、30を設け
ないで、膜接合固定材24、26を直接吸引管として使
用することもできる。その際には、図7に示すように、
多孔板16b上部の通孔の開いていない部分は樹脂50
でシールしておくようにする。
In the separator unit A in each of the above embodiments, the water passage 18 is formed in the vertical direction (see FIG. 2). However, as shown in FIG. 6, the water passage 18 may be formed in the horizontal direction. Good. In this case, the drainage in the stock solution tank is
2. The suction pipes 28, 30 provided through the holes of the perforated plate 16b of the water passage material 16 into the horizontally disposed water passages 18 and disposed in the membrane bonding fixing members 24, 26 from the water passages 18 are removed. Is discharged to the outside. In this case, the membrane bonding fixing members 24 and 26 can be directly used as suction tubes without providing the suction tubes 28 and 30. At that time, as shown in FIG.
The portion of the upper part of the perforated plate 16b where the through holes are not opened is the resin 50
To keep it sealed.

【0020】[0020]

【発明の効果】以上説明したように、本発明に係る請求
項1の浸漬型平膜分離装置では、通水材の両面にろ過膜
を添設し、その上下端の水平方向に膜端固定材をそれぞ
れ装着して分離体ユニットを構成し、これら複数枚の分
離体ユニットを間隔をもって並設し、それらの分離体ユ
ニットの左右端部を膜接合固定材で固定するとともに、
該膜接合固定材に吸引管を配設し、該吸引管を前記通水
材の通水路に連通させている。したがって、原液槽内の
排水がろ過膜全体から通水材内に吸引され、ろ過膜によ
って浄化され、その処理水は通水材の通水路,吸引管を
経て外部へ排出される。その際、空気も処理水とともに
外部へ排出されるため、膜上部に空気が溜まることな
く、膜上部が膨らむことによるろ過膜同士の接触がなく
なり、ろ過膜の損傷を防止できる。
As described above, in the immersion type flat membrane separation apparatus according to the first aspect of the present invention, filtration membranes are provided on both surfaces of the water-permeable material, and the membrane ends are fixed horizontally at the upper and lower ends. Each of the materials is attached to form a separation unit, the plurality of separation units are juxtaposed at intervals, and the left and right ends of the separation units are fixed with a membrane bonding fixing material,
A suction pipe is provided on the membrane-bonded fixing material, and the suction pipe is connected to a water passage of the water-permeable material. Therefore, the wastewater in the undiluted solution tank is sucked into the water-permeable material from the entire filtration membrane, purified by the filtration membrane, and the treated water is discharged to the outside through the water-flow passage of the water-permeable material and the suction pipe. At this time, since the air is also discharged to the outside together with the treated water, the air does not accumulate at the upper part of the membrane, and the filtration membranes do not come into contact with each other due to the swelling of the upper part of the membrane, thereby preventing damage to the filtration membrane.

【0021】また、本発明に係る請求項2の浸漬型平膜
分離装置では、請求項1において、前記上下の膜端固定
材に各分離体ユニットの間隔を維持する膜間保持材をそ
れぞれ1つ以上設けている。したがって、膜間の間隔が
保持されるので、ろ過膜同士の接触がなくなり、ろ過膜
の損傷を防止できる。また、本発明に係る請求項3の浸
漬型平膜分離装置では、請求項1または2において、前
記分離体ユニットの通水路に連通するドレンパイプを備
えている。したがって、装置を水面上に引き上げる際
に、通水材内に滞留している処理水による膜下部の膨れ
を防止し、それによってろ過膜同士の接触がなくなり、
ろ過膜の損傷を防止できる。
Further, in the immersion type flat membrane separation apparatus according to claim 2 of the present invention, in the first aspect, each of the upper and lower membrane edge fixing members is provided with one inter-membrane holding member for maintaining a distance between the respective separator units. More than one. Therefore, since the interval between the membranes is maintained, the contact between the filtration membranes is eliminated, and damage to the filtration membranes can be prevented. Further, in the immersion type flat membrane separation device of claim 3 according to the present invention, in claim 1 or 2, a drain pipe communicating with a water passage of the separator unit is provided. Therefore, when the apparatus is raised above the water surface, the swelling of the lower part of the membrane due to the treated water staying in the water-permeable material is prevented, thereby eliminating the contact between the filtration membranes,
Damage to the filtration membrane can be prevented.

【0022】また、本発明に係る請求項4の浸漬型平膜
分離装置では、請求項1,2または3において、前記分
離体ユニットの下方に散気管を配設するとともに、該散
気管に連通させた空気導入管を前記膜接合固定材に沿っ
て設置している。したがって、分離体ユニットを原水槽
から取り出す際に、散気管および空気導入管も一体に取
り出すことができ、作業性が向上する。
Further, in the immersion type flat membrane separation device according to claim 4 of the present invention, in claim 1, 2, or 3, an air diffuser is provided below the separator unit and communicates with the air diffuser. The air introduction pipe thus set is installed along the membrane bonding fixing material. Therefore, when the separator unit is taken out of the raw water tank, the diffuser tube and the air introduction tube can also be taken out integrally, and workability is improved.

【0023】また、本発明に係る請求項5の浸漬型平膜
分離装置の制御方法では、請求項1,2,3または4の
装置において、ろ過停止状態において、所定時間以内に
一時的に短時間ろ過することを特徴としている。したが
って、長時間のろ過停止状態においても、膜上部が膨れ
る虞れがなく、したがってろ過膜同士の接触がなくな
り、ろ過膜の損傷を防止できる。
According to a fifth aspect of the present invention, in the control method of the immersion type flat membrane separation apparatus, the apparatus according to any one of the first, second, third, and fourth aspects is characterized in that the filtration is temporarily stopped within a predetermined time when the filtration is stopped. It is characterized by filtering over time. Therefore, even when the filtration is stopped for a long time, there is no possibility that the upper portion of the membrane will swell, so that there is no contact between the filtration membranes, and damage to the filtration membrane can be prevented.

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

【図1】本発明に係る浸漬型平膜分離装置の一実施の形
態を示した概念的な一部切欠き斜視図
FIG. 1 is a conceptual partially cutaway perspective view showing an embodiment of an immersion type flat membrane separation device according to the present invention.

【図2】本発明に係る浸漬型平膜分離装置の構造の一部
を示した切欠き斜視図
FIG. 2 is a cutaway perspective view showing a part of the structure of a submerged flat membrane separation device according to the present invention.

【図3】本発明に係る浸漬型平膜分離装置の他の実施の
形態を示した概念的な一部切欠き斜視図
FIG. 3 is a conceptual partially cutaway perspective view showing another embodiment of the immersion type flat membrane separation device according to the present invention.

【図4】本発明に係る浸漬型平膜分離装置のさらに他の
実施の形態を示した概念的な一部切欠き斜視図
FIG. 4 is a conceptual partially cutaway perspective view showing still another embodiment of the immersion type flat membrane separation device according to the present invention.

【図5】本発明に係る浸漬型平膜分離装置のさらに他の
実施の形態を示した概念的な斜視図
FIG. 5 is a conceptual perspective view showing still another embodiment of the immersion type flat membrane separation device according to the present invention.

【図6】本発明に係る浸漬型平膜分離装置のさらに他の
実施の形態を示したもので、構造の一部を示した切欠き
斜視図
FIG. 6 is a cutaway perspective view showing a part of the structure of still another embodiment of the immersion type flat membrane separation device according to the present invention.

【図7】本発明に係る浸漬型平膜分離装置のさらに他の
実施の形態を示したもので、吸引管を設けないで、膜接
合固定材を直接吸引管として使用する構造の一部を示し
た切欠き斜視図
FIG. 7 shows still another embodiment of the immersion type flat membrane separation device according to the present invention, in which a part of a structure in which a membrane bonding fixing material is directly used as a suction tube without providing a suction tube. Notched perspective view shown

【符号の説明】[Explanation of symbols]

10…浸漬型平膜分離装置 12…ろ過膜 14…スペーサ 16…通水材 16a…基材 16b…多孔板 16c…通孔 18…通水路 20、22…膜端固定材 20a…中空部 24、26…膜接合固定材 24a、26a…集水管 28、30…吸引管 32、34…膜間保持材 36、38…ドレン部 40、42…キャップ 44…散気管 46、48…空気導入管 46a、48a…枝管 DESCRIPTION OF SYMBOLS 10 ... Immersion type flat membrane separation apparatus 12 ... Filtration membrane 14 ... Spacer 16 ... Water-permeable material 16a ... Substrate 16b ... Perforated plate 16c ... Through-hole 18 ... Water-passage 20, 22 ... Membrane end fixing material 20a ... Hollow part 24, 26: membrane bonding and fixing material 24a, 26a: water collecting pipe 28, 30 ... suction pipe 32, 34 ... intermembrane holding material 36, 38 ... drain part 40, 42 ... cap 44 ... diffuser pipe 46, 48 ... air introduction pipe 46a, 48a ... Branch pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大西 真人 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 (72)発明者 山寺 利夫 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 (72)発明者 奥野 裕 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 (72)発明者 村井 行男 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 (72)発明者 安藤 尋樹 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 (72)発明者 丹宗 紫朗 大阪府高槻市城西町6−6 株式会社ユア サコーポレーション内 (72)発明者 林 信夫 大阪府高槻市城西町6−6 株式会社ユア サコーポレーション内 Fターム(参考) 4D006 GA06 GA07 HA48 HA93 JA03A JA06A JA08A JA19A JA20A JA22A JA27A JA31A JA71 KA44 KC14 KE24Q MA03 PB08 PB15  ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Masato Onishi 1-1-1 Uchikanda, Chiyoda-ku, Tokyo Inside Hitachi Plant Construction Co., Ltd. (72) Toshio Yamadera 1-1-1 Uchikanda, Chiyoda-ku, Tokyo No. 14 Hitachi Plant Construction Co., Ltd. (72) Inventor Hiroshi Okuno 1-1-14 Uchikanda, Chiyoda-ku, Tokyo (72) Inside Hitachi Plant Construction Co., Ltd. (72) Inventor Yukio Murai 1 Uchikanda, Chiyoda-ku, Tokyo No. 1-114 Hitachi Plant Construction Co., Ltd. (72) Inventor Hiroki Ando 1-11-1 Uchikanda, Chiyoda-ku, Tokyo Inside Hitachi Plant Construction Co., Ltd. (72) Inventor Shirou Tanso Takatsuki-shi, Osaka 6-6 Josai-cho Inside Your Sako Corporation (72) Inventor Nobuo Hayashi 6-6 Josai-cho, Takatsuki-shi, Osaka F term (reference) 4D006 GA06 GA07 HA48 HA93 JA03A JA06A JA08A JA19A JA20A JA22A JA27A JA31A JA71 KA44 KC14 KE24Q MA03 PB08 PB15

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】通水材の両面にろ過膜を添設し、その上下
端の水平方向に膜端固定材をそれぞれ装着して分離体ユ
ニットを構成し、これら複数枚の分離体ユニットを間隔
をもって並設し、それらの分離体ユニットの左右端部を
膜接合固定材で固定するとともに、該膜接合固定材に吸
引管を配設し、該吸引管を前記通水材の通水路に連通さ
せたことを特徴とする浸漬型平膜分離装置。
1. Separation units are constructed by attaching filtration membranes to both sides of a water-permeable material, and attaching a membrane end fixing material horizontally at upper and lower ends thereof to form a separation unit. The left and right ends of these separator units are fixed with a membrane bonding fixing material, and a suction pipe is arranged in the membrane bonding fixing material, and the suction pipe communicates with the water passage of the water flow material. An immersion type flat membrane separation device characterized by having been performed.
【請求項2】前記上下の膜端固定材に各分離体ユニット
の間隔を維持する膜間保持材をそれぞれ1つ以上設けた
ことを特徴とする請求項1に記載の浸漬型平膜分離装
置。
2. The immersion-type flat membrane separation apparatus according to claim 1, wherein one or more intermembrane holding members for maintaining an interval between the respective separator units are provided on the upper and lower membrane edge fixing members. .
【請求項3】前記分離体ユニットの通水路に連通するド
レンパイプを備えたことを特徴とする請求項1または2
に記載の浸漬型平膜分離装置。
3. A drain pipe communicating with a water passage of the separator unit.
2. The immersion type flat membrane separation device according to 1.).
【請求項4】前記分離体ユニットの下方に散気管を配設
するとともに、該散気管に連通させた空気導入管を前記
膜接合固定材に沿って設置したことを特徴とする請求項
1,2または3に記載の浸漬型平膜分離装置。
4. An air diffusion tube is provided below the separator unit, and an air introduction tube communicating with the air diffusion tube is installed along the membrane bonding fixing material. 4. The immersion type flat membrane separation device according to 2 or 3.
【請求項5】請求項1,2,3または4の装置におい
て、ろ過停止状態において、所定時間以内に一時的に短
時間ろ過することを特徴とする浸漬型平膜分離装置の制
御方法。
5. A control method for an immersion type flat membrane separation apparatus according to claim 1, wherein the filtration is temporarily carried out for a short time within a predetermined time when the filtration is stopped.
JP03723399A 1999-02-16 1999-02-16 Immersion type flat membrane separator and control method thereof Expired - Lifetime JP3815645B2 (en)

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