JPH01245894A - Filter apparatus for treatment of water - Google Patents
Filter apparatus for treatment of waterInfo
- Publication number
- JPH01245894A JPH01245894A JP7255388A JP7255388A JPH01245894A JP H01245894 A JPH01245894 A JP H01245894A JP 7255388 A JP7255388 A JP 7255388A JP 7255388 A JP7255388 A JP 7255388A JP H01245894 A JPH01245894 A JP H01245894A
- Authority
- JP
- Japan
- Prior art keywords
- filtration
- filter membranes
- membrane
- water
- membranes
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 239000012528 membrane Substances 0.000 claims abstract description 54
- 238000001914 filtration Methods 0.000 claims abstract description 43
- 239000000706 filtrate Substances 0.000 claims abstract description 5
- 239000010802 sludge Substances 0.000 claims description 11
- 239000012510 hollow fiber Substances 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 2
- 229920003002 synthetic resin Polymers 0.000 claims 1
- 239000000057 synthetic resin Substances 0.000 claims 1
- 238000009792 diffusion process Methods 0.000 abstract 1
- 238000005273 aeration Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ろ過装置に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a filtration device.
従来のろ過装置では、大径のチューブ状膜を被処理液の
流路内に並設して強固に固定してあった。In conventional filtration devices, large-diameter tubular membranes are arranged side by side in the flow path of the liquid to be treated and firmly fixed.
しかし、チューブ状膜で透過能力を上げるためには、ろ
過膜の並設数を増やさなければならず、ろ過装置全体が
大型になる欠点があった。However, in order to increase the permeation capacity with a tubular membrane, it is necessary to increase the number of filtration membranes arranged in parallel, which has the disadvantage of increasing the size of the entire filtration device.
本発明の目的は、ろ過装置全体を大型にせずに、透過能
力を上げられるようにする点にある。An object of the present invention is to increase the permeation capacity without increasing the size of the entire filtration device.
本考案のろ過装置の特徴構成は、被処理液の流路に、中
空糸状のろ過膜を多数並設すると共に、前記ろ過膜の内
側にろ過水回収部を形成し、前記ろ過膜に振動を与える
膜面付着物除去装置を設けてある ことにあり、その作
用効果は、次の通りである。The characteristic configuration of the filtration device of the present invention is that a large number of hollow fiber-like filtration membranes are arranged in parallel in the flow path of the liquid to be treated, a filtrate water recovery section is formed inside the filtration membrane, and vibration is applied to the filtration membrane. This is because a device for removing deposits on the film surface is provided, and its effects are as follows.
つまり、中空糸状膜は、チューブ状膜より微小径で簡単
に単位膜表面積を大きくして透過能力を上げることがで
き、しかも、被処理水からろ過水をろ過膜の内側へ回収
するに伴って、外側膜表面に付着しやすいゲル層は、膜
面付着物除去装置によってろ過膜を振動させることによ
って、膜が中空糸状であるために、楽器の弦のごとく膜
全体が振動して、効果的に剥離される。In other words, hollow fiber membranes have a smaller diameter than tubular membranes, and can easily increase permeability by increasing the unit membrane surface area. The gel layer, which tends to adhere to the outer membrane surface, can be removed by vibrating the filtration membrane with a membrane surface deposit removal device.Since the membrane is hollow fiber-like, the entire membrane vibrates like the strings of a musical instrument, making it more effective. It is peeled off.
従って、ろ過装置全体を小型にして、ろ過水の透過能力
を上げられながら、その透過水量を高く維持でき、ろ過
処理を効率良く行えるようになった。Therefore, it has become possible to downsize the entire filtration device, increase the permeation capacity of filtrate water, maintain a high amount of permeate water, and perform filtration processing efficiently.
次に、本発明の実施例を、図面に基づいて説明する。 Next, embodiments of the present invention will be described based on the drawings.
第1図に示すように、し尿、浄化槽汚泥、団地下水等の
廃水を活性汚泥によって生物処理する処理槽(1)を設
け、ブロワ−(B)からの空気を処理槽(1)内に供給
して曝気する散気管(2)を、処理槽(1)内に配置し
、散気管(2)の上方に多数本の中空糸状ろ過膜(3)
を並設して、それらの両端を張った状態で支持し、吸引
ポンプ(P)をろ過膜(3)に接続して、処理槽(1)
内の汚泥含有水からろ過膜(3)を通してろ過水だけを
引出すように構成して、処理槽(1)で散気管(2)に
よって、散気管(2)とろ過膜(3)との間に汚泥含有
水供給路(4)が形成され、ろ過膜(3)の配置部に形
成される流路(5)を汚泥含有水が通過する間に濃縮さ
れて、ろ過膜(3)の上方から前記散気管(2)にわた
って濃縮汚泥返送路(6)が形成され、上記3つの流路
(4) 、 (5) 、 (6)にわたって処理水が循
環流動するように構成してある。As shown in Figure 1, a treatment tank (1) is installed to biologically treat wastewater such as human waste, septic tank sludge, and underground water using activated sludge, and air from a blower (B) is supplied into the treatment tank (1). An aeration pipe (2) for aeration is placed in the treatment tank (1), and a large number of hollow fiber filtration membranes (3) are placed above the aeration pipe (2).
are installed in parallel and supported with both ends stretched, and the suction pump (P) is connected to the filtration membrane (3), and the treatment tank (1) is
The structure is configured so that only filtrate water is drawn out from the sludge-containing water through the filtration membrane (3), and in the treatment tank (1), the aeration pipe (2) is used to connect the aeration pipe (2) and the filtration membrane (3). A sludge-containing water supply channel (4) is formed in the sludge-containing water supply channel (4), and while the sludge-containing water passes through the flow channel (5) formed in the arrangement part of the filtration membrane (3), it is concentrated and flows above the filtration membrane (3). A concentrated sludge return path (6) is formed from the aeration pipe (2) to the aeration pipe (2), and the treated water is configured to circulate and flow through the three flow paths (4), (5), and (6).
そして、前記ろ過膜(3)の両端支持部(7)に対して
振動を与える振動装置(8)を設け、ろ過膜(3)全体
を振動させて膜表面に付着するゲル層を剥離除去して透
過水量を高(維持するようにしてあると共に、散気管(
2)からの気泡による乱流作用と、ろ過膜(3)に対す
る気泡の衝突作用で、膜表面のゲル層の剥離をより向上
するように構成してある。Then, a vibration device (8) is provided that vibrates the support portions (7) at both ends of the filtration membrane (3), and the entire filtration membrane (3) is vibrated to peel off and remove the gel layer adhering to the membrane surface. It is designed to maintain a high amount of permeated water, and a diffuser pipe (
It is configured to further improve the peeling of the gel layer on the membrane surface by the turbulence effect caused by the bubbles from 2) and the collision effect of the bubbles against the filtration membrane (3).
前記中空糸状ろ過膜(3)は、ポリエチレンから成り、
直径約1 amの可撓性中空糸から成る。The hollow fiber filtration membrane (3) is made of polyethylene,
It consists of flexible hollow fibers with a diameter of about 1 am.
前記ろ過膜(3)には、特別の振動装置(8)を設けず
に、散気管(2)を振動装置(8)に兼用して、散気管
(2)からの気泡が膜面に衝突することによって振動が
得られるだけのものであっても良い。The filtration membrane (3) is not provided with a special vibrating device (8), and the aeration tube (2) is also used as a vibrating device (8), so that the bubbles from the aeration tube (2) collide with the membrane surface. It may be possible to simply obtain vibration by doing so.
前記ろ過膜(3)は、第2図に示すよろに、その多数本
をU字状にして支持部材(9)で両端部を固定し、各ろ
過膜(3)どうしが、からまってろ過動率を抑制しない
ように、U字状の曲がり部(10)の内側に散気管(2
)を通し、支持部材(9)と散気管(2)とでろ過膜(
3)を張るように支持してあっても良い。As shown in Fig. 2, the filtration membranes (3) are formed into a U-shape and fixed at both ends with support members (9), and the filtration membranes (3) are entangled with each other to prevent filtration. In order not to suppress the air flow rate, a diffuser pipe (2
) through the filtration membrane (
3) may be supported so as to stretch.
前記ろ過膜(3)の材質はポリエチレン以外のものであ
っても良く、中空糸状の膜であれば良い。The material of the filtration membrane (3) may be other than polyethylene, as long as it is a hollow fiber membrane.
尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すが、該記入により本発明は添付図面の構造
に限定されるものではない。Incidentally, although reference numerals are written in the claims section for convenient comparison with the drawings, the present invention is not limited to the structure shown in the accompanying drawings.
図面における第1図は水処理装置の概略図を示し、第2
図は別実施例の水処理装置の概略図である。
(3)・・・・・・ろ過膜、(4)・・・・・・汚泥含
有水供給路、(5)・・・・・・流路、(6)・・・・
・・濃縮汚泥返送路、(8)・・・・・・振動装置。The first figure in the drawings shows a schematic diagram of the water treatment equipment, and the second figure shows a schematic diagram of the water treatment equipment.
The figure is a schematic diagram of a water treatment device according to another embodiment. (3)...Filtration membrane, (4)...Sludge-containing water supply channel, (5)...Flow channel, (6)...
... Thickened sludge return path, (8) ... Vibration device.
Claims (1)
接続する流路(5)に、筒状のろ過膜(3)を多数並設
してある水処理用ろ過装置であって、前記ろ過膜(3)
が中空糸状膜であって、前記ろ過膜(3)に振動を与え
る振動装置(8)を設けてある水処理用ろ過装置 2、被処理液の流路(5)に、中空糸状のろ過膜(3)
を多数並設すると共に、前記ろ過膜(3)の内側にろ過
水回収部を形成し、前記ろ過膜(3)に振動を与える膜
面付着物除去装置(8)を設けてあるろ過装置。 3、請求項1及び2記載のろ過膜(3)が、外径2mm
以下の筒状のろ過膜から成るろ過装置。 4、請求項1及び2記載のろ過膜(3)が、合成樹脂か
ら成るろ過装置。[Claims] 1. Water in which a large number of cylindrical filtration membranes (3) are arranged in parallel in the flow path (5) connecting the sludge-containing water supply path (4) and the thickened sludge return path (6). A processing filtration device, the filtration membrane (3)
is a hollow fiber membrane, and is provided with a vibration device (8) that vibrates the filtration membrane (3). (3)
A filtration device in which a large number of filtration membranes (3) are arranged in parallel, a filtrate water recovery section is formed inside the filtration membrane (3), and a membrane surface deposit removal device (8) is provided which applies vibration to the filtration membrane (3). 3. The filtration membrane (3) according to claims 1 and 2 has an outer diameter of 2 mm.
A filtration device consisting of the following cylindrical filtration membrane. 4. A filtration device in which the filtration membrane (3) according to claims 1 and 2 is made of synthetic resin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7255388A JPH01245894A (en) | 1988-03-25 | 1988-03-25 | Filter apparatus for treatment of water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7255388A JPH01245894A (en) | 1988-03-25 | 1988-03-25 | Filter apparatus for treatment of water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01245894A true JPH01245894A (en) | 1989-10-02 |
Family
ID=13492664
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7255388A Pending JPH01245894A (en) | 1988-03-25 | 1988-03-25 | Filter apparatus for treatment of water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01245894A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03262589A (en) * | 1990-03-13 | 1991-11-22 | Kubota Corp | Water treatment plant |
JPH05220358A (en) * | 1992-02-14 | 1993-08-31 | Sanki Eng Co Ltd | Membrane filtration method |
JPH0824594A (en) * | 1994-07-22 | 1996-01-30 | Toto Ltd | Operation of filter |
JP2008238080A (en) * | 2007-03-28 | 2008-10-09 | Tsukishima Kikai Co Ltd | Filtration module and filtration unit |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5763103A (en) * | 1980-09-30 | 1982-04-16 | Yuasa Battery Co Ltd | Filter |
JPS58159811A (en) * | 1982-03-18 | 1983-09-22 | Nitto Electric Ind Co Ltd | Method for removing material stuck on membrane in separation of liquid |
JPS6039303B2 (en) * | 1979-02-15 | 1985-09-05 | 住友化学工業株式会社 | Mixed dye composition and dyeing method using the same |
JPS61129094A (en) * | 1984-11-26 | 1986-06-17 | Nitto Electric Ind Co Ltd | Apparatus for treating membrane |
-
1988
- 1988-03-25 JP JP7255388A patent/JPH01245894A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6039303B2 (en) * | 1979-02-15 | 1985-09-05 | 住友化学工業株式会社 | Mixed dye composition and dyeing method using the same |
JPS5763103A (en) * | 1980-09-30 | 1982-04-16 | Yuasa Battery Co Ltd | Filter |
JPS58159811A (en) * | 1982-03-18 | 1983-09-22 | Nitto Electric Ind Co Ltd | Method for removing material stuck on membrane in separation of liquid |
JPS61129094A (en) * | 1984-11-26 | 1986-06-17 | Nitto Electric Ind Co Ltd | Apparatus for treating membrane |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03262589A (en) * | 1990-03-13 | 1991-11-22 | Kubota Corp | Water treatment plant |
JPH05220358A (en) * | 1992-02-14 | 1993-08-31 | Sanki Eng Co Ltd | Membrane filtration method |
JPH0824594A (en) * | 1994-07-22 | 1996-01-30 | Toto Ltd | Operation of filter |
JP2008238080A (en) * | 2007-03-28 | 2008-10-09 | Tsukishima Kikai Co Ltd | Filtration module and filtration unit |
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