Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3835511B2 - Concentrator - Google Patents
[go: Go Back, main page]

JP3835511B2 - Concentrator - Google Patents

Concentrator Download PDF

Info

Publication number
JP3835511B2
JP3835511B2 JP33223899A JP33223899A JP3835511B2 JP 3835511 B2 JP3835511 B2 JP 3835511B2 JP 33223899 A JP33223899 A JP 33223899A JP 33223899 A JP33223899 A JP 33223899A JP 3835511 B2 JP3835511 B2 JP 3835511B2
Authority
JP
Japan
Prior art keywords
screen
filter
plate
support plate
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.)
Expired - Fee Related
Application number
JP33223899A
Other languages
Japanese (ja)
Other versions
JP2001145899A (en
Inventor
栄一 石垣
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.)
Ishigaki Co Ltd
Original Assignee
Ishigaki Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ishigaki Co Ltd filed Critical Ishigaki Co Ltd
Priority to JP33223899A priority Critical patent/JP3835511B2/en
Publication of JP2001145899A publication Critical patent/JP2001145899A/en
Application granted granted Critical
Publication of JP3835511B2 publication Critical patent/JP3835511B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、下水汚泥等の難ろ過性の汚泥の濃縮装置に関し、特に、ろ材を張設したろ過室を濃縮槽に浸漬させて、分離液を排出する装置の改良に関する。
【0002】
【従来の技術】
従来、二枚のろ過網を合せてろ過室を形成したろ過器をろ過槽の汚泥室内に懸架し汚泥中の水分をろ過室内に取出して、ろ過槽の汚泥を濃縮するろ過濃縮装置は、例えば、特公昭63−13721号公報に記載してあるように公知である。また、ろ過室のろ過面に張設したろ布を濃縮槽の外部に取出して洗浄する装置も、実公平2−27853号公報で出願人が提案している。
【0003】
【発明が解決しようとする課題】
しかしながら、上記従来のろ材としてろ布を用いるものにあっては、ろ布に付着したケーキは剥離し難く、目詰まりしたろ布をろ過室の内部から圧縮空気を供給して逆洗しても圧縮空気が一部のろ材面から目抜けして、充分な洗浄が行なえず目詰り物の取除きが困難であった。そのために、ろ過室に張設したろ布を走行させて濃縮槽の外部でろ布を再生するものにあっては、水中でろ布を走行させる装置と大きな動力を必要としていた。この発明は、ろ材を水中で走行させることなくケーキの剥離性のよいろ材を用いた濃縮装置を提供するものである。
【0004】
【課題を解決するための手段】
この発明の要旨は、濃縮槽にろ過板を浸漬させ、濃縮槽に汚泥の供給管と濃縮液の取出管を連結し、ろ過板に分離液の排出管を接続した装置において、上記ろ過板のろ過室にその表面に多数の小孔を有する圧力タンクを内設し、ろ過室のろ材面と圧力タンクの表面との間に隙間を設けると共に、圧力タンクに圧縮空気管を接続したもので、圧力タンクの周面の小孔からろ過室のろ材面に圧縮空気を吹付けるものである。そして、上記ろ過板は多数の通孔を有する支持板に剥離性の良い金属性のメタルスクリーンを張設したものである。好ましいろ材は、複数枚のメタルスクリーンを支持板に張設し、メタルスクリーンを重設してろ過目を細かくしたものである。具体的には、重設したメタルスクリーンの目を上面層ほど細かくしてろ液の抜出しを容易としたもので、支持板に荒目スクリーンを敷設し、その上部の中間層に中目スクリーンを介装して、表面層に細目スクリーンを張設したものである。また、支持板の通孔は、楔形の断面積を有するスリットとして、ろ過室の内側からスクリーンの目を順次細かくして逆洗しやすくしたものである。
【0005】
【発明の実施の形態】
この発明に係る装置は上記のように構成してあり、汚泥の供給管から濃縮槽に汚泥を供給してろ過板を濃縮槽に浸漬させ、ろ過室の排出管から分離液を排出すると汚泥は濃縮され、ケーキがメッシュスクリーンに付着してろ過性能が低下する。濃縮された汚泥を濃縮槽の取出管から抜出した後、圧縮空気を圧力タンクに圧入すると、圧力タンクの小孔から対向するろ過室のメッシュスクリーンの裏面に向って圧縮空気が噴射され、ろ過性の良いろ過面を圧縮空気で逆洗して再生することができる。再び、濃縮槽に汚泥を供給して汚泥濃縮を開始する。
【0006】
【実施例】
この発明に係るろ過機のろ材について、図面に基づき詳述すると、先ず、図1において、符号1は濃縮槽であって、濃縮槽1の側壁の上部に汚泥の供給管2と濃縮槽1の槽底部に濃縮液の取出管3が連結してあり、汚泥の供給管2と濃縮液の取出管3に自動弁V1、V2が設けてある。濃縮槽1には複数のろ過板4…が並設してあり、ろ過板4にサイホン状の分離液の排出管5が連結されて、濃縮槽1との水位差によりこの排出管5には自動弁V3が設けてある。なお、ろ過板4に連結した排出管5は、図3に示すように、濃縮槽1を貫通して排出させてもよいものである。ろ過板4は、図1及び図2に示すように、ろ過板4は長方形の箱型状の支持板6と支持板6に張設した金属性のメタルスクリーン7とからなっており、ろ過板4の内部にろ過室8が形成してある。
【0007】
ろ過板4についてさらに詳述すると、図4に示すように、支持板6は多数の通孔6aを有しており、この支持板6の通孔6aは断面が楔形で平面視がスリットを形成している。この支持板6に張設したメタルスクリーン7は、支持板6に敷設した荒目スクリーン7aと、その上部の中間層に中目スクリーン7bが介装され、表面層に細目スクリーン7cが張設してあり、重設したメタルスクリーン7a、7b、7cの目を上面層ほど細かくしてあり、ろ材を積層することによりスクリーンの目が細かくなり、小さな粒子も補捉して回収率を高めることができ、ろ材強度も大きくなるものである。これらのスクリーンの目は、原液のろ過性の難易度により、あるいは固形物の粒径によりスクリーンの目の口径を変更できるものであり、スクリーンの口径としては、荒目スクリーン7aは500μm〜1.5mm、その上部の中間層の中目スクリーン7bは100μm〜1.0mm、表面層の細目スクリーン7cは20μm〜0.5mm範囲のものが考えられ、対象原液に応じて任意の口径のメタルスクリーン7a、7b、7cを組合せればよいものである。そして、支持板に支持された複数枚のメタルスクリーン7が重合されて、高圧力にも耐え高脱水作業にも対応しえるものである。なお、支持板6の内周面にパンチングメタル13を敷設してろ過板4を補強してもよいものである。
【0008】
ろ過板4のろ過室8には、図2及び図5に示すように、その表面に多数の小孔9a…を有する圧力タンク9が内設してあり、ろ過板4のろ過面と圧力タンク9の小孔9aを接近させて対向させてある。圧力タンク9には圧縮空気管10が接続してあり、圧縮空気管10は自動弁V4を介して空気圧縮機11に連結してある。そして、メタルスクリーン7が目詰まりしたときには、圧縮空気を噴射すれば、メタルスクリーン7の裏面から圧縮空気が直接スクリーンの目に吹き込まれ、剥離制の良いメタルスクリーン7から目詰り物を取除くことができる。上記ろ液の排出管5の始端開口は圧力タンク9を内設したろ液室8の側端部に設けてあり、排出管5の終端部がろ液貯槽12に開口してある。
【0009】
この発明に係る濃縮装置の作動要領を説明すると、▲1▼濃縮工程:先ず、濃縮汚泥の取出管3の自動弁V2を閉、分離液の排出管5の自動弁V3を閉、圧縮空気管10の自動弁V4を閉として、汚泥の供給管に設けた自動弁V1を開いて濃縮槽1に汚泥を供給してろ過板4を濃縮槽1に浸漬させると、濃縮槽1の汚泥水位のヘッド圧によりろ液はろ過板4のメタルスクリーン7を通過してろ過室8に流入し、固形分はメタルスクリーン7に阻止され、槽底に沈殿してくる。ろ過室8に流入した分離液は、水位差により排出管5からろ液貯槽12に排出される。そして、所定時間後に汚泥の供給管の自動弁V1を閉じて、濃縮槽1への汚泥の流入を停止させる。▲2▼濃縮汚泥の排出工程:引続きろ過室8から分離液を排出すると汚泥は順次濃縮され、やがてケーキがメタルスクリーン7に付着してろ過性能が低下する。濃縮汚泥の取出管3の自動弁V2を開き、濃縮された汚泥を濃縮槽1の取出管3から排出する。▲3▼ろ材の逆洗工程:濃縮槽1の汚泥を排出した後、圧縮空気管10の自動弁V4を開き、空気圧縮機11を駆動して圧縮空気を圧力タンク9に圧入すると、圧力タンク9の多数の小孔9a…から対向するろ過板4のメタルスクリーン7の裏面から圧縮空気が噴射され、ろ過性の良い金属性のろ過面を圧縮空気で逆洗してメタルスクリーン7を再生することができる。なお、メタルスクリーン7の汚れたろ過面の洗浄と、剥離した汚泥の濃縮槽1からの排出のために、洗浄水を分離液の排出管5からろ過室8に供給してもよいものである。そして、再び、濃縮槽に汚泥を供給して汚泥濃縮を開始することができる。
【0010】
【発明の効果】
以上のように、この発明の濃縮装置のろ過板は、多数の通孔を有する支持板に複数枚の金属性のメタルスクリーンを重設し、上面層ほど細かい目のスクリーンを重設したので、スクリーンの目が細かくなり精密ろ過が可能となり、ろ材強度も増加されるものである。そして、従来のろ材としてろ布を用いるものにあっては、目詰まりしたろ布に圧縮空気を供給して逆洗しても圧縮空気が一部のろ材面から目抜けして、目詰り物の取除きが困難であったものであるが、この発明のろ過板は、多数の小孔を有する圧力タンクをメタルスクリーンの裏面に対設したので、圧縮空気が直接メタルスクリーンの目に吹き込まれ、剥離性のよいメタルスクリーンからケーキを剥離できるものであり、逆洗浄浄が容易となるものである。
【図面の簡単な説明】
【図1】この発明に係る濃縮装置の斜視図である。
【図2】この発明に係る圧力タンクを内設したろ過板の概念的な縦断側面図である。
【図3】同じく濃縮装置の他の実施例を示す斜視図である。
【図4】同じくろ過板に配設したろ材の概念的な縦断側面図である。
【図5】同じく濃縮装置の縦断側面図である。
【符号の説明】
1 濃縮槽
2 供給管
3 取出管
4 ろ過板
5 排出管
6 支持板
6a 通孔
7 メタルスクリーン
7a 荒目スクリーン
7b 中目スクリーン
7c 細目スクリーン
8 ろ過室
9 圧力タンク
9a 小孔
10 圧縮空気管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a concentration device for difficult-to-filter sludge such as sewage sludge, and more particularly to improvement of a device for discharging a separation liquid by immersing a filtration chamber provided with a filter medium in a concentration tank.
[0002]
[Prior art]
Conventionally, a filtration concentrator that concentrates the sludge in a filtration tank by suspending a filter that forms a filtration chamber by combining two filtration nets in a sludge chamber of the filtration tank and taking out moisture in the sludge into the filtration chamber, for example, This is known as described in JP-B-63-13721. Moreover, the applicant has also proposed an apparatus for taking out and washing the filter cloth stretched on the filtration surface of the filtration chamber outside the concentration tank in Japanese Utility Model Publication No. 2-27853 .
[0003]
[Problems to be solved by the invention]
However, in the case of using a filter cloth as the conventional filter medium, the cake attached to the filter cloth is difficult to peel off, and the clogged filter cloth can be backwashed by supplying compressed air from the inside of the filtration chamber. Compressed air was missing from the surface of some of the filter media, and sufficient cleaning could not be performed, making it difficult to remove clogged material. Therefore, in the case where the filter cloth stretched in the filtration chamber is run to regenerate the filter cloth outside the concentration tank, a device for running the filter cloth in water and great power are required. The present invention provides a concentrating device using a filter medium having good cake peelability without running the filter medium in water.
[0004]
[Means for Solving the Problems]
The gist of the present invention is that the filter plate is immersed in the concentration tank, the sludge supply pipe and the concentrate discharge pipe are connected to the concentration tank, and the separation liquid discharge pipe is connected to the filter plate. A pressure tank having a large number of small holes on its surface is installed in the filtration chamber, a gap is provided between the filter medium surface of the filtration chamber and the surface of the pressure tank, and a compressed air pipe is connected to the pressure tank. Compressed air is blown from the small holes on the peripheral surface of the pressure tank to the filter medium surface of the filtration chamber. The filter plate is a support plate having a large number of through holes and a metallic metal screen with good peelability. A preferred filter medium is one in which a plurality of metal screens are stretched on a support plate, and metal screens are overlapped to make the filter screen fine. Specifically, the top of the metal screen is made finer so that the filtrate can be drawn out more easily. The coarse screen is laid on the support plate, and the middle screen is placed on the upper intermediate layer. A fine screen is stretched on the surface layer. Further, the through holes of the support plate are slits having a wedge-shaped cross-sectional area, and the screen eyes are successively made finer from the inside of the filtration chamber to facilitate backwashing.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
The apparatus according to the present invention is configured as described above. When sludge is supplied from the sludge supply pipe to the concentration tank, the filter plate is immersed in the concentration tank, and the separation liquid is discharged from the discharge pipe of the filtration chamber, the sludge is As a result, the cake adheres to the mesh screen and the filtration performance decreases. After extracting the concentrated sludge from the extraction pipe of the concentration tank, when compressed air is pressed into the pressure tank, the compressed air is injected from the small hole of the pressure tank toward the back of the mesh screen of the opposing filtration chamber, and the filterability A good filtration surface can be backwashed with compressed air and regenerated. Again, sludge is supplied to the concentration tank and sludge concentration is started.
[0006]
【Example】
The filter medium of the filter according to the present invention will be described in detail with reference to the drawings. First, in FIG. 1, reference numeral 1 is a concentration tank, and a sludge supply pipe 2 and a concentration tank 1 are disposed on the upper side wall of the concentration tank 1. A concentrate extraction pipe 3 is connected to the bottom of the tank, and automatic valves V1 and V2 are provided on the sludge supply pipe 2 and the concentrate extraction pipe 3, respectively. A plurality of filtration plates 4 are arranged in parallel in the concentration tank 1, and a siphon-like separation liquid discharge pipe 5 is connected to the filtration board 4, and the discharge pipe 5 is connected to the concentration pipe 1 due to a difference in water level with the concentration tank 1. An automatic valve V3 is provided. In addition, the discharge pipe 5 connected to the filter plate 4 may be discharged through the concentration tank 1 as shown in FIG. As shown in FIGS. 1 and 2, the filter plate 4 comprises a rectangular box-shaped support plate 6 and a metallic metal screen 7 stretched on the support plate 6. A filtration chamber 8 is formed inside 4.
[0007]
The filter plate 4 will be described in further detail. As shown in FIG. 4, the support plate 6 has a large number of through holes 6a. The through holes 6a of the support plate 6 have a wedge shape in cross section and form slits in plan view. is doing. The metal screen 7 stretched on the support plate 6 has a coarse screen 7a laid on the support plate 6, an intermediate screen 7b interposed in an intermediate layer above it, and a fine screen 7c stretched on the surface layer. The eyes of the metal screens 7a, 7b, and 7c that are overlaid are made finer as the upper surface layer. By laminating filter media, the screen becomes finer, and small particles can be captured to increase the recovery rate. And the strength of the filter medium is increased. The eyes of these screens can change the aperture of the screen according to the degree of difficulty of filterability of the stock solution or the particle size of the solid matter. As for the aperture of the screen, the coarse screen 7a is 500 μm to 1. It is conceivable that the intermediate screen 7b of the intermediate layer on the upper side thereof is 100 μm to 1.0 mm and the fine screen 7c of the surface layer is in the range of 20 μm to 0.5 mm, and a metal screen 7a having an arbitrary diameter depending on the target stock solution. , 7b, 7c may be combined. A plurality of metal screens 7 supported by the support plate are superposed to withstand high pressure and to cope with high dehydration work. The filter plate 4 may be reinforced by laying a punching metal 13 on the inner peripheral surface of the support plate 6.
[0008]
As shown in FIGS. 2 and 5, a pressure tank 9 having a large number of small holes 9 a... Is provided in the surface of the filtration chamber 8 of the filter plate 4. Nine small holes 9a are made to approach and face each other. A compressed air pipe 10 is connected to the pressure tank 9, and the compressed air pipe 10 is connected to an air compressor 11 via an automatic valve V4. When the metal screen 7 is clogged, if the compressed air is jetted, the compressed air is blown directly into the screen from the back surface of the metal screen 7, and the clogging material is removed from the metal screen 7 having a good peeling system. Can do. The opening of the filtrate discharge pipe 5 is provided at the side end of the filtrate chamber 8 in which the pressure tank 9 is provided, and the end of the discharge pipe 5 is opened to the filtrate storage tank 12.
[0009]
The operation procedure of the concentration apparatus according to the present invention will be described. (1) Concentration step: First, the automatic valve V2 of the concentrated sludge discharge pipe 3 is closed, the automatic valve V3 of the separation liquid discharge pipe 5 is closed, and the compressed air pipe When the automatic valve V4 of 10 is closed and the automatic valve V1 provided in the sludge supply pipe is opened to supply sludge to the concentration tank 1 and the filter plate 4 is immersed in the concentration tank 1, the sludge water level of the concentration tank 1 is reduced. Due to the head pressure, the filtrate passes through the metal screen 7 of the filter plate 4 and flows into the filtration chamber 8, and the solid content is blocked by the metal screen 7 and precipitates at the bottom of the tank. The separated liquid flowing into the filtration chamber 8 is discharged from the discharge pipe 5 to the filtrate storage tank 12 due to the difference in water level. Then, after a predetermined time, the automatic valve V1 of the sludge supply pipe is closed, and the inflow of sludge into the concentration tank 1 is stopped. (2) Concentrated sludge discharge process: When the separation liquid is continuously discharged from the filtration chamber 8, the sludge is sequentially concentrated, and eventually the cake adheres to the metal screen 7 and the filtration performance decreases. The automatic valve V2 of the concentrated sludge take-out pipe 3 is opened, and the concentrated sludge is discharged from the take-out pipe 3 of the concentration tank 1. (3) Filter medium backwashing process: After discharging sludge in the concentration tank 1, the automatic valve V4 of the compressed air pipe 10 is opened, and the air compressor 11 is driven to press-fit the compressed air into the pressure tank 9. Compressed air is jetted from the back surface of the metal screen 7 of the filter plate 4 facing from a plurality of small holes 9a, and the metal screen 7 is regenerated by backwashing the metal filtration surface with good filterability with compressed air. be able to. The cleaning water may be supplied from the separation liquid discharge pipe 5 to the filtration chamber 8 for cleaning the dirty filtration surface of the metal screen 7 and discharging the separated sludge from the concentration tank 1. . And again, sludge can be supplied to a concentration tank and sludge concentration can be started.
[0010]
【The invention's effect】
As described above, the filter plate of the concentrator of the present invention has a plurality of metallic metal screens superimposed on a support plate having a large number of through holes, and a finer screen is superimposed on the upper surface layer. The screen becomes finer and fine filtration is possible, and the strength of the filter medium is increased. And in the case of using a filter cloth as a conventional filter medium, even if the compressed air is supplied to the clogged filter cloth and backwashed, the compressed air will pass through a part of the filter medium surface, resulting in clogging. However, in the filter plate of the present invention, a pressure tank having many small holes is provided on the back surface of the metal screen, so that compressed air is blown directly into the metal screen. The cake can be peeled off from a metal screen with good peelability, which facilitates reverse cleaning.
[Brief description of the drawings]
FIG. 1 is a perspective view of a concentrating device according to the present invention.
FIG. 2 is a conceptual vertical side view of a filter plate having a pressure tank according to the present invention.
FIG. 3 is a perspective view showing another embodiment of the concentrator.
FIG. 4 is a conceptual vertical side view of the filter medium similarly disposed on the filter plate.
FIG. 5 is a longitudinal side view of the concentrator.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Concentration tank 2 Supply pipe 3 Extraction pipe 4 Filtration plate 5 Discharge pipe 6 Support plate 6a Through hole 7 Metal screen 7a Rough screen 7b Medium screen 7c Fine screen 8 Filtration chamber 9 Pressure tank 9a Small hole 10 Compressed air pipe

Claims (5)

濃縮槽(1)にろ過板(4)を浸漬させ、濃縮槽(1)に汚泥の供給管(2)と濃縮液の取出管(3)を連結し、ろ過板(4)に分離液の排出管(5)を接続した装置において、上記ろ過板(4)のろ過室(8)にその表面に多数の小孔(9a…)を有する圧力タンク(9)を内設し、ろ過室(8)のろ材面と圧力タンク(9)の表面との間に隙間を設けると共に、圧力タンク(9)に圧縮空気管(10)を接続したことを特徴とする濃縮装置。  The filter plate (4) is immersed in the concentration tank (1), the sludge supply pipe (2) and the concentrate discharge pipe (3) are connected to the concentration tank (1), and the separation liquid is connected to the filter plate (4). In the apparatus to which the discharge pipe (5) is connected, a pressure tank (9) having a large number of small holes (9a ...) on its surface is installed in the filtration chamber (8) of the filtration plate (4), and the filtration chamber ( A concentrating device characterized in that a gap is provided between the filter medium surface of 8) and the surface of the pressure tank (9), and a compressed air pipe (10) is connected to the pressure tank (9). 上記ろ過板(4)が多数の通孔(6a…)を有する支持板(6)に金属性のメタルスクリーン(7a、7b、7c)を張設してあることを特徴とする請求項1記載の濃縮装置。  2. The metal plate (7a, 7b, 7c) is stretched around a support plate (6) having a large number of through holes (6a) in the filter plate (4). Concentration device. 上記支持板(6)に張設したろ材が複数枚のメタルスクリーン(7a、7b、7c)からなり、重設したメタルスクリーン(7a、7b、7c)の目を上面層ほど細かくしたことを特徴とする請求項2記載の濃縮装置。  The filter medium stretched on the support plate (6) is composed of a plurality of metal screens (7a, 7b, 7c), and the eyes of the superimposed metal screens (7a, 7b, 7c) are made finer as the upper surface layer. The concentrator according to claim 2. 上記重設したメタルスクリーン(7a、7b、7c)が、支持板に荒目スクリーン(7a)を敷設し、その上部の中間層に中目スクリーン(7b)を介装して、表面層に細目スクリーン(7c)を張設したことを特徴とする請求項2または3記載の濃縮装置。  The superposed metal screens (7a, 7b, 7c) are provided with a coarse screen (7a) on the support plate, and a middle screen (7b) is interposed in the upper intermediate layer, with fine meshes on the surface layer. The concentrating device according to claim 2 or 3, wherein a screen (7c) is stretched. 上記支持板(6)の通孔(6a)は、楔形の断面積を有するスリットであることを特徴とする請求項2乃至4のいずれか1項に記載の濃縮装置。The concentrating device according to any one of claims 2 to 4, wherein the through hole (6a) of the support plate (6) is a slit having a wedge-shaped cross-sectional area.
JP33223899A 1999-11-24 1999-11-24 Concentrator Expired - Fee Related JP3835511B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33223899A JP3835511B2 (en) 1999-11-24 1999-11-24 Concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33223899A JP3835511B2 (en) 1999-11-24 1999-11-24 Concentrator

Publications (2)

Publication Number Publication Date
JP2001145899A JP2001145899A (en) 2001-05-29
JP3835511B2 true JP3835511B2 (en) 2006-10-18

Family

ID=18252731

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33223899A Expired - Fee Related JP3835511B2 (en) 1999-11-24 1999-11-24 Concentrator

Country Status (1)

Country Link
JP (1) JP3835511B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101391681B1 (en) 2007-09-28 2014-05-07 메타워터 가부시키가이샤 Filtration concentration device
US8540079B2 (en) 2007-10-21 2013-09-24 Metawater Co., Ltd. Sludge filtration apparatus and filter assembly thereof
JP5102913B2 (en) * 2008-12-02 2012-12-19 メタウォーター株式会社 Apparatus and method for concentrating backwash wastewater from membrane filtration

Also Published As

Publication number Publication date
JP2001145899A (en) 2001-05-29

Similar Documents

Publication Publication Date Title
JPS5826964B2 (en) "Filtration" method and device
JPH09138298A (en) Filtration device using hollow fiber membrane and backwashing method thereof
CA1242979A (en) Pressure filter (hpc clarifil)
JPS5811008A (en) Filter device
JP3835511B2 (en) Concentrator
RU1820846C (en) Process of dewatering in filter press
JPH05285354A (en) Washing and regenerating method for filter membrane
JP2709026B2 (en) Membrane separation device and cleaning method thereof
JPH03224609A (en) Method and device for filtration of liquid
CN2677003Y (en) Multpipe filter
JP3738649B2 (en) Filter press filter plate using metal filter media
US1743525A (en) Filtering medium
JP3419037B2 (en) Filtration device and filtration method
JP2004525633A (en) Beer filter
JP3191559B2 (en) Solid-liquid separation device
JP3058635B1 (en) Filtration treatment method and filtration treatment device using fibrous filter medium
JPH07275611A (en) Filtering device for waste liquid and method for washing filter medium
JPH0884913A (en) Complex filter
JP3031402B2 (en) External pressure type membrane filtration device
KR100338525B1 (en) Underdrain mat system for rapid filtration
JP2629667B2 (en) Filtration device using flat membrane filter media
JPH0227848Y2 (en)
JP2000062833A (en) Solid-liquid separation device
JP2001137628A (en) Filter media for filtration machine
JPH01111405A (en) filtration device

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040624

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060518

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060615

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060705

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060718

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees