JP2001145899A - Concentration apparatus - Google Patents

Concentration apparatus

Info

Publication number
JP2001145899A
JP2001145899A JP33223899A JP33223899A JP2001145899A JP 2001145899 A JP2001145899 A JP 2001145899A JP 33223899 A JP33223899 A JP 33223899A JP 33223899 A JP33223899 A JP 33223899A JP 2001145899 A JP2001145899 A JP 2001145899A
Authority
JP
Japan
Prior art keywords
screen
filter
tank
sludge
pipe
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
JP33223899A
Other languages
Japanese (ja)
Other versions
JP3835511B2 (en
Inventor
Eiichi Ishigaki
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

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

Abstract

PROBLEM TO BE SOLVED: To provide a concentration apparatus wherein a filter plate is immersed in a concentration tank to discharge a separated liquid from hardly filterable sludge such as sewage sludge or the like and the peelability of a cake is enhanced. SOLUTION: In a concentration apparatus wherein a filter plate 4 is immersed in a concentration tank 1 and a sludge supply pipe 2 and a concentrated liquid tanking-out pipe 3 and connected to the concentration tank 1 and a separated liquid discharge pipe 5 is connected to the filter plate 4, a pressure tank 9 having a large number of small holes 9a... formed on the surface thereof is disposed in the filter chamber 8 of the filter plate 4 and a gap is formed between the surface of the filter medium of the filter chamber 8 and the surface of the pressure tank 9 and a compressed air pipe 10 is connected to the pressure tank 9. Since the pressure tank having a large number of the small holes is disposed in opposed relation to the rear surface of the filter medium, compressed air is directly blown in the meshes of a screen to peel a cake from the screen. As the filter medium, metal screens 7a, 7b, 7c good in peelability are arranged in a superposed state and the filtering meshes thereof are made fine.

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】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。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for concentrating hard-to-filter sludge such as sewage sludge, and more particularly, to an apparatus for discharging a separated liquid by immersing a filtration chamber in which a filter medium is stretched in a concentration tank. About.

【0002】[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、特公平2−27853号公報で出願人が提案してい
る。
2. Description of the Related Art Conventionally, a filter in which a filtration chamber is formed by combining two filtration nets is suspended in a sludge chamber of a filtration tank, and water in the sludge is taken out into the filtration chamber to concentrate the sludge in the filtration tank. Concentrators are known, for example, as described in JP-B-63-13721. In addition, the applicant proposes a device for removing the filter cloth stretched on the filtration surface of the filtration chamber to the outside of the concentration tank and washing the filter cloth in Japanese Patent Publication No. 2-27853.

【0003】[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。
However, in the above-mentioned conventional filter medium using a filter cloth, cake adhering to the filter cloth is difficult to peel off, and the clogged filter cloth is removed from the inside of the filtration chamber by compressed air. , The compressed air leaked through some of the filter media surfaces, and sufficient washing could not be performed, making it difficult to remove clogs. For this reason, in the apparatus in which the filter cloth stretched in the filtration chamber is run to regenerate the filter cloth outside the concentration tank, a device for moving the filter cloth in water and a large power are required. SUMMARY OF THE INVENTION The present invention provides a concentrating device using a filter medium having good cake releasability without running the filter medium in water.

【0004】[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。
The gist of the present invention is that a filter plate is immersed in a concentration tank, a sludge supply pipe and a concentrate discharge pipe are connected to the concentration tank, and a separation liquid discharge pipe is connected to the filter plate. In the connected device, a pressure tank having a large number of small holes is provided inside the filtration chamber of the filtration plate, and a gap is provided between the filter medium surface of the filtration chamber and the surface of the pressure tank. A compressed air pipe is connected, and compressed air is blown from a small hole on the peripheral surface of the pressure tank to the filter medium surface of the filtration chamber. The filter plate has a support plate having a large number of through holes and a metal screen with good releasability stretched over the support plate. A preferred filter medium is one in which a plurality of metal screens are stretched on a support plate, and the metal screens are superposed to reduce the filtration mesh. Specifically, the mesh of the superposed metal screen is made finer to the upper layer to facilitate the extraction of the filtrate.A rough screen is laid on the support plate, and a middle screen is interposed on the intermediate layer above it. And a fine screen stretched over the surface layer. In addition, the through hole of the support plate is a slit having a wedge-shaped cross-sectional area, and the mesh of the screen is sequentially made finer from the inside of the filtration chamber to facilitate backwashing.

【0005】[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。
BEST MODE FOR CARRYING OUT THE INVENTION The apparatus according to the present invention is constructed as described above. Sludge is supplied from a sludge supply pipe to a thickening tank, a filter plate is immersed in the thickening tank, and a sludge is discharged from a discharge pipe of a filtering chamber. When the separated liquid is discharged, the sludge is concentrated, 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, pressurized air is injected into the pressure tank, and compressed air is injected from the small hole of the pressure tank toward the back surface of the mesh screen of the opposite filtration chamber, and the filterability is improved. Good filtration surface can be regenerated by backwashing with compressed air. Again, sludge is supplied to the concentration tank to start sludge concentration.

【0006】[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。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A filter medium of a filter according to the present invention will be described in detail with reference to the drawings. First, in FIG. 1, reference numeral 1 denotes a thickening tank, and a sludge supply pipe 2 is provided above a side wall of the thickening tank 1.
And a concentrated liquid take-out pipe 3 connected to the bottom of the condensing tank 1. An automatic valve V 1 is connected to the sludge supply pipe 2 and the concentrated liquid take-out pipe 3.
V2 is provided. A plurality of filter plates 4 are arranged side by side in the concentration tank 1, and the sieve-like discharge pipe 5
Are connected to each other, and the discharge pipe 5
Is provided with an automatic valve V3. 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 is a rectangular box-shaped support plate 6.
And a metal screen 7 stretched over a support plate 6, and a filtration chamber 8 is formed inside the filtration plate 4.

【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7
a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〜1.0
mm、表面層の細目スクリーン7cは20μm〜0.5
mm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。
The filter plate 4 will be described in more detail.
As shown in the figure, the support plate 6 has a large number of through holes 6a, and the through holes 6a of the support plate 6 have a wedge-shaped cross section and form a slit in plan view. The metal screen 7 stretched on the support plate 6 is a rough screen 7 laid on the support plate 6.
a, a middle screen 7b is interposed in the upper intermediate layer, a fine screen 7c is stretched in the surface layer, and the eyes of the superposed metal screens 7a, 7b, 7c are made finer toward the upper surface layer. In addition, by laminating the filter media, the mesh of the screen becomes finer, small particles can be captured, the recovery rate can be increased, and the filter media strength is also increased. The eyes of these screens can change the aperture of the screen by the difficulty of filtration of the stock solution or by the particle size of the solid material.
The coarse screen 7a has a thickness of 500 μm to 1.5 mm, and the intermediate screen 7b on the upper portion has a thickness of 100 μm to 1.0 mm.
mm, the fine screen 7c of the surface layer is 20 μm to 0.5 μm.
It is possible to combine metal screens 7a, 7b, 7c of any diameter according to the target stock solution. Then, the plurality of metal screens 7 supported by the support plate are superimposed to withstand a high pressure and can cope with a high dehydration operation. In addition, a perforated metal 13 may be laid on the inner peripheral surface of the support plate 6 to reinforce the filter plate 4.

【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1
0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。
As shown in FIGS. 2 and 5, a pressure tank 9 having a large number of small holes 9a is internally provided in the filtration chamber 8 of the filtration plate 4. And the small hole 9a of the pressure tank 9 are brought close to each other and opposed to each other. A compressed air pipe 10 is connected to the pressure tank 9.
0 is connected to the air compressor 11 via an automatic valve V4. Then, when the metal screen 7 is clogged, if compressed air is injected, the compressed air is directly blown into the eyes of the screen from the back surface of the metal screen 7 to remove the clogged material from the metal screen 7 with good peeling ability. Can be. The starting end opening of the filtrate discharge pipe 5 is provided at a side end of a filtrate chamber 8 in which a pressure tank 9 is provided.
Is open to the filtrate storage tank 12.

【0009】この発明に係る濃縮装置の作動要領を説明
すると、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。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。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V
4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。
The operation of the concentrating apparatus according to the present invention will be described. Concentrating step: First, the automatic valve V2 of the concentrated sludge discharge pipe 3 is closed, the automatic valve V3 of the separated liquid discharge pipe 5 is closed, and the compressed air pipe is closed. When the automatic valve V4 of 10 is closed and the automatic valve V1 provided on 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 settles 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 a difference in water level. Then, after a predetermined time, the automatic valve V1 of the sludge supply pipe is closed, and the inflow of the sludge into the concentration tank 1 is stopped. Condensed sludge discharge step: When the separated liquid is continuously discharged from the filtration chamber 8, the sludge is sequentially concentrated, and the cake adheres to the metal screen 7 and the filtration performance is reduced. The automatic valve V2 of the concentrated sludge discharge pipe 3 is opened, and the concentrated sludge is discharged from the discharge pipe 3 of the concentration tank 1. Backwashing process of filter media: After discharging sludge from the thickening tank 1, the automatic valve V of the compressed air pipe 10
4, the compressed air is pressed into the pressure tank 9 by driving the air compressor 11, and a number of small holes 9a in the pressure tank 9 are formed.
Then, compressed air is injected from the back surface of the metal screen 7 of the filter plate 4 facing the filter screen, and the metal screen 7 having good filterability can be backwashed with the compressed air to regenerate the metal screen 7. In order to wash the dirty filtration surface of the metal screen 7 and discharge the separated sludge from the concentration tank 1, the washing water may be supplied to the filtration chamber 8 from the separation liquid discharge pipe 5. . Then, sludge can be supplied to the concentration tank again to start sludge concentration.

【0010】[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。
As described above, the filter plate of the concentrator according to the present invention has a plurality of metallic metal screens stacked on a support plate having a large number of through-holes, and a finer screen is formed on the upper surface layer. Since the screens are superposed, the screen becomes finer and fine filtration becomes possible, and the filter medium strength is increased. And, in the case of using a filter cloth as a conventional filter medium, even if compressed air is supplied to the clogged filter cloth and backwashed, the compressed air passes through a part of the filter medium surface and the clogged material is clogged. Although it was difficult to remove the filter, the filter plate of the present invention provided a pressure tank having a number of small holes on the back of the metal screen, so that compressed air was directly blown into the eyes of the metal screen. The cake can be peeled off from the metal screen having good peelability, and the backwashing and purification can be easily performed.

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

【図1】この発明に係る濃縮装置の斜視図である。FIG. 1 is a perspective view of a concentration device according to the present invention.

【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。
FIG. 2 is a conceptual vertical sectional side view of a filter plate provided with a pressure tank according to the present invention.

【図3】同じく濃縮装置の他の実施例を示す斜視図であ
る。
FIG. 3 is a perspective view showing another embodiment of the concentrator.

【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。
FIG. 4 is a conceptual vertical sectional side view of a filter medium provided on the filter plate.

【図5】同じく濃縮装置の縦断側面図である。FIG. 5 is a vertical sectional side view of the concentrating device.

【符号の説明】[Explanation of symbols]

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 DESCRIPTION OF SYMBOLS 1 Concentration tank 2 Supply pipe 3 Extraction pipe 4 Filter plate 5 Discharge pipe 6 Support plate 6a Through hole 7 Metal screen 7a Coarse screen 7b Medium screen 7c Fine screen 8 Filtration chamber 9 Pressure tank 9a Small hole 10 Compressed air pipe

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 29/38 520A 530A 540 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B01D 29/38 520A 530A 540

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 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。
1. A filter plate (4) is immersed in a concentration tank (1), and a sludge supply pipe (2) and a concentrated liquid extraction pipe (3) are connected to the concentration tank (1). ) Is connected to a separation liquid discharge pipe (5), and a pressure tank (9) having a large number of small holes (9a...) On its surface is installed in a filtration chamber (8) of the filtration plate (4). A concentrating device characterized by providing a gap between the surface of the filter medium (9) and the filter medium surface of the filtration chamber (8), and connecting a compressed air pipe (10) to the pressure tank (9).
【請求項2】 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 filter plate (4) has a large number of through holes (6a).
2. The concentrator according to claim 1, wherein a metal screen (7a, 7b, 7c) made of metal is stretched on the support plate (6) having (...).
【請求項3】 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。
3. The filter medium stretched on the support plate (6) comprises a plurality of metal screens (7a, 7b, 7c).
3. The concentrator according to claim 2, wherein the superposed metal screens (7a, 7b, 7c) have finer eyes toward the upper surface layer.
【請求項4】 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。
4. The superposed metal screen (7a,
7b, 7c) lay a coarse screen (7a) on a support plate, interpose a medium screen (7b) on an intermediate layer above the support screen, and stretch a fine screen (7c) on a surface layer. The concentrator according to claim 2 or 3, wherein:
【請求項5】 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1乃至3記載の濃縮装置。
5. The concentrator according to claim 1, 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)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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JP3835511B2 JP3835511B2 (en) 2006-10-18

Family

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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010131474A (en) * 2008-12-02 2010-06-17 Metawater Co Ltd Apparatus and method for concentrating backwash effluent in membrane filtration
US8540079B2 (en) 2007-10-21 2013-09-24 Metawater Co., Ltd. Sludge filtration apparatus and filter assembly thereof
KR101391681B1 (en) 2007-09-28 2014-05-07 메타워터 가부시키가이샤 Filtration concentration device

Cited By (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
JP2010131474A (en) * 2008-12-02 2010-06-17 Metawater Co Ltd Apparatus and method for concentrating backwash effluent in membrane filtration

Also Published As

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