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JP2003062600A - Method for thickening and dehydrating sludge and apparatus for thickening sludge used therefor - Google Patents

Method for thickening and dehydrating sludge and apparatus for thickening sludge used therefor

Info

Publication number
JP2003062600A
JP2003062600A JP2001259722A JP2001259722A JP2003062600A JP 2003062600 A JP2003062600 A JP 2003062600A JP 2001259722 A JP2001259722 A JP 2001259722A JP 2001259722 A JP2001259722 A JP 2001259722A JP 2003062600 A JP2003062600 A JP 2003062600A
Authority
JP
Japan
Prior art keywords
sludge
screen
filtrate
thickening
scraper
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.)
Withdrawn
Application number
JP2001259722A
Other languages
Japanese (ja)
Inventor
Hiroyuki Yamada
浩之 山田
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP2001259722A priority Critical patent/JP2003062600A/en
Publication of JP2003062600A publication Critical patent/JP2003062600A/en
Withdrawn legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To provide a method for thickening and dehydrating sludge capable of dehydrating hardly-dehydratable sludge without adding much coagulant thereto, and an apparatus for thickening the sludge used therefor. SOLUTION: Coagulated sludge is thickened through a thickening apparatus 3 by separating from water without breaking floe and is dehydrated by force feeding to a pressure dehydrator. The thickening apparatus 3 has a structure wherein a screen 11 is provided in a pressure vessel 10, inside of the screen being a sludge channel 12 and outside being a filtrate chamber 13, and the sludge channel 12 is provided therein with a hollow scraper 18, slowly rotating along the inner surface of the screen 11, the hollow scraper 18 having through holes, through which the filtrate in the filtrate chamber 13 is sucked in via the screen 11.

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、汚泥の濃縮脱水方
法及びそれに用いられる汚泥濃縮装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge concentrating and dewatering method and a sludge concentrating apparatus used therefor.

【0002】[0002]

【従来の技術】下水汚泥等の脱水には従来から各種の脱
水装置が使用されているが、その多くは構造が複雑で装
置が大型であるうえ、臭気洩れの問題がある。そこで最
近このような問題を解決した脱水装置として、図4に示
されるような圧入式脱水機が提案されている。
2. Description of the Related Art Conventionally, various dehydrating devices have been used for dehydrating sewage sludge and the like, but most of them have a complicated structure and are large in size, and also have a problem of odor leakage. Therefore, as a dehydrating device that solves such a problem, a press-fitting type dehydrator as shown in FIG. 4 has recently been proposed.

【0003】この圧入式脱水機は、円形のケーシング5
1の内部に低速回転する円盤状のローター52を設けた
ものであり、ケーシング51とローター52との間隙は
両側がスクリーン53で挟まれたろ室54となってい
る。凝集装置で凝集させた汚泥はこのろ室54に圧入さ
れ、ローター52及びスクリーン53の回転につれてケ
ーシング51内を移動する間に水分がスクリーン53を
通して外側のろ液流路55に排出され、徐々に脱水が進
行する。そして脱水汚泥はろ室54の終端に設けられた
ゲート弁56を押し開きながら外部に排出される。この
ような圧入式脱水機は、装置構造が簡単でコンパクトで
あり、ほとんど騒音がなく、しかも密閉構造であるため
に臭気が外部に洩れにくいという利点がある。
This press-fitting type dehydrator has a circular casing 5
A disk-shaped rotor 52 that rotates at a low speed is provided inside 1, and the gap between the casing 51 and the rotor 52 is a filter chamber 54 sandwiched by screens 53 on both sides. The sludge agglomerated by the aggregating device is press-fitted into the filter chamber 54, and while moving in the casing 51 as the rotor 52 and the screen 53 rotate, moisture is discharged through the screen 53 to the outer filtrate flow channel 55, and gradually. Dehydration progresses. Then, the dehydrated sludge is discharged to the outside while pushing and opening the gate valve 56 provided at the end of the filter chamber 54. Such a press-fitting type dehydrator has the advantages that the device structure is simple and compact, there is almost no noise, and the odor is unlikely to leak to the outside due to the closed structure.

【0004】しかし、上記の圧入式脱水機により消化汚
泥や余剰汚泥のような難脱水性汚泥を脱水しようとする
場合には、フロキュレーター(凝集装置)において予め
大量の凝集剤を添加しなければならず、ランニングコス
トが高くなるという問題があった。またこのような圧入
式脱水機は構造的に汚泥の滞留時間が短いため、難脱水
性汚泥を脱水する場合に処理量を増やすと汚泥中の自由
水が抜けきらず、圧搾工程に入る前にそのまま排出され
てしまうこととなって脱水不能に陥る可能性があった。
従って、このような圧入式脱水機は、消化汚泥や余剰汚
泥のような難脱水性の汚泥を脱水するには用いにくいも
のであった。
However, when attempting to dehydrate difficult-to-dewater sludge such as digested sludge and excess sludge by the press-fitting type dehydrator, a large amount of coagulant must be added in advance in a flocculator (coagulating device). However, there is a problem that running cost becomes high. In addition, such a press-fitting type dewatering machine structurally has a short residence time of sludge, so if the treatment amount is increased when dewatering hard-to-dewater sludge, the free water in the sludge will not be exhausted, and it will remain as it is before entering the pressing process. There is a possibility that it will be discharged and it will become impossible to dehydrate.
Therefore, such a press-fitting type dehydrator is difficult to be used for dehydrating difficult-to-dewater sludge such as digested sludge and excess sludge.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、消化汚泥や余剰汚泥のような難脱水
性の汚泥をも大量の凝集剤を添加することなく脱水する
ことができる汚泥の濃縮脱水方法を提供することを第1
の目的とするものである。また本発明の第2の目的は、
凝集フロックを破壊することなく、また目詰まりを生じ
ることなく難脱水性の汚泥を濃縮することができる汚泥
濃縮装置を提供することである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and is capable of dewatering hard-to-dewater sludge such as digested sludge and excess sludge without adding a large amount of coagulant. The first is to provide a method of concentrating and dehydrating sludge that can be performed
Is the purpose of. The second object of the present invention is to
It is an object of the present invention to provide a sludge concentrating device capable of concentrating non-dewatering sludge without destroying agglomerated flocs and without causing clogging.

【0006】[0006]

【課題を解決するための手段】上記した第1の目的を達
成するためになされた請求項1の発明は、凝集汚泥を周
囲がスクリーンで囲まれた汚泥流路に通してフロックを
壊すことなく水分を分離して濃縮したうえ、圧入式脱水
機に打ち込んで脱水することを特徴とするものである。
ここで圧入式脱水機として、ケーシングの内部に低速回
転する円盤状のローターを設け、ケーシングとローター
との間隙を両側がスクリーンで挟まれたろ室としたもの
を用いることが好ましい。
In order to achieve the above-mentioned first object, the invention of claim 1 does not break flocs by passing the coagulated sludge through a sludge flow path surrounded by a screen. It is characterized in that water is separated and concentrated, and then it is driven into a press-fitting type dehydrator for dehydration.
Here, as the press-fitting type dehydrator, it is preferable to use a disc-shaped rotor that rotates at a low speed inside the casing, and a gap between the casing and the rotor is a filter chamber whose both sides are sandwiched by screens.

【0007】また上記した第2の目的を達成するために
なされた請求項3の発明は、圧力容器の内部に筒状のス
クリーンを設けてその内側を汚泥流路、外側をろ液室と
するとともに、汚泥流路内にはスクリーンの内周面に沿
って緩やかに回転する中空のスクレーパーを設け、この
スクレーパーにろ液室内のろ液をスクリーンを介して吸
引する透孔を設けたことを特徴とするものである。な
お、スクレーパーの回転軸にろ液排出ポンプを接続した
構造とすることが好ましく、またろ液排出ポンプが、汚
泥流路への汚泥送入口とろ液室との差圧を一定に保つも
のであることが好ましい。
In order to achieve the above-mentioned second object, the invention of claim 3 provides a cylindrical screen inside the pressure vessel, the inside of which is a sludge flow path, and the outside is a filtrate chamber. In addition, a hollow scraper that gently rotates along the inner peripheral surface of the screen is provided in the sludge channel, and this scraper is provided with a through hole for sucking the filtrate in the filtrate chamber through the screen. It is what In addition, it is preferable to have a structure in which a filtrate discharge pump is connected to the rotary shaft of the scraper, and the filtrate discharge pump keeps a constant differential pressure between the sludge feed port to the sludge flow path and the filtrate chamber. It is preferable.

【0008】本発明の汚泥の濃縮脱水方法によれば、汚
泥の濃縮と脱水とを分離して行うことにより、消化汚泥
や余剰汚泥のような難脱水性の汚泥をも大量の凝集剤を
添加することなく脱水することができる。また本発明の
汚泥濃縮装置によれば、凝集汚泥を筒状のスクリーンの
内側に形成された汚泥流路に流すようにしたので、凝集
フロックを破壊することなく難脱水性の汚泥を濃縮する
ことができる。しかもスクレーパーに設けた透孔からろ
液室内のろ液をスクリーンを介して吸引するようにした
ので、装置を停止して洗浄しなくても、スクリーンが目
詰まりすることがない。
According to the method for concentrating and dehydrating sludge of the present invention, a large amount of coagulant is added to sludge that is difficult to dehydrate such as digested sludge and surplus sludge by separately performing concentration and dehydration of sludge. You can dehydrate without doing. Further, according to the sludge concentrating device of the present invention, the coagulated sludge is caused to flow in the sludge flow path formed inside the cylindrical screen, so that the hardly dehydratable sludge can be concentrated without destroying the coagulated flocs. You can Moreover, since the filtrate in the filtrate chamber is sucked through the screen from the through hole provided in the scraper, the screen will not be clogged even if the apparatus is not stopped and washed.

【0009】[0009]

【発明の実施の形態】以下に本発明の好ましい実施形態
を示す。図1は本発明の汚泥の濃縮脱水方法を説明する
全体図であり、1はフロキュレーター(凝集装置)、2
は本発明の汚泥濃縮装置、3は圧入式脱水機である。フ
ロキュレーター1は周知のもので、汚泥供給ポンプ4に
より供給される汚泥(一般に固形分が2〜4%程度の汚
泥)に凝集剤ポンプ5によって高分子凝集剤を添加し、
攪拌機を備えた槽内で攪拌して凝集フロックを形成する
装置である。凝集汚泥は汚泥濃縮装置2に送られ、以下
に述べるように濃縮されたうえで圧入式脱水機3によっ
て脱水される。
BEST MODE FOR CARRYING OUT THE INVENTION Preferred embodiments of the present invention are shown below. FIG. 1 is an overall view for explaining the method for concentrating and dehydrating sludge of the present invention, in which 1 is a flocculator (coagulation device), 2
Is a sludge concentrating device of the present invention, and 3 is a press-fitting type dehydrator. The flocculator 1 is well-known, and a polymer flocculant is added to the sludge (generally, sludge having a solid content of about 2 to 4%) supplied by the sludge supply pump 4 by the coagulant pump 5.
It is an apparatus that forms agglomerated flocs by stirring in a tank equipped with a stirrer. The coagulated sludge is sent to the sludge concentrating device 2, concentrated as described below, and then dehydrated by the press-fitting type dehydrator 3.

【0010】汚泥濃縮装置2は図2、図3に示されると
おり、円筒状の圧力容器10の内部に円筒状のスクリー
ン11を設けてその内側を汚泥流路12、外側をろ液室
13としたものである。凝集汚泥は圧力容器10の一端
の汚泥送入口14から汚泥流路12に送り込まれ、汚泥
流路12の内部を進行する間に自由水が周囲のスクリー
ン11を介してろ液室13側に抜けることによって固形
分が7〜8%程度となるまで濃縮される。濃縮汚泥は他
端の排出口15から連続的に取り出される。
As shown in FIGS. 2 and 3, the sludge concentrator 2 is provided with a cylindrical screen 11 inside a cylindrical pressure vessel 10, the inside of which is a sludge channel 12, and the outside is a filtrate chamber 13. It was done. The coagulated sludge is fed into the sludge flow passage 12 from the sludge inlet 14 at one end of the pressure vessel 10, and while traveling inside the sludge flow passage 12, free water escapes to the filtrate chamber 13 side through the surrounding screen 11. Is concentrated until the solid content becomes about 7 to 8%. The concentrated sludge is continuously taken out from the discharge port 15 at the other end.

【0011】この汚泥流路12の内部には、中空軸16
を中心としてモーター17によって緩やかに回転される
スクレーパー18が設けられている。このスクレーパー
18はスクリーン11の内周面に沿って緩やかに回転す
る中空のもので、この実施形態では中空軸16に平行な
3本の棒状体を、端部の中空アーム19によって一体化
した構造となっている。スクレーパー18の本数は適宜
増減することができる。なお凝集フロックの破壊を防止
するために、スクレーパー18の回転速度は1rpm以
下の低速としておくことが好ましい。
A hollow shaft 16 is provided inside the sludge passage 12.
A scraper 18 is provided which is gently rotated by a motor 17 around the center. This scraper 18 is a hollow one that gently rotates along the inner peripheral surface of the screen 11. In this embodiment, three rod-shaped bodies parallel to the hollow shaft 16 are integrated by a hollow arm 19 at the end. Has become. The number of scrapers 18 can be appropriately increased or decreased. In order to prevent the flocculation of flocs, it is preferable that the scraper 18 be rotated at a low speed of 1 rpm or less.

【0012】スクレーパー18のスクリーン11と接触
する面には、多数の透孔20が形成されている。スクリ
ーン11の開口径が0.5〜1mmであるのに対して、
スクレーパー18の透孔20の径は5mm程度と大きく
しておく。各透孔20は、スクレーパー18の中空アー
ム19を介して中空軸16の内部に連通している。また
中空軸16の端部にはろ液排出ポンプ21が接続されて
いるため、スクレーパー18の透孔20はスクリーン1
1を介してその外側のろ液室13内のろ液を吸引するこ
とができる。このため、スクリーン11は回転するスク
レーパー18と接触する度にろ液によって洗浄されるこ
ととなり、目詰まりが生ずるおそれがない。ろ液排出ポ
ンプ21としては、モーノポンプ(商品名)として知ら
れる一軸偏心回転ポンプを用いることができる。
A large number of through holes 20 are formed on the surface of the scraper 18 that contacts the screen 11. While the opening diameter of the screen 11 is 0.5 to 1 mm,
The diameter of the through hole 20 of the scraper 18 is set to be as large as about 5 mm. Each through hole 20 communicates with the inside of the hollow shaft 16 via the hollow arm 19 of the scraper 18. Further, since the filtrate discharge pump 21 is connected to the end of the hollow shaft 16, the through hole 20 of the scraper 18 is formed in the screen 1
The filtrate in the filtrate chamber 13 on the outer side can be sucked through 1 through 1. Therefore, the screen 11 is washed with the filtrate each time it comes into contact with the rotating scraper 18, and there is no risk of clogging. As the filtrate discharge pump 21, a uniaxial eccentric rotary pump known as a MONO pump (trade name) can be used.

【0013】なお、図2に示すように汚泥送入口14と
ろ液室13にはそれぞれ圧力センサー22,23が設け
られており、ろ液室13の圧力が汚泥送入口14の圧力
よりも常に一定値だけ低くなるように、ろ液排出ポンプ
21を制御する。これによりスクリーン11によるろ過
差圧が過大にならないように制御し、凝集フロックの破
壊を防止する。このようにして、凝集汚泥は汚泥濃縮装
置2において凝集フロックを破壊することなく濃縮され
る。
As shown in FIG. 2, the sludge inlet 14 and the filtrate chamber 13 are provided with pressure sensors 22 and 23, respectively, so that the pressure of the filtrate chamber 13 is always more constant than the pressure of the sludge inlet 14. The filtrate discharge pump 21 is controlled so as to lower the value. As a result, the filtration differential pressure by the screen 11 is controlled so as not to become excessive and the aggregation flocs are prevented from being broken. In this way, the coagulated sludge is concentrated in the sludge concentrating device 2 without destroying the coagulated flocs.

【0014】圧入式脱水機3は図4に示されるような構
造であり、既に説明したようにケーシング51の内部に
低速回転する円盤状のローター52とスクリーン53で
挟まれたろ室54を形成したものである。汚泥濃縮装置
2で水分が7〜8%となるまで濃縮された汚泥はこのろ
室54に圧入され、ケーシング51内を移動する間に脱
水され、ゲート弁56を押し開きながら外部に排出され
る。圧入式脱水機3に打ち込まれる前に自由水は汚泥濃
縮装置2において分離されているため、圧入式脱水機3
においては確実に脱水が行なわれ、難脱水性汚泥であっ
ても固形分が20〜25%となるまで脱水することがで
きる。得られた脱水汚泥は、乾燥、焼却、溶融などの後
工程に送られ処理される。
The press-fitting type dehydrator 3 has a structure as shown in FIG. 4, and has a filter chamber 54 sandwiched between a disk-shaped rotor 52 rotating at a low speed and a screen 53 inside the casing 51 as described above. It is a thing. The sludge concentrated in the sludge concentrating device 2 until the water content becomes 7 to 8% is pressed into the filter chamber 54, dehydrated while moving in the casing 51, and discharged to the outside while opening the gate valve 56. . Since the free water is separated in the sludge concentrating device 2 before being driven into the press-fitting type dehydrator 3, the press-fitting type dehydrator 3
In this case, dehydration is surely performed, and even sludge that is difficult to dehydrate can be dehydrated until the solid content becomes 20 to 25%. The dehydrated sludge thus obtained is sent to a subsequent process such as drying, incineration, melting and the like for treatment.

【0015】[0015]

【発明の効果】以上に説明したように、本発明の汚泥の
濃縮脱水方法によれば、汚泥濃縮装置と圧入式脱水機と
を組み合わせて自由水の分離工程と圧搾工程とをそれぞ
れの装置で行なわせることにより、難脱水性の汚泥をも
無理なく脱水することができる。このため従来のような
大量の凝集剤を必要とせず、ランニングコストを引き下
げることができる。
As described above, according to the method for concentrating and dewatering sludge of the present invention, the sludge concentrating device and the press-fitting type dehydrator are combined to perform the free water separating step and the squeezing step respectively. By carrying out the treatment, it is possible to dehydrate the sludge that is difficult to dehydrate without difficulty. Therefore, it is possible to reduce the running cost without requiring a large amount of a flocculant as in the conventional case.

【0016】また本発明の汚泥濃縮装置によれば、フロ
ックを破壊することなく難脱水性の汚泥を濃縮すること
ができる。しかも、スクレーパーに設けた透孔によりろ
室室内のろ液をスクリーンを介して吸引することによ
り、スクリーンの目詰まりを防止することができるか
ら、運転を停止して洗浄を行なう必要がなく、洗浄水も
不要となるなどの利点がある。
Further, according to the sludge concentrating device of the present invention, it is possible to concentrate the hardly dehydratable sludge without destroying the flocs. Moreover, since the filtrate in the filter chamber can be sucked through the screen through the through holes provided in the scraper, it is possible to prevent clogging of the screen, so there is no need to stop the operation and perform cleaning. There is an advantage that water is unnecessary.

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

【図1】本発明の汚泥の濃縮脱水方法を説明する全体図
である。
FIG. 1 is an overall diagram illustrating a method for concentrating and dehydrating sludge according to the present invention.

【図2】本発明の汚泥濃縮装置の軸線方向の断面図であ
る。
FIG. 2 is an axial sectional view of the sludge concentrating device of the present invention.

【図3】本発明の汚泥濃縮装置の軸線に垂直方向の断面
図である。
FIG. 3 is a cross-sectional view of the sludge concentrator of the present invention in a direction perpendicular to the axis.

【図4】圧入式脱水機の説明図であり、(A)は回転軸
方向の断面図、(B)は回転軸に垂直方向の断面図であ
る。
4A and 4B are explanatory views of a press-fitting type dehydrator, in which FIG. 4A is a cross-sectional view in the direction of the rotating shaft, and FIG. 4B is a cross-sectional view in the direction perpendicular to the rotating shaft.

【符号の説明】[Explanation of symbols]

1 フロキュレーター、2 汚泥濃縮装置、3 圧入式
脱水機、4 汚泥供給ポンプ、5 凝集剤ポンプ、10
圧力容器、11 スクリーン、12 汚泥流路、13
ろ液室、14 汚泥送入口、15 排出口、16 中
空軸、17 モーター、18 スクレーパー、19 中
空アーム、20 透孔、21 ろ液排出ポンプ、22
圧力センサー、23 圧力センサー、51 ケーシン
グ、52ローター、53 スクリーン、54 ろ室、5
5 ろ液流路、56 ゲート弁
1 flocculator, 2 sludge concentrator, 3 press-fitting dehydrator, 4 sludge supply pump, 5 coagulant pump, 10
Pressure vessel, 11 screen, 12 sludge channel, 13
Filtrate chamber, 14 sludge inlet, 15 discharge port, 16 hollow shaft, 17 motor, 18 scraper, 19 hollow arm, 20 through hole, 21 filtrate discharge pump, 22
Pressure sensor, 23 pressure sensor, 51 casing, 52 rotor, 53 screen, 54 filter chamber, 5
5 filtrate flow path, 56 gate valve

───────────────────────────────────────────────────── 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 36/02 B01D 29/38 550E 29/30 501 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 36/02 B01D 29/38 550E 29/30 501

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 凝集汚泥を周囲がスクリーンで囲まれた
汚泥流路に通してフロックを壊すことなく水分を分離し
て濃縮したうえ、圧入式脱水機に打ち込んで脱水するこ
とを特徴とする汚泥の濃縮脱水方法。
1. A sludge characterized in that coagulated sludge is passed through a sludge channel surrounded by a screen to separate and concentrate water without breaking flocs, and is then driven into a press-fitting type dehydrator for dehydration. Concentration dehydration method.
【請求項2】 圧入式脱水機として、ケーシングの内部
に低速回転する円盤状のローターを設け、ケーシングと
ローターとの間隙を両側がスクリーンで挟まれたろ室と
したものを用いる請求項1記載の汚泥の濃縮脱水方法。
2. The press-fitting type dehydrator, wherein a disk-shaped rotor that rotates at a low speed is provided inside a casing, and a gap between the casing and the rotor is a filter chamber whose both sides are sandwiched by screens. Condensation and dewatering method of sludge.
【請求項3】 圧力容器の内部に筒状のスクリーンを設
けてその内側を汚泥流路、外側をろ液室とするととも
に、汚泥流路内にはスクリーンの内周面に沿って緩やか
に回転する中空のスクレーパーを設け、このスクレーパ
ーにろ液室内のろ液をスクリーンを介して吸引する透孔
を設けたことを特徴とする汚泥濃縮装置。
3. A cylindrical screen is provided inside the pressure vessel, the inside of which serves as a sludge channel and the outside thereof as a filtrate chamber, and the sludge channel gently rotates along the inner peripheral surface of the screen. A sludge concentrating device characterized in that a hollow scraper is provided, and a through hole for sucking the filtrate in the filtrate chamber through a screen is provided in this scraper.
【請求項4】 スクレーパーの回転軸にろ液排出ポンプ
を接続した請求項3記載の汚泥濃縮装置。
4. The sludge concentrating device according to claim 3, wherein a filtrate discharge pump is connected to the rotary shaft of the scraper.
【請求項5】 ろ液排出ポンプが、汚泥流路への汚泥送
入口とろ液室との差圧を一定に保つものである請求項4
記載の汚泥濃縮装置。
5. The filtrate discharge pump keeps a constant differential pressure between the sludge feed port to the sludge passage and the filtrate chamber.
The described sludge concentrator.
JP2001259722A 2001-08-29 2001-08-29 Method for thickening and dehydrating sludge and apparatus for thickening sludge used therefor Withdrawn JP2003062600A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100688887B1 (en) 2006-03-31 2007-03-02 한국생산기술연구원 Hermetic condenser with vertical reciprocating screen cleaner for dewatering sludge
JP2007090264A (en) * 2005-09-29 2007-04-12 Kurita Water Ind Ltd Sludge concentration apparatus and sludge concentration method
JP2007296441A (en) * 2006-04-28 2007-11-15 Arai Tekkosho:Kk Scraper and its fluid filtration or transfer device
CN101850200A (en) * 2010-03-31 2010-10-06 李立功 Multi-path sewage filtering integrated machine
JP2012143702A (en) * 2011-01-12 2012-08-02 Nishimatsu Constr Co Ltd Muddy water treatment system and muddy water treatment method
CN102716612A (en) * 2012-06-11 2012-10-10 大连葆光节能空调设备厂 Swirling dirt separator for sewage
CN105107260A (en) * 2015-09-29 2015-12-02 上海市机械施工集团有限公司 Mud-water separation device
CN107335279A (en) * 2017-08-21 2017-11-10 郑州大学 A kind of highly effective sludge drying process device
CN113286764A (en) * 2019-11-11 2021-08-20 株式会社Lg化学 Centrifugal dehydrator and centrifugal dehydration method
CN121225850A (en) * 2025-11-28 2025-12-30 四川省生态环境科学研究院 A sludge thickening treatment device

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007090264A (en) * 2005-09-29 2007-04-12 Kurita Water Ind Ltd Sludge concentration apparatus and sludge concentration method
KR100688887B1 (en) 2006-03-31 2007-03-02 한국생산기술연구원 Hermetic condenser with vertical reciprocating screen cleaner for dewatering sludge
JP2007296441A (en) * 2006-04-28 2007-11-15 Arai Tekkosho:Kk Scraper and its fluid filtration or transfer device
CN101850200A (en) * 2010-03-31 2010-10-06 李立功 Multi-path sewage filtering integrated machine
CN101850200B (en) * 2010-03-31 2012-07-25 李立功 Multi-path sewage filtering integrated machine
JP2012143702A (en) * 2011-01-12 2012-08-02 Nishimatsu Constr Co Ltd Muddy water treatment system and muddy water treatment method
CN102716612A (en) * 2012-06-11 2012-10-10 大连葆光节能空调设备厂 Swirling dirt separator for sewage
CN105107260A (en) * 2015-09-29 2015-12-02 上海市机械施工集团有限公司 Mud-water separation device
CN107335279A (en) * 2017-08-21 2017-11-10 郑州大学 A kind of highly effective sludge drying process device
CN113286764A (en) * 2019-11-11 2021-08-20 株式会社Lg化学 Centrifugal dehydrator and centrifugal dehydration method
US12234169B2 (en) 2019-11-11 2025-02-25 Lg Chem, Ltd. Centrifugal dehydrator and centrifugal dehydration method
CN121225850A (en) * 2025-11-28 2025-12-30 四川省生态环境科学研究院 A sludge thickening treatment device

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