JPS60190209A - Method and apparatus for discharging concentrated sludge - Google Patents

Method and apparatus for discharging concentrated sludge

Info

Publication number
JPS60190209A
JPS60190209A JP59044531A JP4453184A JPS60190209A JP S60190209 A JPS60190209 A JP S60190209A JP 59044531 A JP59044531 A JP 59044531A JP 4453184 A JP4453184 A JP 4453184A JP S60190209 A JPS60190209 A JP S60190209A
Authority
JP
Japan
Prior art keywords
sludge
valve mechanism
concn
thickened
bag
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
Application number
JP59044531A
Other languages
Japanese (ja)
Inventor
Yoshinari Iijima
飯島 良也
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.)
Tsukishima Kikai Co Ltd
Original Assignee
Tsukishima Kikai 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 Tsukishima Kikai Co Ltd filed Critical Tsukishima Kikai Co Ltd
Priority to JP59044531A priority Critical patent/JPS60190209A/en
Publication of JPS60190209A publication Critical patent/JPS60190209A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To make it possible to discharge concn. sludge out of an apparatus with good efficiency, by receiving concn. sludge in an expansible and shrinkable bag and enabling the discharge of said sludge by the water head pressure of a filter tank. CONSTITUTION:The filtering concn. work of sludge is allowed to advance in a filter tank 1 and concn. sludge with a proper thickness is formed to the surface of each filter plate 2 and, thereafter, the sludge in the filter tank 1 is withdrawn from a raw sludge supply pipe 10. The conc. sludge adhered to each filter plate 2 is thereafter peeled off by air blow and the conc. cake is fallen in a storage part 5 through an opened valve mechanism 4. The valve mechanism 4 is hermetically closed in this state and new raw sludge is supplied into the filter tank 1 and the valve 12 of a conc. sludge discharge pipe 11 is opened simultaneously with the start of filtering to allow the water head pressure in the filter tank 1 and the raw sludge supply pipe 10 on a bag 7 to compress said bag 7 while the concn. sludge in the bag 7 is squeezed out and discharged to the outside from a concn. sludge discharge pipe 11. At this time, the filtering work in the filter tank 1 is advancing simultaneously.

Description

【発明の詳細な説明】 本発明は濃縮汚泥の排出方法およびその装置に関し、特
にFiM濃縮装置において生成した濃縮汚泥を効率よく
装置外に排出可能とした方法および装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for discharging thickened sludge, and more particularly to a method and apparatus for efficiently discharging thickened sludge produced in a FiM thickening apparatus.

一般に上水場から排出される上水汚泥中には90%以上
の水分が含有されているため、ケーキ化処理の前に上水
汚泥をr過積内でr過し上水汚泥の含水率を低下させた
上でケーキ化処理している。
Generally, water sludge discharged from water supply plants contains more than 90% water, so before caking treatment, water sludge is passed through an overload chamber to reduce the moisture content of water sludge. After lowering the temperature, it is processed into cake.

r過積は、内部にr液の流路を有し、表面にr布を張り
上端にr液排出管を取りつけたr過板を垂直状態で等間
隔に複数枚設置したものであり、r過積内に供給された
汚泥の水分をr過板内に吸収してr液排出管から外部へ
流出し、r過板表面に濃縮して付着した汚泥粒子が適当
な厚さの濃縮汚泥となったらr過板から剥離除去し、槽
底部から排出するものである。
An r-overload is a system in which a plurality of r-overboards are installed vertically at equal intervals, each having a flow path for the r-liquid inside, the surface covered with r-cloth and an r-liquid discharge pipe attached to the upper end. The moisture of the sludge supplied into the overload is absorbed into the r-filter plate and flows out from the r-liquid discharge pipe, and the sludge particles that are concentrated and attached to the r-filter plate surface become concentrated sludge of an appropriate thickness. When this happens, it should be peeled off from the overboard and discharged from the bottom of the tank.

第1図は従来のFit!54縮装置の一例を示し、同図
においてAは内部に多数のr過板を有するr過積であり
、このr過積A内にバルブBから原汚泥を供給してr過
濃縮作業を行い、各r過板表面に適当厚さの濃縮汚泥が
生成した後濃縮汚泥以外の汚泥を抜き出し、その後エア
ーブローによりr過板表面の濃縮汚泥を剥離して槽下部
に設置したスクリューコンヘアから成る濃縮汚泥排出装
置Cから更に排出ポンプDを介して外部に排出する。
Figure 1 shows the conventional Fit! An example of a 54-condensing device is shown, and in the same figure, A is an overload with a large number of overload plates inside, and raw sludge is supplied from valve B into this overload A to perform overconcentration work. After thickened sludge of appropriate thickness is generated on the surface of each r-filter plate, the sludge other than the thickened sludge is extracted, and then the thickened sludge on the surface of the r-filter plate is peeled off by air blowing, and the screw container is installed at the bottom of the tank. The concentrated sludge is further discharged from the concentrated sludge discharge device C to the outside via a discharge pump D.

このような従来のr過濃縮装置においては次の各工程を
1サイクルとしてい゛る。
In such a conventional superconcentrator, each of the following steps constitutes one cycle.

原汚泥供給−r過濃縮→残汚泥抜出→濃縮汚泥剥離−濃
縮汚泥排出。この工程を終了して始めて次のサイクル原
汚泥供給工程に入ることができるが、従来技術ではr過
濃縮以外のロスタイムが長い欠点を有している。
Raw sludge supply - r Overconcentration → Remaining sludge extraction → Thickened sludge peeling - Thickened sludge discharge. Only after this step is completed can the next cycle raw sludge supply step be started, but the conventional technology has the drawback of long loss time for processes other than r-overconcentration.

即ち、 原汚泥供給 15分 子過濃縮 60分 残汚泥抜出 15分 濃縮汚泥剥till 5分 濃縮汚泥排出 20分 以上合計115分の時間を必要とするが、濃縮汚泥は流
動性が悪いために前記濃縮汚泥排出装置Cにおける排出
工程に特に長時間を要している。
That is, raw sludge supply, 15 molecule superconcentration, 60 minutes, residual sludge removal, 15 minutes, thickened sludge stripping, 5 minutes, thickened sludge discharge, 20 minutes or more, and a total of 115 minutes, but since thickened sludge has poor fluidity, the above-mentioned The discharge process in the thickened sludge discharge device C takes a particularly long time.

また濃縮汚泥排出のためにスクリューコンヘア、排出ポ
ンプ等の高価な設備が必要となるため設備費が高くなり
、濃縮汚泥排出装置駆動のための電動機の電力・ポンプ
、スクリューコンベア部品の必要性のため維持管理費が
高く更にスクリューコンベア用軸シール部から汚泥が漏
れる等々の欠点を有していた。
In addition, expensive equipment such as screw conveyors and discharge pumps are required to discharge the thickened sludge, which increases equipment costs. Therefore, maintenance costs are high and sludge leaks from the screw conveyor shaft seal.

本発明は上記する従来のr過濃縮装置に鑑み、r過積下
部にバルブ機構を介して濃縮汚泥貯留部を設置し、排出
動力を必要とせずに濃縮汚泥を排出させるとともに濃縮
汚泥排出をr過濃縮工程と同時に行っ゛ζロスタイムを
短縮させることにより能力を増大させたr過濃縮機の濃
縮汚泥の排出方法およびその装置を提供することを目的
とする。
In view of the above-mentioned conventional overconcentration equipment, the present invention installs a thickened sludge storage section through a valve mechanism in the lower part of the overloaded area, and discharges the thickened sludge without requiring discharge power. It is an object of the present invention to provide a method for discharging thickened sludge from a superconcentrator, which is performed simultaneously with the superconcentration step, and whose capacity is increased by shortening the loss time, and an apparatus therefor.

以下図面に従って本発明の一実施例を詳細に説明する。An embodiment of the present invention will be described in detail below with reference to the drawings.

第2図乃至第4図において1はr過積であり、内部に多
数のr過板2を等間隔で立設し、上部に:JF′液排出
管3を連結する従来公知のものである。
In Figs. 2 to 4, reference numeral 1 denotes an r-overload, which is a conventionally known type in which a large number of r-overboards 2 are erected at equal intervals inside, and a JF' liquid discharge pipe 3 is connected to the upper part. .

r過積1下部にはバルブ機構4を介して濃縮汚泥貯留部
5が設置される。
A thickened sludge storage section 5 is installed under the r overload 1 via a valve mechanism 4.

バルブ機構4および貯留部5内金面には気体又は液体で
膨張収縮するホースにより開閉するシール6およびバッ
グ7が装填しである。シール6およびバッグ7は上部を
開口した一体の袋状となっており、第5図に示すように
開口上端と貯留部5頚部においてシール6はケース8に
固定しである。
The inner surfaces of the valve mechanism 4 and the storage section 5 are loaded with a seal 6 and a bag 7 that are opened and closed by a hose that expands and contracts with gas or liquid. The seal 6 and the bag 7 are in the form of an integral bag with an open top, and the seal 6 is fixed to the case 8 at the top of the opening and the neck of the storage section 5, as shown in FIG.

バルブ機構4には液圧或いは空気圧供給管9に連結して
膨張ホースが、バラグツ側面には濃縮汚泥排出管11に
連なる濃縮汚泥排出口が連結してあり、また貯留部5に
は公知の原汚泥供給管10が連結しである。
An expansion hose connected to a hydraulic or pneumatic supply pipe 9 is connected to the valve mechanism 4, and a concentrated sludge discharge port connected to a concentrated sludge discharge pipe 11 is connected to the side of the bulkhead. A sludge supply pipe 10 is connected.

上記構成において原汚泥供給管10からr過積l内に原
汚泥を従来と同様に供給する。この時汚泥が貯留部5内
に流入するのを防止するため膨張ホースに液圧或いは空
気圧を付与して第5図鎖線に示すようにシール6を左右
から圧接してバルブ機構4を密閉する。前記シール6の
圧接は有効な片側空気押圧または機械式ピンチ形式によ
っても良い。
In the above configuration, raw sludge is supplied from the raw sludge supply pipe 10 into the excess volume l in the same manner as in the past. At this time, in order to prevent sludge from flowing into the storage section 5, hydraulic or air pressure is applied to the expansion hose to press the seals 6 from the left and right sides as shown by the chain lines in FIG. 5, thereby sealing the valve mechanism 4. The seal 6 may be pressed by an effective one-sided pneumatic pressure or by a mechanical pinch type.

r過積1内において汚泥のr過濃縮作業が進行し、各r
過板2表面に適当厚さの濃縮汚泥が生成した後r過積1
内の汚泥を原汚泥供給管10から抜き出す。その後エア
ーブローにより各r過板2に付着する濃縮汚泥を剥離し
、開口するバルブ機構4を通して貯留部5内に濃縮ケー
キを落下させる。この状態においてバルブ機構4を前記
と同様にして密閉し、r過積1内には新たな原汚泥を供
給しr過開始と同時に濃縮汚泥排出管11のバルブ12
を開くことによりr過槽1および供給管10内の水頭圧
がバッグ7に作用してバッグ7は圧縮され、バッグ7内
の濃縮lr5泥は排出管11から外部へ絞り排出される
ことになる。
The sludge overconcentration work progresses in the overload 1, and each
After thickened sludge of appropriate thickness is generated on the surface of the overload plate 2, overload 1
The sludge inside is extracted from the raw sludge supply pipe 10. Thereafter, the concentrated sludge adhering to each r-filter plate 2 is removed by air blowing, and the concentrated cake is dropped into the storage section 5 through the valve mechanism 4 that opens. In this state, the valve mechanism 4 is sealed in the same manner as described above, new raw sludge is supplied into the excess volume 1, and the valve 12 of the concentrated sludge discharge pipe 11 is
By opening it, the water head pressure in the r overtank 1 and the supply pipe 10 acts on the bag 7, compressing the bag 7, and the concentrated lr5 mud in the bag 7 is squeezed and discharged from the discharge pipe 11 to the outside. .

この時にはr過槽1におけるr過作業は同時進行してい
る。従って原汚泥供給−r過濃縮−残汚泥抜出一濃縮l
η泥排出のr過すイクルにおいてr過濃縮と濃縮汚泥排
出作業を同時になすことができ、r過すイクルタイムを
下記のように短縮することができる。
At this time, the r-over work in the r-over tank 1 is progressing simultaneously. Therefore, raw sludge supply - r superconcentration - residual sludge extraction - concentration l
In the cycle of sludge discharge, overconcentration and concentrated sludge discharge work can be performed simultaneously, and the cycle time can be shortened as described below.

原汚泥供給 15分 子iI!JR縮 60分 残汚泥抜出 15分 濃縮汚泥剥離 5分 バルブ機構閉じ 1分 合計のサイクルタイムを96分とすることができ、能カ
アノブ率は従来と比較して16.5%となり更に高価な
スクリューコンベア、排出ポンプを必要とせずまた駆動
電力を節約できる等を総合的に比較すれば従来より設備
費で1/10以下、ランニングコストで1/25以下と
なる。
Raw sludge supply 15 molecules iI! JR compaction 60 minutes residual sludge removal 15 minutes thickened sludge removal 5 minutes valve mechanism closed 1 minute The total cycle time can be made 96 minutes, and the efficiency rate is 16.5% compared to the conventional method, which is more expensive. Comprehensively comparing features such as not requiring a screw conveyor or discharge pump and saving drive power, the equipment cost is less than 1/10 and the running cost is less than 1/25 compared to conventional methods.

尚、上記説明においてバルブ機構4は液圧、空気圧等に
より密閉可能としたが、これに限定されずta械的圧力
によりシール6を圧接可能としてもよい。
In the above description, the valve mechanism 4 can be sealed by hydraulic pressure, pneumatic pressure, etc., but the present invention is not limited to this, and the seal 6 may be able to be pressed by mechanical pressure.

上記する如く本発明によれば濃縮汚泥を膨張・収縮自在
なバッグ7内に収容し、r過積水頭圧により排出可能と
したことにより簡単な装置で濃縮汚泥排出を効果的にな
すことができ、更に濃縮汚泥排出とr過濃縮作業を同時
になすことができr過濃縮能率を結果的に増大すること
ができる。
As described above, according to the present invention, the thickened sludge is housed in the bag 7 that can be expanded and contracted, and the thickened sludge can be discharged using excess water head pressure, thereby making it possible to effectively discharge the thickened sludge with a simple device. Furthermore, the discharge of thickened sludge and the superconcentration work can be performed simultaneously, and the superconcentration efficiency can be increased as a result.

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

第1図は従来のr過濃縮装置の一例を示す概略正面図、
第2図は本発明r過濃縮装置の一実施例を示す概略正面
図、第3図は要部の拡大正面図、第4図は第3図のA−
A線概略断面図、第5図は要部の拡大断面図である。 1はr過積、2はr過板、4はバルブ機構、5は貯留部
、6はシール、7はバッグ、IOは原汚泥供給管、11
は濃縮汚泥排出管である。 第1図 第2図
FIG. 1 is a schematic front view showing an example of a conventional r-perconcentrator;
FIG. 2 is a schematic front view showing an embodiment of the superconcentrator of the present invention, FIG. 3 is an enlarged front view of the main parts, and FIG. 4 is a
A schematic sectional view taken along the line A, and FIG. 5 is an enlarged sectional view of the main parts. 1 is r overload, 2 is r overboard, 4 is valve mechanism, 5 is storage section, 6 is seal, 7 is bag, IO is raw sludge supply pipe, 11
is the thickened sludge discharge pipe. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】 +1):f′通過室まわりをr有精で囲んでなるr過板
をr過積の汚泥室内に複数枚縣架し、汚泥中の水分をr
室内にr過させr過室と連通して設けられたr液排出管
を通してr液を排出するようにしたr過濃縮機において
、r過積の下部にバルブ機構を介して濃縮汚泥貯留部を
設け、濃縮汚泥を受け入れた後バルブ機構を閉とし、濃
縮汚泥の排出をr過濃縮工程と同時に行うことを特徴と
するr過濃縮機における濃縮汚泥の排出方法。 (2)r過室のまわりをr有精で囲んでなるr過板をr
過積の汚泥室内に複数枚縣架し、汚泥中の水分をr室内
にr通させr過室と連通して設けられたr液排出管を通
してr液を排出するようにしたr過濃縮機において、r
過積の下部にバルブ機構を介して変形自在なバッグを装
填した濃縮汚泥貯留部を設け、濃縮汚泥を受け入れた後
バルブ機構を閉とし、バッグ外面よりr過積原汚泥水頭
で加圧して排出することを特徴とするf過濃縮機におけ
る濃縮汚泥の排出方法。 (3)特許請求の範囲第1項、第2項記載のr過濃縮機
においてバルブ機構が気体又は液体で膨張・収縮するこ
とにより開閉するピンチ又はダイ十フラム式バルブであ
ることを特徴とするr過濃縮機における濃縮汚泥の排出
装置。
[Scope of Claims] +1): A plurality of r-pass plates made of r-sperm surrounding the f' passage chamber are suspended in an overloaded sludge chamber, and the water in the sludge is removed by r.
In a superconcentrator in which liquid is discharged through a liquid discharge pipe that is connected to a liquid discharge chamber, a thickened sludge storage section is connected to the lower part of the liquid through a valve mechanism. A method for discharging thickened sludge in a super-thickener, characterized in that after receiving the thickened sludge, the valve mechanism is closed and the thickened sludge is discharged at the same time as the super-thickening step. (2) The r overplate formed by surrounding the r overchamber with r spermatozoa is r
A superconcentrator in which multiple sheets of sludge are suspended in an overloaded sludge chamber, water in the sludge passes through the sludge chamber, and the sludge is discharged through a liquid discharge pipe connected to the sludge chamber. In, r
A thickened sludge storage section loaded with a deformable bag via a valve mechanism is provided at the bottom of the overloaded area, and after receiving the thickened sludge, the valve mechanism is closed and the overloaded raw sludge is pressurized from the outside of the bag by the head of the overloaded raw sludge and discharged. A method for discharging thickened sludge in an f-concentrator, characterized in that: (3) The superconcentrator described in claims 1 and 2 is characterized in that the valve mechanism is a pinch or diphragm type valve that opens and closes by expanding and contracting with gas or liquid. r A device for discharging thickened sludge in a superconcentrator.
JP59044531A 1984-03-08 1984-03-08 Method and apparatus for discharging concentrated sludge Pending JPS60190209A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59044531A JPS60190209A (en) 1984-03-08 1984-03-08 Method and apparatus for discharging concentrated sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59044531A JPS60190209A (en) 1984-03-08 1984-03-08 Method and apparatus for discharging concentrated sludge

Publications (1)

Publication Number Publication Date
JPS60190209A true JPS60190209A (en) 1985-09-27

Family

ID=12694092

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59044531A Pending JPS60190209A (en) 1984-03-08 1984-03-08 Method and apparatus for discharging concentrated sludge

Country Status (1)

Country Link
JP (1) JPS60190209A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013148191A (en) * 2012-01-23 2013-08-01 Swing Corp Automatic valve and method of opening/closing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013148191A (en) * 2012-01-23 2013-08-01 Swing Corp Automatic valve and method of opening/closing the same

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