JPS5811085A - Automatic controller for floating and concentrating tank - Google Patents

Automatic controller for floating and concentrating tank

Info

Publication number
JPS5811085A
JPS5811085A JP10819581A JP10819581A JPS5811085A JP S5811085 A JPS5811085 A JP S5811085A JP 10819581 A JP10819581 A JP 10819581A JP 10819581 A JP10819581 A JP 10819581A JP S5811085 A JPS5811085 A JP S5811085A
Authority
JP
Japan
Prior art keywords
sludge
floating
thickness
layer
concd
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
JP10819581A
Other languages
Japanese (ja)
Inventor
Kazuo Shibazaki
柴崎 和夫
Ryosuke Miura
良輔 三浦
Itaru Takahashi
高橋 格
Yukio Toya
遠矢 幸男
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
Tokyo Shibaura Electric 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 Toshiba Corp, Tokyo Shibaura Electric Co Ltd filed Critical Toshiba Corp
Priority to JP10819581A priority Critical patent/JPS5811085A/en
Publication of JPS5811085A publication Critical patent/JPS5811085A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To maintain the tickness of a floating concd. sludge layer in an optimum range by providing a thickness detector for the floating concd. sludge layer, a comparator for the output thereof and the preset upper and lower limit values of the thickness of the concd. sludge layer, and a controller for a concd. sludge scraper. CONSTITUTION:The thickness of a floating concd. sludge layer 3 is detected by a floating concd. sludge layer detector 10 provided in a floating tank 2. The upper and lower limit values of the layer 3 by which predetermined concn. of sludge and clarity of separated liquid are obtained are deforehand inputted to a comparator 11, which compares the upper and lower limit values and the output from the detector 10. A controller 12 emits and instruction for starting the operation of a sludge scraper 4 when the thickness of the layer 3 is equal to the upper limit value or larger than the same. At the point of the time when the thickness of the layer 3 decreases equal to or smaller than the lower limit value, the controller emits an instruction for stopping the scraper 4.

Description

【発明の詳細な説明】 本発明は下廃水汚泥を浮上濃縮させる際の自動制御装置
に係り、特に浮上濃縮汚泥層の厚さを一定範囲内に保つ
ようにする自動制御装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an automatic control device for flotation and concentration of sewage sludge, and more particularly to an automatic control device for maintaining the thickness of a flotation and thickening sludge layer within a certain range.

従来、下廃水汚泥を濃縮する方法としては重力濃縮法が
多く採用されていた。この方法は運転コストが比較的安
く、且つ維持管理も比較的容易であるという利点があっ
た。しかし、濃縮の推進力は重力であるため、根本的(
=それほどの濃縮効果は期待できないという欠点があっ
た。%(=近年、下廃水汚泥中の有機物含有用が増加し
たために、その濃縮性は悪化してきており、重力濃縮法
では所期の濃縮率を得られない場合が生じてきている。
Conventionally, the gravity concentration method has often been adopted as a method for concentrating sewage sewage sludge. This method has the advantages of relatively low operating costs and relatively easy maintenance. However, since the driving force for enrichment is gravity, the fundamental (
=The drawback was that it was not possible to expect such a concentration effect. % (=In recent years, as the amount of organic matter contained in sewage sludge has increased, its concentration has deteriorated, and there are cases where the gravity concentration method cannot achieve the desired concentration rate.

さら(二、汚泥が季節によって質的な変化を生じること
も多々あるため、重力濃縮法では安定した処理が難かし
いという欠点もあった。
Furthermore, because sludge often changes in quality depending on the season, the gravity concentration method has the disadvantage that stable treatment is difficult.

重力濃縮法には上述したような欠点があるため、近年安
定した処理が可能な浮上法が採用されるようになりつつ
ある。
Since the gravitational concentration method has the above-mentioned drawbacks, in recent years flotation methods, which can provide stable processing, have been increasingly adopted.

浮上法の原理は次の通りである。汚泥分離後の処理水(
分離水)の一部を循環水として取シ出し、4〜5KP/
dの加圧下で空気を溶解させた後汚泥原水と合流させる
。この時循環水は大気解放され、多量の微細気泡が発生
する。この微細気泡が汚泥(=付着して浮力を与え、汚
泥は浮上し濃縮される。
The principle of the levitation method is as follows. Treated water after sludge separation (
A part of the separated water) is taken out as circulating water, and 4 to 5 KP/
After dissolving the air under the pressure of d, it is combined with the raw sludge water. At this time, the circulating water is released to the atmosphere and a large amount of fine bubbles are generated. These microbubbles adhere to the sludge and provide buoyancy, causing the sludge to float and become concentrated.

重力法、浮上法などの濃縮プロセスの目的は当然ながら
、高濃度の汚泥を得ること、清澄な分離水を得ることで
あυ、この丸め浮上法では浮上濃縮汚泥層の厚さを適正
に管理する必要がある。浮上濃縮汚泥層の厚さが厚いほ
ど濃縮汚泥の濃度は高くなる。一方、浮上濃縮汚泥層の
厚さをあまり厚くしすぎると、分離水の清澄度は低下し
てしまう。
The purpose of concentration processes such as the gravity method and flotation method is, of course, to obtain highly concentrated sludge and clear separated water, and in this round flotation method, the thickness of the flotation thickened sludge layer is appropriately controlled. There is a need to. The thicker the floating thickened sludge layer, the higher the concentration of the thickened sludge. On the other hand, if the thickness of the floating thickened sludge layer is made too thick, the clarity of the separated water will decrease.

従来、浮上濃縮汚泥層の厚さは操作員の経験と勘で、タ
イマなど(二より適当な頻度で浮上濃縮汚泥をかき取っ
てコントロールされていた(通常、かき取り頻度は数回
7日〜1回7時)。
Conventionally, the thickness of the floated thickened sludge layer was controlled by the operator's experience and intuition by scraping the floated thickened sludge at an appropriate frequency using a timer (usually the scraping frequency was several times every 7 days or more). (Once at 7:00).

このような従来方法では、汚泥原水の負荷変動など(=
よって浮上濃縮汚泥層の厚さが厚くなυ過ぎたシ、ある
いは逆(二薄くなり過ぎたりすることがあ如、処理水の
清澄度、汚泥の濃縮度を満足させ得ない場合があった。
In this conventional method, load fluctuations in raw sludge water, etc.
Therefore, if the thickness of the floating thickened sludge layer becomes too thick, or vice versa, the clarity of the treated water and the concentration of the sludge may not be satisfied.

本発明は上述した欠点を解消し、常に高濃度の汚泥が得
られ、且つ清澄な分離水を得られるような浮上濃縮槽の
自動制御装置を得ることを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to eliminate the above-mentioned drawbacks and provide an automatic control device for a flotation thickening tank that can always obtain highly concentrated sludge and clear separated water.

本発明の特徴は、汚泥を浮上濃縮させる装置において、
浮上槽の上部に位置する浮上濃縮汚泥層め設定されてい
る浮上濃縮汚泥層の厚さの上下限値とを比較する比較器
と、該比較器からの出力(−よって濃縮汚泥かき取り装
置dの運転の開始、停止を指示する装置とから構成され
ていることである。
The feature of the present invention is that in an apparatus for floating and concentrating sludge,
A comparator that compares the upper and lower limits of the thickness of the floated thickened sludge layer located at the top of the flotation tank, and an output from the comparator (-therefore, the thickened sludge scraping device d It consists of a device that instructs the start and stop of operation.

前述したよう(=、浮上法では浮」;濃縮汚泥層の厚さ
を適正範囲(=保つことが最も重要である。本発明にお
いては、汚泥の濃縮度、分離液の清澄度を満足できる浮
上濃縮汚泥層の厚さの上下限値を予め設定しておき、浮
上濃縮汚泥層の厚さが上限値(二なつだ時(二は、汚泥
かき取り装置を運転して浮上濃縮汚泥層の厚さを減少さ
せていき、下限値になったら汚泥かき取シ装置を停止さ
せ、常(二上下限値の範囲内(−保つよう(−したもの
である。
As mentioned above, it is most important to maintain the thickness of the thickened sludge layer within an appropriate range (= floating in the flotation method). The upper and lower limits of the thickness of the thickened sludge layer are set in advance. The sludge scraping device is stopped when the lower limit value is reached, and the sludge scraping device is always kept within the upper and lower limit values.

図は本発明の装置の一例を模式的に示した図である。The figure is a diagram schematically showing an example of the apparatus of the present invention.

汚泥原水は管路1を経て浮」1槽2(二流入する。Raw sludge flows through pipe 1 and into tank 2.

同時に加圧ポンプ5で加圧され管路6がら空気を吸引し
た循環水が管路8を経て浮上槽2に流入する。浮上槽2
では循環水が大気解放されるので、この中に溶存してい
た空気が微細気泡となって発生し、汚泥(二付着して汚
泥を浮上させ浮上濃縮汚泥層の上部から、汚泥かき取り
装置4(二よって濃縮汚泥はかき取られ、濃縮汚泥受槽
9(二排出される。
At the same time, circulating water pressurized by the pressurizing pump 5 and sucking air from the pipe line 6 flows into the flotation tank 2 via the pipe line 8. Flotation tank 2
Since the circulating water is released to the atmosphere, the air dissolved in it is generated as fine bubbles, which adhere to the sludge and float the sludge from the top of the floating thickened sludge layer to the sludge scraping device 4. (Thus, the thickened sludge is scraped off and discharged to the thickened sludge receiving tank 9.

このような浮上濃縮槽において、浮上槽2内(=設置さ
れ上下動できるようにしである浮上濃縮汚泥層検出装置
10によって浮上濃縮汚泥層3の厚さを検出する。さら
(二、比較器11には所定の汚泥濃縮度、分離液清澄度
を達成できる浮上濃縮汚泥層3の厚さの上下限値を実験
(=よシ予め決定し入力されておυ、この上下限値と浮
上濃縮汚泥層検出装置10からの出力とを比較する。制
御器12では比較器11からの出力を受けて、浮上濃縮
汚泥層3の厚さが上限値に等しいかあるいは大きい場合
C二は汚泥かき取シ装置4の運転開始の指示を出す。汚
泥かき取)装置4が運転されると浮上濃縮汚泥層3の厚
さは徐々)二減少していく。そして、浮上濃縮汚泥層3
の厚さが下限値と等しいがもしくは小さくなった時点で
、汚泥かき取)装置4の停止の指示を出す。
In such a flotation thickening tank, the thickness of the flotation thickened sludge layer 3 is detected by a flotation thickened sludge layer detection device 10 which is installed in the flotation tank 2 and can move up and down. The upper and lower limits of the thickness of the flotation thickened sludge layer 3 that can achieve the predetermined sludge concentration and separation liquid clarity are determined by experiment (=Yoshi), which are predetermined and input υ, and these upper and lower limit values and the flotation thickened sludge The controller 12 receives the output from the comparator 11, and when the thickness of the floated thickened sludge layer 3 is equal to or larger than the upper limit value, C2 is the sludge scraping system. An instruction is given to start operation of the device 4. When the sludge scraping device 4 is operated, the thickness of the floated thickened sludge layer 3 gradually decreases.
When the thickness of the sludge scraper becomes equal to or smaller than the lower limit, an instruction to stop the sludge scraping device 4 is issued.

ここで、浮上濃縮汚泥層検出装置10には光透過方式の
適用が望ましいが、これ(二限るものではない。また、
浮上濃縮汚泥層検出装置10はここで説明したような上
下動可能なものでなくてもよく、予め設定しである上下
限値の位置に光源と受光器を設置してもよい。
Here, it is desirable to apply a light transmission method to the floating thickened sludge layer detection device 10, but it is not limited to this method.
The floating thickened sludge layer detection device 10 does not have to be vertically movable as described here, and the light source and light receiver may be installed at preset upper and lower limit positions.

以上説明したよう(二、本発明によれば最も重要な管理
指標である浮上濃縮汚泥層の厚さを常に適正な範囲(−
保つことができるので、高濃度の汚泥、清澄な分離液を
常に安定して得ることができる。
As explained above (2. According to the present invention, the thickness of the floating thickened sludge layer, which is the most important management index, is always kept within the appropriate range (-
Because it can be maintained, highly concentrated sludge and clear separated liquid can always be stably obtained.

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

図面は本発明の一実施例を模式的に示した図である。 The drawings are diagrams schematically showing one embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 汚泥を浮上濃縮させる装置(二おいて、浮上槽の上部(
二位置する浮上濃縮汚泥層の厚さを検出する装置と、該
装置からの出力と予め設定されている浮上濃縮汚泥層の
厚さの上下限値とを比較する比較器と、該比較器からの
出力によって濃縮汚泥かき取シ装置の運転の開始、停止
を指示する装置とから構成されていることを特徴とする
浮上濃縮槽の自動制御装置。
Equipment for flotation and concentration of sludge (2) The upper part of the flotation tank (
2. A device that detects the thickness of the floated thickened sludge layer, a comparator that compares the output from the device with preset upper and lower limits of the thickness of the floated thickened sludge layer, and An automatic control device for a flotation thickening tank, comprising a device that instructs to start and stop operation of a thickened sludge scraping device based on the output of the device.
JP10819581A 1981-07-13 1981-07-13 Automatic controller for floating and concentrating tank Pending JPS5811085A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10819581A JPS5811085A (en) 1981-07-13 1981-07-13 Automatic controller for floating and concentrating tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10819581A JPS5811085A (en) 1981-07-13 1981-07-13 Automatic controller for floating and concentrating tank

Publications (1)

Publication Number Publication Date
JPS5811085A true JPS5811085A (en) 1983-01-21

Family

ID=14478414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10819581A Pending JPS5811085A (en) 1981-07-13 1981-07-13 Automatic controller for floating and concentrating tank

Country Status (1)

Country Link
JP (1) JPS5811085A (en)

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