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
JPH0829268B2 - Centrifugal dehydrator chemical injection rate controller - Google Patents
[go: Go Back, main page]

JPH0829268B2 - Centrifugal dehydrator chemical injection rate controller - Google Patents

Centrifugal dehydrator chemical injection rate controller

Info

Publication number
JPH0829268B2
JPH0829268B2 JP3358136A JP35813691A JPH0829268B2 JP H0829268 B2 JPH0829268 B2 JP H0829268B2 JP 3358136 A JP3358136 A JP 3358136A JP 35813691 A JP35813691 A JP 35813691A JP H0829268 B2 JPH0829268 B2 JP H0829268B2
Authority
JP
Japan
Prior art keywords
liquid
centrifugal dehydrator
amount
concentration
chemical
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
JP3358136A
Other languages
Japanese (ja)
Other versions
JPH05177153A (en
Inventor
肇 田原
満也 田口
裕司 甲斐
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.)
NISHIHARA KANKYO EISEI KENKYUSHO KK
Original Assignee
NISHIHARA KANKYO EISEI KENKYUSHO KK
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 NISHIHARA KANKYO EISEI KENKYUSHO KK filed Critical NISHIHARA KANKYO EISEI KENKYUSHO KK
Priority to JP3358136A priority Critical patent/JPH0829268B2/en
Publication of JPH05177153A publication Critical patent/JPH05177153A/en
Publication of JPH0829268B2 publication Critical patent/JPH0829268B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Centrifugal Separators (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は汚泥を固液分離して分
離液と脱水ケーキとを生成するための遠心脱水機の薬注
率制御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 chemical injection rate control device for a centrifugal dehydrator for solid-liquid separation of sludge to produce a separated liquid and a dehydrated cake.

【0002】[0002]

【従来の技術】周知のように遠心脱水機の薬注率制御装
置は図5に示すように構成されている。図において、汚
泥を固液分離して分離液と脱水ケーキとを生成する遠心
脱水機1は外胴2と内胴3とで構成され、外胴2の一方
の傾斜側端部2aには脱水ケーキ排出口4が設けられる
と共に、他方の大径端部2bには分離液排出口5が設け
られている。
2. Description of the Related Art As is well known, a chemical injection rate control device for a centrifugal dehydrator is constructed as shown in FIG. In the figure, a centrifugal dehydrator 1 for solid-liquid separating sludge to produce a separated liquid and a dehydrated cake is composed of an outer case 2 and an inner case 3, and one inclined side end 2a of the outer case 2 is dehydrated. A cake discharge port 4 is provided, and a separated liquid discharge port 5 is provided at the other large-diameter end 2b.

【0003】また、内胴3は内部に汚泥などの被処理液
を供給する流入管6が配置され、周面にスクリュー7と
薬品である処理液を供給する流入孔8とが設けられてい
る。
Further, an inner pipe 3 is provided with an inflow pipe 6 for supplying a liquid to be treated such as sludge, and a screw 7 and an inflow hole 8 for supplying a treatment liquid which is a chemical are provided on a peripheral surface thereof. .

【0004】さらに、遠心脱水機1は固液分離されて生
成された分離液の濃度を計測する濃度計9が設けられ、
この濃度計9によって計測された濃度に基づいて薬品の
添加量を調整するように構成されている。
Further, the centrifugal dehydrator 1 is provided with a densitometer 9 for measuring the concentration of the separated liquid produced by solid-liquid separation,
The amount of chemicals added is adjusted based on the concentration measured by the densitometer 9.

【0005】また、上記外胴2の一方の軸にはメインモ
ータ10に連動した駆動プーリ11が設けられ、他方の
軸には内胴3と連結して遊星ギヤなどからなる歯車機構
13が配置されている。上記外胴2はメインモータ10
によって回転され、この回転は歯車機構13を介して内
胴3に伝えられる。
Further, a drive pulley 11 interlocked with the main motor 10 is provided on one shaft of the outer case 2, and a gear mechanism 13 composed of a planetary gear or the like is connected to the inner case 3 on the other shaft. Has been done. The outer body 2 is a main motor 10
And the rotation is transmitted to the inner case 3 via the gear mechanism 13.

【0006】そして、内胴3と外胴2とは同じ方向に若
干の回転差を以て回転する。差速モータ14にはその電
流値を検出する検出器15と、この検出器15よりの検
出値をあらかじめ設定した所定の範囲の設定値と比較
し、この設定値に近似するように上記差速モータ14を
制御するコントローラ16とからなる制御手段17が設
けられている。
The inner case 3 and the outer case 2 rotate in the same direction with a slight rotational difference. The differential speed motor 14 has a detector 15 for detecting the current value thereof, and a detection value from the detector 15 is compared with a preset value in a preset range, and the differential speed motor is approximated to the preset value. A control unit 17 including a controller 16 that controls the motor 14 is provided.

【0007】そして、遠心脱水機1の薬品添加量に対す
る分離液濃度の関係は図6に示すように最初のうちは薬
品添加量が増加するに伴って分離液濃度は清澄となり、
次いで薬品添加量が多すぎる状態となると分離液濃度が
濁ってくる特性を示す。
As shown in FIG. 6, the relationship between the amount of chemicals added to the centrifugal dehydrator 1 and the concentration of the separated liquid becomes clear as the amount of the added chemicals increases at the beginning, as shown in FIG.
Next, when the amount of chemicals added is too large, the concentration of the separated liquid becomes cloudy.

【0008】[0008]

【発明が解決しようとする課題】従来の遠心脱水機の分
離液濃度と薬品添加量との関係は図6に示すように薬品
添加量が増加すると分離液濃度は清澄となるが、薬品添
加量が多すぎると逆に分離液濃度が悪化する特性曲線で
あるので、分離液濃度は過少添加時のXと過剰添加時の
Yとで同じになり、分離液濃度だけでは薬品添加量が過
少であるか過剰であるかを判断することができず、よっ
て自動制御で被処理液に対して最適な薬品添加量を調整
することができないという問題点があった。
As shown in FIG. 6, the separation liquid concentration of the conventional centrifugal dehydrator and the chemical addition amount become clear as the chemical addition amount increases, but the chemical addition amount increases. If the amount is too large, on the contrary, the concentration of the separation liquid deteriorates. Therefore, the concentration of the separation liquid becomes the same for X when it is excessively added and Y when it is excessively added. There is a problem that it is not possible to determine whether there is an excess or excess, and therefore it is not possible to adjust the optimum chemical addition amount for the liquid to be treated by automatic control.

【0009】この発明は上記のような問題点を解消する
ためになされたもので、薬品添加量が過少か過剰かを判
断できるようにして被処理液に対する薬品添加量を自動
調整できるようにした遠心脱水機の薬注率制御装置を提
供することを目的とする。
The present invention has been made to solve the above problems, and it is possible to automatically adjust the amount of chemical addition to the liquid to be treated by making it possible to judge whether the amount of chemical addition is too small or excessive. An object is to provide a chemical injection rate control device for a centrifugal dehydrator.

【0010】[0010]

【課題を解決するための手段】この発明に係る遠心脱水
機の薬注率制御装置は被処理液を固液分離する遠心脱水
機から生成される分離液の濃度を濃度計により計測する
と共に、上記分離液の泡の色を光学的色センサにより計
測するもので、上記濃度計で計測した濃度計測値と光学
的色センサで計測した分離液の泡の色計測値とから判断
手段で被処理液に対する薬品添加量の多判断するもので
ある。
A chemical injection rate control device for a centrifugal dehydrator according to the present invention measures the concentration of a separated liquid produced from a centrifugal dehydrator for solid-liquid separation of a liquid to be treated with a densitometer, The color of bubbles of the separation liquid is measured by an optical color sensor, and is processed by a determination means from the concentration measurement value measured by the densitometer and the color measurement value of the bubbles of the separation liquid measured by the optical color sensor. This is a large judgment as to the amount of chemicals added to the liquid.

【0011】[0011]

【作用】この発明における遠心脱水機の薬注率制御装置
は光学的色センサを使用して遠心脱水機が生成する分離
液の泡の色を計測すると共に、分離液の濃度を計測し、
この分離液の泡の色計測値および濃度計測値から遠心脱
水機に添加する薬品の量が過剰添加か過少添加かを判断
手段で判断するようにした。
The chemical injection rate control device of the centrifugal dehydrator according to the present invention uses an optical color sensor to measure the color of bubbles of the separated liquid generated by the centrifugal dehydrator and also to measure the concentration of the separated liquid.
Based on the color measurement value and the concentration measurement value of the bubbles of the separated liquid, it is determined by the determination means whether the amount of the chemical added to the centrifugal dehydrator is excessive or excessive.

【0012】[0012]

【実施例】以下、この発明の一実施例を図に基づいて説
明する。図1はこの発明に係る一実施例を示す概要構成
図で、図1において図3と同一または均等な構成部分に
は同一符号を付して重複説明を省略する。図において、
18は被処理液に対する薬品添加量が多いか少ないかを
判断する光学的色センサで、この光学的色センサ18は
分離液の上部に発生する泡の色を計測する。19は光学
的色センサ18が計測した分離液の計測値と濃度計9の
計測値から被処理液に対する薬品添加量の多少を判断し
て薬品添加量を自動調整する判断手段としての制御部で
ある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic configuration diagram showing an embodiment according to the present invention. In FIG. 1, the same or equivalent components as in FIG. In the figure,
Reference numeral 18 is an optical color sensor that determines whether the amount of chemical added to the liquid to be treated is large or small. The optical color sensor 18 measures the color of bubbles generated on the upper portion of the separation liquid. Reference numeral 19 is a control unit as a judgment unit for automatically adjusting the chemical addition amount by judging the amount of the chemical addition to the liquid to be treated from the measured value of the separated liquid measured by the optical color sensor 18 and the measured value of the concentration meter 9. is there.

【0013】次に動作について説明する。光学的色セン
サ18は白色と黒色およびその中間色の度合を光反射量
によって示すと、図2のような結果で計測できる。ま
た、遠心脱水機1の分離液は泡が発生し、泡の色は薬品
添加量が増加すると白くなる傾向がみられる。このた
め、薬品添加量と分離液の泡の色度合との関係を特性曲
線で示すと図3に示すようなる。
Next, the operation will be described. When the optical color sensor 18 indicates the degrees of white, black, and intermediate colors thereof by the amount of light reflection, the optical color sensor 18 can measure the result as shown in FIG. In addition, bubbles are generated in the separated liquid of the centrifugal dehydrator 1, and the color of the bubbles tends to become white as the amount of chemicals added increases. Therefore, the relationship between the added amount of chemicals and the color degree of bubbles of the separated liquid is shown in a characteristic curve in FIG.

【0014】光学的色センサ18は遠心脱水機1から排
出され、貯留槽(図示せず)に貯留される分離液の泡を
光学的色センサ18により計測し、また併せて分離液濃
度を濃度計9により計測する。そして、光学的色センサ
18および濃度計9によって計測した泡の色の計測値お
よび分離液濃度から遠心脱水機1に添加した薬品が過剰
であったか過少であったかを制御部19により判断して
薬品添加量を自動調整するものである。
The optical color sensor 18 measures the bubbles of the separated liquid discharged from the centrifugal dehydrator 1 and stored in a storage tank (not shown) by the optical color sensor 18, and also determines the concentration of the separated liquid. It is measured by a total of 9. Then, based on the measured value of the color of the foam measured by the optical color sensor 18 and the densitometer 9 and the concentration of the separated liquid, it is judged by the control unit 19 whether the chemical added to the centrifugal dehydrator 1 is excessive or insufficient, and the chemical addition is performed. The amount is automatically adjusted.

【0015】すなわち、光学的色センサ18および濃度
計9によって計測した泡の色の計測値および濃度計測値
から遠心脱水機1に添加した薬品が過剰であるか過少で
あるかを判断し、図4に示す特性曲線の適性範囲となる
ように制御部19で被処理液に対する薬品添加量を自動
調整するものである。
That is, it is determined whether the amount of chemical added to the centrifugal dehydrator 1 is excessive or insufficient based on the foam color measurement value and the concentration measurement value measured by the optical color sensor 18 and the densitometer 9, The controller 19 automatically adjusts the amount of chemicals added to the liquid to be treated so that the characteristic curve shown in FIG.

【0016】以上のことから分離液の濃度計9と光学的
色センサ18とを併用し、図4に示す特性曲線の適性範
囲に分離液の濃度および光学的色センサ18の出力電圧
が存在するように制御部19で薬品添加量を制御するこ
とにより、被処理液に対する薬品添加量を適性範囲に抑
える自動制御が行える。
From the above, the concentration meter 9 for the separation liquid and the optical color sensor 18 are used together, and the concentration of the separation liquid and the output voltage of the optical color sensor 18 exist within the appropriate range of the characteristic curve shown in FIG. By controlling the chemical addition amount by the control unit 19 as described above, automatic control for suppressing the chemical addition amount to the liquid to be treated within an appropriate range can be performed.

【0017】このように光学的色センサ18と濃度計9
とを用いて薬品の過剰添加を防止し、適正薬品量におけ
る分離液状態の計測が可能になり、分離液濃度を指標と
する遠心脱水機1の自動制御が可能となった。
Thus, the optical color sensor 18 and the densitometer 9 are
It was possible to prevent the excessive addition of chemicals by using, and to measure the state of the separated liquid at an appropriate amount of chemical, and it became possible to automatically control the centrifugal dehydrator 1 using the concentration of the separated liquid as an index.

【0018】[0018]

【発明の効果】以上のようにこの発明によれば被処理液
を固液分離する遠心脱水機から生成される分離液の濃度
を濃度計により計測すると共に、上記分離液の泡の色を
光学的色センサにより計測するもので、上記濃度計で計
測した濃度計測値と光学的色センサで計測した分離液の
泡の色計測値とから被処理液に対する薬品添加量の多少
を判断するように構成したので、薬品添加量が過少か過
剰かを判断して被処理液に対する薬品添加量を自動調整
させることができるという効果がある。
As described above, according to the present invention, the concentration of the separated liquid produced from the centrifugal dehydrator for solid-liquid separation of the liquid to be treated is measured by a densitometer, and the color of bubbles in the separated liquid is optically measured. It is measured by a static color sensor, and it is possible to judge the amount of chemicals added to the liquid to be treated from the concentration measurement value measured by the above densitometer and the color measurement value of the bubbles of the separation liquid measured by the optical color sensor. Since it is configured, there is an effect that it is possible to automatically adjust the chemical addition amount to the liquid to be treated by judging whether the chemical addition amount is too small or excessive.

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

【図1】この発明の一実施例による遠心脱水機の薬注率
制御装置を示す概略構成図である。
FIG. 1 is a schematic configuration diagram showing a chemical injection rate control device for a centrifugal dehydrator according to an embodiment of the present invention.

【図2】光学的色センサの出力電圧特性を示す特性曲線
図である。
FIG. 2 is a characteristic curve diagram showing an output voltage characteristic of an optical color sensor.

【図3】薬品添加量と分離液の泡の色度合との関係を示
す特性曲線図である。
FIG. 3 is a characteristic curve diagram showing the relationship between the amount of chemicals added and the chromaticity of bubbles in the separated liquid.

【図4】分離液濃度および光学的色センサに対する薬品
添加量を示す特性曲線図である。
FIG. 4 is a characteristic curve diagram showing the concentration of a separated liquid and the amount of chemicals added to an optical color sensor.

【図5】従来の遠心脱水機の薬注率制御装置の一例を示
す概略構成図である。
FIG. 5 is a schematic configuration diagram showing an example of a conventional chemical injection rate control device for a centrifugal dehydrator.

【図6】分離液濃度と薬品添加量との関係を示す特性曲
線図である。
FIG. 6 is a characteristic curve diagram showing the relationship between the concentration of separated liquid and the amount of chemicals added.

【符号の説明】[Explanation of symbols]

1 遠心脱水機 9 濃度計 18 光学的色センサ 19 制御部(判断手段) 1 Centrifugal dehydrator 9 Densitometer 18 Optical color sensor 19 Control unit (determination means)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 薬品を遠心脱水機内に注入して被処理液
を固液分離して分離液と脱水ケーキとを生成するための
遠心脱水機の薬注率制御装置において、上記遠心脱水機
から生成される分離液の濃度を計測する濃度計と、上記
分離液の泡の色を計測する光学的色センサと、上記濃度
計で計測した濃度計測値と光学的色センサで計測した分
離液の泡の色計測値とから被処理液に対する薬品添加量
の多少を判断する判断手段とを備えた遠心脱水機の薬注
率制御装置。
1. A chemical injection rate control device for a centrifugal dehydrator for injecting a chemical into a centrifugal dehydrator to perform solid-liquid separation of a liquid to be treated to produce a separated liquid and a dehydrated cake. A densitometer that measures the concentration of the generated separation liquid, an optical color sensor that measures the color of the bubbles in the separation liquid, and a concentration measurement value measured by the densitometer and the separation liquid measured by the optical color sensor. A chemical injection rate control device for a centrifugal dehydrator, comprising a determination means for determining the amount of a chemical added to a liquid to be treated based on the color measurement value of bubbles.
JP3358136A 1991-12-27 1991-12-27 Centrifugal dehydrator chemical injection rate controller Expired - Fee Related JPH0829268B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3358136A JPH0829268B2 (en) 1991-12-27 1991-12-27 Centrifugal dehydrator chemical injection rate controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3358136A JPH0829268B2 (en) 1991-12-27 1991-12-27 Centrifugal dehydrator chemical injection rate controller

Publications (2)

Publication Number Publication Date
JPH05177153A JPH05177153A (en) 1993-07-20
JPH0829268B2 true JPH0829268B2 (en) 1996-03-27

Family

ID=18457733

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3358136A Expired - Fee Related JPH0829268B2 (en) 1991-12-27 1991-12-27 Centrifugal dehydrator chemical injection rate controller

Country Status (1)

Country Link
JP (1) JPH0829268B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3565944B2 (en) * 1995-05-08 2004-09-15 株式会社西原環境テクノロジー Separated liquid monitoring device
CN112403693B (en) * 2019-08-23 2022-06-03 石小和 Three-phase separator

Also Published As

Publication number Publication date
JPH05177153A (en) 1993-07-20

Similar Documents

Publication Publication Date Title
US4964728A (en) Blood coagulation time measuring device
US5037559A (en) Process for conditioning and dewatering sludges
EP0526860A2 (en) Control device for washing machine
FR2476343A1 (en) METHOD AND DEVICE FOR ADJUSTING THE ROTATION SPEED DIFFERENCE OF TWO WORKPIECES WHICH ROTATE AT DIFFERENT RATES, ESPECIALLY A CENTRIFUGAL DRUM AND A CONTINUOUS SCREW OF A CENTRIFUGE
GB1583517A (en) Solid bowl decanter centrifuges of the scroll discharge type
JP3731292B2 (en) Operation control method of sludge centrifugal dehydrator
JPH0829268B2 (en) Centrifugal dehydrator chemical injection rate controller
CN113265833A (en) Washing control method of washing machine
JP2532988B2 (en) Dry cleaner turbidity detector
JP3346055B2 (en) Automatic bread maker
JPH11138030A (en) Rice mill control device
JPS6097858A (en) Waste ink tank
JPH06105985A (en) Washing machine
JPH0625747U (en) Sludge concentration measuring device
KR960014249B1 (en) How to detect the amount of washing machine
JPH0699104A (en) Clogging inclination judging device of discharge control valve in horizontal centrifugal concentrator
JP2897902B2 (en) Abnormality determination device for concentration meter in horizontal centrifugal concentrator
JPH0368500A (en) Method for controlling rate of addition of polymer flocculant
JPH0323304B2 (en)
JPS62102848A (en) Torque control method for decanter centrifuge
JP3016327B2 (en) Control method of coagulation mixing tank
JPS60206458A (en) Centrifugal separator
JPH0688002B2 (en) Centrifugal concentrator
KR900006916B1 (en) Washing machine
JPS57105579A (en) Operation control device for blower

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees