JPH10151370A - Method of controlling centrifugal dehydrator - Google Patents

Method of controlling centrifugal dehydrator

Info

Publication number
JPH10151370A
JPH10151370A JP8326157A JP32615796A JPH10151370A JP H10151370 A JPH10151370 A JP H10151370A JP 8326157 A JP8326157 A JP 8326157A JP 32615796 A JP32615796 A JP 32615796A JP H10151370 A JPH10151370 A JP H10151370A
Authority
JP
Japan
Prior art keywords
screw conveyor
centrifugal dehydrator
separated liquid
speed difference
turbidity
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
JP8326157A
Other languages
Japanese (ja)
Inventor
Noboru Suzuki
鈴木  登
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP8326157A priority Critical patent/JPH10151370A/en
Publication of JPH10151370A publication Critical patent/JPH10151370A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To make operation control easy by detecting turbidity of separated liquid and accordingly, automatically control the difference of rotational speed between a bowl and a screw conveyor. SOLUTION: When subjecting sludge to solid-liquid separation by a centrifugal dehydrator 1 containing a screw conveyor 4 rotated with relative speed difference between it and a bowl 3, separated liquid from the centrifugal dehydrator 1 is put in a separated liquid tank 15 provided with a turbid meter 16, and the turbidity of the separated liquid is measured there, and based on the result, the rotation of a hydraulic motor 9 for sending oil to a differential speed device 8 for controlling the rotation of the screw conveyor 4 is automatically controlled to always control the rotational speed difference between the bowl 3 and the screw conveyor 1 to an optimum state.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、下水等の汚泥を遠心脱
水する場合において、排出された分離液の濁度に応じて
運転の制御を行う方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling the operation of sludge such as sewage in accordance with the turbidity of a discharged separated liquid when centrifugally dewatering the sludge.

【0002】[0002]

【従来の技術】水処理過程で発生する汚泥は、一般に、
濃縮→(消化)→脱水→焼却等の各工程を経て処理され
ている。このうち、脱水処理にはフィルタープレス法、
ベルトプレス法、遠心脱水法が多く用いられている。
2. Description of the Related Art Sludge generated in a water treatment process is generally
It is processed through each process such as concentration → (digestion) → dehydration → incineration. Of these, the filter press method is used for the dehydration treatment,
A belt press method and a centrifugal dehydration method are often used.

【0003】遠心脱水法には、標準型と高効率型とがあ
り、標準型は差速一定、高効率型はケーキ搬送トルクを
検知して差速を変化させることにより、標準型よりも高
い脱水性があり、また、ある程度の汚泥性状の変動に対
しても追従できることが特徴となっている。
The centrifugal dewatering method includes a standard type and a high-efficiency type. The standard type has a constant differential speed, and the high-efficiency type detects a cake conveying torque to change the differential speed, thereby increasing the differential speed. It is characterized by being dehydrated and capable of following a certain degree of change in sludge properties.

【0004】[0004]

【発明が解決しようとする課題】しかし、上記高効率型
による遠心脱水においても、汚泥性状の変動が許容範囲
を越えた場合や、遠心脱水機の立ち上げ時には、人が分
離液の状態を見ながら運転条件を設定する必要があるた
め、常に運転状況を確認しなければならず、制御に熟練
を要し、制御操作が面倒なものであった。
However, even in the above-mentioned high-efficiency centrifugal dehydration, when fluctuations in sludge properties exceed an allowable range or when the centrifugal dehydrator is started, a person checks the state of the separated liquid. However, since it is necessary to set operating conditions, it is necessary to constantly check the operating conditions, which requires skill in control and complicates the control operation.

【0005】本発明は、上記従来の問題点を解決するた
めになされたもので、分離液の濁度を検出し、それに応
じて、ボウルとスクリューコンベアの回転差速を自動的
に制御できるようにし、運転管理の容易化と脱水効率の
向上と安定した固液分離が図れるようにしようとするも
のである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned conventional problems, and is intended to detect the turbidity of a separated liquid and automatically control the rotational speed difference between a bowl and a screw conveyor accordingly. It is intended to facilitate operation management, improve dewatering efficiency, and achieve stable solid-liquid separation.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
めの本発明の構成について、実施例に対応する図面を参
照して説明すると、本発明は、高速回転されるボール3
内に、このボール3と相対速度差をもって回転されるス
クリューコンベア4を収容した遠心脱水機1により、汚
泥の固液分離を行うにあたって、遠心脱水機1より排出
される分離液の濁度を測定し、その測定値に基づいて、
スクリューコンベア4に相対速度差を付与する差速装置
8に送油する油圧モータ9の回転を自動的に制御するこ
とを特徴とするものである。
The configuration of the present invention for achieving the above object will be described with reference to the drawings corresponding to the embodiments.
The turbidity of the separated liquid discharged from the centrifugal dehydrator 1 is measured when the solid-liquid separation of the sludge is performed by the centrifugal dehydrator 1 containing the screw conveyor 4 rotated at a relative speed difference from the ball 3. And based on that measurement,
It is characterized in that the rotation of a hydraulic motor 9 that feeds oil to a speed difference device 8 that gives a relative speed difference to the screw conveyor 4 is automatically controlled.

【0007】[0007]

【発明の実施の形態】以下、本発明の実施の形態につい
て図面を参照して説明する。図において、1は横型の遠
心脱水機で、従来公知のように、ケーシング2の中にボ
ウル3と、中空の回転軸5の外周にスクリュー6を有す
るスクリューコンベア4が納められており、ボウル3は
ケーシング2の先端側に設けられた主モータ7によって
高速で回転し、スクリューコンベア4は、同じくケーシ
ング2の先端側に設けられた差速装置8を介して、ボウ
ル3とわずかな相対速度差(差速)をもって回転される
ようになっている。そして、差速装置8はこれに油を送
る油圧モータ9によって制御されるようになっている。
Embodiments of the present invention will be described below with reference to the drawings. In the figure, reference numeral 1 denotes a horizontal centrifugal dehydrator. As is conventionally known, a bowl 3 and a screw conveyor 4 having a screw 6 on the outer periphery of a hollow rotary shaft 5 are housed in a casing 2 as conventionally known. Is rotated at a high speed by a main motor 7 provided on the tip side of the casing 2, and the screw conveyor 4 is slightly rotated by the speed difference device 8 provided on the tip side of the casing 2. (Differential speed). The speed difference device 8 is controlled by a hydraulic motor 9 that sends oil thereto.

【0008】汚泥は、汚泥タンク10に貯留され、これよ
り汚泥供給ポンプ11によって遠心脱水機1へと供給され
る。このとき、薬品溶解タンク12で溶解された凝集剤が
薬品供給ポンプ13によって供給され、汚泥は凝集して分
離しやすい状態となる。脱水された汚泥は、遠心脱水機
1の先端部より機外に排出され、ケーキ搬送設備14によ
って系外に搬出される。他方、分離液は遠心脱水機1の
基端部から取り出され、一度、分離液タンク15に貯留さ
れてから系外に排出される。
The sludge is stored in a sludge tank 10 and supplied to the centrifugal dehydrator 1 by a sludge supply pump 11. At this time, the coagulant dissolved in the chemical dissolution tank 12 is supplied by the chemical supply pump 13, and the sludge is coagulated and easily separated. The dewatered sludge is discharged out of the centrifugal dewatering machine 1 from the front end thereof, and is carried out of the system by the cake transport facility 14. On the other hand, the separated liquid is taken out from the base end of the centrifugal dehydrator 1 and once stored in the separated liquid tank 15 and then discharged out of the system.

【0009】遠心脱水機の運転においては、ボウル3と
スクリューコンベア4の差速を小さくしたときには、脱
水機内に汚泥が貯まり、圧密効果によって含水率の低い
脱水ケーキが排出される。しかし、差速を小さくしすぎ
ると分離性が悪くなり、分離液側に固形物が逃げるた
め、分離液が濁ることになる。これを回避するために
は、油圧モータ9の送油量を増大して差速を大きくして
やる必要がある。また、差速を大きくした場合は、脱水
機内の汚泥の通過が早くなるため分離液の濁度は低くな
るが、脱水ケーキの含水率は高くなる。このような場合
には、油圧モータ9の送油量を減少して差速を小さくし
てやる必要がある。
In the operation of the centrifugal dehydrator, when the speed difference between the bowl 3 and the screw conveyor 4 is reduced, sludge is accumulated in the dehydrator, and a dewatered cake having a low water content is discharged due to the consolidation effect. However, if the differential speed is too small, the separation property deteriorates, and solids escape to the separation liquid side, so that the separation liquid becomes turbid. In order to avoid this, it is necessary to increase the oil supply amount of the hydraulic motor 9 to increase the speed difference. In addition, when the differential speed is increased, the turbidity of the separated liquid decreases because the sludge passes through the dehydrator faster, but the water content of the dehydrated cake increases. In such a case, it is necessary to reduce the difference in speed by reducing the oil supply amount of the hydraulic motor 9.

【0010】本発明では、上記分離液タンク15に濁度計
16を設置し、分離液の濁度を測定する。そして、その濁
度の測定値に基づいて、差速装置8に油を送る油圧モー
タ9を自動的に制御するのである。すなわち、濁度計16
には濁度規定値が設定できるようになっており、測定さ
れた濁度がその規定値よりも高いときは、油圧モータ9
の回転数を増大して差速装置8への送油量を増大し、差
速を大きくし、逆に測定された濁度が規定値よりも低い
場合には、油圧モータ9の回転数を減少して差速装置8
への送曲量を少なくし、差速を小さくするのである。
In the present invention, the turbidity meter is
Set 16 and measure the turbidity of the separated solution. Then, based on the measured value of the turbidity, the hydraulic motor 9 for feeding oil to the speed difference device 8 is automatically controlled. That is, the turbidity meter 16
The turbidity specified value can be set in the hydraulic motor 9 when the measured turbidity is higher than the specified value.
When the measured turbidity is lower than the specified value, the rotational speed of the hydraulic motor 9 is increased. Reduced speed difference device 8
The amount of music to be transmitted is reduced, and the speed difference is reduced.

【0011】[0011]

【発明の効果】以上説明したように、本発明によれば、
遠心脱水機より排出された分離液の濁度を検知し、その
測定結果に基づいて、差速装置へ送油する油圧モータを
制御することにより、脱水ケーキ含水率を低く保つこと
ができるとともに、分離液濁度を低くおさえることがで
きて、水処理への返流水負荷を少なくできる。また、ボ
ウルとスクリューコンベアとの差速に係る運転条件が自
動的に変更、設定できるので、運転管理が熟練を要さず
容易にでき、遠心脱水機の処理効率の向上が図れる。
As described above, according to the present invention,
By detecting the turbidity of the separated liquid discharged from the centrifugal dehydrator and controlling the hydraulic motor that feeds the oil to the speed difference device based on the measurement result, the water content of the dewatered cake can be kept low, Separation liquid turbidity can be kept low, and the return water load to water treatment can be reduced. In addition, since the operating conditions relating to the speed difference between the bowl and the screw conveyor can be automatically changed and set, operation management can be easily performed without skill, and the processing efficiency of the centrifugal dehydrator can be improved.

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

【図1】本発明の一実施例を示した説明図である。FIG. 1 is an explanatory diagram showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 遠心脱水機 2 ケーシング 3 ボウル 4 スクリューコンベア 7 主モータ 8 差速装置 9 油圧モータ 10 汚泥タンク 11 汚泥供給ポンプ 12 薬品溶解タンク 13 薬品供給ポンプ 15 分離液タンク 16 濁度計 DESCRIPTION OF SYMBOLS 1 Centrifugal dehydrator 2 Casing 3 Bowl 4 Screw conveyor 7 Main motor 8 Differential speed device 9 Hydraulic motor 10 Sludge tank 11 Sludge supply pump 12 Chemical dissolution tank 13 Chemical supply pump 15 Separation liquid tank 16 Turbidity meter

Claims (1)

【特許請求の範囲】[Claims] 高速回転されるボール内に、このボールと相対速度差を
もって回転されるスクリューコンベアを収容した遠心脱
水機により、汚泥の固液分離を行うにあたって、遠心脱
水機より排出される分離液の濁度を測定し、その測定値
に基づいて、スクリューコンベアに相対速度差を付与す
る差速装置に送油する油圧モータの回転を自動的に制御
することを特徴とする、遠心脱水機の制御方法。
In a high-speed rotating ball, a centrifugal dehydrator containing a screw conveyor rotated with a relative speed difference from this ball, when performing solid-liquid separation of sludge, the turbidity of the separated liquid discharged from the centrifugal dehydrator A method for controlling a centrifugal dehydrator, comprising measuring and automatically controlling the rotation of a hydraulic motor that feeds oil to a speed difference device that gives a relative speed difference to a screw conveyor based on the measured value.
JP8326157A 1996-11-21 1996-11-21 Method of controlling centrifugal dehydrator Pending JPH10151370A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8326157A JPH10151370A (en) 1996-11-21 1996-11-21 Method of controlling centrifugal dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8326157A JPH10151370A (en) 1996-11-21 1996-11-21 Method of controlling centrifugal dehydrator

Publications (1)

Publication Number Publication Date
JPH10151370A true JPH10151370A (en) 1998-06-09

Family

ID=18184695

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8326157A Pending JPH10151370A (en) 1996-11-21 1996-11-21 Method of controlling centrifugal dehydrator

Country Status (1)

Country Link
JP (1) JPH10151370A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100400404B1 (en) * 2000-12-28 2003-10-10 주식회사 로얄정공 centrifugal enriched sinking set adhered sludge discharge automatic controller
KR100531511B1 (en) * 2003-02-28 2005-11-28 주식회사 무한기술 The eddy current coupling variable speed brake of a centrifuge screw decanter
JP2007152344A (en) * 2005-11-08 2007-06-21 Zenitaka Corp Powder muddy water treatment agent, muddy water dehydrating method, and muddy water volume-reduction device
KR100794850B1 (en) 2006-01-20 2008-01-15 문일성 Hydroextractor using rotation speed difference for drum screen and screw
CN102612411A (en) * 2009-10-29 2012-07-25 阿尔法拉瓦尔股份有限公司 A centrifugal separator
CN103191835A (en) * 2013-02-23 2013-07-10 仙桃市中星电子材料有限公司 Titanium tetrachloride slag-liquid separation centrifugal machine
WO2013183287A1 (en) * 2012-06-05 2013-12-12 巴工業株式会社 Centrifugal separation device
CN115318453A (en) * 2022-07-27 2022-11-11 扬州工业职业技术学院 Processing apparatus of oiliness solid waste

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100400404B1 (en) * 2000-12-28 2003-10-10 주식회사 로얄정공 centrifugal enriched sinking set adhered sludge discharge automatic controller
KR100531511B1 (en) * 2003-02-28 2005-11-28 주식회사 무한기술 The eddy current coupling variable speed brake of a centrifuge screw decanter
JP2007152344A (en) * 2005-11-08 2007-06-21 Zenitaka Corp Powder muddy water treatment agent, muddy water dehydrating method, and muddy water volume-reduction device
KR100794850B1 (en) 2006-01-20 2008-01-15 문일성 Hydroextractor using rotation speed difference for drum screen and screw
CN102612411A (en) * 2009-10-29 2012-07-25 阿尔法拉瓦尔股份有限公司 A centrifugal separator
WO2013183287A1 (en) * 2012-06-05 2013-12-12 巴工業株式会社 Centrifugal separation device
CN103191835A (en) * 2013-02-23 2013-07-10 仙桃市中星电子材料有限公司 Titanium tetrachloride slag-liquid separation centrifugal machine
CN115318453A (en) * 2022-07-27 2022-11-11 扬州工业职业技术学院 Processing apparatus of oiliness solid waste

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