JPS6125478B2 - - Google Patents

Info

Publication number
JPS6125478B2
JPS6125478B2 JP58005878A JP587883A JPS6125478B2 JP S6125478 B2 JPS6125478 B2 JP S6125478B2 JP 58005878 A JP58005878 A JP 58005878A JP 587883 A JP587883 A JP 587883A JP S6125478 B2 JPS6125478 B2 JP S6125478B2
Authority
JP
Japan
Prior art keywords
belt
sludge
amount
flocculant
liquid level
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
Application number
JP58005878A
Other languages
Japanese (ja)
Other versions
JPS59133996A (en
Inventor
Hajime Sato
Kazuyuki Nishida
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.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha 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 Mitsubishi Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP587883A priority Critical patent/JPS59133996A/en
Publication of JPS59133996A publication Critical patent/JPS59133996A/en
Publication of JPS6125478B2 publication Critical patent/JPS6125478B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/24Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)

Description

【発明の詳細な説明】 本発明は、上水・下水・産業廃水等の水処理に
おいて発生する汚泥を脱水処理するベルトプレス
型脱水装置の制御方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling a belt press type dewatering apparatus for dewatering sludge generated in the treatment of water such as tap water, sewage, and industrial wastewater.

ベルトプレス型脱水装置では、汚泥と高分子凝
集剤を均一混合撹拌し、凝集汚泥をつくる凝集部
を前段とし、前記凝集汚泥を走行する一枚の無端
布ベルト上で重力により脱水する重力脱水部
と、該重力脱水部で得られた汚泥を前記無端布
ベルトと該ベルトと対向して平行に設けた上部走
行無端布ベルトとの2枚のベルトに狭みこみ複
数のロール間を走行することにより圧縮と剪断力
により更に脱水する加圧脱水部とを設けている。
このベルトプレス型脱水装置は、運転操作が簡単
で維持管理が容易であり、又少ない凝集剤の使用
で固形分回収率高く、脱水効果が高い等のため近
年急速に普及してきている。前記装置の重力脱水
部では、供給した汚泥を全量処理しなければ、ベ
ルトサイドからのはみ出し等が生じ性能を充分発
揮させることができないため公知のこの種装置で
は凝集剤供給量を処理量に基づいて決定し凝集剤
を自動的に一定量供給し、最適な凝集フロツクを
形成させている。しかし、汚泥の性状等に変動を
生じた場合凝集剤量の過不足が生じ凝集不完全と
なりベルトサイドの汚泥のはみ出しや液の濁り
等が発生し、固形分回収率も悪くなる。このた
め、汚泥性状の変動等が多い場合には自動運転が
むずかしい欠点が有る。本発明はこのような事情
に鑑みてなされたものであり、前記欠点を取り除
き最適な運転条件を維持して自動運転を可能なら
しめる制御方法を提供するものでその要旨とする
ところは、無端の布ベルトを複数のロール間を
送行するよう張設し、重力脱水部と加圧脱水部を
設け、且つ制御回路を夫々具備する凝集剤供給装
置、無端ベルト送行駆動装置及び原液供給装置を
備えたベルトプレス型脱水装置の制御方法におい
て、前記重力脱水部に汚泥液面の検出手段を設
け、汚泥液面が一定となるよう前記検出手段から
の出力信号によつて凝集剤供給量、無端ベルト送
行速度及び原液供給量とを該順序で順次調節すべ
く前記制御回路を作動することを特徴とするベル
トプレス型脱水装置の制御方法である。
In a belt press type dewatering device, the first stage is a flocculating section that uniformly mixes and stirs sludge and a polymer flocculant to create flocculated sludge, and the gravity dewatering section that dewaters the flocculated sludge by gravity on a running endless cloth belt. Then, the sludge obtained in the gravity dewatering section is squeezed between two belts, the endless cloth belt and an endless cloth belt running at the top, which is provided in parallel with the belt, and the sludge is passed between a plurality of rolls. A pressurized dehydration section is provided for further dehydration by compression and shear force.
This belt press type dewatering apparatus has become rapidly popular in recent years because it is easy to operate, easy to maintain, and uses a small amount of flocculant, has a high solid content recovery rate, and has a high dewatering effect. In the gravity dewatering section of the device, unless the entire amount of supplied sludge is treated, the sludge may protrude from the belt side and the performance cannot be fully demonstrated. A certain amount of flocculant is automatically supplied based on the determined amount, forming an optimal flocculation floc. However, if there is a change in the properties of the sludge, the amount of flocculant may be too much or insufficient, resulting in incomplete flocculation, causing sludge to protrude from the belt side, turbidity of the liquid, etc., and the solids recovery rate to deteriorate. For this reason, there is a drawback that automatic operation is difficult when there are many variations in sludge properties. The present invention has been made in view of these circumstances, and provides a control method that eliminates the above-mentioned drawbacks, maintains optimal operating conditions, and enables automatic driving. A cloth belt is stretched so as to be conveyed between a plurality of rolls, and a gravity dehydration section and a pressure dehydration section are provided, and a flocculant supply device, an endless belt conveyance drive device, and a stock solution supply device each having a control circuit are provided. In a method for controlling a belt press type dewatering device, a means for detecting a sludge liquid level is provided in the gravity dewatering section, and the flocculant supply amount and endless belt feeding are controlled based on an output signal from the detecting means so that the sludge liquid level is constant. This is a method of controlling a belt press type dewatering apparatus, characterized in that the control circuit is operated to sequentially adjust the speed and the amount of stock solution supplied in the above order.

本発明の一実施例を図面に基づいて記述する。
第一図は本発明に係る一実施例の系統図である。
1は下水汚泥等の原液Aを定量供給する原液供給
装置、2は高分子凝集剤等の凝集剤Bを定量供給
する凝集剤供給装置、3は前記装置、1,2から
供給された汚泥と凝集剤を頂部に取り付けた撹拌
機により均一に混合し汚泥の凝集を計る凝集混和
槽、4は後記の重力脱水部4′と加圧脱水部4″を
設け汚泥を脱水処理するベルトプレス型脱水機、
4′は凝集混和槽3から導入される凝集汚泥を走
行する一枚の無端布ベルト5上で重力により脱
水する重力脱水部、4″は脱水汚泥を前記無端
布ベルト5と対向して平行に設けた上部走行無端
布6との2枚のベルトに狭みこみ複数のロール
間を走行することにより圧縮と剪断力により更に
脱水する加圧脱水部、5,6はナイロンやポリエ
ステル等の合成繊維等で織られた一定巾で帯上の
布ベルトでありロール間に無端に張設され駆動
装置7により矢印方向に一定速度で走行する。7
は布ベルト5,6の布ベルト駆動装置、8は
重力脱水部4′の布ベルト5を底面として凝集
汚泥を受け入れ滞留させる汚泥受槽、9は布ベ
ルト5,6に狭まれて送行してきた汚泥を徐々に
低圧で圧搾する大径の低圧ロール、10は更に高
圧の圧搾力をかけるために設けた小径のプレスロ
ールで複数個で構成されており前記布ベルト
5,6がロール間を走行することによりケーキに
剪断力を伴う圧力をかけている。11,11′は
布ベルト5,6の駆動ロールであり布を反転
させスクレーパ17により脱水汚泥の剥離を行い
脱水ケーキCとして系外へ排出する。12は過
された液を集液する集液器である。集液された
液Dは抜き出され系外へ排出される。このよう
な公知のベルトプレス型脱水装置の重力脱水部
4′に設けた汚泥受槽8に液面検出手段として、
信号発信回路を設けた液面制御計13を設置し、
汚泥の液面高さを連続的に検出し各制御回路1
5,16,14へ順次信号を発することにより常
に最適運転がされるようなされている。以上の様
な構成のベルトプレス型脱水装置において汚泥受
槽8中の汚泥液面が凝集剤の添加量が不足したた
めに設定された一定の高さを越えた場合について
記述すると、液面制御計13から凝集剤供給装置
2の供給量制御回路15に信号を出力し供給装置
2の回転数を増大させることにより供給量を比例
して増大し、一定時間経過しても液面が下がらな
い場合には無端ベルト走行駆動装置7の回転速度
制御回路16に信号を出力し駆動装置7の回転数
を増大させることにより布ベルト5,6の走行
速度を増大させ、更にその後一定時間経過しても
改善が見られない場合には原液供給装置1の供給
量制御回路14に信号を出力し供給装置1の回転
数を減少させることにより原液供給量を減少させ
る。必要であれば警報器を取り付け警報を発する
ようにしてもよい。以上の操作によつても改善で
きない場合には原液、凝集剤の供給を停止し、一
定時間経過後附属関連機器を含め全系を停止す
る。又上記は汚泥受槽8中の汚泥の液面高さを連
続的に検知して信号を出力し、各制御回路15,
16,14を順次を連続的に切り換えているが凝
集剤供給量を増加し、一定時間経過しても液面が
下がらない場合更に凝集剤供給量を増加し、それ
でも改善がみられない場合更に凝集剤供給量を増
加するというように液面制御計13からの信号に
より各制御回路15,16,14を順次段階的に
切り換えてもよく、又他の実施例では上記とは逆
に汚泥受槽8の汚泥の液面が設定された一定の高
さ以下になつた場合には、凝集剤供給量を比例し
て減少させ最適の凝集剤量として運転することも
できる。
An embodiment of the present invention will be described based on the drawings.
FIG. 1 is a system diagram of an embodiment according to the present invention.
1 is a stock solution supply device that supplies a fixed amount of stock solution A such as sewage sludge, 2 is a flocculant supply device that supplies a fixed amount of flocculant B such as a polymer flocculant, and 3 is the sludge supplied from the devices 1 and 2. A flocculation mixing tank that uniformly mixes flocculant with a stirrer attached to the top and measures the flocculation of sludge, and 4 is a belt press type dewatering device that is equipped with a gravity dewatering section 4' and a pressure dewatering section 4'', which will be described later, to dewater the sludge. machine,
4' is a gravity dewatering section that dewaters the coagulated sludge introduced from the flocculation mixing tank 3 by gravity on a running endless cloth belt 5; A pressurized dehydration section which further dehydrates water by compression and shear force by being sandwiched between two belts with an upper running endless cloth 6 provided and running between a plurality of rolls, 5 and 6 are synthetic fibers such as nylon and polyester, etc. It is a cloth belt with a constant width woven with a belt, stretched endlessly between rolls, and run at a constant speed in the direction of the arrow by a drive device 7.
8 is a cloth belt drive device for the cloth belts 5 and 6; 8 is a sludge receiving tank in which the flocculated sludge is received and retained using the cloth belt 5 of the gravity dewatering section 4' as a bottom surface; 9 is a sludge conveyed between the cloth belts 5 and 6; The cloth belts 5 and 6 run between the rolls, and the fabric belts 5 and 6 run between the rolls. This applies shearing pressure to the cake. Reference numerals 11 and 11' denote drive rolls for the cloth belts 5 and 6, which invert the cloth, peel off the dehydrated sludge with a scraper 17, and discharge it as a dehydrated cake C out of the system. 12 is a liquid collector for collecting the filtered liquid. The collected liquid D is extracted and discharged outside the system. In the sludge receiving tank 8 provided in the gravity dewatering section 4' of such a known belt press type dewatering device, as a liquid level detection means,
A liquid level control meter 13 equipped with a signal transmission circuit is installed,
Each control circuit 1 continuously detects the liquid level of sludge.
Optimum operation is always performed by sequentially issuing signals to 5, 16, and 14. In the belt press type dewatering device having the above configuration, a case where the sludge liquid level in the sludge receiving tank 8 exceeds a predetermined height due to an insufficient amount of flocculant added will be described. outputs a signal to the supply amount control circuit 15 of the flocculant supply device 2 and increases the rotation speed of the supply device 2, thereby increasing the supply amount proportionally.If the liquid level does not drop even after a certain period of time, outputs a signal to the rotation speed control circuit 16 of the endless belt running drive device 7 to increase the number of rotations of the drive device 7, thereby increasing the running speed of the cloth belts 5, 6, and even after a certain period of time has elapsed, there is no improvement. If this is not observed, a signal is output to the supply amount control circuit 14 of the stock solution supply device 1 to reduce the number of rotations of the supply device 1, thereby reducing the stock solution supply amount. If necessary, an alarm may be installed to issue an alarm. If the above operations do not resolve the problem, stop supplying the stock solution and flocculant, and after a certain period of time, shut down the entire system including attached related equipment. In addition, the above system continuously detects the liquid level of sludge in the sludge receiving tank 8 and outputs a signal, and each control circuit 15,
16 and 14 in sequence, but if the flocculant supply rate is increased and the liquid level does not drop even after a certain period of time has passed, further increase the flocculant supply rate, and if no improvement is seen, further increase the flocculant supply rate. Each control circuit 15, 16, 14 may be switched in a stepwise manner in response to a signal from the liquid level controller 13 to increase the flocculant supply amount, or in other embodiments, the sludge receiving tank When the liquid level of the sludge in step 8 becomes below a predetermined height, the amount of flocculant supplied can be proportionally reduced to operate with the optimum amount of flocculant.

上水、下水、産業廃水等の水処理において発生
する汚泥を脱水処理するにあたつて上記のように
構成された本発明の制御機構を設けたベルトプレ
ス型脱水装置を用いて本発明の制御方法により汚
泥の脱水処理を行えば汚泥の性状等に変動を生じ
た場合でも凝集剤供給量が不足し汚泥の凝集が不
完全となりベルトサイドからの汚泥のはみ出し
や、液の濁り等が発生することもなく又装置を
完全自動化し無人運転可能ならしめる事ができる
ので産業上極めて有効な制御方法である。
When dewatering sludge generated in the treatment of water such as clean water, sewage, and industrial wastewater, the control of the present invention is carried out using a belt press type dehydrator equipped with the control mechanism of the present invention configured as described above. If sludge is dehydrated using this method, even if the properties of the sludge change, the amount of flocculant supplied will be insufficient and the flocculation of the sludge will be incomplete, resulting in sludge protruding from the belt side and turbidity of the liquid. This is an extremely effective control method industrially because it can completely automate the equipment and enable unmanned operation.

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

第1図は本発明に係る一実施例の系統図であ
る。 1:原液供給装置、2:凝集剤供給装置、3:
凝集混和槽、4:ベルトプレス型脱水機、4′:
重力脱水部、4″:加圧脱水部、5,6:布ベ
ルト、7:布ベルト駆動装置、8:汚泥受槽、
9:低圧ロール、10:プレスロール、11,1
1:駆動ロール、12:集液器、13:液面制御
計、14:原液供給量制御回路、15:凝集剤供
給量制御回路、16:回転速度制御回路、17:
スクレーパー、A:原液、B:凝集剤、C:脱水
ケーキ、D:液。
FIG. 1 is a system diagram of an embodiment according to the present invention. 1: Stock solution supply device, 2: Coagulant supply device, 3:
Coagulation mixing tank, 4: Belt press type dehydrator, 4':
Gravity dewatering section, 4'': Pressure dewatering section, 5, 6: Cloth belt, 7: Cloth belt drive device, 8: Sludge receiving tank,
9: Low pressure roll, 10: Press roll, 11,1
1: Drive roll, 12: Liquid collector, 13: Liquid level controller, 14: Stock solution supply amount control circuit, 15: Coagulant supply amount control circuit, 16: Rotation speed control circuit, 17:
Scraper, A: Stock solution, B: Coagulant, C: Dehydrated cake, D: Liquid.

Claims (1)

【特許請求の範囲】[Claims] 1 無端の布ベルトを複数のロール間を送行す
るよう張設し、重力脱水部と加圧脱水部を設け、
且つ制御回路を夫々具備する凝集剤供給装置、無
端ベルト送行駆動装置及び原液供給装置を備えた
ベルトプレス型脱水装置の制御方法において、前
記重力脱水部に汚泥液面の検出手段を設け、汚泥
液面が一定となるよう前記検出手段からの出力信
号によつて凝集剤供給量、無端ベルト送行速度及
び原液供給量とを該順序で順次調節すべく前記制
御回路を作動することを特徴とするベルトプレス
型脱水装置の制御方法。
1. An endless cloth belt is stretched between multiple rolls, and a gravity dehydration section and a pressure dehydration section are provided.
In the method for controlling a belt press type dewatering device including a flocculant supply device, an endless belt conveyance drive device, and a stock solution supply device each having a control circuit, a means for detecting a sludge liquid level is provided in the gravity dewatering section, and the sludge liquid level is The belt is characterized in that the control circuit is operated to sequentially adjust the amount of coagulant supplied, the endless belt feeding speed, and the amount of stock solution supplied in this order based on the output signal from the detection means so that the surface of the belt is constant. Control method for press type dewatering equipment.
JP587883A 1983-01-19 1983-01-19 Belt press type dehydrator Granted JPS59133996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP587883A JPS59133996A (en) 1983-01-19 1983-01-19 Belt press type dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP587883A JPS59133996A (en) 1983-01-19 1983-01-19 Belt press type dehydrator

Publications (2)

Publication Number Publication Date
JPS59133996A JPS59133996A (en) 1984-08-01
JPS6125478B2 true JPS6125478B2 (en) 1986-06-16

Family

ID=11623161

Family Applications (1)

Application Number Title Priority Date Filing Date
JP587883A Granted JPS59133996A (en) 1983-01-19 1983-01-19 Belt press type dehydrator

Country Status (1)

Country Link
JP (1) JPS59133996A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0240880U (en) * 1988-09-14 1990-03-20

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AUPQ083599A0 (en) * 1999-06-08 1999-07-01 Technological Resources Pty Limited Direct smelting vessel
US7964105B2 (en) * 2008-08-07 2011-06-21 William Harris Moss Method for improving belt press dewatering
JP4849383B2 (en) * 2008-09-17 2012-01-11 株式会社石垣 Operation control method for belt type concentrator

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5546267U (en) * 1978-09-22 1980-03-26
JPS5670811A (en) * 1979-11-13 1981-06-13 Kubota Ltd Dehydrator
JPS5946719B2 (en) * 1980-02-08 1984-11-14 株式会社クボタ Dehydration equipment
JPS56111595A (en) * 1980-02-08 1981-09-03 Kubota Ltd Dehydrating device
JPS5731449A (en) * 1980-07-31 1982-02-19 Kouka Kuroomu Kogyo Kk Mold for continuous casting of steel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0240880U (en) * 1988-09-14 1990-03-20

Also Published As

Publication number Publication date
JPS59133996A (en) 1984-08-01

Similar Documents

Publication Publication Date Title
US3531404A (en) Sewage treatment system
US4792406A (en) Method for dewatering a slurry using a twin belt press with cationic amine salts
JPS6363310B2 (en)
JP2689366B2 (en) Portable turbid water treatment device
JP4253353B1 (en) Sludge dewatering method and system
NO159787B (en) PROCEDURE FOR TREATING WATERLY OIL SLAY IN A DOUBLE SILVER PRESSURE.
US4062779A (en) Apparatus for thickening and extracting the liquid from a sludge
JPS6125478B2 (en)
JP5041299B2 (en) Operation control method of screw press connected to rotary concentrator
KR20100059094A (en) An apparatus and method of dehydrate in concentration sludge
JP2010247044A5 (en)
JP5481654B2 (en) Sludge treatment method and treatment system
JP4129479B1 (en) Sludge treatment method and treatment system
JPH11254000A (en) Method and apparatus for concentrating dehydration
JP4310863B2 (en) Sludge dewatering equipment
CN2469977Y (en) Predewatering-dewatering integral belt-type press filter
JP2000334600A (en) Automatic screen cleaning method for screw press type dehydrator
JPS6034331Y2 (en) sludge dehydrator
JP2001070997A (en) Treatment method of filtrate and washing wastewater in sludge dewatering machine
JPH063500U (en) Sludge dewatering device
JPS6047040B2 (en) Sludge dewatering equipment
CN213537687U (en) A rotary drum concentration and dehydration integrated device and processing system
JP2000301200A (en) Sludge dehydrating treatment method and apparatus
JP2000262817A (en) Waste liquid treatment equipment
JP2008221115A (en) Filtration concentrator