JPS59133996A - Belt press type dehydrator - Google Patents

Belt press type dehydrator

Info

Publication number
JPS59133996A
JPS59133996A JP587883A JP587883A JPS59133996A JP S59133996 A JPS59133996 A JP S59133996A JP 587883 A JP587883 A JP 587883A JP 587883 A JP587883 A JP 587883A JP S59133996 A JPS59133996 A JP S59133996A
Authority
JP
Japan
Prior art keywords
sludge
control circuit
liquid
feed rate
flocculating agent
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.)
Granted
Application number
JP587883A
Other languages
Japanese (ja)
Other versions
JPS6125478B2 (en
Inventor
Hajime Sato
佐藤 ▲肇▼
Kazuyuki Nishida
西田 和幸
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

Abstract

PURPOSE:To provide a titled device which maintains an optimum condition according to the fluctuation in the characteristic of sludge and permits automatic operation by the constitution wherein the feed rate of a raw liquid, the feed rate of a flocculating agent and the speed of filter cloth belts are controlled by the output signal from a liquid level detecting means provided in a gravity dehydrating part. CONSTITUTION:A liquid level controller 13 is provided to a sludge receiving tank 8 in a gravity dehydrating part 4' to detect continuously the liquid height of sludge in a belt press type dehydrator which extends and runs endless filter cloth belts 5, 6 between a low pressure roll 9 and a press roll 10, introduces a raw liquid A mixed with a flocculating agent B through a flocculating and mixing tank 3 into the part 4' and a pressure dehydrating part 4'' and separates the liquid to dehydrated cake C and filtrate D. The controller outputs a control signal according to the detected value to control a flocculating agent feeder 2 via a control circuit 15 thereby adjusting the feed rate of the flocculating agent. A driving device 7 for the filter cloth belts is also controlled via a control circuit 16 for rotating speed. A raw liquid feeder 1 is further controlled via a control circuit 14 according to need to adjust the feed rate of the raw liquid.

Description

【発明の詳細な説明】 一本発明は、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に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to 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
−混合攪秤し、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ン戸布ベルト上で重力
(こよりIR水する重力IR木部と、該重力脱水部で得
られた汚泥を前菖己無端炉布ベルトと該ベルトと対向し
て平行ζこ設番すた上部走行無端炉布ベルトとの2枚の
ベルト(こ挟みこみ複数のロール間を走行すること【こ
より圧縮と剪断力により更(こ脱水する加圧N免水部と
を設けている。このベルトプレス型脱水装置(よ、運転
操作が簡単で維持管理力す容易であり、又少ない凝集剤
の使用で固形分回収車高<、II免氷水効果高い等のた
め近年急速ζこ普及してきてし)る。
In a belt press type dewatering device, sludge and a polymer flocculant are uniformly mixed and weighed, and a flocculation section that creates flocculated sludge is the first stage. The gravity IR wood section that carries IR water, the sludge obtained in the gravity dewatering section, is separated by two sheets: an endless furnace cloth belt that runs on the front side, and an endless furnace cloth belt that runs parallel to the top and runs parallel to the belt. This belt press type dewatering device (which runs between multiple rolls) is equipped with a pressurized N water release section that removes water by compression and shear force. It has become popular in recent years because it is simple and easy to maintain, uses a small amount of flocculant, has a solid content collection vehicle height, and has high deicing water effect.

前記装置の重力脱水部で(よ、供給した汚泥を全量処理
しなければ、ベルトサイド力〉らのζよみ出し等が生じ
性能を充分発揮させること力やできないため公知のこの
種装置でζよ凝集1i1J供給量を処理量に基づいて決
定し凝集剤を自動的(こ一定量供給し、最適な凝集フロ
ックを形成させてl、%る。
If the supplied sludge is not completely treated in the gravity dewatering section of the device, ζ build-up due to belt side force etc. will occur, making it impossible to fully demonstrate the performance. The supply amount of flocculation 1i1J is determined based on the processing amount, and the flocculant is automatically supplied in a fixed amount to form an optimal flocculation floc.

しかし、汚泥の性状等こと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
み出しやろ液の濁り等力τ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。本発明はとのよ0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装置
を提供するものでその要旨とするところは、無端のシ戸
布ベルトを複数のロール間を走行するよう張設し、重力
脱水部と加圧脱水部を設けたベルトプレス型脱水装置に
おいて、前記重力脱水部(4Iに液面検出手段(13)
を設け、該検出手段(13)の出力信号により作動する
凝集剤供給装置(2)の制御回路(15)、原液供給装
置(1)の制御回路(14)及び無端ベルト送行駆動装
M(7)の制御回路(16)とを設けたことを特徴とす
るベルトプレス型脱水装置である。
However, if the properties of the sludge change, the amount of coagulant may be too much or too little, resulting in incomplete coagulation, resulting in sludge protruding from the belt side, clouding of the filtrate, etc., and the solids recovery rate is also poor. 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 the above-mentioned circumstances, and provides a device that eliminates the above-mentioned drawbacks, maintains optimal operating conditions, and makes automatic driving possible. In a belt press type dewatering device in which a Shito cloth belt is stretched so as to run between a plurality of rolls and is provided with a gravity dewatering section and a pressure dehydrating section, the gravity dewatering section (4I has a liquid level detection means (13)).
A control circuit (15) of the flocculant supply device (2) which is operated by the output signal of the detection means (13), a control circuit (14) of the stock solution supply device (1), and an endless belt feeding drive device M (7). ) A control circuit (16) is provided.

本発明の一実施例を図面に基づいて記述する。An embodiment of the present invention will be described based on the drawings.

第一図は本発明に係る一実施例の系統図である。FIG. 1 is a system diagram of an embodiment according to the present invention.

fil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攪秤機によ
り均一に混合し汚泥の凝集を計る凝集混和槽、(1)は
後記の重力脱水部(41と加圧脱水部(4)を設は汚泥
を脱水処理するベルトプレス型脱水装置、(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
端ン戸布ベルト(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ン戸布ベルト(5)と
対向して平行に設けた上部走行無端シ戸布(6)との2
枚のベルトに挟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wA維等
で織られた一定巾で帯上のシ戸布ベルトでありロール間
に無端に張設され駆動装W(7)により矢印方向に一定
速度で走行する。(7)はり炉布ベルト(5)、(6)
のシ戸布ベルト駆動装置、(8)は重力脱水部(4)の
)炉布ベルト(5)を底面として凝集汚泥を受は入れ滞
留させる汚泥受槽、(9)はり炉布ベルト(5)、(5
1g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、叫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
り前記炉布ベルト(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。
fil 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 device (1) and (2). ) A coagulation mixing tank that uniformly mixes the sludge and flocculant supplied from the sludge with an agitator attached to the top and measures the flocculation of the sludge. is a belt press type dewatering device that dehydrates sludge (4 is a gravity-fed dewatering device that dewaters flocculated sludge introduced from the flocculation mixing tank (3) on a single endless belt (5) that runs on it by gravity) The dewatering section (4) is an upper running endless cloth belt (6) provided parallel to and opposite to the endless cloth belt (5) for removing dehydrated sludge.
A pressurized dewatering section (5
) and (6) are cloth belts with a constant width woven from synthetic WA fibers such as nylon or polyester, which are stretched endlessly between rolls and are constantly driven in the direction of the arrow by a driving device W (7). Run at speed. (7) Beam furnace cloth belt (5), (6)
(8) is a sludge receiving tank that receives and retains flocculated sludge with the furnace cloth belt (5) of the gravity dewatering section (4) as the bottom surface, (9) beam furnace cloth belt (5) ,(5
It consists of a large-diameter low-pressure roll that gradually compresses the 1g of sludge that has been conveyed under low pressure, and a plurality of small-diameter press rolls that are installed to apply even higher pressure to the furnace fabric. By running between the rolls, belts (5) and (6) apply pressure accompanied by shearing force to the cake.

(11)、(11’)はシ戸布ベルト(5)、(6)の
駆動ロールであり)炉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)はシ濾過されたン戸液を集液する集
液器である。集液されたン戸液り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(41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
(14)、(15)、(16)へ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tコめに設
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)から凝集剤供給量M f21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
より炉布ベルト(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I (11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乙と
により原液供給量を減少させる。必要であれば警報器を
取り付は警報を発するようにしてもよい。以上の操作に
よっ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濶を含め全系を停止す
る。
(11) and (11') are drive rolls for the cloth belts (5) and (6), and the scraper (17) reverses the furnace cloth.
The dehydrated sludge is peeled off and discharged as dehydrated cake C to the outside of the system. (12) is a liquid collector that collects the filtered liquid. The collected liquid is extracted and discharged outside the system. A liquid level control meter (13) equipped with a signal transmission circuit is installed as a liquid level detection means in the sludge receiving tank (8) provided in the gravity dewatering section (41) of such a known belt press type dewatering device, and the sludge The liquid level height is continuously detected and signals are sent to each control circuit (14), (15), and (16) to ensure optimum operation at all times. Sludge receiving tank (8
) describes the case where the sludge liquid level in the sludge exceeds a certain height set when the amount of flocculant added is insufficient.
A signal is output from the liquid level controller (13) to the supply amount control circuit (15) of the flocculant supply amount Mf21 to increase the rotation speed of the supply device (2), thereby proportionally increasing the supply amount;
If the liquid level does not drop even after a certain period of time has elapsed, a signal is output to the rotation speed control circuit (16) of the endless belt running drive device (7) and the rotation speed of the drive device (7) is increased. increasing the running speed of the belts (5) and (6);
Furthermore, if no improvement is seen even after a certain period of time has passed, the stock solution supply device I (B outputs a signal to the supply amount control circuit (14) of 11 and reduces the rotation speed of the supply device (1)). Decrease the supply amount.If necessary, an alarm may be installed to issue an alarm.If the above operation does not resolve the problem, stop supplying the stock solution and flocculant, and after a certain period of time, remove the attached Stop the entire system including related machines.

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(14)、(15)
、(16)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(14)、(15
)、(16)を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った場合には、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
もてきる。
In addition, the above continuously detects the liquid level of sludge in the sludge receiving tank (8) and outputs a signal, and each control circuit (14), (15)
, (16) are being switched continuously, but if the flocculant supply rate is increased and the liquid level does not drop after a certain period of time, the flocculant supply rate is further increased, and if no improvement is seen, further flocculation is performed. Each control circuit (14), (15) increases the amount of agent supplied by a signal from the liquid level controller (13).
), (16) may be switched in stages, or in other embodiments, contrary to the above, when the liquid level of sludge in the sludge receiving tank (8) falls below a predetermined height, It is also possible to reduce the amount of flocculant supplied proportionally and 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ずる汚泥
を脱水処理するにあたっ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れ
ば汚泥の性状等に変動を生し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、ン戸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−めろ事がて
きるのて産業上極めて有効な装置である。
When dewatering sludge generated in the water treatment of tap water, sewage, industrial wastewater, etc., if a belt press type dehydrator equipped with the control mechanism of the present invention configured as described above is used, changes in the properties of the sludge can be prevented. Even if the sludge does not coagulate, the amount of flocculant supplied will be insufficient and the sludge will not flocculate incompletely, causing sludge to protrude from the belt side or turbidity of the door liquid.In addition, the equipment can be fully automated and can be operated unmanned. -It is an extremely effective device in industry because it can cause problems.

【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。 11+・原液供給装置、(2):凝集剤供給装置、(3
):凝集混和槽、(イ):ベルトプレス型脱水機、+4
i :重力脱水部、(j’r :加圧脱水部、(6)、
(6)ニジ戸布ペルh、(71:5戸布ベルト駆動装置
、(8):汚泥受槽、(9):低圧ロール、QOI: 
プレスロール、 (11)、+111 :駆動ロール、
+12):集液器、+131: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:  ン戸
液 特許出願人:三菱化工機株式会社
FIG. 1 is a system diagram of an embodiment according to the present invention. 11+・Stock solution supply device, (2): Coagulant supply device, (3
): Coagulation mixing tank, (a): Belt press type dehydrator, +4
i: gravity dehydration section, (j'r: pressure dehydration section, (6),
(6) Niji Tofu Pel h, (71:5 Tofu belt drive device, (8): Sludge receiving tank, (9): Low pressure roll, QOI:
Press roll, (11), +111: Drive roll,
+12): Liquid collector, +131: 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: Noodle liquid patent application Person: Mitsubishi Kakoki Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 無端のf布ベルトを複数のロール間を走行するよう張設
し、重力脱水部と加圧脱水部を設けたベルトプレス型脱
水装置において、前記重力脱水部(4)に液面検出手段
(13)を設け、該検出手段(13)の出力信号により
作動する凝集剤供給装置(2)の制御回路(15)、原
液供給装置(1)の制御回路(14)及び無端ベルト送
行駆動装置(7)の制御回路(16)とを設けたことを
特徴とするベルトプレス型脱水装置。
In a belt press type dewatering device in which an endless f-cloth belt is stretched to run between a plurality of rolls and is provided with a gravity dewatering section and a pressure dehydrating section, a liquid level detection means (13) is provided in the gravity dewatering section (4). ), a control circuit (15) for the flocculant supply device (2), a control circuit (14) for the stock solution supply device (1), and an endless belt conveyance drive device (7) operated by the output signal of the detection means (13). ) A control circuit (16) is provided.
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 true JPS59133996A (en) 1984-08-01
JPS6125478B2 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 (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001004279A (en) * 1999-06-08 2001-01-12 Technological Resources Pty Ltd Direct refining container
JP2010069390A (en) * 2008-09-17 2010-04-02 Ishigaki Co Ltd Method for operating and controlling belt type concentrator
US7964105B2 (en) * 2008-08-07 2011-06-21 William Harris Moss Method for improving belt press dewatering

Families Citing this family (1)

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

Citations (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
JPS56111595A (en) * 1980-02-08 1981-09-03 Kubota Ltd Dehydrating device
JPS56111597A (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

Patent Citations (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
JPS56111595A (en) * 1980-02-08 1981-09-03 Kubota Ltd Dehydrating device
JPS56111597A (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 (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001004279A (en) * 1999-06-08 2001-01-12 Technological Resources Pty Ltd Direct refining container
US7964105B2 (en) * 2008-08-07 2011-06-21 William Harris Moss Method for improving belt press dewatering
JP2010069390A (en) * 2008-09-17 2010-04-02 Ishigaki Co Ltd Method for operating and controlling belt type concentrator

Also Published As

Publication number Publication date
JPS6125478B2 (en) 1986-06-16

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