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JP2003117599A - Sludge treating equipment - Google Patents

Sludge treating equipment

Info

Publication number
JP2003117599A
JP2003117599A JP2001314379A JP2001314379A JP2003117599A JP 2003117599 A JP2003117599 A JP 2003117599A JP 2001314379 A JP2001314379 A JP 2001314379A JP 2001314379 A JP2001314379 A JP 2001314379A JP 2003117599 A JP2003117599 A JP 2003117599A
Authority
JP
Japan
Prior art keywords
sludge
flocculation
coagulant
tank
coagulation
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
JP2001314379A
Other languages
Japanese (ja)
Other versions
JP3630130B2 (en
Inventor
Toshiyuki Nakae
俊之 中江
Yoichi Arima
洋一 有馬
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.)
Toray Engineering Co Ltd
Original Assignee
Toray Engineering 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 Toray Engineering Co Ltd filed Critical Toray Engineering Co Ltd
Priority to JP2001314379A priority Critical patent/JP3630130B2/en
Publication of JP2003117599A publication Critical patent/JP2003117599A/en
Application granted granted Critical
Publication of JP3630130B2 publication Critical patent/JP3630130B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a sludge treating equipment which flocculates sludge by using a flocculating agent and dewaters the sludge. SOLUTION: (1) In this sludge treating equipment for dewatering the sludge stored in a sludge storing vessel by sending the sludge to a flocculation agitating vessel, adding the flocculating agent to the sludge in the flocculation agitating vessel and sending the sludge mixed with the flocculating agent in the flocculation agitating vessel to a sludge dewatering machine, a batch operated treatment of sending the sludge by as much as the specific capacity of the flocculation agitating vessel to the flocculation agitating vessel, mixing the sludge with the flocculating agent in the flocculation agitating vessel to send all of the corresponding capacities to the sludge dewatering machine after the flocculation reaction attains a prescribed state is adopted to complete the flocculation reaction in the one flocculation agitating vessel. (2) The number of revolutions of the agitating vessel is fluctuated so as to attain the optimum agitating conditions by effectively utilizing the batch treatment process. (3) A corrosion system flocculating agent to permit the direct charging of the flocculating agent each by a fixed amount to the flocculation agitating vessel is used as the flocculating agent.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は汚泥処理装置に関す
る、特に、汚泥を凝集剤を用いて凝集し、汚泥脱水する
汚泥処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge treatment device, and more particularly to a sludge treatment device for aggregating sludge with a coagulant and dewatering the sludge.

【0002】[0002]

【従来の技術】従来の汚泥処理装置における汚泥供給か
ら凝集、汚泥脱水機へ供給するプロセスについて、特許
公開公報平成11年169891号同169892号な
どに類似技術が記載されているが、図3を用いて説明す
る。まず、高分子凝集剤からなる凝集助剤の供給から説
明する。凝集助剤貯留タンク110に貯留されている凝
集助剤は凝集助剤注入ポンプ111を通じて凝集助剤混
和槽112へ供給される。凝集助剤混和槽112は、槽
内部に攪拌機112aを有し、槽上部に凝集助剤注入管
113と汚泥移送管122を有する。この凝集助剤混和
槽112は、凝集助剤注入管113が凝集助剤注入ポン
プ111と連絡され、汚泥供給ポンプ120から供給さ
れる汚泥に凝集助剤注入管113から供給される凝集助
剤を汚泥の濃度と性状等に応じて選択された割合で混合
して攪拌機112aで攪拌する。
2. Description of the Related Art Regarding the process of supplying sludge from a sludge supply device to a coagulation and sludge dewatering device in a conventional sludge treatment device, a similar technique is described in Patent Publication Nos. 169891 and 169892 of 1999. It demonstrates using. First, the supply of the coagulation aid composed of the polymer coagulant will be described. The flocculation aid stored in the flocculation aid storage tank 110 is supplied to the flocculation aid mixing tank 112 through the flocculation aid injection pump 111. The coagulation aid mixing tank 112 has a stirrer 112a inside the tank, and a coagulation aid injection pipe 113 and a sludge transfer pipe 122 at the upper part of the tank. In this coagulation auxiliary agent mixing tank 112, the coagulation auxiliary agent injection pipe 113 is connected to the coagulation auxiliary agent injection pump 111, and the coagulation auxiliary agent supplied from the coagulation auxiliary agent injection pipe 113 is added to the sludge supplied from the sludge supply pump 120. The sludge is mixed at a ratio selected according to the concentration and properties of the sludge and stirred by the stirrer 112a.

【0003】次にポリ塩化鉄等からなる凝集剤供給につ
いて説明する。原液凝集剤タンク101は凝集剤原液を
攪拌機101aにより攪拌し貯留する。この原液凝集剤
タンク101には凝集剤原液を吐出する原液凝集剤ポン
プ102が設けられ、原液凝集剤ポンプ102の吐出ポ
ートが凝集剤自動溶解槽104に連絡される。凝集剤自
動溶解槽104は上水移送管130と上水電磁弁131
を介して連絡した入り口と、原液凝集剤ポンプ102と
連絡した入口と凝集剤貯留槽106に連絡した出口を有
し、上水移送管130から供給される上水と原液凝集剤
ポンプ102が吐出する原液と凝集剤自動溶解槽104
内の攪拌機104aにて、混合して凝集剤貯留槽106
に送出する。
Next, the supply of the coagulant made of polyiron chloride will be described. The stock solution coagulant tank 101 stirs and stores the coagulant stock solution with a stirrer 101a. A stock solution coagulant pump 102 for discharging the stock solution coagulant solution is provided in the stock solution coagulant tank 101, and a discharge port of the stock solution coagulant pump 102 is connected to a coagulant automatic dissolution tank 104. The coagulant automatic dissolution tank 104 includes a clean water transfer pipe 130 and a clean water solenoid valve 131.
Has an inlet communicating with the stock solution coagulant pump 102 and an outlet communicating with the stock solution coagulant pump 106, and discharges the clean water supplied from the clean water transfer pipe 130 and the stock solution coagulant pump 102. Undiluted solution and flocculant automatic dissolution tank 104
In the agitator 104a inside, the mixture is mixed and the coagulant storage tank 106
Send to.

【0004】次に凝集剤混和槽109での作用について
説明する。凝集剤混和槽109は、凝集剤貯留槽106
から配管を経て送られる凝集剤を混和する。この凝集剤
貯留槽106には凝集剤を吐出する凝集剤注入ポンプ1
07が設けられ、この凝集剤注入ポンプ107の吐出ポ
ートが配管により凝集剤混和槽109に連絡する。この
凝集剤注入ポンプ107は、定量吐出ポンプが用いら
れ、コントローラーにより、制御されて凝集剤混和槽1
09への汚泥の供給量と相応した量の凝集剤を凝集剤混
和槽109に供給する。この凝集剤と混合された汚泥を
流出管150から脱水機160に送出する。
Next, the operation of the flocculant mixing tank 109 will be described. The coagulant mixing tank 109 is the coagulant storage tank 106.
The coagulant sent from the pipe through the pipe is mixed. A coagulant injection pump 1 for discharging the coagulant is provided in the coagulant storage tank 106.
No. 07 is provided, and the discharge port of the coagulant injection pump 107 communicates with the coagulant mixing tank 109 by piping. As the coagulant injection pump 107, a fixed-quantity discharge pump is used, and the coagulant mixing tank 1 is controlled by a controller.
The coagulant in an amount corresponding to the sludge supply amount to 09 is supplied to the coagulant mixing tank 109. The sludge mixed with this coagulant is sent from the outflow pipe 150 to the dehydrator 160.

【0005】凝集剤自動溶解槽104、凝集助剤混和槽
112および凝集剤混和槽109には貯留量を検出する
水位計等が設けられ、原液凝集剤ポンプ102にはフロ
ートスイッチ103が、凝集剤注入ポンプにはフロート
スイッチ108が汚泥供給ポンプ120にはフロートス
イッチ121がそれぞれ設けられそれらの検知出力等に
基づきコントローラにより駆動制御される。
The coagulant automatic dissolution tank 104, the coagulant aid mixing tank 112 and the coagulant mixing tank 109 are provided with water level gauges for detecting the storage amount, and the stock solution coagulant pump 102 is provided with the float switch 103 and the coagulant. The injection pump is provided with a float switch 108, and the sludge supply pump 120 is provided with a float switch 121, which are controlled by the controller based on their detection outputs and the like.

【0006】脱水については、脱水機は160多重板外
胴式スクリュー脱水機やスクリュープレス式脱水機等が
用いられ、凝集剤と混和した汚泥を脱水し、含水率が8
5%以下の脱水ケーキを作成する。
For dewatering, a 160 multi-plate outer shell type screw dewatering machine, a screw press type dewatering machine or the like is used as the dewatering machine, and the sludge mixed with the coagulant is dewatered to obtain a water content of 8
Make a dehydrated cake of 5% or less.

【0007】[0007]

【発明が解決しようとする課題】従来の技術の項にて記
載の様に、汚泥処理の凝集工程においては、高分子凝集
剤が用いられることが一般的であり、原液凝集剤と凝集
助剤を凝集攪拌槽にて凝集反応を生じさせる直前に混合
し供給する必要があった。従い、凝集剤の供給の段階
で、装置を複雑にし、運転形態も複雑なものとしてい
た。また、汚泥を凝集助剤で混和し、さらに凝集剤を混
和する為、凝集攪拌槽を2槽設備し、連続的に流す方法
しか取れなかった。従い凝集攪拌槽を2槽設備し攪拌機
を制御する必要があり装置を複雑にしていた。しかし、
当該汚泥処理装置に関しては、小規模なところに設置、
運転される場合が多く、運転の維持、保守に対する人
材、費用面で多く問題を生じていた
As described in the section of the prior art, a polymer flocculant is generally used in the flocculation step of sludge treatment. Had to be mixed and supplied in the coagulation stirring tank immediately before the coagulation reaction occurred. Therefore, at the stage of supplying the coagulant, the apparatus is complicated and the operation mode is also complicated. Further, in order to mix the sludge with the coagulation auxiliary agent and further mix the coagulant, only a method of providing two coagulation stirring tanks and continuously flowing it was possible. Therefore, it is necessary to control the agitator by providing two agitation stirring tanks, which complicates the apparatus. But,
Regarding the sludge treatment device, install it in a small scale,
It was often driven, and it caused many problems in terms of maintenance and maintenance personnel and cost.

【0008】[0008]

【課題を解決するための手段】上記問題を解決する為
に、本発明の発明者は装置を簡素化する手段を見出し
た。
In order to solve the above problems, the inventor of the present invention has found means for simplifying the apparatus.

【0009】請求項1に記載の様に、汚泥貯留槽に貯留
した汚泥を凝集攪拌槽に送り凝集攪拌槽で汚泥に凝集剤
を添加し該凝集攪拌槽で凝集剤と混合した汚泥を汚泥脱
水機に送り脱水する汚泥処理装置において、汚泥を該凝
集攪拌槽の仕様容量分送り該凝集攪拌槽にて凝集剤と混
合しその凝集反応が所定の状態になった後該容量分全て
を汚泥脱水機に送るバッチ式処理をすることにより、一
つの凝集攪拌槽にて、凝集反応を完了させる。
As described in claim 1, sludge stored in the sludge storage tank is sent to a coagulation stirring tank, a coagulant is added to the sludge in the coagulation stirring tank, and the sludge mixed with the coagulant in the coagulation stirring tank is sludge dehydrated. In the sludge treatment device that sends the sludge to the machine and feeds it in the specified volume of the flocculation stirring tank, mix it with the flocculant in the flocculation stirring tank, and after the flocculation reaction reaches a predetermined state, sludge dehydration of the entire volume The flocculation reaction is completed in one flocculation and agitation tank by performing a batch-type process of sending the flocculation to the machine.

【0010】また、請求項2に記載の様に、凝集攪拌槽
に凝集剤を直接投入可能な凝集剤を用いる。請求項3に
記載の様に、当該発明では、バッチ式処理をすることに
より、汚泥を凝集攪拌槽に供給する段階では急速攪拌、
凝集が進む段階では緩速攪拌、その後しばらく静置、汚
泥脱水機へ供給の段階では、微速攪拌とバッチ処理プロ
セスの段階で最適な攪拌条件になる様に攪拌機の回転数
を変動させることを特徴としている。請求項4に記載の
様に、凝集攪拌槽に凝集剤を定量づつ直接投入可能な凝
集剤として、腐植系凝集剤を用いた。特に好ましい腐植
系凝集剤として、当該発明では、エム・シー砿産株式会
社製の商品名「パピルスNO.525」を用いた。
Further, as described in claim 2, a coagulant capable of directly adding the coagulant to the coagulation stirring tank is used. According to the third aspect of the present invention, in the present invention, rapid stirring is performed at the stage of supplying the sludge to the coagulation stirring tank by performing batch processing.
When the flocculation progresses, it is slowly stirred, then left standing for a while, and at the stage of supplying it to the sludge dehydrator, the rotation speed of the stirrer is changed so that it becomes the optimal stirring condition at the stage of the slow speed stirring and the batch treatment process. I am trying. As described in claim 4, a humus-based coagulant is used as the coagulant capable of directly adding the coagulant to the coagulation stirring tank in a fixed amount. As a particularly preferable humus-based flocculant, in the present invention, a trade name “Papyrus No. 525” manufactured by MC Kinsan Co., Ltd. was used.

【0011】[0011]

【発明の実施の形態】DETAILED DESCRIPTION OF THE INVENTION

【実施例】以下、本発明の実施の形態を図及び表を用い
て説明する。図1に本発明の汚泥処理装置の模式図を示
す。汚泥処理装置1は余剰汚泥脱水部2、生ゴミ投入部
3、発酵部4からなる。また、余剰汚泥脱水部2は、汚
泥貯留槽10、凝集攪拌槽13、汚泥脱水機16から成
り、汚泥脱水機16から取り出された汚泥ケーキは生ゴ
ミ投入部3の破砕機5から送られた破砕された生ゴミと
共に、スクリューコンベアー6を介して発酵部4の発酵
装置に送られ処理される。また、発酵部4を用いず直接
コンポストとして搬出される場合もある。
Embodiments of the present invention will be described below with reference to the drawings and tables. FIG. 1 shows a schematic diagram of the sludge treatment device of the present invention. The sludge treatment device 1 includes a surplus sludge dewatering unit 2, a raw garbage input unit 3, and a fermentation unit 4. The excess sludge dewatering unit 2 is composed of a sludge storage tank 10, a coagulation stirring tank 13, and a sludge dewatering machine 16, and the sludge cake taken out from the sludge dewatering machine 16 was sent from the crusher 5 of the garbage disposal section 3. Along with the crushed raw garbage, it is sent to the fermentation device of the fermentation section 4 through the screw conveyor 6 and processed. Further, it may be directly delivered as compost without using the fermentation section 4.

【0012】当該発明は余剰汚泥脱水部2にかかわるも
のである。従いその範囲について詳細に記載する。汚泥
は汚泥貯留槽10に一旦溜められる、汚泥貯留槽10か
ら汚泥供給・移送切替弁11を通じて、汚泥供給・移送
ポンプ12に汚泥が送られる。汚泥供給・移送ポンプ1
2は凝集攪拌槽13に汚泥を供給する。水位計14にて
汚泥が満杯であることを検知した段階で、定量フィーダ
ー15から凝集剤を定量送り、凝集攪拌槽13に付随す
る攪拌機13aにて攪拌する。攪拌については、汚泥供
給時及び凝集剤添加時には急速攪拌、凝集反応時には緩
速攪拌運転攪拌を停止し静置すると言うように制御され
る。凝集剤は天然剤の腐植系凝集剤を採用することによ
り、生成コンポストの安全性を確保することが可能とな
る。
The present invention relates to the excess sludge dewatering section 2. Therefore, the range will be described in detail. The sludge is temporarily stored in the sludge storage tank 10. The sludge is sent from the sludge storage tank 10 to the sludge supply / transfer pump 12 through the sludge supply / transfer switching valve 11. Sludge supply / transfer pump 1
2 supplies sludge to the coagulation stirring tank 13. When the water level gauge 14 detects that the sludge is full, a fixed amount of the coagulant is fed from the fixed amount feeder 15 and is stirred by the stirrer 13 a attached to the coagulation stirring tank 13. The agitation is controlled such that rapid agitation is performed during sludge supply and coagulant addition, and slow agitation operation agitation is stopped and agitation is allowed to stand during a flocculation reaction. By adopting a humus-based flocculant, which is a natural agent, as the flocculant, it is possible to ensure the safety of the produced compost.

【0013】また、凝集剤の形態が粉体1種類であり、
凝集剤の混合が不要となり設備としては従来の技術に開
示の技術の設備に比べ簡素化される。次に、凝集攪拌槽
13にて凝集が完了した後、汚泥供給・移送切替弁11
を切替え、汚泥供給・移送ポンプ12を作動させて凝集
された汚泥を汚泥脱水機16へ送る。汚泥脱水機16
は、二軸式スクリュープレス方式を採用している。特徴
としては、テフロン製二軸式対向スクリューを用いる
為、スラリー状のものに対して推進力が大きく共廻りせ
ず搬送可能な様になっている。目詰まり防止策として水
切りの良いシリンダーが摺動する異形バースクリーンを
採用するなど工夫してある。当該汚泥脱水機16を用い
て送られた凝集済みの汚泥から余剰汚泥を含水率85%
以下に脱水する。脱水して出来た汚泥ケーキはスクリュ
ーコンベアー6を介して発酵部4の発酵装置に送られ処
理される。また、発酵部4を用いず直接コンポストとし
て搬出される場合もある。
Further, the form of the aggregating agent is one kind of powder,
The coagulant does not need to be mixed, and the equipment is simplified as compared with the equipment disclosed in the conventional art. Next, after coagulation is completed in the coagulation stirring tank 13, the sludge supply / transfer switching valve 11
And the sludge supply / transfer pump 12 is operated to send the coagulated sludge to the sludge dehydrator 16. Sludge dehydrator 16
Uses a twin-screw screw press system. As a feature, it uses a Teflon-made twin-screw opposed screw, so that it can be conveyed without a large co-rotation of the propulsive force with respect to the slurry-like one. As a measure to prevent clogging, it is devised such as adopting a deformed bar screen on which a well-drained cylinder slides. Excess sludge is contained from the coagulated sludge sent using the sludge dehydrator 16 with a water content of 85%.
Dehydrate to the following: The sludge cake produced by dehydration is sent to the fermentation device of the fermentation section 4 via the screw conveyor 6 and processed. Further, it may be directly delivered as compost without using the fermentation section 4.

【0014】次に、当該発明の余剰汚泥脱水部2の各機
器の動作について個々に記述する。汚泥供給・移送ポン
プ12は、凝集攪拌槽13に対してモーターを正転・逆
転させることにより汚泥の供給運転と移送運転の両方向
の作動が可能な機能を持つ。同時にインバーター制御に
よりモーター回転数を制御し、汚泥供給・移動量の調整
可能な機能も備える。手動運転、自動運転切替えられる
が運転速度はインバーターにて自由に設定出来る、自動
運転時は運転タイムチャートに基き作動する。凝集攪拌
槽13の攪拌機13aであるが、急速、緩速、静置、微
速と運転速度を凝集の段階を追って変化させることが可
能である。それぞれ速度はインバータにて自由に設定出
来る。手動運転、自動運転切替えられるが自動運転時は
運転タイムチャートにより汚泥供給時は急速攪拌、凝集
剤添加時は緩速攪拌、静置、凝集済汚泥を移送時は微速
運転と切り替わる。凝集剤供給する定量フィーダー15
は、同様手動運転、自動運転切替えられるが自動運転時
は汚泥供給時運転され凝集剤を定量供給した時点でタイ
マーで停止する様になっている。
Next, the operation of each device of the excess sludge dewatering unit 2 of the present invention will be individually described. The sludge supply / transfer pump 12 has a function capable of operating in both directions of sludge supply operation and transfer operation by rotating the motor in the forward and reverse directions with respect to the coagulation stirring tank 13. At the same time, it also has the function of controlling the motor speed by inverter control and adjusting the sludge supply and movement amount. Manual operation or automatic operation can be switched, but the operation speed can be freely set with the inverter. During automatic operation, it operates based on the operation time chart. Although it is the stirrer 13a of the flocculation stirring tank 13, it is possible to change the operating speed such as rapid, slow, stationary, slow and slow depending on the stage of flocculation. Each speed can be freely set by the inverter. Manual operation or automatic operation can be switched, but during automatic operation, the operation time chart shows rapid stirring when sludge is supplied, slow agitation when coagulant is added, stationary, and slow speed operation when transferring coagulated sludge. Quantitative feeder for supplying flocculant 15
Similarly, the manual operation and the automatic operation can be switched, but during the automatic operation, the operation is performed when sludge is supplied and the timer is stopped when a fixed amount of the coagulant is supplied.

【0015】汚泥脱水機16は同様手動運転、自動運転
切替えられるが手動時は汚泥脱水機16のモーター軸速
度をインバーターにより任意に設定することによって汚
泥脱水状態の調整が可能としている。自動運転時は予め
選択されたモーター軸速度にインバーターで設定された
条件で運転タイムチャートに基く自動運転であり脱水完
了後タイマーにて停止する。汚泥供給移送時の切替をす
る汚泥供給・移送切替弁11は手動運転時、汚泥の凝集
攪拌槽13への供給時については汚泥供給側を開、移送
時については移送側を開とする。自動運転時は運転タイ
ムチャートに従って切り替わり、供給時は供給側が開、
移送時は移送側が開となる。各機器の動作については、
余剰汚泥脱水部動作表として表1に示す。
Similarly, the sludge dewatering machine 16 can be switched between manual operation and automatic operation. In manual operation, the sludge dewatering state can be adjusted by arbitrarily setting the motor shaft speed of the sludge dewatering machine 16 with an inverter. At the time of automatic operation, it is an automatic operation based on the operation time chart under the condition set by the inverter at the preselected motor shaft speed, and it is stopped by the timer after the completion of dehydration. The sludge supply / transfer switching valve 11, which switches the sludge supply / transfer, is opened during manual operation, when the sludge is supplied to the coagulation stirring tank 13, the sludge supply side is opened, and during transfer, the transfer side is opened. During automatic operation, it switches according to the operation time chart, and during supply, the supply side opens,
The transfer side is open during transfer. For the operation of each device,
Table 1 is an operation table for the excess sludge dewatering unit.

【0016】表1 Table 1

【0017】バッチ式での余剰汚泥脱水システムの運転
タイムチャート(図2)に基き自動運転について説明す
る。
The automatic operation will be described based on the operation time chart (FIG. 2) of the batch type excess sludge dewatering system.

【0018】待機工程で運転開始タイマーが作動、汚泥
供給・移送切替弁11の供給側が開となる。次に汚泥供
給工程に移り、汚泥供給・移送ポンプ12が作動し、汚
泥を凝集攪拌槽13へ供給する。その時凝集攪拌槽13
の攪拌機13aが、汚泥供給し始めて後凝集攪拌槽13
の水位計14が中レベルの水位に達したところで水位を
感知しタイマー作動と同時に急速攪拌し始める。同時に
定量フィーダー15からタイマー作動と共に凝集剤が定
量送られ始める。定量フィーダー15はタイマーが設定
されており、凝集剤を定量凝集攪拌槽13へ注入した後
停止する。
In the standby process, the operation start timer is activated and the supply side of the sludge supply / transfer switching valve 11 is opened. Next, in the sludge supply step, the sludge supply / transfer pump 12 operates to supply the sludge to the coagulation stirring tank 13. At that time, the coagulation stirring tank 13
The agitator 13a of the first agglomerating and agitating tank 13 after starting to supply sludge
When the water level meter 14 reaches a medium level, it senses the water level and starts rapid stirring at the same time when the timer is activated. At the same time, the fixed amount of the flocculant starts to be fed from the fixed amount feeder 15 with the timer. The fixed-quantity feeder 15 is set with a timer, and stops after injecting the coagulant into the fixed-quantity coagulation stirring tank 13.

【0019】その間、凝集攪拌槽13が満杯となり急速
攪拌用のタイマーがタイムアップした後、緩速攪拌工程
に移り、安定的凝集作用として、凝集攪拌槽13内の攪
拌機13aがタイマーにて一定時間の緩速攪拌運転に入
る。同時に凝集が完了した汚泥を凝集攪拌槽13から汚
泥供給・移送ポンプ12を作動させて汚泥脱水機16へ
供給する為の準備として汚泥供給・移送切替弁11は移
送側が開の状態と切り替わる。
In the meantime, after the agitation stirring tank 13 is full and the timer for rapid stirring has timed up, the process proceeds to the slow stirring step, and the stirring machine 13a in the agitation stirring tank 13 uses a timer for a certain time as a stable aggregation action. Enter the slow stirring operation. At the same time, the sludge supply / transfer switching valve 11 is switched to an open state on the transfer side in preparation for supplying the sludge, which has completed coagulation, from the coagulation stirring tank 13 to operate the sludge supply / transfer pump 12 to supply it to the sludge dehydrator 16.

【0020】静置工程では凝集攪拌槽13の攪拌機13
aが停止され、そのまま凝集攪拌槽13は凝集反応が完
了するまで静置される。脱水工程では凝集攪拌槽13の
攪拌機13aをタイマーにて微速運転に切り替えるとと
もに汚泥供給・移送ポンプ12を作動させ凝集攪拌槽1
3から汚泥を移送し、当該攪拌機13aを微速運転する
と同時に運転を開始している汚泥脱水機16に汚泥供給
・移送切替弁11を通じて供給する。微速攪拌していた
凝集攪拌槽13の攪拌機13aは凝集攪拌槽13の水位
計14の感知する水位が低レベルを示したところで停止
する。
In the stationary step, the agitator 13 of the aggregating agitation tank 13 is used.
a is stopped, and the agitation stirring tank 13 is left as it is until the aggregating reaction is completed. In the dehydration step, the agitator 13a of the coagulation stirring tank 13 is switched to a slow speed operation by a timer, and the sludge supply / transfer pump 12 is operated to operate the coagulation stirring tank 1
The sludge is transferred from No. 3, and the stirrer 13a is operated at a very low speed, and at the same time, it is supplied to the sludge dewatering machine 16 which is in operation through the sludge supply / transfer switching valve 11. The stirrer 13a of the aggregating and stirring tank 13 that was being stirred at a low speed is stopped when the water level detected by the water level gauge 14 of the aggregating and stirring tank 13 shows a low level.

【0021】汚泥供給・移送ポンプ12が凝集攪拌槽1
3の水位計14が凝集攪拌槽13の水位が無いと示した
ところで、汚泥供給・移送切替弁11を供給側開に切り
替わり、洗浄工程として次のバッチ工程の準備に入る。
その後、汚泥脱水機16のタイマーが働き停止する。詳
細は省略するが、汚泥脱水機16の停止後、タイマー作
動とともに汚泥脱水機16の洗浄装置がタイマーにより
一定時間作動後停止する。その後次のバッチ工程として
待機工程に戻る。
The sludge supply / transfer pump 12 is a coagulation stirring tank 1
When the water level gauge 14 of 3 indicates that there is no water level in the coagulation stirring tank 13, the sludge supply / transfer switching valve 11 is switched to open on the supply side, and preparation for the next batch process is started as a cleaning process.
After that, the timer of the sludge dehydrator 16 stops working. Although details will be omitted, after the sludge dewatering machine 16 is stopped, the timer operates and the cleaning device of the sludge dewatering machine 16 operates for a certain time and then stops. After that, the process returns to the standby process as the next batch process.

【0022】次に、本発明のバッチ式余剰汚泥脱水シス
テムの諸条件について記載する。まず、本発明で採用し
ている腐植系凝集剤として、当該発明では、エム・シー
砿産株式会社製の商品名「パピルスNO.525」を用
いた。使用量は、凝集攪拌槽13の容量が0.4立方メ
ートルであるのに対し、1回のバッチ処理あたり約0.
28キログラム重を用い、定量フィーダー15を用いて
1.5分程度で投入する。また、インバーターにて設定
する凝集槽攪拌機13aについては、急速運転時が40
から60Hzとし標準設定値としては45Hz(攪拌機
回転数としては45回転/分)、緩速運転時が15〜4
0Hzとし標準設定値としては25Hz(攪拌機回転数
としては25回転/分)回転数、微速運転時が0〜15
Hzとし、標準設定値としては、10Hz(攪拌機回転
数としては10回転/分)である。
Next, various conditions of the batch type excess sludge dewatering system of the present invention will be described. First, as the humus-based flocculant used in the present invention, the product name "Papyrus No. 525" manufactured by MC Kinsan Co., Ltd. was used in the present invention. The amount used is about 0. 3 per batch process while the capacity of the coagulation stirring tank 13 is 0.4 cubic meter.
A 28 kilogram weight is used and it is charged in about 1.5 minutes using the quantitative feeder 15. In addition, the flocculation tank agitator 13a set by the inverter is 40
From 60 Hz to 60 Hz as a standard setting value of 45 Hz (45 rpm for agitator rotation speed), 15 to 4 during slow operation
0 Hz and the standard setting value is 25 Hz (the agitator rotation speed is 25 rotations / minute), and the rotation speed is 0 to 15 at low speed operation.
The standard setting value is 10 Hz (the rotation speed of the stirrer is 10 rotations / minute).

【0023】また、各工程での時間であるが、図2の運
転タイムチャートにも記載の様に、凝集攪拌槽13の容
量が0.4立方メートルの場合で、汚泥供給工程が10
分、緩速攪拌時が5分、静置時間が5分、脱水工程が9
0分であり、汚泥脱水機16の運転時間は凝集攪拌槽1
3の汚泥移送完了後の運転時間40分を含めると合計約
130分である。汚泥脱水機16の運転時間が汚泥供
給、緩速攪拌、静置時間の総計に比べ長い為、待機工程
から汚泥供給工程への移行開始は、汚泥脱水完了時間を
見越して設定される。
Regarding the time in each step, as shown in the operation time chart of FIG. 2, when the capacity of the flocculation stirring tank 13 is 0.4 cubic meters, the sludge supply step has 10 steps.
Minutes, slow stirring 5 minutes, standing time 5 minutes, dehydration step 9
It is 0 minutes, and the operation time of the sludge dehydrator 16 is 1
Including the operation time of 40 minutes after the completion of the sludge transfer of No. 3, it is about 130 minutes in total. Since the operating time of the sludge dewatering machine 16 is longer than the total of sludge supply, slow stirring, and stationary time, the start of transition from the standby process to the sludge supply process is set in anticipation of the sludge dewatering completion time.

【0024】[0024]

【発明の効果】従来の汚泥処理における余剰汚泥脱水に
ついては、従来の技術に開示した様に連続式の設備であ
った為、常に一定の条件でしか凝集の反応プロセスを行
うことができなかった。本発明では、一定量の汚泥を凝
集攪拌槽に供給し、バッチ式に凝集プロセスが完了する
まで、攪拌を急速、緩速、静置、微速と変化させて行い
凝集剤の性能に見合った方法で、着実な凝集反応を行う
ことを可能とした。また、それによって汚泥脱水機につ
いても脱水洗浄のサイクルを回すことにより、常に良い
運転状態を保つことが出来るという効果が得られる。
As for the excess sludge dewatering in the conventional sludge treatment, since it is a continuous type equipment as disclosed in the prior art, the coagulation reaction process can always be carried out only under constant conditions. . In the present invention, a method of supplying a certain amount of sludge to a flocculation stirring tank and varying the stirring speed rapidly, slowly, statically, and slowly until the flocculation process is completed batchwise, which is suitable for the performance of the flocculant. Thus, it was possible to carry out a steady aggregation reaction. Further, by doing so, the sludge dewatering machine can be kept in good operating condition by repeating the dehydration and washing cycle.

【0025】また、凝集剤について当該発明では、粉末
を混合攪拌するだけで凝集反応が得られる天然の腐植系
凝集剤を採用した為、設備が簡素化され、従来の技術に
示したような、高分子凝集剤に見られる凝集剤を攪拌す
るタンクと攪拌機及び凝集剤を送るポンプ、また、凝集
助剤を攪拌するタンクと攪拌機、さらには、汚泥との凝
集過程における混和槽に関しても凝集助剤混和槽と凝集
剤混和槽の2槽を必要とし工程が複雑になり設備費がか
さむと共に、運用、メンテナンスの上でも複雑になると
いうような問題が解決される。
Regarding the coagulant, in the present invention, since a natural humus-based coagulant that can obtain the coagulation reaction by simply mixing and stirring the powder is adopted, the equipment is simplified and, as shown in the prior art, A tank and a stirrer that stir the flocculant found in the polymer flocculant and a pump that sends the flocculant, a tank and a stirrer that stir the flocculation aid, and also a flocculation aid in the mixing tank in the coagulation process with sludge. The problem that two tanks, a mixing tank and a coagulant mixing tank, are required, the process is complicated, the equipment cost is increased, and the operation and maintenance are complicated, is solved.

【0026】機器数で比較すると、従来の設備では汚泥
供給ポンプ、凝集剤貯留、槽凝集剤注入ポンプ、原液凝
集剤タンク及び原液凝集剤タンク用攪拌機、原液凝集剤
ポンプ、凝集剤自動溶解槽及び凝集剤自動溶解槽用攪拌
機、凝集助剤貯留タンク、凝集助剤注入ポンプ、凝集助
剤混和槽及び凝集助剤講話槽用攪拌機、凝集剤混和槽及
び凝集剤混和槽用攪拌機、汚泥脱水機と15点を要すの
に対し、当該発明で同様の処理能力を上げる為に必要な
機器数は汚泥供給・移送切替弁、汚泥供給・移送ポン
プ、凝集攪拌槽、攪拌機、定量フィーダー、汚泥脱水機
の6点と簡素化を可能とした。
In comparison with the number of equipment, in the conventional equipment, a sludge supply pump, a coagulant storage, a tank coagulant injection pump, a stock solution coagulant tank and an agitator for a stock solution coagulant tank, a stock solution coagulant pump, a coagulant automatic dissolution tank and Stirrer for coagulant automatic dissolution tank, coagulant aid storage tank, coagulant aid injection pump, coagulant aid admixture tank and coagulant aid talker tank agitator, coagulant admixture tank and coagulant admixture tank agitator, sludge dehydrator While 15 points are required, the number of equipment required to increase the same processing capacity in the present invention is a sludge supply / transfer switching valve, a sludge supply / transfer pump, a coagulation stirring tank, a stirrer, a quantitative feeder, a sludge dewatering machine. 6 points and simplification is possible.

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

【図1】本発明の汚泥処理装置の模式図である。FIG. 1 is a schematic diagram of a sludge treatment device of the present invention.

【図2】本発明の汚泥処理に関する運転タイムチャート
である。
FIG. 2 is an operation time chart relating to sludge treatment of the present invention.

【図3】従来の技術の汚泥処理装置の模式図例である。FIG. 3 is an example of a schematic view of a conventional sludge treatment device.

【符号の説明】[Explanation of symbols]

1 汚泥処理装置 2 余剰汚泥脱水部 3 生ゴミ投入部 4 発酵部 5 破砕機 6 スクリューコンンベアー 7 発酵装置 10 汚泥貯留槽 11 汚泥供給・移送切替弁 12 汚泥供給・移送ポンプ 13 凝集攪拌槽 13a 攪拌機 14 水位計 15 定量フィーダー 16 汚泥脱水機 101 原液凝集剤タンク 101a 攪拌機 102 原液凝集剤ポンプ 103 フロースイッチ 104 凝集剤自動溶解槽 106 凝集剤貯留槽 107 凝集剤注入ポンプ 108 フロースィッチ 109 凝集剤混和槽 109a 攪拌機 110 凝集助剤貯留タンク 111 凝集助剤注入ポンプ 112 凝集助剤混和槽 112a 攪拌機 113 凝集助剤注入管 120 汚泥供給ポンプ 121 フロースイッチ 122 汚泥移送管 130 上水移送管 131 上水電磁弁 140 処理水 150 流出管 160 脱水機 1 Sludge treatment equipment 2 Excess sludge dewatering section 3 Raw garbage input department 4 Fermentation Department 5 crusher 6 Screw Conveyor 7 Fermentation equipment 10 Sludge storage tank 11 Sludge supply / transfer switching valve 12 Sludge supply / transfer pump 13 Aggregation stirring tank 13a Stirrer 14 Water gauge 15 Quantitative feeder 16 Sludge dehydrator 101 Stock Solution Flocculant Tank 101a stirrer 102 Stock solution coagulant pump 103 flow switch 104 Flocculant automatic dissolution tank 106 Flocculant storage tank 107 Flocculant injection pump 108 Flow Switch 109 Flocculant mixing tank 109a stirrer 110 Flocculant storage tank 111 Agglomeration aid injection pump 112 Coagulation auxiliary agent mixing tank 112a stirrer 113 Agglutination aid injection tube 120 Sludge supply pump 121 flow switch 122 Sludge transfer pipe 130 Clean water transfer pipe 131 Water solenoid valve 140 treated water 150 outflow pipe 160 dehydrator

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】汚泥貯留槽に貯留した汚泥を凝集攪拌槽に
送り凝集攪拌槽で汚泥に凝集剤を添加し該凝集攪拌槽で
凝集剤と混合した汚泥を汚泥脱水機に送り脱水する汚泥
処理装置において、汚泥を該凝集攪拌槽の仕様容量分送
り該凝集攪拌槽にて凝集剤と混合しその凝集反応が所定
の状態になった後該容量分全てを汚泥脱水機に送ること
を繰り返すバッチ式処理をすることを特徴とする汚泥処
理装置。
1. A sludge treatment in which sludge stored in a sludge storage tank is sent to a coagulation stirring tank, a coagulant is added to the sludge in the coagulation stirring tank, and sludge mixed with the coagulant in the coagulation stirring tank is sent to a sludge dehydrator for dehydration. In the apparatus, a batch in which sludge is fed by the specified volume of the flocculation stirring tank, mixed with a flocculant in the flocculation stirring tank, and after the flocculation reaction reaches a predetermined state, the entire volume is fed to a sludge dehydrator A sludge treatment device that is characterized by performing a type treatment.
【請求項2】凝集攪拌槽に凝集剤を直接投入することを
特徴とする請求項1に記載の汚泥処理装置。
2. The sludge treatment device according to claim 1, wherein the coagulant is directly charged into the coagulation stirring tank.
【請求項3】凝集攪拌槽での攪拌に関し、攪拌機の回転
数を変化させることを特徴とする請求項1又は2に記載
の汚泥処理装置。
3. The sludge treatment device according to claim 1, wherein the number of revolutions of the stirrer is changed for stirring in the coagulation stirring tank.
【請求項4】汚泥を凝集するにあたって、腐植系凝集剤
を用いることを特徴とする請求項1、2又は3に記載の
汚泥処理装置。
4. The sludge treatment device according to claim 1, 2 or 3, wherein a humus-type flocculant is used in flocculating the sludge.
JP2001314379A 2001-10-11 2001-10-11 Sludge treatment equipment Expired - Fee Related JP3630130B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001314379A JP3630130B2 (en) 2001-10-11 2001-10-11 Sludge treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001314379A JP3630130B2 (en) 2001-10-11 2001-10-11 Sludge treatment equipment

Publications (2)

Publication Number Publication Date
JP2003117599A true JP2003117599A (en) 2003-04-22
JP3630130B2 JP3630130B2 (en) 2005-03-16

Family

ID=19132704

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006341147A (en) * 2005-06-07 2006-12-21 Tsurumi Mfg Co Ltd Method and apparatus for adjusting sludge solids supply in sludge dewatering machine
KR100854369B1 (en) * 2006-12-22 2008-09-02 주식회사 포스코 Blocking device for coagulation supply line for coagulation of oxidation scale
KR101641710B1 (en) * 2015-09-02 2016-07-22 주식회사 신우엔지니어링 Batch type waste water treatment system and treating method using the same
CN114685027A (en) * 2022-03-23 2022-07-01 江苏卓亚环保有限公司 Easily-detachable stacked spiral sludge dewatering machine and dewatering method thereof
CN114940575A (en) * 2022-05-27 2022-08-26 国投信开水环境投资有限公司 Device and method for conditioning sludge

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006341147A (en) * 2005-06-07 2006-12-21 Tsurumi Mfg Co Ltd Method and apparatus for adjusting sludge solids supply in sludge dewatering machine
KR100854369B1 (en) * 2006-12-22 2008-09-02 주식회사 포스코 Blocking device for coagulation supply line for coagulation of oxidation scale
KR101641710B1 (en) * 2015-09-02 2016-07-22 주식회사 신우엔지니어링 Batch type waste water treatment system and treating method using the same
CN114685027A (en) * 2022-03-23 2022-07-01 江苏卓亚环保有限公司 Easily-detachable stacked spiral sludge dewatering machine and dewatering method thereof
CN114940575A (en) * 2022-05-27 2022-08-26 国投信开水环境投资有限公司 Device and method for conditioning sludge

Also Published As

Publication number Publication date
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