JP2020025920A - Coagulation/sedimentation apparatus, control method for the same and sedimentation tank - Google Patents

Coagulation/sedimentation apparatus, control method for the same and sedimentation tank Download PDF

Info

Publication number
JP2020025920A
JP2020025920A JP2018151717A JP2018151717A JP2020025920A JP 2020025920 A JP2020025920 A JP 2020025920A JP 2018151717 A JP2018151717 A JP 2018151717A JP 2018151717 A JP2018151717 A JP 2018151717A JP 2020025920 A JP2020025920 A JP 2020025920A
Authority
JP
Japan
Prior art keywords
sedimentation
coagulation
tank
pit
stirring
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
JP2018151717A
Other languages
Japanese (ja)
Other versions
JP7450328B2 (en
Inventor
田中 一平
Ippei Tanaka
一平 田中
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP2018151717A priority Critical patent/JP7450328B2/en
Priority to PCT/JP2019/026495 priority patent/WO2020031566A1/en
Priority to KR1020217000419A priority patent/KR20210040935A/en
Publication of JP2020025920A publication Critical patent/JP2020025920A/en
Application granted granted Critical
Publication of JP7450328B2 publication Critical patent/JP7450328B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/28Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
    • B01D21/286Means for gentle agitation for enhancing flocculation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/712Feed mechanisms for feeding fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/01Separation of suspended solid particles from liquids by sedimentation using flocculating agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02Settling tanks with single outlets for the separated liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02Settling tanks with single outlets for the separated liquid
    • B01D21/08Settling tanks with single outlets for the separated liquid provided with flocculating compartments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/245Discharge mechanisms for the sediments
    • B01D21/2472Means for fluidising the sediments, e.g. by jets or mechanical agitators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/26Separation of sediment aided by centrifugal force or centripetal force
    • B01D21/267Separation of sediment aided by centrifugal force or centripetal force by using a cyclone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/30Control equipment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7176Feed mechanisms characterised by the means for feeding the components to the mixer using pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/75Discharge mechanisms
    • B01F35/754Discharge mechanisms characterised by the means for discharging the components from the mixer
    • B01F35/7547Discharge mechanisms characterised by the means for discharging the components from the mixer using valves, gates, orifices or openings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5209Regulation methods for flocculation or precipitation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5227Processes for facilitating the dissolution of solid flocculants in water

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Accessories For Mixers (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

To provide a coagulation/sedimentation apparatus and a sedimentation tank which can suppress solidification and fixation of sediments in a pit of the sedimentation tank, and a control method for a coagulation/sedimentation apparatus.SOLUTION: The coagulation/sedimentation apparatus comprises: first and second coagulation tanks 2 and 3 in which suspended substances in raw water are added with sedimentation accelerating materials and coagulants to be coagulated as a flock; a sedimentation tank 4; a cyclone 20 in which slurry pulled out from the sedimentation tank 4 is separated into sludge and the sedimentation accelerating materials and the separated sedimentation accelerating materials are returned to the coagulation tank 3; and a stirring member 30 including a bar-shape or a belt-shape lengthy member extending downward provided in a pit 17 of the sedimentation tank 4. The stirring member 30 has an arm 33 in a radiation direction and stirring bars 34 and 35 vertically installed in the arm.SELECTED DRAWING: Figure 1

Description

本発明は、懸濁物質を含む原水に沈降促進材と凝集剤を添加して凝集沈殿させて汚泥と処理水とに分離する凝集沈殿装置およびその制御方法に関し、とくに沈殿槽から抜き出したスラリーをサイクロンにより汚泥と沈降促進材とに分離し、沈降促進材を凝集槽に返送するよう構成された凝集沈殿装置およびその制御方法に関する。また、本発明は、この凝集沈殿装置に用いるのに好適な沈殿槽に関する。   The present invention relates to a coagulation sedimentation apparatus and a control method thereof, in which a sedimentation promoting material and a coagulant are added to raw water containing a suspended substance to cause coagulation and sedimentation to separate sludge and treated water, and a method for controlling the same. The present invention relates to a coagulation sedimentation apparatus configured to separate sludge and a sedimentation promoting material by a cyclone, and to return the sedimentation promoting material to a coagulation tank, and a control method thereof. Further, the present invention relates to a sedimentation tank suitable for use in the coagulation sedimentation apparatus.

懸濁物質(以下、SS[Suspended Solid] と称することもある。)を原水中から凝集沈殿により分離除去する凝集沈殿装置として、原水に粒径10〜200μm程度の粒状物(砂など)よりなる沈降促進材と凝集剤とを添加して凝集フロックを形成させる凝集槽と、凝集槽から流出する凝集フロックを沈降分離する沈殿槽と、沈殿槽から引き抜いたスラリーを粒状物と汚泥に分離するサイクロンとを備え、粒状物を凝集槽に返送し、汚泥を排出するよう構成された装置が知られている(特許文献1〜3)。   A coagulation sedimentation device that separates and removes suspended substances (hereinafter, also referred to as SS [Suspended Solid]) from raw water by coagulation and sedimentation, consists of granular material (sand etc.) having a particle size of about 10 to 200 μm in raw water. A flocculation tank for forming a flocculated floc by adding a settling accelerator and a flocculant; a sedimentation tank for sedimenting and separating flocculated floc flowing out of the flocculation tank; There are known devices configured to return particulate matter to a flocculation tank and discharge sludge (Patent Documents 1 to 3).

特許文献1〜3の凝集沈殿装置にあっては、凝集槽に導入された原水に無機凝集剤を添加して攪拌機で攪拌し、次いで高分子凝集剤を添加して凝集槽に導入し、攪拌機で攪拌して粒状物(砂など)とともに凝集フロックを形成させる。この凝集処理水を沈殿槽に導入して沈降分離し、沈殿槽上部から処理水を流出させる。また、沈殿槽の下部から引抜ポンプによりスラリーを抜き出し、サイクロンに送る。サイクロンでは、汚泥と粒状物とを遠心分離し、分離された汚泥が凝集沈殿装置外に排出される。サイクロンで分離された粒状物は凝集槽に返送され、再度沈殿分離に利用される。   In the coagulation sedimentation apparatuses of Patent Documents 1 to 3, the inorganic coagulant is added to the raw water introduced into the coagulation tank and stirred by a stirrer, and then the polymer coagulant is added and introduced into the coagulation tank. To form coagulated flocs with the particulate matter (sand, etc.). The coagulated water is introduced into a sedimentation tank to separate it by sedimentation, and the treated water flows out from the upper part of the sedimentation tank. Also, the slurry is extracted from the lower part of the settling tank by a drawing pump and sent to a cyclone. In the cyclone, the sludge and the particulate matter are centrifuged, and the separated sludge is discharged outside the coagulation and sedimentation device. The particulate matter separated by the cyclone is returned to the flocculation tank and reused for sedimentation.

特開2000−317220号公報JP 2000-317220 A 特開2002−355507号公報JP 2002-355507 A 特開2014−237122号公報JP 2014-237122 A

このような凝集沈殿装置の配管や沈殿槽のピットにあっては、スラリーが沈降促進材を含むところから、沈殿物等が固化し、閉塞が生じる恐れがある。   In a pipe of such a coagulating sedimentation apparatus or a pit of a sedimentation tank, a sediment or the like may be solidified and clogged because the slurry contains a sedimentation promoting material.

沈殿槽のピットの閉塞を防止するために、ピット内に回転翼を設けることが考えられる。   In order to prevent clogging of the pit of the sedimentation tank, it is conceivable to provide a rotating blade in the pit.

ピットに回転翼を設けた場合、翼とピット内の沈殿物との接触面積が大きい。そのため、沈殿物が固結した場合や、沈殿物が大量になったりした場合には、翼を駆動できなくなるおそれがある。また、それを防ぐために、トルクの大きい駆動装置を設置することが必要となる。
また、回転翼を用いると、ピット内の凝集フロックがピット内液ごと回転して共回りが発生する可能性がある。この場合、沈殿物の固結の抑制効果が弱くなることが懸念される。
When a rotating wing is provided in the pit, the contact area between the wing and the sediment in the pit is large. Therefore, when the sediment solidifies or when the sediment becomes large, the blades may not be driven. Further, in order to prevent this, it is necessary to install a driving device having a large torque.
In addition, if a rotary wing is used, there is a possibility that coagulated flocs in the pit rotate together with the liquid in the pit and co-rotate. In this case, there is a concern that the effect of suppressing the solidification of the precipitate may be weakened.

本発明は、沈殿槽のピット内における沈殿物を十分にほぐして固結しないよう分散させることができる凝集沈殿装置及び沈殿槽と、凝集沈殿装置の制御方法を提供することを目的とする。   SUMMARY OF THE INVENTION An object of the present invention is to provide a coagulating sedimentation apparatus and a sedimentation tank capable of sufficiently dispersing sediment in a pit of a sedimentation tank so that the sediment does not solidify, and a method of controlling the coagulation sedimentation apparatus.

第1発明の凝集沈殿装置は、原水が導入され、第1凝集剤により凝集処理する第1凝集槽と、該第1凝集槽から排出された第1凝集処理水が導入され、第2凝集剤と沈降促進材により凝集処理する第2凝集槽と、該第2凝集槽から排出された第2凝集処理水が導入され、処理水とスラリーとに沈降分離する沈殿槽と、該沈殿槽の底部に設けられたピットと、該ピットからスラリーを抜き出す引抜ポンプと、該ピットから抜き出したスラリーを分離汚泥と沈降促進材とに分離し、分離した沈降促進材を該第2凝集槽に戻すサイクロンとを備えた凝集沈殿装置において、該ピット内のスラリーを撹拌するピット撹拌手段が設けられており、該ピット撹拌手段は、上下方向に延在する回転軸と、該回転軸を回転させる駆動手段と、一端が該回転軸に固定され、他端が棒形または帯形の長尺部材として下方向に延伸して下端がピット内に位置する撹拌部材とを有することを特徴とする。   The first coagulation and sedimentation apparatus according to the first aspect of the invention includes a first coagulation tank into which raw water is introduced and coagulation treatment with a first coagulation agent, and a first coagulation treatment water discharged from the first coagulation tank. A second flocculation tank for performing flocculation treatment with the sedimentation promoting material, a second flocculation treatment water discharged from the second flocculation tank, introduced thereinto, and settled and separated into treated water and slurry, and a bottom portion of the precipitation tank A pit provided in the pit, a drawing pump for extracting the slurry from the pit, a cyclone for separating the slurry extracted from the pit into a separated sludge and a sedimentation promoting material, and returning the separated sedimentation promoting material to the second flocculation tank. In the coagulation sedimentation apparatus provided with, pit stirring means for stirring the slurry in the pit is provided, the pit stirring means, a rotating shaft extending in the vertical direction, a driving means for rotating the rotating shaft, , One end of the rotating shaft Is constant, the other end and having a stirring member which is the lower end extends downwards as long member of the bar-shaped or strip-shaped positioned in a pit.

本発明の一態様では、前記撹拌部材は、前記回転軸から放射方向に延出したアームと、該アームから下方に延在する撹拌バーである。   In one embodiment of the present invention, the stirring member includes an arm extending radially from the rotation axis and a stirring bar extending downward from the arm.

本発明の一態様では、前記アームは、前記回転軸の周方向に間隔をおいて複数本設けられており、各アームに、アーム長手方向に間隔をおいて複数本の前記撹拌バーが設置されている。   In one aspect of the present invention, a plurality of the arms are provided at intervals in a circumferential direction of the rotating shaft, and a plurality of the stirring bars are installed on each arm at intervals in the arm longitudinal direction. ing.

本発明の一態様では、前記撹拌バーは、垂直に交わる第1片及び第2片を備えた、L字形の水平断面形状を有しており、該第1片が前記放射方向を指向している。   In one embodiment of the present invention, the stirring bar has an L-shaped horizontal cross-sectional shape including a first piece and a second piece that intersect vertically, and the first piece is oriented in the radiation direction. I have.

本発明の一態様では、前記ピットの側周面は下方ほど小径となっており、前記撹拌バーとして、下端がピットの底面の上方に位置する第1の撹拌バーと、下端が該側周面の上方に位置する第2の撹拌バーとが設けられており、該第1の撹拌バーの下端は第2の撹拌バーの下端よりも下位となっている。   In one aspect of the present invention, the side peripheral surface of the pit has a smaller diameter toward the lower side, and the first stirring bar whose lower end is located above the bottom surface of the pit as the stirring bar, and the lower end is the side peripheral surface And a second stir bar located above the first stir bar. The lower end of the first stir bar is lower than the lower end of the second stir bar.

本発明の一態様では、前記凝集沈殿装置による凝集沈殿処理運転の停止期間中に間欠的又は連続的に前記第2凝集槽の撹拌手段を作動させる撹拌制御手段を備える。   In one embodiment of the present invention, the apparatus further includes a stirring control unit that intermittently or continuously activates the stirring unit of the second flocculation tank during a suspension period of the flocculation / sedimentation treatment operation by the flocculation / sedimentation apparatus.

本発明の一態様では、前記第1凝集槽への原水供給を停止し、所定時間が経過した後に前記引抜ポンプを停止する制御部を備える。   In one aspect of the present invention, a control unit is provided for stopping supply of raw water to the first coagulation tank and stopping the drawing pump after a predetermined time has elapsed.

第2発明の凝集沈殿装置の制御方法は、原水が導入され、第1凝集剤により凝集処理する第1凝集槽と、該第1凝集槽から排出された第1凝集処理水が導入され、第2凝集剤と沈降促進材により凝集処理する第2凝集槽と、該第2凝集槽から排出された第2凝集処理水が導入され、処理水とスラリーとに沈降分離する沈殿槽と、該沈殿槽の底部に設けられたピットと、該ピットからスラリーを抜き出す引抜ポンプと、該ピットから抜き出したスラリーを分離汚泥と沈降促進材とに分離し、分離した沈降促進材を該第2凝集槽に戻すサイクロンとを備えた凝集沈殿装置において、該第1凝集槽への原水供給を停止し、所定時間が経過した後に前記引抜ポンプを停止する制御部を備えたことを特徴とする。   In the control method of the coagulation sedimentation apparatus according to the second invention, a raw water is introduced, a first coagulation tank for coagulation treatment with a first coagulant, and a first coagulation treatment water discharged from the first coagulation tank are introduced. (2) a second coagulation tank for coagulating with a coagulant and a sedimentation promoting material, a sedimentation tank into which the second coagulation treatment water discharged from the second coagulation tank is introduced, and sedimented and separated into treated water and slurry; A pit provided at the bottom of the tank, a drawing pump for extracting the slurry from the pit, and separating the slurry extracted from the pit into a separated sludge and a sedimentation promoting material, and separating the separated sedimentation promoting material into the second flocculation tank. A coagulating sedimentation apparatus provided with a returning cyclone, comprising a control unit for stopping supply of raw water to the first coagulating tank and stopping the drawing pump after a predetermined time has elapsed.

第2発明の一態様では、前記凝集沈殿装置は、凝集沈殿処理運転の停止期間中に間欠的又は連続的に前記第2凝集槽内を撹拌する。   In one aspect of the second invention, the coagulation-sedimentation apparatus stirs the inside of the second coagulation tank intermittently or continuously during the suspension period of the coagulation-sedimentation treatment operation.

第3発明の凝集沈殿装置の制御方法は、原水が導入され、第1凝集剤により凝集処理する第1凝集槽と、該第1凝集槽から排出された第1凝集処理水が導入され、第2凝集剤と沈降促進材により凝集処理する第2凝集槽と、該第2凝集槽から排出された第2凝集処理水が導入され、処理水とスラリーとに沈降分離する沈殿槽と、該沈殿槽の底部に設けられたピットと、該ピットからスラリーを抜き出す引抜ポンプと、該ピットから抜き出したスラリーを分離汚泥と沈降促進材とに分離し、分離した沈降促進材を該第2凝集槽に戻すサイクロンとを備えた凝集沈殿装置を制御する方法において、該凝集沈殿装置を停止させるときに、該第1凝集槽への原水供給を停止し、所定時間が経過した後に前記引抜ポンプを停止するよう制御することを特徴とする。   In the control method of the coagulation sedimentation apparatus of the third invention, the raw water is introduced, the first coagulation tank for coagulation treatment with the first coagulant, and the first coagulation treatment water discharged from the first coagulation tank are introduced. (2) a second coagulation tank for coagulating with a coagulant and a sedimentation promoting material, a sedimentation tank into which the second coagulation treatment water discharged from the second coagulation tank is introduced, and sedimented and separated into treated water and slurry; A pit provided at the bottom of the tank, a drawing pump for extracting the slurry from the pit, and separating the slurry extracted from the pit into a separated sludge and a sedimentation promoting material, and separating the separated sedimentation promoting material into the second flocculation tank. In the method for controlling the coagulation and sedimentation apparatus including the returning cyclone, when the coagulation and sedimentation apparatus is stopped, supply of raw water to the first coagulation tank is stopped, and after a predetermined time has elapsed, the drawing pump is stopped. Specially to control To.

第4発明の沈殿槽は、底部にピットを有する沈殿槽において、該ピット内のスラリーを撹拌するピット撹拌手段が設けられており、該ピット撹拌手段は、上下方向に延在する回転軸と、該回転軸を回転させる駆動手段と、一端が該回転軸に固定され、他端が棒形または帯形の長尺部材として下方向に延在して下端がピット内に位置する撹拌部材とを有することを特徴とする。   The sedimentation tank of the fourth invention is a sedimentation tank having a pit at the bottom, wherein a pit stirring means for stirring the slurry in the pit is provided, and the pit stirring means comprises a rotating shaft extending in a vertical direction; Driving means for rotating the rotating shaft, and a stirring member having one end fixed to the rotating shaft, the other end extending downward as a rod-shaped or band-shaped elongated member, and a lower end positioned in the pit. It is characterized by having.

本発明の凝集沈殿装置では、撹拌部材が下方向に延伸する棒形または帯形の長尺部材を含んでおり、ピット内のスラリーを十分に撹拌することができる。このため、凝集沈殿処理効果が悪化したときに、ピット内の閉塞を抑制しつつ、凝集剤や沈降促進材の添加量を多くする運転を行うことが可能となる。   In the coagulation sedimentation apparatus of the present invention, the stirring member includes a rod-shaped or band-shaped long member extending downward, and the slurry in the pit can be sufficiently stirred. Therefore, when the effect of the coagulation / sedimentation treatment is deteriorated, it is possible to perform an operation of increasing the amount of the coagulant or the sedimentation promoting material while suppressing the clogging in the pit.

本発明の一態様では、凝集沈殿装置を停止させるときに、第1凝集槽への原水供給を停止した後、引抜ポンプを停止させることにより、ピット、引抜ライン、サイクロン内に沈降促進材が残ることが防止ないし抑制される。このため、凝集沈殿処理効果が悪化したときに、ピット、引抜ライン、サイクロン内の閉塞を抑制しつつ、凝集剤や沈降促進材の添加量を多くする運転を行うことが可能となる。   In one embodiment of the present invention, when stopping the coagulation and sedimentation device, after stopping the supply of raw water to the first coagulation tank, the drawing pump is stopped, so that the sedimentation promoting material remains in the pit, the drawing line, and the cyclone. Is prevented or suppressed. Therefore, when the effect of the coagulation and sedimentation treatment is deteriorated, it is possible to perform an operation of increasing the amount of the coagulant or the sedimentation promoting material while suppressing the clogging in the pit, the drawing line, and the cyclone.

本発明の一態様では、凝集沈殿装置の停止期間中に第2凝集槽内を撹拌することにより、第2凝集槽内での沈殿物の固化ないし固着を防止することができる。   In one embodiment of the present invention, by stirring the inside of the second flocculation tank during the suspension period of the flocculation and sedimentation device, solidification or fixation of the precipitate in the second flocculation tank can be prevented.

実施の形態に係る凝集沈殿装置の構成図である。It is a block diagram of the coagulation sedimentation apparatus which concerns on embodiment. 沈殿槽のピット部分の縦断面図である。It is a longitudinal cross-sectional view of the pit part of a sedimentation tank. 図2のIII−III線断面図である。FIG. 3 is a sectional view taken along line III-III of FIG. 2.

以下に、本発明の望ましい実施の形態を、図面を参照して説明する。図1は、実施の形態に係る凝集沈殿装置1を示している。この凝集沈殿装置1は、第1凝集槽2と、第2凝集槽3と、それに隣接配置された沈殿槽4を備えている。第1凝集槽2には、原水槽(図示略)から原水ポンプ5を介して原水が導入され、第1凝集剤として無機凝集剤(図1ではPAC)が第1薬注装置6によって添加されて、攪拌機7によって攪拌される。第1凝集槽2においては、無機凝集剤が懸濁物質を凝集させて微細なフロックが生成する。図示は省略するが、第1凝集槽2には、pH計及びpH調整剤(苛性ソーダ、硫酸、塩酸など)の添加装置とを有するpH調整装置が設けられており、第1凝集槽2内のpHを所定範囲に維持できるよう構成されている。   Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. FIG. 1 shows a coagulation sedimentation apparatus 1 according to an embodiment. This coagulation-sedimentation apparatus 1 includes a first coagulation tank 2, a second coagulation tank 3, and a sedimentation tank 4 disposed adjacent to the first coagulation tank 2. Raw water is introduced into the first flocculation tank 2 from a raw water tank (not shown) via a raw water pump 5, and an inorganic flocculant (PAC in FIG. 1) is added as a first flocculant by a first chemical injection device 6. Then, the mixture is stirred by the stirrer 7. In the first flocculation tank 2, the inorganic flocculant flocculates the suspended substance to generate fine flocs. Although not shown, the first flocculating tank 2 is provided with a pH adjusting device having a pH meter and a device for adding a pH adjusting agent (caustic soda, sulfuric acid, hydrochloric acid, etc.). It is configured so that the pH can be maintained in a predetermined range.

第1凝集槽2からの第1凝集処理水は移流口8を介して第2凝集槽3に導入され、第2凝集剤として高分子凝集剤(ポリマー)が第2薬注装置9によって添加される。第2凝集槽3内には、砂などの沈降促進材が添加されており、攪拌機10による攪拌により、沈降促進材を取り込んだ、比重の大きい凝集フロックが成長する。
撹拌機7,10(撹拌手段)は、それぞれ、回転軸と、その上部の駆動モータMと、下部の撹拌翼とで構成されている。
The first coagulation treatment water from the first coagulation tank 2 is introduced into the second coagulation tank 3 through the advection port 8, and a polymer coagulant (polymer) is added as a second coagulant by the second chemical injecting device 9. You. A sedimentation promoting material such as sand is added to the second flocculation tank 3, and the agglomerated floc having a large specific gravity and incorporating the sedimentation promoting material grows by stirring by the stirrer 10.
Each of the stirrers 7 and 10 (stirring means) includes a rotating shaft, a drive motor M at an upper portion thereof, and a lower stirring blade.

沈降促進材としては、砂のほか、各種スラグの破砕物なども用いることができる。沈降促進材の平均粒径は0.01〜0.5mm程度が好ましく、真比重は2以上特に2.5以上で4以下が好ましいが、これに限定されない。   As the sedimentation promoting material, not only sand but also crushed materials of various slags can be used. The average particle diameter of the sedimentation promoting material is preferably about 0.01 to 0.5 mm, and the true specific gravity is preferably 2 or more, particularly 2.5 or more and 4 or less, but is not limited thereto.

成長した凝集フロックを含む第2凝集処理水は、越流堰12を越流して沈殿槽4に導入される。沈殿槽4では、第2凝集処理水中の凝集フロックが沈殿する。沈殿槽4内の上部には、複数の傾斜板13よりなるセパレータが設置されており、凝集フロックの沈殿分離が促進される。セパレータを通り抜けた処理水は、流出室15を経て流出配管16から取り出される。沈殿槽4の底面は沈降促進材の安息角以上に傾斜して下方ほど縮径するテーパ形となっている。   The second flocculated water containing the flocculated flocs that have grown flows over the overflow weir 12 and is introduced into the sedimentation tank 4. In the sedimentation tank 4, flocculated flocs in the second flocculated water are precipitated. At the upper part in the sedimentation tank 4, a separator composed of a plurality of inclined plates 13 is provided to promote sedimentation and separation of flocculated flocs. The treated water that has passed through the separator is taken out of the outflow pipe 16 through the outflow chamber 15. The bottom surface of the sedimentation tank 4 has a tapered shape inclining above the angle of repose of the sedimentation promoting material and decreasing in diameter downward.

沈殿槽4には、底面に沿って旋回するレーキ14が設けられており、沈殿した凝集フロックがピット17に寄せ集められる。レーキ14の下辺部にはゴム製のヘラ(図示略)が設けられている。ピット17には撹拌部材30が設けられている。このピット17は、側周面17aと、底面17bとを有する。側周面17aは、下方ほど縮径するテーパー形となっている。   The sedimentation tank 4 is provided with a rake 14 that swivels along the bottom surface. A rubber spatula (not shown) is provided on the lower side of the rake 14. A stirring member 30 is provided in the pit 17. The pit 17 has a side peripheral surface 17a and a bottom surface 17b. The side peripheral surface 17a has a tapered shape whose diameter decreases toward the lower side.

この実施の形態では、沈殿槽4は側周面の水平断面は正方形、底面は下部ほど縮径するテーパ形であり、レーキ14の回転軸14aは沈殿槽4の軸心部に鉛直に設置されている。ピット17の底面には、回転軸14aを支持する軸受14bが設けられている。回転軸14aは上部駆動モータM(駆動手段)により回転駆動する。回転軸14aとその上部の駆動モータMと撹拌部材とでピット撹拌手段が構成されている。   In this embodiment, the sedimentation tank 4 has a square horizontal cross section of the side peripheral surface, and a tapered shape in which the bottom surface is reduced in diameter toward the bottom, and the rotating shaft 14a of the rake 14 is installed vertically at the axis of the sedimentation tank 4. ing. On the bottom surface of the pit 17, a bearing 14b for supporting the rotating shaft 14a is provided. The rotation shaft 14a is rotationally driven by an upper drive motor M (drive means). Pit stirring means is constituted by the rotating shaft 14a, the drive motor M above the rotation shaft 14a, and the stirring member.

ピット17の側周面17aの下部(又は底面17b)には、沈殿した凝集フロックを含むスラリーを抜き出すための引抜ライン18が接続されている。この引抜ライン18の接続部は、ピット17内に残留する沈降促進材の量を少なくするために、可能な限り低い位置とすることが好ましい。引抜ライン18には、抜き出したスラリーをサイクロン20に送る引抜ポンプ19が設けられている。引抜ライン18内のスラリー流速が500m/h以上となるように設計されるのが好ましい。   A drawing line 18 is connected to a lower portion (or bottom surface 17b) of the side peripheral surface 17a of the pit 17 for extracting slurry containing precipitated floc. The connecting portion of the drawing line 18 is preferably located as low as possible in order to reduce the amount of the sedimentation promoting material remaining in the pit 17. The drawing line 18 is provided with a drawing pump 19 for feeding the extracted slurry to the cyclone 20. It is preferable that the slurry flow rate in the drawing line 18 is designed to be 500 m / h or more.

サイクロン20は、軸心方向を鉛直方向として設置されている。サイクロン20では、送られてきたスラリーを遠心分離により、サイクロン軸心部に集まる汚泥と、サイクロン側周面に集まる沈降促進材とに分離する。分離された沈降促進材は、サイクロン20の底部から、配管21によって再び第2凝集槽3内に戻されて循環使用される。   The cyclone 20 is installed such that the axial direction is a vertical direction. In the cyclone 20, the sent slurry is separated by centrifugation into sludge collected at the center of the cyclone and sedimentation promoting material collected at the peripheral surface on the cyclone side. The separated sedimentation promoting material is returned from the bottom of the cyclone 20 to the second flocculation tank 3 again by the pipe 21 and used for circulation.

サイクロン20で軸心側に集められた分離汚泥は、サイクロン20の上面中央部の汚泥出口に接続された配管22に流出する。   The separated sludge collected on the axis side by the cyclone 20 flows out to the pipe 22 connected to the sludge outlet at the center of the upper surface of the cyclone 20.

この凝集沈殿装置は、原水ポンプ5、撹拌機7,10上部の駆動モータM、撹拌部材30(レーキ14)の上部の駆動モータM及び引抜ポンプ19を制御する制御器25が設置されている。   This coagulation sedimentation apparatus is provided with a raw water pump 5, a drive motor M above the stirrers 7, 10, a drive motor M above the stirrer 30 (rake 14), and a controller 25 for controlling the drawing pump 19.

撹拌部材30は、図2,3に詳細に示される通り、レーキ14の回転軸14aに固設されたフランジ31と、基端側が該フランジ31に対しリベット、ボルト等の固着手段32によって固定され、放射方向に延設された複数本のアーム33と、該アーム33からピット17内を下方に向かって延設された棒形の長尺部材としての第1及び第2の撹拌バー34,35とを有する。   As shown in detail in FIGS. 2 and 3, the stirring member 30 is fixed to a flange 31 fixed to the rotating shaft 14 a of the rake 14 and a base end side thereof is fixed to the flange 31 by fixing means 32 such as rivets and bolts. A plurality of arms 33 extending in the radial direction, and first and second stirring bars 34 and 35 as rod-shaped long members extending downward from the arms 33 in the pit 17. And

この実施の形態では、フランジ31は、ピット17の上端付近の高さに設置されているが、それよりも若干上又は下に設置されてもよい。また、アーム33は回転軸14aの周方向に90°毎に合計4本設けられているが、その本数はこれに限定されない。   In this embodiment, the flange 31 is installed at a height near the upper end of the pit 17, but may be installed slightly above or below it. Further, a total of four arms 33 are provided at every 90 ° in the circumferential direction of the rotating shaft 14a, but the number is not limited to this.

撹拌バー35はアーム33の先端側に設けられている。撹拌バー35はピット17の側周面17aの上方に位置している。撹拌バー34は、撹拌バー35とフランジ31との間に設けられている。撹拌バー34はピット17の底面17bの上方に位置している。撹拌バー35の下端とピット17の側周面17aとの上下間隔、及び撹拌バー34の下端とピット17の底面17bとの間隔は、いずれも可能な限り小さいことが好ましい。   The stirring bar 35 is provided on the tip side of the arm 33. The stirring bar 35 is located above the side peripheral surface 17 a of the pit 17. The stirring bar 34 is provided between the stirring bar 35 and the flange 31. The stirring bar 34 is located above the bottom surface 17 b of the pit 17. The vertical distance between the lower end of the stirring bar 35 and the side peripheral surface 17a of the pit 17 and the distance between the lower end of the stirring bar 34 and the bottom surface 17b of the pit 17 are preferably as small as possible.

各撹拌バー34,35は、水平断面がL字形のアングル材よりなる。撹拌バー34,35は、アーム33に重なる第1片34a,35aと、該第1片34a,35aに垂直な第2片34b,35bを有している。第1片34a,35a及び第2片34b,35bの幅は40〜150mm特に60〜90mm程度が好ましい。撹拌バー34,35の間隔は、80〜200mm特に120〜160mm程度が好ましい。   Each of the stirring bars 34 and 35 is formed of an angle material having an L-shaped horizontal cross section. The stirring bars 34, 35 have first pieces 34a, 35a overlapping the arm 33, and second pieces 34b, 35b perpendicular to the first pieces 34a, 35a. The width of the first pieces 34a, 35a and the second pieces 34b, 35b is preferably about 40 to 150 mm, particularly preferably about 60 to 90 mm. The interval between the stirring bars 34 and 35 is preferably about 80 to 200 mm, particularly preferably about 120 to 160 mm.

この実施の形態では、撹拌バーは各アーム33に2本ずつ設けられているが、3本以上設けられてもよい。   In this embodiment, two stirring bars are provided for each arm 33, but three or more stirring bars may be provided.

また、この実施の形態では、撹拌バー34,35の設置位置(回転軸14aからの距離)は各アーム33において同じとなっているが、撹拌バー34,35の設置位置を一部のアーム33で又は各アーム33毎に異ならせてもよい。   In this embodiment, the installation positions (distance from the rotation shaft 14a) of the stirring bars 34 and 35 are the same in each arm 33. However, the installation positions of the stirring bars 34 and 35 are changed to some of the arms 33. Or for each arm 33.

撹拌部材30は、図3において時計回り方向に回転駆動されるが、反時計回り方向に回転駆動されてもよい。   The stirring member 30 is driven to rotate clockwise in FIG. 3, but may be driven to rotate counterclockwise.

この凝集沈殿装置1では、撹拌部材30が回転する際に、該撹拌バー34,35がピット17内の沈殿物から受ける反力は比較的小さい。また、撹拌バー34,35がアーム35の長手方向に間隔をおいて設けられているので、共回りを防止しつつピット17内の沈殿物の全体を十分に撹拌することができる。   In the coagulating sedimentation apparatus 1, when the stirring member 30 rotates, the reaction force received by the stirring bars 34 and 35 from the sediment in the pit 17 is relatively small. Further, since the stirring bars 34 and 35 are provided at intervals in the longitudinal direction of the arm 35, the entire sediment in the pit 17 can be sufficiently stirred while preventing co-rotation.

この実施の形態では、撹拌バー34,35は、第1片34a,35aに対し垂直な第2片34b,35bを備えているので、剛性が高く、撹拌部材30が回転する際に撓むことが防止される。
この実施の形態では、長尺部材として直線状の棒形のバーが鉛直方向に設けられているが、斜め方向に設けてもよいし、曲線状でもよく、また棒形でなく帯形のもの(例えばリボンスクリュー)でもよく、共回りが発生しにくく、かつピット内のスラリーの全体を十分にほぐすことができれば特に限定されない。
In this embodiment, since the stirring bars 34 and 35 have the second pieces 34b and 35b perpendicular to the first pieces 34a and 35a, the stirring bars 34 and 35 have high rigidity and bend when the stirring member 30 rotates. Is prevented.
In this embodiment, a straight bar-shaped bar is provided as a long member in the vertical direction, but may be provided diagonally, may be curved, and may be a band rather than a bar. (For example, a ribbon screw), it is not particularly limited as long as co-rotation hardly occurs and the entire slurry in the pit can be sufficiently loosened.

この凝集沈殿装置1にあっては、原水槽(図示略)内の水位が規定水位よりも低下したときには、原水ポンプ5、第1及び第2薬注装置6,9と、撹拌機10とを停止させ、pH調整装置(図示略)と撹拌機7と引抜ポンプ19とは継続して稼働させる。   In the coagulating sedimentation apparatus 1, when the water level in a raw water tank (not shown) falls below a specified water level, the raw water pump 5, the first and second chemical injection devices 6, 9 and the stirrer 10 are connected. The operation is stopped, and the pH adjuster (not shown), the stirrer 7 and the drawing pump 19 are continuously operated.

凝集沈殿装置1の運転を停止するに際しては、まず原水ポンプ5の停止、第1及び第2薬注装置6,9の停止を行い、それから所定時間(例えば5〜20分特に5〜10分程度)が経過した後、撹拌機7,10、撹拌部材30及び引抜ポンプ19を停止させるようにするのが好ましい。このようにすれば、ピット17、引抜ライン18、サイクロン20内に残留する沈降促進材その他の沈殿物が少なくなり、沈降促進材等が固結ないし固着することが防止される。   When stopping the operation of the coagulation sedimentation apparatus 1, first, the raw water pump 5 and the first and second chemical injection apparatuses 6, 9 are stopped, and then a predetermined time (for example, about 5 to 20 minutes, especially about 5 to 10 minutes) After the elapse), it is preferable to stop the stirrers 7, 10, the stirring member 30, and the drawing pump 19. By doing so, the sedimentation promoting material and other precipitates remaining in the pit 17, the drawing line 18, and the cyclone 20 are reduced, and the sedimentation promoting material and the like are prevented from solidifying or sticking.

この凝集沈殿装置1にあっては、原水の処理を行わない運転停止期間中にも間欠的又は連続的に第2凝集槽3内を撹拌し、沈殿物の固着ないし固結を防止してもよい。なお、運転停止期間中に間欠的に撹拌する場合は、連続的に作動させる場合よりも動力コストが安価となる。   In the coagulation and sedimentation apparatus 1, even if the inside of the second coagulation tank 3 is intermittently or continuously stirred even during the operation stop period in which the raw water is not treated, it is possible to prevent the sediment from sticking or caking. Good. In the case of intermittent stirring during the operation stop period, the power cost is lower than in the case of continuous operation.

本発明に係る凝集沈殿装置およびその制御方法は、製鉄所やセメント工場等のヤード排水の処理に好適であるが、その他の各種排水の処理にも適用可能である。   The coagulating sedimentation apparatus and the method for controlling the same according to the present invention are suitable for treating yard wastewater in steel works and cement plants, but can also be applied to the treatment of other various wastewater.

本発明において使用する無機凝集剤や高分子凝集剤の種類はとくに限定されず、無機凝集剤としては、たとえばポリ塩化アルミニウム(PAC)、塩化第二鉄、硫酸第二鉄、ポリ硫酸鉄などを使用できる。高分子凝集剤としては、たとえばノニオン性、カチオン性、アニオン性あるいは両性の高分子凝集剤を用いることができる。   The type of the inorganic coagulant and the polymer coagulant used in the present invention is not particularly limited, and examples of the inorganic coagulant include polyaluminum chloride (PAC), ferric chloride, ferric sulfate, and polyiron sulfate. Can be used. As the polymer flocculant, for example, a nonionic, cationic, anionic or amphoteric polymer flocculant can be used.

上記実施の形態は本発明の一例であり、本発明は上記以外の態様とされてもよい。例えば、上記実施の形態では、撹拌部材30はレーキ14と共に回転軸14a回りに回転するものとされているが、レーキ14とは別の回転軸及び駆動手段によって回転駆動されてもよい。   The above embodiment is an example of the present invention, and the present invention may be applied to other aspects. For example, in the above-described embodiment, the stirring member 30 rotates around the rotation shaft 14a together with the rake 14, but the stirring member 30 may be rotationally driven by a rotation shaft and driving means different from the rake 14.

上記説明は凝集沈殿装置に関するものであり、沈殿槽4は凝集沈殿装置1に組み込まれたものとなっているが、上記構成の沈殿槽4は凝集沈殿装置1から独立した固液分離設備として用いられてもよい。   The above description relates to the coagulating sedimentation apparatus, and the sedimentation tank 4 is incorporated in the coagulation sedimentation apparatus 1. However, the sedimentation tank 4 having the above configuration is used as a solid-liquid separation facility independent of the coagulation sedimentation apparatus 1. You may be.

1 凝集沈殿装置
2 第1凝集槽
3 第2凝集槽
4 沈殿槽
5 原水ポンプ
6 第1薬注装置
9 第2薬注装置
19 引抜ポンプ
20 サイクロン
30 撹拌部材
33 アーム
34 第1の撹拌バー
35 第2の撹拌バー
34a,35a 第1片
34b,35b 第2片
DESCRIPTION OF SYMBOLS 1 Coagulation sedimentation apparatus 2 1st coagulation tank 3 2nd coagulation tank 4 Sedimentation tank 5 Raw water pump 6 1st chemical injection device 9 2nd chemical injection device 19 Extraction pump 20 Cyclone 30 Stirring member 33 Arm 34 1st stirring bar 35th 2 stirrer bars 34a, 35a first piece 34b, 35b second piece

Claims (11)

原水が導入され、第1凝集剤により凝集処理する第1凝集槽と、該第1凝集槽から排出された第1凝集処理水が導入され、第2凝集剤と沈降促進材により凝集処理する第2凝集槽と、該第2凝集槽から排出された第2凝集処理水が導入され、処理水とスラリーとに沈降分離する沈殿槽と、該沈殿槽の底部に設けられたピットと、該ピットからスラリーを抜き出す引抜ポンプと、該ピットから抜き出したスラリーを分離汚泥と沈降促進材とに分離し、分離した沈降促進材を該第2凝集槽に戻すサイクロンとを備えた凝集沈殿装置において、
該ピット内のスラリーを撹拌するピット撹拌手段が設けられており、
該ピット撹拌手段は、上下方向に延在する回転軸と、該回転軸を回転させる駆動手段と、一端が該回転軸に固定され、他端が棒形または帯形の長尺部材として下方向に延伸して下端がピット内に位置する撹拌部材とを有することを特徴とする凝集沈殿装置。
A first coagulation tank into which raw water is introduced and subjected to coagulation treatment with a first coagulant, and a first coagulation treatment water discharged from the first coagulation tank are introduced and coagulated by a second coagulation agent and a sedimentation promoting material. (2) a coagulation tank, a sedimentation tank into which the second coagulation treatment water discharged from the second coagulation tank is introduced, and sedimentation and separation into treated water and slurry; a pit provided at the bottom of the sedimentation tank; A coagulating sedimentation apparatus comprising: a drawing pump for extracting slurry from the pit, and a cyclone for separating the slurry extracted from the pit into a separated sludge and a sedimentation promoting material, and returning the separated sedimentation promoting material to the second coagulation tank.
Pit stirring means for stirring the slurry in the pit is provided,
The pit stirring means includes a rotating shaft extending vertically, a driving means for rotating the rotating shaft, and one end fixed to the rotating shaft and the other end in a downward direction as a rod-shaped or band-shaped elongated member. And a stirring member whose lower end is located in the pit.
前記撹拌部材は、前記回転軸から放射方向に延出したアームと、該アームから下方に延在する撹拌バーであることを特徴とする、請求項1に記載の凝集沈殿装置。   The apparatus according to claim 1, wherein the stirring member includes an arm extending radially from the rotation axis and a stirring bar extending downward from the arm. 前記アームは、前記回転軸の周方向に間隔をおいて複数本設けられており、
各アームに、アーム長手方向に間隔をおいて複数本の前記撹拌バーが設置されていることを特徴とする、請求項2に記載の凝集沈殿装置。
A plurality of the arms are provided at intervals in a circumferential direction of the rotation shaft,
The coagulating sedimentation apparatus according to claim 2, wherein a plurality of the stirring bars are provided at intervals in the arm longitudinal direction on each arm.
前記撹拌バーは、垂直に交わる第1片及び第2片を備えた、L字形の水平断面形状を有しており、
該第1片が前記放射方向を指向していることを特徴とする、請求項3に記載の凝集沈殿装置。
The stirring bar has an L-shaped horizontal cross-sectional shape with a first piece and a second piece that intersect vertically,
4. The coagulating sedimentation apparatus according to claim 3, wherein the first piece is oriented in the radiation direction.
前記ピットの側周面は下方ほど小径となっており、
前記撹拌バーとして、下端がピットの底面の上方に位置する第1の撹拌バーと、下端が該側周面の上方に位置する第2の撹拌バーとが設けられており、
該第1の撹拌バーの下端は第2の撹拌バーの下端よりも下位となっていることを特徴とする、請求項3又は4に記載の凝集沈殿装置。
The side peripheral surface of the pit has a smaller diameter as it goes down,
As the stirring bar, a first stirring bar whose lower end is located above the bottom surface of the pit, and a second stirring bar whose lower end is located above the side peripheral surface are provided,
5. The coagulating sedimentation apparatus according to claim 3, wherein the lower end of the first stirring bar is lower than the lower end of the second stirring bar.
前記凝集沈殿装置による凝集沈殿処理運転の停止期間中に間欠的又は連続的に前記第2凝集槽の撹拌手段を作動させる撹拌制御手段を備えたことを特徴とする、請求項1〜5のいずれか1項に記載の凝集沈殿装置。   6. A stirring control means for intermittently or continuously operating a stirring means of the second flocculation tank during a suspension period of a flocculation / sedimentation treatment operation by the flocculation / sedimentation apparatus, wherein: The coagulation sedimentation apparatus according to claim 1. 前記第1凝集槽への原水供給を停止し、所定時間が経過した後に前記引抜ポンプを停止する制御部を備えたことを特徴とする請求項1〜5のいずれか1項に記載の凝集沈殿装置。   The coagulation sediment according to any one of claims 1 to 5, further comprising a control unit that stops supply of raw water to the first coagulation tank and stops the drawing pump after a predetermined time has elapsed. apparatus. 原水が導入され、第1凝集剤により凝集処理する第1凝集槽と、該第1凝集槽から排出された第1凝集処理水が導入され、第2凝集剤と沈降促進材により凝集処理する第2凝集槽と、該第2凝集槽から排出された第2凝集処理水が導入され、処理水とスラリーとに沈降分離する沈殿槽と、該沈殿槽の底部に設けられたピットと、
該ピットからスラリーを抜き出す引抜ポンプと、該ピットから抜き出したスラリーを分離汚泥と沈降促進材とに分離し、分離した沈降促進材を該第2凝集槽に戻すサイクロンとを備えた凝集沈殿装置において、
該第1凝集槽への原水供給を停止し、所定時間が経過した後に前記引抜ポンプを停止する制御部を備えた
ことを特徴とする凝集沈殿装置。
A first coagulation tank into which raw water is introduced and subjected to coagulation treatment with a first coagulant, and a first coagulation treatment water discharged from the first coagulation tank are introduced and coagulated by a second coagulation agent and a sedimentation promoting material. (2) a coagulation tank, a sedimentation tank into which second coagulation treatment water discharged from the second coagulation tank is introduced, and sedimentation and separation into treated water and slurry, and a pit provided at the bottom of the sedimentation tank;
A coagulating sedimentation apparatus comprising: a drawing pump for extracting slurry from the pit; and a cyclone for separating the slurry extracted from the pit into a separated sludge and a sedimentation promoting material, and returning the separated sedimentation promoting material to the second coagulation tank. ,
A coagulation sedimentation apparatus comprising: a control unit for stopping supply of raw water to the first coagulation tank and stopping the drawing pump after a predetermined time has elapsed.
前記凝集沈殿装置は、凝集沈殿処理運転の停止期間中に間欠的又は連続的に前記第2凝集槽内を撹拌することを特徴とする、請求項8に記載の凝集沈殿装置。   The coagulation-sedimentation apparatus according to claim 8, wherein the coagulation-sedimentation apparatus intermittently or continuously stirs the inside of the second coagulation tank during a period in which the coagulation-sedimentation processing operation is stopped. 原水が導入され、第1凝集剤により凝集処理する第1凝集槽と、該第1凝集槽から排出された第1凝集処理水が導入され、第2凝集剤と沈降促進材により凝集処理する第2凝集槽と、該第2凝集槽から排出された第2凝集処理水が導入され、処理水とスラリーとに沈降分離する沈殿槽と、該沈殿槽の底部に設けられたピットと、
該ピットからスラリーを抜き出す引抜ポンプと、該ピットから抜き出したスラリーを分離汚泥と沈降促進材とに分離し、分離した沈降促進材を該第2凝集槽に戻すサイクロンとを備えた凝集沈殿装置を制御する方法において、
該凝集沈殿装置を停止させるときに、該第1凝集槽への原水供給を停止し、所定時間が経過した後に前記引抜ポンプを停止するよう制御することを特徴とする凝集沈殿装置の制御方法。
A first coagulation tank into which raw water is introduced and subjected to coagulation treatment with a first coagulant, and a first coagulation treatment water discharged from the first coagulation tank are introduced and coagulated by a second coagulation agent and a sedimentation promoting material. (2) a coagulation tank, a sedimentation tank into which second coagulation treatment water discharged from the second coagulation tank is introduced, and sedimentation and separation into treated water and slurry, and a pit provided at the bottom of the sedimentation tank;
A coagulating sedimentation device comprising a drawing pump for extracting the slurry from the pit and a cyclone for separating the slurry extracted from the pit into separated sludge and a sedimentation promoting material and returning the separated sedimentation promoting material to the second coagulation tank. In the method of controlling,
A method for controlling a coagulation-sedimentation apparatus, comprising: stopping supply of raw water to the first coagulation tank when the coagulation-sedimentation apparatus is stopped, and stopping the drawing pump after a predetermined time has elapsed.
底部にピットを有する沈殿槽において、
該ピット内のスラリーを撹拌するピット撹拌手段が設けられており、
該ピット撹拌手段は、上下方向に延在する回転軸と、該回転軸を回転させる駆動手段と、一端が該回転軸に固定され、他端が棒形または帯形の長尺部材として下方向に延在して下端がピット内に位置する撹拌部材とを有することを特徴とする沈殿槽。
In a sedimentation tank with a pit at the bottom,
Pit stirring means for stirring the slurry in the pit is provided,
The pit stirring means includes a rotating shaft extending vertically, a driving means for rotating the rotating shaft, and one end fixed to the rotating shaft and the other end in a downward direction as a rod-shaped or band-shaped elongated member. And a stirring member whose lower end is located in the pit.
JP2018151717A 2018-08-10 2018-08-10 Coagulation sedimentation device, its control method and sedimentation tank Active JP7450328B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2018151717A JP7450328B2 (en) 2018-08-10 2018-08-10 Coagulation sedimentation device, its control method and sedimentation tank
PCT/JP2019/026495 WO2020031566A1 (en) 2018-08-10 2019-07-03 Flocculation and sedimentation device, control method thereof and sedimentation tank
KR1020217000419A KR20210040935A (en) 2018-08-10 2019-07-03 Coagulation and precipitation device, its control method, and settling tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2018151717A JP7450328B2 (en) 2018-08-10 2018-08-10 Coagulation sedimentation device, its control method and sedimentation tank

Publications (2)

Publication Number Publication Date
JP2020025920A true JP2020025920A (en) 2020-02-20
JP7450328B2 JP7450328B2 (en) 2024-03-15

Family

ID=69415454

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2018151717A Active JP7450328B2 (en) 2018-08-10 2018-08-10 Coagulation sedimentation device, its control method and sedimentation tank

Country Status (3)

Country Link
JP (1) JP7450328B2 (en)
KR (1) KR20210040935A (en)
WO (1) WO2020031566A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117303535A (en) * 2023-11-28 2023-12-29 滨州市骏达再生源环保纤维有限公司 Straw pulping wastewater treatment device and treatment method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113750862B (en) * 2021-09-05 2024-04-19 广州瑞希环保工程有限公司 Dosing equipment for industrial wastewater treatment

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4832966U (en) * 1971-08-23 1973-04-20
JPS5016092B1 (en) * 1966-01-13 1975-06-10
JPS5874107A (en) * 1981-10-29 1983-05-04 Hitachi Constr Mach Co Ltd Discharging device for sludge from flocculating and settling device
JPS6122511U (en) * 1984-07-16 1986-02-10 日立造船株式会社 Thickener with solid sediment cutting device
JPS6332604U (en) * 1986-08-15 1988-03-02
JP2014237122A (en) * 2013-05-07 2014-12-18 新日鐵住金株式会社 Coagulation sedimentation equipment and method

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4073116B2 (en) 1999-05-12 2008-04-09 オルガノ株式会社 Coagulation sedimentation equipment
JP3866054B2 (en) 2001-05-31 2007-01-10 オルガノ株式会社 Aggregation precipitation apparatus and control method thereof
JP3954391B2 (en) 2002-01-15 2007-08-08 住友重機械工業株式会社 Coagulation sedimentation apparatus and operation method thereof
SI2049623T1 (en) 2006-07-12 2011-09-30 Inst Univ Ciencia I Tecnologia Use of a product comprising glycerol formal monoesters of fatty acids as a biofuel
KR101139020B1 (en) 2009-09-29 2012-04-26 엘지이노텍 주식회사 Multi-Resistive type touch screen and Manufacturing method of the same
WO2012172628A1 (en) 2011-06-13 2012-12-20 富士通株式会社 Mobile station device, base station device, communication system, and communication method
JP5874107B2 (en) 2012-01-26 2016-03-02 日本表面化学株式会社 Zinc-nickel alloy plating solution and nickel supply method
JP6332604B2 (en) 2014-02-27 2018-05-30 セイコーエプソン株式会社 Pretreatment liquid for inkjet printing and printing method
JP6763806B2 (en) * 2017-03-01 2020-09-30 オルガノ株式会社 Coagulation sedimentation device and its driving method
JP6825999B2 (en) * 2017-06-12 2021-02-03 オルガノ株式会社 Operation method of coagulation sedimentation device and coagulation sedimentation device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5016092B1 (en) * 1966-01-13 1975-06-10
JPS4832966U (en) * 1971-08-23 1973-04-20
JPS5874107A (en) * 1981-10-29 1983-05-04 Hitachi Constr Mach Co Ltd Discharging device for sludge from flocculating and settling device
JPS6122511U (en) * 1984-07-16 1986-02-10 日立造船株式会社 Thickener with solid sediment cutting device
JPS6332604U (en) * 1986-08-15 1988-03-02
JP2014237122A (en) * 2013-05-07 2014-12-18 新日鐵住金株式会社 Coagulation sedimentation equipment and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117303535A (en) * 2023-11-28 2023-12-29 滨州市骏达再生源环保纤维有限公司 Straw pulping wastewater treatment device and treatment method
CN117303535B (en) * 2023-11-28 2024-02-20 滨州市骏达再生源环保纤维有限公司 Straw pulping wastewater treatment device and treatment method

Also Published As

Publication number Publication date
JP7450328B2 (en) 2024-03-15
WO2020031566A1 (en) 2020-02-13
KR20210040935A (en) 2021-04-14

Similar Documents

Publication Publication Date Title
RU2316483C2 (en) Device and method for mineral slurry precipitation
JP3691768B2 (en) Sludge treatment method
KR100599985B1 (en) Coagulation reaction device
CN109661261B (en) Coagulation sedimentation device
JP2010274199A (en) Coagulation sedimentation apparatus
JP2010214360A (en) Solid separation system
KR102406986B1 (en) Wastewater treatment device
KR20070043687A (en) Coagulating and separating apparatus
WO2020031566A1 (en) Flocculation and sedimentation device, control method thereof and sedimentation tank
JP6067268B2 (en) Water treatment system
JP2010207670A (en) Device for treating turbid water
JP5173538B2 (en) Water treatment method
KR101606845B1 (en) Processing Equipment For Muddy Water
KR20170011845A (en) Rapid flocculation and coagulation tank and water treatment apparatus comprising the same
JP2012035221A (en) Apparatus for flocculation and precipitation treatment and method for flocculation precipitation treatment
KR102583508B1 (en) Water treatment device with integrated ballast flocculation and decantation and corresponding method
KR200421751Y1 (en) Precipitation having circular inclined plate
JP2000317214A (en) Flocculating and settling device
JP2017013029A (en) Flocculation tank and flocculation treatment method
JPH1034162A (en) Wastewater treatment apparatus
US11319247B2 (en) Fine grit classifier
KR101077248B1 (en) Solid and liquid separator using micro bubble
JP6825999B2 (en) Operation method of coagulation sedimentation device and coagulation sedimentation device
KR101726747B1 (en) Packaged mobile plant system for water treatment
JP2009022873A (en) Sludge flocculating/mixing device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20210329

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20220419

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20221004

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20221227

C60 Trial request (containing other claim documents, opposition documents)

Free format text: JAPANESE INTERMEDIATE CODE: C60

Effective date: 20221227

A911 Transfer to examiner for re-examination before appeal (zenchi)

Free format text: JAPANESE INTERMEDIATE CODE: A911

Effective date: 20230112

C21 Notice of transfer of a case for reconsideration by examiners before appeal proceedings

Free format text: JAPANESE INTERMEDIATE CODE: C21

Effective date: 20230117

A912 Re-examination (zenchi) completed and case transferred to appeal board

Free format text: JAPANESE INTERMEDIATE CODE: A912

Effective date: 20230217

C211 Notice of termination of reconsideration by examiners before appeal proceedings

Free format text: JAPANESE INTERMEDIATE CODE: C211

Effective date: 20230221

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20240119

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20240305

R150 Certificate of patent or registration of utility model

Ref document number: 7450328

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150