JP5465638B2 - Sediment separation system and water separator for sand basin - Google Patents

Sediment separation system and water separator for sand basin Download PDF

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JP5465638B2
JP5465638B2 JP2010196906A JP2010196906A JP5465638B2 JP 5465638 B2 JP5465638 B2 JP 5465638B2 JP 2010196906 A JP2010196906 A JP 2010196906A JP 2010196906 A JP2010196906 A JP 2010196906A JP 5465638 B2 JP5465638 B2 JP 5465638B2
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忠則 友永
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Sumitomo Heavy Industries Environment Co Ltd
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Description

本発明は、沈砂池に貯められた原水から砂を分離する沈砂分離システムに関する。   The present invention relates to a sand settling system for separating sand from raw water stored in a sand settling basin.

沈砂池設備では、沈砂池の底に沈殿した砂を噴射ノズル等によって集砂ピットに収集し、集砂ピットに収集された砂を含む原水をジェットポンプやサンドポンプ等のポンプ動力によって沈砂分離機まで揚水し、揚砂水から沈砂分離機によって砂を分離し除去している。この沈砂分離機には、揚砂水を貯めるための槽が設けられているが、この槽の小型化が図れると沈砂分離機を小型化することが可能となり好ましい。   In the sand basin facility, the sand settled at the bottom of the sand basin is collected in a sand collection pit by a jet nozzle, etc., and the raw water containing the sand collected in the sand collection pit is collected by a sand pump using a jet pump or sand pump The sand is separated and removed from the pumped water by a sand settling machine. This sand settling machine is provided with a tank for storing the pumped-up water. However, if this tank can be miniaturized, it is possible to reduce the size of the sand settling machine.

ここで、実用新案登録第3128554号公報には、汚濁水から汚泥を分離するいわゆるサイクロンと呼ばれる渦流汚泥分離回収装置が開示されている。この渦流汚泥分離回収装置は円筒形より成る回流分離槽本体を有し、この回流分離槽本体の中間部には汚濁水を回流させるための回流部が、下部には逆円錐形沈殿器が内装された沈殿部が、上部には清水をオーバーフローさせて回収する益流部がそれぞれ設けられている。そして、汚濁水を回流部に流入して渦巻状の水流を発生させることで、遠心力によって汚濁水から汚泥を分離して益流部から清水を回収し、逆円錐形沈殿器の下部に設けられた排土管から汚泥を排出するようになっている。   Here, utility model registration No. 3128554 discloses a so-called cyclone eddy current sludge separation and recovery device for separating sludge from polluted water. This vortex sludge separation and recovery device has a cylindrical circulatory separation tank main body, a circulatory part for circulating sewage water is provided in the middle part of the circulatory separation tank main body, and an inverted conical precipitator is installed in the lower part. In the upper part of the settling portion, a profit flow portion for overflowing and recovering fresh water is provided. And by flowing the polluted water into the circulating section and generating a spiral water flow, the sludge is separated from the polluted water by centrifugal force, and the fresh water is collected from the profit stream section, and installed at the bottom of the inverted conical precipitator Sludge is discharged from the drainage pipe.

沈砂池設備では、上述のようなサイクロンを沈砂池と沈砂分離機との間に配設し、サイクロンによって揚砂水より上澄み液を回収すると共に、この上澄み液を分離することで、濃縮された揚砂水を沈砂分離機の槽に投入し、槽に投入する揚砂水の量を少なくして槽の小型化を実現できる。   In the sedimentation basin facility, the cyclone as described above is arranged between the sedimentation basin and the sedimentation separator, and the cyclone collects the supernatant liquid from the sanded water and separates the supernatant liquid to concentrate it. It is possible to reduce the size of the tank by putting the sanding water into the tank of the sand settling machine and reducing the amount of the sanding water charged into the tank.

実用新案登録第3128554号公報Utility Model Registration No. 3128554

しかしながら、サイクロンは汚濁水から汚泥を分離するための遠心力を得るために大きな動力を必要とするため、サイクロンを沈砂池と沈砂分離機との間に設ける場合、砂を含む原水を揚水しサイクロンに圧送する、例えばジェットポンプやサンドポンプ等の揚砂水ポンプに大きな動力が必要となり好ましくない。   However, since cyclones require a large amount of power to obtain centrifugal force to separate sludge from polluted water, when a cyclone is installed between a settling basin and a sand settling machine, raw water containing sand is pumped and the cyclone is drawn up. For example, a large amount of power is required for a pumped sand water pump such as a jet pump or a sand pump.

本発明は、このような課題を解決するために成されたものであり、揚砂水ポンプに大きな動力を必要とすることなく、揚砂水から砂を分離することができる沈砂分離システムを提供することを目的とする。   The present invention has been made to solve such a problem, and provides a sand settling system capable of separating sand from pumped water without requiring a large amount of power for the pumped sand water pump. The purpose is to do.

本発明に係る沈砂分離システムは、沈砂池から砂を含む原水を揚水する揚砂水ポンプと、揚砂水ポンプによって揚水された揚砂水を、砂を含む濃縮揚砂水と上澄み液とに分水する分水器と、分水器によって分水された濃縮揚砂水を、砂を含む固形分と分離水とに分離する固液分離装置とを備え、分水器は、正立した中空截頭円錐台から成る本体部と、本体部の側部に設けられ、揚砂水ポンプによって揚水された揚砂水を側部の接線に沿って本体部内に流入させる流入口と、本体部の流入口より上部に設けられ、本体部から溢流する上澄み液を本体部の外部へ排出する上澄み液排水部と、本体部の流入口より下部に設けられ、上澄み液が分離された濃縮揚砂水を固液分離装置へ排出する排出口とを有する。   A sand settling system according to the present invention includes a pumped-up water pump that pumps raw water containing sand from a settling basin, and a pumped-up water pumped by the pumped-up water pump into concentrated pumped-up water containing sand and a supernatant liquid. A water separator for separating water, and a solid-liquid separator for separating the concentrated pumped sand water separated by the water separator into a solid content containing sand and a separated water. A main body composed of a hollow truncated cone, an inlet provided on a side portion of the main body portion, into which the pumped water pumped by the sand pump is introduced into the main body portion along the tangent of the side portion, and the main body portion The supernatant liquid drainage part that is provided above the inlet of the main body and discharges the supernatant liquid overflowing from the main body part to the outside of the main body part, and the concentration pump that is provided below the inlet of the main body part and separated from the supernatant liquid And an outlet for discharging the sand water to the solid-liquid separator.

本発明によれば、砂を含む原水がポンプによって沈砂池から分水器まで揚水される。分水器まで揚水された揚砂水は、正立した中空截頭円錐台から成る本体部の側部に設けられた流入口から側部の接線にそって本体部内に流入されるため、本体部内には側部の円形壁面に沿った渦巻状の水流が中空截頭円錐台形状に従い下向きに良好に発生する。揚砂水が側部の壁面に沿って流れる際、揚砂水に含まれる砂は壁面と衝突し、中空截頭円錐台形状に従い壁面から下向きの力を受ける。下向きの力を受けると共に下向きの渦巻状の水流に従う砂は壁面に沿って落下し、排水口より一部の水と共に固液分離装置へ排水される。一方、砂が除去された上澄み液は砂より軽量のため本体部内を上昇し、上澄み液排出部より本体部の外部へ排出される。このように、揚砂水に含まれる砂は、分水器の壁面から下向きの力を受けると共に下向きの渦巻状の水流に従い落下することで揚砂水から分離されるため、大きな遠心力が得られなくても揚砂水から砂を容易に分離することができる。よって、揚砂水ポンプに大きな動力を必要とすることなく、揚砂水から砂を分離することができる。   According to the present invention, raw water containing sand is pumped from a sand basin to a water separator by a pump. The pumped sand water pumped up to the water separator flows into the main body part along the tangent of the side part from the inflow port provided on the side part of the main body part composed of the upright hollow truncated cone. In the part, a spiral water flow along the circular wall surface of the side part is favorably generated downward according to the shape of the hollow truncated cone. When the pumped sand water flows along the side wall surface, the sand contained in the pumped water collides with the wall surface and receives a downward force from the wall surface according to the shape of the hollow truncated cone. The sand that receives the downward force and follows the downward spiral water flow falls along the wall surface, and is drained from the drain port together with a part of the water to the solid-liquid separator. On the other hand, since the supernatant liquid from which the sand has been removed is lighter than the sand, it rises in the main body and is discharged from the supernatant liquid discharge section to the outside of the main body section. In this way, the sand contained in the pumped sand water receives a downward force from the wall of the water separator and is separated from the pumped sand water by falling in accordance with the downward spiral water flow. If not, the sand can be easily separated from the pumped water. Therefore, the sand can be separated from the pumped sand water without requiring a large power for the pumped sand water pump.

ここで、上澄み液排出部は大気開放されていると、分水器内の液面には大気圧が作用するため、分水器で発生する圧損を低減できる。   Here, if the supernatant liquid discharge part is open to the atmosphere, atmospheric pressure acts on the liquid level in the water separator, so that the pressure loss generated in the water separator can be reduced.

本発明によれば、揚砂水ポンプに大きな動力を必要とすることなく、揚砂水から砂を分離することができる。   ADVANTAGE OF THE INVENTION According to this invention, sand can be isolate | separated from a sand pumping water, without requiring big motive power for a sand pump.

本発明の実施形態に係る沈砂分離システムを示す概略構成図である。It is a schematic structure figure showing a sedimentation separation system concerning an embodiment of the present invention. 本発明の実施形態に係る分水器を示す図である。It is a figure which shows the water divider which concerns on embodiment of this invention. 従来のサイクロンを示す断面図である。It is sectional drawing which shows the conventional cyclone.

以下、図面を参照しつつ本発明の沈砂分離システムの好適な実施形態について詳細に説明する。   Hereinafter, a preferred embodiment of a sand sedimentation separation system of the present invention will be described in detail with reference to the drawings.

図1は、本発明の実施形態に係る沈砂分離システムを示す概略構成図である。   FIG. 1 is a schematic configuration diagram showing a sedimentation separation system according to an embodiment of the present invention.

本実施形態に係る沈砂分離システム100は、例えば下水処理場等の沈砂池設備に適用される。この沈砂分離システム100は沈砂池1を備えており、この沈砂池1は砂等の沈降性物質(以下、単に砂と称す)Sを含有する原水Dを導入する。沈砂池1の池底中心部には、砂Sを収集するための集砂ピット11が設けられている。   The sedimentation separation system 100 according to this embodiment is applied to a sedimentation basin facility such as a sewage treatment plant, for example. The sand settling system 100 includes a sand settling basin 1. The sand settling basin 1 introduces raw water D containing settling substances (hereinafter simply referred to as sand) S such as sand. A sand collection pit 11 for collecting sand S is provided at the center of the pond bottom of the sand basin 1.

沈砂池1には底部近傍に噴射ノズル2A〜2Dがそれぞれ設けられており、各噴射ノズル2A〜2Dはそれぞれ電動弁3A〜3Dを介して高圧ポンプ4と接続されている。この高圧ポンプ4は供給水タンク5に接続されており、この供給水タンク5には供給水Wが貯められている。そして高圧ポンプ4は、その駆動により、供給水Wを各噴射ノズル2A〜2Dに圧送し、各噴射ノズル2A〜2Dから高圧水を噴射させ、沈砂池1の池底に沈降した砂を集砂ピット11に収集する。   In the sand basin 1, injection nozzles 2A to 2D are respectively provided in the vicinity of the bottom, and each of the injection nozzles 2A to 2D is connected to the high-pressure pump 4 via electric valves 3A to 3D, respectively. The high-pressure pump 4 is connected to a supply water tank 5, and supply water W is stored in the supply water tank 5. The high-pressure pump 4 is driven to pump the supply water W to each of the injection nozzles 2A to 2D and to inject high-pressure water from each of the injection nozzles 2A to 2D. Collect in pit 11.

集砂ピット11の上方にはジェットポンプ(揚砂水ポンプ)6が設けられている。このジェットポンプ6は、吸込部61、エジェクタ部62及び揚砂管63を有しており、高圧ポンプ4に接続されている。そして、ジェットポンプ6は、高圧ポンプにより供給水Wが圧送されると、エジェクタ部62で揚砂管63内に高圧水を噴射し、この高圧水の噴射によって生じるエジェクタ機能(いわゆるジェットポンプ機能)によって、集砂ピット11に収集された砂Sを集砂ピット11付近の原水Dと共に吸込部61から吸い込み揚水する。   Above the sand collecting pit 11, a jet pump (pumped water pump) 6 is provided. This jet pump 6 has a suction part 61, an ejector part 62 and a sand raising pipe 63, and is connected to the high-pressure pump 4. When the supply water W is pumped by the high-pressure pump, the jet pump 6 injects high-pressure water into the sand pipe 63 by the ejector 62, and an ejector function (so-called jet pump function) generated by this high-pressure water injection. Thus, the sand S collected in the sand collection pit 11 is sucked and pumped from the suction portion 61 together with the raw water D in the vicinity of the sand collection pit 11.

沈砂池1の上方には、沈砂分離器(固液分離装置)7が設けられており、さらに沈砂分離器7の上方には、ジェットポンプ6と沈砂分離器7とに接続される分水器8が設置されている。図2は分水器8を示す図であり、図2(a)は平面図、図2(b)は図2(a)中のIIb-IIb矢視図、図2(c)は図2(a)中のIIc-IIc矢視図をそれぞれ示している。   Above the settling basin 1, a settling sand separator (solid-liquid separator) 7 is provided. Above the settling sand separator 7, a water separator connected to the jet pump 6 and the settling sand separator 7. 8 is installed. FIG. 2 is a view showing the water diverter 8. FIG. 2 (a) is a plan view, FIG. 2 (b) is a view taken along the arrow IIb-IIb in FIG. 2 (a), and FIG. The IIc-IIc arrow directional view in (a) is shown, respectively.

図2に示すように、分水器8は、成立した中空截頭円錐台から成る本体部81を有している。この本体部81の側部であって上下方向略中央部には、本体部81の側部の接線に沿って流入口82が設けられており、この流入口82はジェットポンプ6の揚砂管63に接続されている(図1参照)。   As shown in FIG. 2, the water separator 8 has a main body portion 81 formed of a formed hollow truncated cone. An inlet 82 is provided along the tangent to the side of the main body 81 at a side portion of the main body 81 and at a substantially central portion in the vertical direction. The inlet 82 is a sandpipe of the jet pump 6. 63 (see FIG. 1).

本体部81の上端部は開口して開口部83となっており、本体部81の上部には開口部83から溢流した上澄み液を受けられるように、皿状のオーバーフロー受(上澄み液排水部)84が設けられている。このオーバーフロー受84は、上部が大気開放されている。オーバーフロー受84には上澄み液排水口85が設けられており、上澄み液排水口85に接続された配管は沈砂池1まで延びている(図1参照)。そして、本体部81の底部であって側部壁面の近傍には、上澄み液が分離された濃縮揚砂水を沈砂分離器7へ排出するための下部排出口86が設けられている。   The upper end portion of the main body portion 81 is opened to form an opening portion 83, and the upper portion of the main body portion 81 receives a supernatant liquid overflowing from the opening portion 83. ) 84 is provided. The overflow receiver 84 is open to the atmosphere at the top. The overflow receiver 84 is provided with a supernatant liquid drain port 85, and a pipe connected to the supernatant liquid drain port 85 extends to the sand basin 1 (see FIG. 1). In the vicinity of the side wall surface at the bottom of the main body 81, a lower discharge port 86 is provided for discharging concentrated sanded water from which the supernatant liquid has been separated to the sand settling separator 7.

図1に戻り、沈砂分離器7には、分水器8の下部排出口86から排出された濃縮揚砂水を貯留する本体槽71が設けられている。この本体槽71には、貯留された濃縮揚砂水中の砂Sを水切りしながら斜め上方に搬送し固形分として分離するスクリューコンベア72が取り付けられていると共に、このスクリューコンベア72には、搬送された固形分を排出するための排出部73が設けられている。そして、本体槽71には、砂Sが分離された分離水を沈砂池1に戻すための配管が接続されている。   Returning to FIG. 1, the sand set separator 7 is provided with a main body tank 71 for storing concentrated pumped water discharged from the lower discharge port 86 of the water separator 8. The main body tank 71 is attached with a screw conveyor 72 that transports the sand S in the concentrated concentrated sanded water obliquely upward while draining it and separates it as a solid content. A discharge portion 73 for discharging the solid content is provided. The main body tank 71 is connected to a pipe for returning the separated water from which the sand S has been separated to the settling basin 1.

このような沈砂分離システム100では、砂Sを含む原水Dがジェットポンプ6によって沈砂池1から分水器8まで揚水され、分水器8まで揚水された揚砂水は、正立した中空截頭円錐台から成る本体部81の側部に設けられた流入口82から側部の接線に沿って本体部81内に流入される。   In such a sand settling system 100, the raw water D containing sand S is pumped from the settling basin 1 to the water separator 8 by the jet pump 6, and the pumped sand water pumped up to the water separator 8 is an upright hollow gutter. It flows into the main body 81 along the tangent of the side from an inflow port 82 provided on the side of the main body 81 composed of a truncated cone.

このとき、本体部81内には側部の円形壁面に沿った渦巻状の水流が中空截頭円錐台形状に従い下向きに良好に発生する。   At this time, a spiral water flow along the circular wall surface of the side portion is favorably generated downward in the main body portion 81 according to the shape of the truncated truncated cone.

揚砂水が側部の壁面に沿って流れる際、揚砂水に含まれる砂Sは壁面と衝突し、中空截頭円錐台形状に従い壁面から下向きの力を受ける。従って、この下向きの力を受けると共に下向きの渦巻状の水流に従う砂Sは壁面に沿って底部まで落下し、壁面近傍に設けられた下部排水口86より一部の水と共に下方の沈砂分離器7へ排水される。   When the pumped sand water flows along the side wall surface, the sand S contained in the pumped sand water collides with the wall surface and receives a downward force from the wall surface in accordance with the hollow truncated cone shape. Accordingly, the sand S that receives the downward force and follows the downward spiral water flow falls to the bottom along the wall surface, and a sand sediment separator 7 below with a part of the water from the lower drainage port 86 provided near the wall surface. Drained into

一方、砂Sが除去された上澄み液は砂Sより軽量のため本体部81内を上昇し、開口部83よりオーバーフロー受84に溢流して上澄み液排水口85から本体部81の外部へ排出され、沈砂池1へ戻される。   On the other hand, since the supernatant liquid from which the sand S has been removed is lighter than the sand S, it rises in the main body 81, overflows from the opening 83 into the overflow receiver 84, and is discharged from the supernatant liquid outlet 85 to the outside of the main body 81. Return to the settling basin 1.

このように、本実施形態に係る分水器8では、揚砂水に含まれた砂Sは、分水器8の壁面から下向きの力を受けると共に下向きの渦巻状の水流に従い落下することで揚砂水から分離されるため、大きな遠心力が得られなくても揚砂水から砂Sを容易に分離することができる。よって、ジェットポンプ6に大きな動力を必要とすることなく、揚砂水から砂Sを分離することができる。   Thus, in the water separator 8 according to the present embodiment, the sand S contained in the pumped water receives a downward force from the wall surface of the water separator 8 and falls according to the downward spiral water flow. Since it is separated from the pumped sand water, the sand S can be easily separated from the pumped sand water even if a large centrifugal force is not obtained. Therefore, the sand S can be separated from the pumped sand water without requiring large power for the jet pump 6.

なお、図3に示すような従来のサイクロン9を採用すると、揚砂水は本体部91の上部に設けられた流入口92から側部の接線に沿って本体部91内に流入し、本体部91内の壁面に沿って渦巻状の水流が下向きに発生する。揚砂水が壁面に沿って流れる際、揚砂水に含まれる砂Sは壁面と衝突するが、本体部91の中下部は倒立した中空截頭円錐台形状であるため、砂Sは壁面より上向きの力を受ける。従って、従来のサイクロン9では、揚砂水に含まれる砂Sに下向きの力は作用せず、揚砂水ポンプに大きな動力を要することになる。   In addition, when the conventional cyclone 9 as shown in FIG. 3 is adopted, the sand pumping water flows into the main body 91 from the inlet 92 provided at the upper portion of the main body 91 along the tangent of the side, A spiral water flow is generated downward along the wall surface in 91. When the pumped sand water flows along the wall surface, the sand S contained in the pumped water collides with the wall surface, but since the middle part of the main body 91 has an inverted hollow truncated cone shape, the sand S is more than the wall surface. Receives upward force. Therefore, in the conventional cyclone 9, a downward force does not act on the sand S contained in the pumped sand water, and a large power is required for the pumped sand water pump.

また、本実施形態に係る分水器8では、流入口82から下部排水口86までの距離は任意に設定できる。これに対し、図3に示す従来のサイクロン9では、本体部91の下部が垂直方向に対して所定の角度で絞られて下部排出口93とする必要があり、これによって流入口92から下部排出口93まで距離を要し装置が大型化して製造コストが増大してしまう。一方、本実施形態に係る分水器8では、従来のサイクロン9に比して装置の小型化及び製造コストの低減を図ることができる。   Moreover, in the water divider 8 which concerns on this embodiment, the distance from the inflow port 82 to the lower drainage port 86 can be set arbitrarily. On the other hand, in the conventional cyclone 9 shown in FIG. 3, the lower portion of the main body portion 91 needs to be narrowed at a predetermined angle with respect to the vertical direction to form a lower discharge port 93, thereby A distance to the outlet 93 is required, and the apparatus becomes large and the manufacturing cost increases. On the other hand, in the water divider 8 according to the present embodiment, the apparatus can be downsized and the manufacturing cost can be reduced as compared with the conventional cyclone 9.

また、本実施形態に係る分水器8では、オーバーフロー受84が大気開放されているため、分水器8内の液面には大気圧が作用し、分水器8で発生する圧損を低減できる。   Further, in the water divider 8 according to the present embodiment, the overflow receiver 84 is open to the atmosphere, so that the atmospheric pressure acts on the liquid level in the water divider 8 and reduces the pressure loss generated in the water divider 8. it can.

また、本実施形態に係る分水器8では、本体部81の底部であって壁面近傍に下部排水口86が設けられているため、本体部81内を壁面に沿って落下する砂Sを良好に本体部81の外部へ排出することができる。   Moreover, in the water separator 8 which concerns on this embodiment, since the lower drainage port 86 is provided in the bottom part of the main-body part 81 and the wall surface vicinity, the sand S which falls along the wall surface in the main-body part 81 is favorable. It can be discharged outside the main body 81.

以上、本発明の実施形態に係る沈砂分離システムついて説明したが、本発明は上記実施形態に限られない。例えば、上記実施形態においては、分水器8のオーバーフロー受84は大気開放としているが、大気開放としないものでも良い。また、上記実施形態においては、揚砂水ポンプとしてジェットポンプ6を用いているが、ジェットポンプ6に代えてサンドポンプを用いても良い。   As mentioned above, although the sedimentation separation system which concerns on embodiment of this invention was demonstrated, this invention is not limited to the said embodiment. For example, in the above embodiment, the overflow receiver 84 of the water separator 8 is open to the atmosphere, but may not be open to the atmosphere. Moreover, in the said embodiment, although the jet pump 6 is used as a pumping sand water pump, it may replace with the jet pump 6 and a sand pump may be used.

1…沈砂池、6…ジェットポンプ(揚砂水ポンプ)、7…沈砂分離器(固液分離装置)、8…分水器、81…本体部、82…流入口、84…オーバーフロー受(上澄み液排水部)、86…下部排出口。   DESCRIPTION OF SYMBOLS 1 ... Sand basin, 6 ... Jet pump (pumped water pump), 7 ... Sand sediment separator (solid-liquid separator), 8 ... Water separator, 81 ... Main part, 82 ... Inlet, 84 ... Overflow receiver (supernatant) (Liquid drainage part), 86 ... lower discharge port.

Claims (2)

沈砂池から砂を含む原水を揚水する揚砂水ポンプと、
前記揚砂水ポンプによって揚水された揚砂水を、前記砂を含む濃縮揚砂水と上澄み液とに分水する分水器と、
前記分水器によって分水された前記濃縮揚砂水を、前記砂を含む固形分と分離水とに分離する固液分離装置とを備え、
前記分水器は、
正立した中空截頭円錐台から成る本体部と、
前記本体部の側部に設けられ、前記揚砂水ポンプによって揚水された前記揚砂水を前記側部の接線に沿って前記本体部内に流入させる流入口と、
前記本体部の前記流入口より上部に設けられ、当該本体部から溢流する前記上澄み液を当該本体部の外部へ排出する上澄み液排水部と、
前記本体部の前記流入口より下部に設けられ、前記上澄み液が分離された前記濃縮揚砂水を前記固液分離装置へ排出する排出口とを有し、
前記上澄み液排水部は大気開放されていることを特徴とする、
沈砂分離システム。
A pumping water pump for pumping raw water containing sand from a sand basin;
A water separator for diverting the pumped sand water pumped by the pumped sand water pump into a concentrated pumped sand water containing the sand and a supernatant;
A solid-liquid separation device that separates the concentrated pumped water divided by the water separator into a solid containing the sand and separated water;
The water divider is
A main body composed of an upright hollow truncated cone,
An inlet that is provided at a side of the main body, and that allows the pumped sand pumped by the sand pump to flow into the main body along a tangent to the side,
A supernatant liquid drainage part provided above the inflow port of the main body part and discharging the supernatant liquid overflowing from the main body part to the outside of the main body part;
Wherein provided in the lower than the inlet of the main body, possess an outlet for discharging the concentrated Agesuna water the supernatant liquid is separated into the solid-liquid separator,
The supernatant liquid drainage part is open to the atmosphere ,
Sand settling system.
沈砂池から揚砂水ポンプによって揚水された揚砂水を、砂を含む濃縮揚砂水と上澄み液とに分水する分水器であって、A water separator that divides the pumped sand pumped by a pumped sand pump from a sand basin into concentrated pumped sand water containing a sand and a supernatant liquid,
前記分水器は、The water divider is
正立した中空截頭円錐台から成る本体部と、A main body composed of an upright hollow truncated cone,
前記本体部の側部に設けられ、前記揚砂水ポンプによって揚水された前記揚砂水を前記側部の接線に沿って前記本体部内に流入させる流入口と、An inlet that is provided at a side of the main body, and that allows the pumped sand pumped by the sand pump to flow into the main body along a tangent to the side,
前記本体部の前記流入口より上部に設けられ、当該本体部から前記上澄み液を当該本体部の外部へ排出する上澄み液排水部と、A supernatant drainage unit provided above the inflow port of the main body, and discharging the supernatant from the main body to the outside of the main body;
前記本体部の前記流入口より下部に設けられ、前記上澄み液が分離された前記濃縮揚砂水を排出する排出口と、を有し、An outlet that is provided below the inflow port of the main body and discharges the concentrated deep-sand water from which the supernatant liquid has been separated;
前記上澄み液排水部は大気開放されていることを特徴とする、The supernatant liquid drainage part is open to the atmosphere,
沈砂池設備用分水器。Water separator for sand basin equipment.
JP2010196906A 2010-09-02 2010-09-02 Sediment separation system and water separator for sand basin Expired - Fee Related JP5465638B2 (en)

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