JP2007111676A - Operation method of sand-separating washing apparatus - Google Patents

Operation method of sand-separating washing apparatus Download PDF

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JP2007111676A
JP2007111676A JP2005308361A JP2005308361A JP2007111676A JP 2007111676 A JP2007111676 A JP 2007111676A JP 2005308361 A JP2005308361 A JP 2005308361A JP 2005308361 A JP2005308361 A JP 2005308361A JP 2007111676 A JP2007111676 A JP 2007111676A
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sand
water
solid
liquid separation
bottom wall
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Taisuke Nakano
泰典 中野
Terukazu Araoka
輝一 新阜
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Hitachi Plant Technologies Ltd
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Hitachi Plant Technologies Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an operation method of a sand-separating washing apparatus by which throughput over of the sand-separating washing apparatus can be prevented from getting over its limit by adjusting sand concentration in muddy sand mixed water at every job site. <P>SOLUTION: A back washing pipe 18 is connected from a driving water pump 22 of a jet pump 21 to the lower part of a strainer 3. A sand pumping stroke for introducing the muddy sand mixed water and a water supply back washing stroke for supplying water via the back washing pipe 18 are alternately repeated for optional time to adjust sand concentration in the muddy sand mixed water. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、砂分離洗浄装置の運転方法に関し、特に、汚砂混合水の砂濃度を現場毎に調整することにより、砂分離洗浄装置の処理能力オーバーを防止することができる砂分離洗浄装置の運転方法に関するものである。   The present invention relates to a method for operating a sand separation and cleaning device, and in particular, a sand separation and cleaning device capable of preventing the processing capacity of the sand separation and cleaning device from being exceeded by adjusting the sand concentration of the sewage mixed water for each site. It relates to the driving method.

従来、下水処理場や浄水場等の沈砂池からジェットポンプを用いて揚砂された沈砂は、比重差分離、遠心分離等を用いた固液分離装置により固液分離され、砂分のみを回収するようにしている。   Conventionally, sand that has been pumped from a sand basin such as a sewage treatment plant or water treatment plant using a jet pump is solid-liquid separated by a solid-liquid separation device using specific gravity difference separation, centrifugal separation, etc., and only the sand is collected. Like to do.

ところで、これらの砂分離洗浄装置では、大雨の後などの沈砂の堆積が多いときに、ジェットポンプが一度に大量の沈砂を揚砂することがあり、これにより、砂分離洗浄装置の処理能力をオーバーすることがある。   By the way, in these sand separation and cleaning devices, when there is a lot of sedimentation, such as after heavy rain, the jet pump may pump a large amount of sand at a time, which increases the processing capacity of the sand separation and cleaning device. May overrun.

本発明は、上記従来の砂分離洗浄装置が有する問題点に鑑み、汚砂混合水の砂濃度を現場毎に調整することにより、砂分離洗浄装置の処理能力オーバーを防止することができる砂分離洗浄装置の運転方法を提供することを目的とする。   In view of the problems of the conventional sand separation and washing apparatus, the present invention is capable of preventing the sand separation and washing apparatus from exceeding its processing capacity by adjusting the sand concentration of the sewage mixed water for each site. It aims at providing the operating method of a washing device.

上記目的を達成するため、本発明の砂分離洗浄装置の運転方法は、ジェットポンプにより汚砂混合水を固液分離槽に接線方向に導入し、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、逆さ裁頭円錐状の篩により砂と砂利とを粒径分離する砂分離洗浄装置の運転方法において、ジェットポンプの駆動水ポンプから篩の下方に逆洗管を接続し、汚砂混合水を導入する揚砂行程と、逆洗管を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整することを特徴とする。   In order to achieve the above-mentioned object, the operation method of the sand separation and washing apparatus of the present invention is to introduce sewage mixed water into the solid-liquid separation tank tangentially by a jet pump and to remove sewage sand and garbage by centrifugal force by swirl flow. In the operation method of the sand separation and washing device that disperses and separates the specific gravity and separates the particle size of sand and gravel with an inverted frustoconical sieve, a backwash pipe is connected from the jet pump drive water pump to the lower part of the sieve. In addition, the sand concentration process for introducing the sewage mixed water and the water supply backwash process for supplying water through the backwash pipe are alternately repeated at any time to adjust the sand concentration of the sewage mixed water. To do.

この場合において、前記砂分離洗浄装置が、汚砂混合水が導入される固液分離槽と、該固液分離槽の下に設置される沈降槽とを備え、前記固液分離槽が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁と、該筒壁の底部に配設された逆さ裁頭円錐状の篩からなる底壁と、該底壁の中心付近の水を外部に排出する排水ダクトとを備えることができる。   In this case, the sand separation and washing apparatus includes a solid-liquid separation tank into which the sewage mixed water is introduced, and a sedimentation tank installed under the solid-liquid separation tank, and the solid-liquid separation tank is tangential. A cylindrical tube wall that generates a swirling flow that descends along the peripheral wall by flowing in the sewage mixed water in a direction, and a bottom wall composed of an inverted frustoconical sieve disposed at the bottom of the tube wall; And a drainage duct for discharging water near the center of the bottom wall to the outside.

また、前記砂分離洗浄装置が、汚砂混合水が導入される固液分離槽と、該固液分離槽の下に設置される沈降槽とを備え、前記固液分離槽が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁と、該筒壁の底部に配設された逆さ裁頭円錐状の篩からなる底壁と、該底壁の開口部と固液分離槽の上部とを接続する循環ダクトと、該循環ダクトの一部に接続されたエジェクタとを備えることができる。   Further, the sand separation and cleaning device includes a solid-liquid separation tank into which sewage mixed water is introduced, and a sedimentation tank installed under the solid-liquid separation tank, and the solid-liquid separation tank is in a tangential direction. A cylindrical tube wall that generates a swirling flow descending along the peripheral wall by flowing in the sewage mixed water, a bottom wall made of an inverted frustoconical sieve disposed at the bottom of the tube wall, and A circulation duct connecting the opening of the bottom wall and the upper part of the solid-liquid separation tank, and an ejector connected to a part of the circulation duct can be provided.

本発明の砂分離洗浄装置の運転方法によれば、ジェットポンプにより汚砂混合水を固液分離槽に接線方向に導入し、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、逆さ裁頭円錐状の篩により砂と砂利とを粒径分離する砂分離洗浄装置の運転方法において、ジェットポンプの駆動水ポンプから篩の下方に逆洗管を接続し、汚砂混合水を導入する揚砂行程と、逆洗管を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整することから、大雨の後などにジェットポンプが一度に大量の沈砂を揚砂した場合でも、揚砂行程と給水逆洗行程とを任意の時間ずつ交互に繰り返すことにより、汚砂混合水の砂濃度を現場毎に調整することができ、これにより、砂分離洗浄装置の処理能力オーバーを防止することができる。
また、逆洗用のポンプが不要となり、従来の駆動水ポンプ1台で揚砂、集砂、給水及び逆洗をこなすことが可能となる。
According to the operation method of the sand separation and washing apparatus of the present invention, the sewage mixed water is introduced into the solid-liquid separation tank in the tangential direction by a jet pump, and the sewage sand and garbage are dispersed by centrifugal force by the swirling flow to separate the specific gravity. At the same time, in the operation method of the sand separation and washing device that separates the particle size of sand and gravel with an inverted conical sieve, a backwash pipe is connected to the lower part of the sieve from the driving water pump of the jet pump to mix the sand Since the sanding process for introducing water and the water supply backwash process for supplying water through the backwash pipe are alternately repeated for an arbitrary period of time to adjust the sand concentration of the sewage mixed water, it can be used after a heavy rain. Even when the pump pumps a large amount of sand at a time, the sand concentration of the mixed sand can be adjusted at each site by alternately repeating the sanding process and the water supply backwash process at any time. As a result, the processing capacity of the sand separation and cleaning device is increased. It is possible to prevent the over.
Moreover, a pump for backwashing becomes unnecessary, and it becomes possible to carry out sanding, sand collection, water supply and backwashing with one conventional driving water pump.

この場合、前記砂分離洗浄装置が、汚砂混合水が導入される固液分離槽と、該固液分離槽の下に設置される沈降槽とを備え、前記固液分離槽が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁と、該筒壁の底部に配設された逆さ裁頭円錐状の篩からなる底壁と、該底壁の中心付近の水を外部に排出する排水ダクトとを備えることにより、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、底壁の篩により砂と砂利とを粒径分離し、これにより、底壁の中心付近に比重差の大きいごみと砂利とを集め、比重の大きい砂利は底壁中心から沈降槽に落下させて砂と共に回収する一方、比重の小さいごみを効率よく選択的に排水ダクトにより水と共に排出することができる。
すなわち、従来では、砂とごみ、砂利が混在した状態で比重差分離をしていることから、砂の流出を抑えるために、排水ダクトの吸込流速を大きくすることができなかったが、この砂分離洗浄装置では、比重が大きく異なる砂利とごみを比重差分離するため、従来に比べて吸込流速を大きくすることが可能となり、ごみの除去効率を高めることができる。
また、排水ダクトの強い吸込流で沈降槽内の水を吸い込むことにより、底壁の篩通過流量を増やすことができ、これにより、篩効果を高めることができる。
In this case, the sand separation and washing apparatus includes a solid-liquid separation tank into which the sewage mixed water is introduced, and a sedimentation tank installed under the solid-liquid separation tank, and the solid-liquid separation tank is in a tangential direction. A cylindrical tube wall that generates a swirling flow that descends along the peripheral wall by allowing the mixed sand water to flow into the bottom wall, and a bottom wall made of an inverted frustoconical sieve disposed at the bottom of the tube wall; By providing a drainage duct for discharging water near the center of the bottom wall to the outside, the centrifugal force generated by the swirling flow disperses and separates the specific gravity and separates the specific gravity, and sand and gravel are separated by the bottom wall sieve. In this way, dust and gravel with a large specific gravity difference are collected near the center of the bottom wall, and gravel with a large specific gravity is dropped from the center of the bottom wall into the sedimentation tank and collected together with the sand, while the specific gravity is small. Garbage can be efficiently and selectively discharged together with water through the drainage duct.
That is, in the past, since the specific gravity difference separation was performed in a state where sand, waste, and gravel were mixed, the suction flow velocity of the drainage duct could not be increased in order to suppress the outflow of sand. In the separation and cleaning apparatus, gravel and waste having different specific gravities are separated by specific gravity difference, so that the suction flow rate can be increased as compared with the conventional case, and the dust removal efficiency can be increased.
Moreover, by sucking the water in the sedimentation tank with a strong suction flow of the drainage duct, the flow rate of the sieve wall passing through the bottom wall can be increased, thereby enhancing the sieving effect.

また、前記砂分離洗浄装置が、汚砂混合水が導入される固液分離槽と、該固液分離槽の下に設置される沈降槽とを備え、前記固液分離槽が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁と、該筒壁の底部に配設された逆さ裁頭円錐状の篩からなる底壁と、該底壁の開口部と固液分離槽の上部とを接続する循環ダクトと、該循環ダクトの一部に接続されたエジェクタとを備えることにより、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、底壁の篩により砂と砂利とを粒径分離して、底壁の中心付近に比重差の大きいごみと砂利を集め、エジェクタ及び循環ダクトにより一定時間毎に溜まったごみと砂利を固液分離槽内を再循環させ、運転完了後に残ったごみや砂利を槽外に引き抜くことにより、砂利と共に沈降する可能性のあるレキ片やガラス片と区別し、砂のみを回収することができる。
このとき、処分上、砂利とごみは分離する必要があるため、砂利ごみ分離機が必要となるが、砂利ごみ分離機は従来製品の上向流式分級機等を用いることができる。
Further, the sand separation and cleaning device includes a solid-liquid separation tank into which sewage mixed water is introduced, and a sedimentation tank installed under the solid-liquid separation tank, and the solid-liquid separation tank is in a tangential direction. A cylindrical tube wall that generates a swirling flow descending along the peripheral wall by flowing in the sewage mixed water, a bottom wall made of an inverted frustoconical sieve disposed at the bottom of the tube wall, and Distributing dirt sand and waste by centrifugal force due to swirling flow by providing a circulation duct connecting the opening of the bottom wall and the upper part of the solid-liquid separation tank and an ejector connected to a part of the circulation duct In addition to separating the specific gravity difference, sand and gravel are separated by particle size using a sieve on the bottom wall, and garbage and gravel with a large specific gravity difference are collected near the center of the bottom wall, and collected at regular intervals by the ejector and circulation duct. Garbage and gravel are recirculated through the solid-liquid separation tank and left after the operation is completed. By pulling out of the tank, distinguished from the gravel pieces or glass pieces which may be precipitated with gravel, it is possible to recover the sand only.
At this time, gravel and waste need to be separated for disposal, and therefore a gravel waste separator is required. As the gravel waste separator, a conventional product upward flow classifier or the like can be used.

以下、本発明の砂分離洗浄装置の運転方法の実施の形態を、図面に基づいて説明する。   DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of a method for operating a sand separation and cleaning apparatus of the present invention will be described with reference to the drawings.

図1〜図3に、本発明の砂分離洗浄装置の運転方法の第1実施例を示す。
砂分離洗浄装置は、汚砂混合水が導入される固液分離槽1と、該固液分離槽1の下に設置される沈降槽2とを備えている。
そして、固液分離槽1が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁3と、該筒壁3の底部に配設された逆さ裁頭円錐状の篩からなる底壁4と、該底壁4の中心付近の水を外部に排出する排水ダクト5とを備えている。
本実施例の砂分離洗浄装置の運転方法は、かかる砂分離洗浄装置において、ジェットポンプ21の駆動水ポンプ22から篩3の下方に逆洗管18を接続し、汚砂混合水を導入する揚砂行程と、逆洗管18を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整する。
1 to 3 show a first embodiment of the operation method of the sand separation and cleaning apparatus of the present invention.
The sand separation and cleaning device includes a solid-liquid separation tank 1 into which dirty sand mixed water is introduced, and a sedimentation tank 2 installed under the solid-liquid separation tank 1.
The solid-liquid separation tank 1 is disposed at a cylindrical cylindrical wall 3 that generates a swirling flow that descends along the peripheral wall by allowing the sewage mixed water to flow in a tangential direction, and at the bottom of the cylindrical wall 3. A bottom wall 4 made of an inverted frustoconical sieve and a drainage duct 5 for discharging water near the center of the bottom wall 4 to the outside are provided.
The operation method of the sand separating and cleaning apparatus of the present embodiment is as follows. In this sand separating and cleaning apparatus, the backwash pipe 18 is connected to the lower side of the sieve 3 from the driving water pump 22 of the jet pump 21 to introduce the contaminated sand mixed water. The sand process and the water supply back-washing process of supplying water through the backwash pipe 18 are alternately repeated at arbitrary times to adjust the sand concentration of the sewage-mixed water.

揚砂行程と給水逆洗行程の切替は、配管に配設した電動弁M1〜M5の開閉によって行う。
揚砂行程は、駆動水ポンプ22の水を通常通りジェットノズルに送ることにより揚砂し、給水逆洗行程は、電動弁M1〜M5を切り替えることにより、駆動水ポンプ22の水をジェットノズルに送らずに逆洗管18に送る。
この場合、図2に示すように、揚砂行程を任意の時間T1行った後、給水逆洗行程を任意の時間T2行い、繰り返し回数nが予定回数kになるまでこの交互運転を繰り返す。
揚砂行程時間T1が短く、予定回数kが多ければ、1回の揚砂量は少なく、また、揚砂行程時間T1が長く、予定回数kが少なければ、1回の揚砂量は多くなる。
Switching between the sanding stroke and the water supply backwashing stroke is performed by opening and closing motor-operated valves M1 to M5 disposed in the pipe.
In the sanding stroke, the water of the driving water pump 22 is sent to the jet nozzle as usual, and in the water supply backwashing stroke, the water of the driving water pump 22 is changed to the jet nozzle by switching the motorized valves M1 to M5. Send to backwash tube 18 without sending.
In this case, as shown in FIG. 2, after the sanding stroke is performed for an arbitrary time T1, the water supply backwashing stroke is performed for an arbitrary time T2, and this alternating operation is repeated until the number of repetitions n reaches the predetermined number of times k.
If the sanding stroke time T1 is short and the scheduled number of times k is large, the amount of sanding at one time is small, and if the sanding stroke time T1 is long and the number of scheduled times k is small, the amount of sanding at one time is large. .

ジェットポンプ21は大雨の後など、沈砂の堆積が多い場合、短時間で大量の沈砂が一気に揚砂される場合がある。
この場合、瞬時的な投入量が限界処理能力を大きく超える場合が予想されるため、従来のシステムに配管23を追加し、投入量を調整できるようにする。
スラブ上にジェットポンプ21を設置するときは、揚砂工程と給水逆洗工程とを一定回数カウントした後に駆動水ポンプ22を一旦停止させることができるフローとする。なお、停止期間はサンドポンプのときと同様に5〜10秒程度とする。
砂分離洗浄装置の運転は、基本的に1バッチ運転/1池とし、1番目の池の揚砂後は、揚砂ポンプを停止した後、2番目の池の揚砂を開始する。
汚砂集中処理においても長時間の連続投入は避け、適度な期間毎に休止期間を設ける。また、汚砂の受入量を制限する等の考慮が必要である。
When there is a lot of sedimentation, such as after heavy rain, the jet pump 21 may cause a large amount of sedimentation to be pumped at once.
In this case, since it is expected that the instantaneous input amount greatly exceeds the limit processing capacity, the piping 23 is added to the conventional system so that the input amount can be adjusted.
When installing the jet pump 21 on a slab, it is set as the flow which can stop the drive water pump 22 once after counting a fixed sanding process and a feed water backwash process a fixed number of times. The stop period is about 5 to 10 seconds as in the sand pump.
The operation of the sand separating and cleaning apparatus is basically one batch operation / one pond. After the sanding of the first pond, the sand pump is stopped and then the sanding of the second pond is started.
Even in the wastewater concentration treatment, continuous input for a long time is avoided, and a pause period is provided for each appropriate period. In addition, it is necessary to consider such as limiting the amount of dirt received.

次に、前記した砂分離洗浄装置を説明する。
筒壁3の上部には、反転した旋回流を越流させる分離ホッパ6が設けられるとともに、該分離ホッパ6と筒壁3との間を旋回流が通るように汚砂混合水の流入管7が接線方向に接続されている。
流入管7には、ジェットポンプ21等の揚砂ポンプ(図示省略)から汚砂混合水が圧送され、また、分離ホッパ6の周囲には、該分離ホッパ6の越流水を受ける環状の越流トラフ61が設置されている。
Next, the above sand separation and cleaning apparatus will be described.
A separation hopper 6 for allowing the inverted swirling flow to flow over is provided at the upper part of the cylindrical wall 3, and an inflow pipe 7 for the mixed waste sand so that the swirling flow passes between the separating hopper 6 and the cylindrical wall 3. Are connected tangentially.
The sand mixing water is pumped into the inflow pipe 7 from a sand pump (not shown) such as the jet pump 21, and an annular overflow that receives the overflow water of the separation hopper 6 around the separation hopper 6. A trough 61 is installed.

底壁4は、パンチングスクリーン等により篩目が形成されたすり鉢状のものからなり、中央部には開口部41が形成されている。
この底壁4は、図3(b)に示すように、コイルばね8等によって上下動可能に弾支することも可能であり、これにより、汚砂混合水の投入時に、砂利やごみの衝突、ごみの堆積や旋回流により常に変動する水圧等により、底壁4の篩が振動(揺動)し、篩面で捕捉された砂利には常に上下方向の慣性力が働くことになり、篩目への砂利の挟まりを防止することができる。
The bottom wall 4 is formed in a mortar shape having a sieve mesh formed by a punching screen or the like, and an opening 41 is formed at the center.
As shown in FIG. 3 (b), the bottom wall 4 can be elastically supported by a coil spring 8 or the like so as to move up and down. The sieve of the bottom wall 4 vibrates (oscillates) due to the water pressure that constantly fluctuates due to the accumulation of dust and the swirling flow, and the vertical gravitational force always acts on the gravel captured on the sieve surface. It is possible to prevent gravel from getting caught in the eyes.

排水ダクト5は、底壁中心の上方に開口部を有する管からなり、排水ダクト5の上方で、側壁の高さによって生じる水面のヘッド差hによって排水をオーバーフローさせることで、篩目から沈降する砂を吸い込まない程度の吸込流を発生させ、底壁4の中心付近に集まる砂利とごみの内、比重の小さいごみだけを水と共に吸い込んで外部に排出するようにしている。   The drainage duct 5 is composed of a pipe having an opening above the center of the bottom wall. The drainage duct overflows due to the head difference h of the water surface caused by the height of the side wall above the drainage duct 5, thereby sinking from the sieve mesh. A suction flow is generated so as not to suck sand, and only gravel and dust collected near the center of the bottom wall 4 are sucked together with water and discharged to the outside.

沈降槽2は、固液分離槽1の下に底壁4を境として連続的に配設されており、本実施例では、下部にスクリューコンベア9が一体に配設された矩形のものからなる。
沈降槽2には、逆洗管18が接続されており、給水逆洗行程時には、この逆洗管18を介してジェットポンプ21の駆動水ポンプ22から駆動水が供給される。
The sedimentation tank 2 is continuously disposed below the solid-liquid separation tank 1 with the bottom wall 4 as a boundary. In this embodiment, the sedimentation tank 2 is formed in a rectangular shape in which a screw conveyor 9 is integrally disposed at the lower part. .
A backwash pipe 18 is connected to the settling tank 2, and drive water is supplied from the drive water pump 22 of the jet pump 21 through the backwash pipe 18 during a water supply backwash process.

一方、上記砂分離洗浄装置において、図5に示すように、底壁4の開口部41に下方から気泡を供給し、底壁4の中心付近に乱流を発生させるエア供給装置14を設けることができる。
エア供給装置14は、ブロア15から配管16を介して、底壁4の開口部41の下方に設置した散気ノズル17から多数の微細気泡を発生させる。
また、このエア供給装置14は、図6に示すように、底壁4の裏面に下方から微細気泡を供給することもできる。
例えば、底壁4の下に設置した逆洗管18から逆洗水を供給するときには、逆洗効果を高めるために、ブロア15からのエアを散気ノズル17側から底壁裏面の逆洗ノズル19側にバルブを切り替え、底壁4の篩に付着したごみをエアブロー効果により浮上させることができる。
On the other hand, in the sand separating and cleaning apparatus, as shown in FIG. 5, an air supply device 14 that supplies bubbles from below to the opening 41 of the bottom wall 4 and generates turbulence near the center of the bottom wall 4 is provided. Can do.
The air supply device 14 generates a large number of fine bubbles from the air diffuser nozzle 17 installed below the opening 41 of the bottom wall 4 from the blower 15 through the pipe 16.
Further, as shown in FIG. 6, the air supply device 14 can also supply fine bubbles to the back surface of the bottom wall 4 from below.
For example, when backwash water is supplied from a backwash pipe 18 installed under the bottom wall 4, in order to enhance the backwash effect, air from the blower 15 is blown from the diffuser nozzle 17 side to the backwash nozzle on the back of the bottom wall. The valve is switched to the 19th side, and the dust adhering to the sieve of the bottom wall 4 can be floated by the air blow effect.

砂分離洗浄装置では、図7に示すように、ごみは、底壁4の表面上に形成される旋回流に乗って底壁4の中心付近に集まり、排水ダクト5の上向流によって引き抜かれるようになっている。
ところで、例えば、缶ジュースのプルタブや厚みの薄いゴム類等の薄板状のごみ20は、旋回流に対しては、水流を受ける面積が大きいことから流れに乗りやすい。
ところが、この薄板状のごみ20は、旋回流の作用によって縦向きの姿勢で集まることから、上向流に対しては水流を受ける面積が小さくなって流れに乗りにくくなり、これにより底壁4の開口部41から沈降する。
そこで、図5に示すように、底壁4の開口部41に下方から気泡を供給し、底壁4の中心付近に乱流を発生させることにより、縦向きの姿勢で集められた薄板状のごみ20を、乱流によって排水ダクト5に吸い込まれやすい縦向き以外の姿勢にし、これにより、沈降しやすい薄板状のごみ20を排水ダクト5の上向流で吸い込むようにする。
In the sand separating and cleaning apparatus, as shown in FIG. 7, the dust is collected in the vicinity of the center of the bottom wall 4 on the swirl flow formed on the surface of the bottom wall 4 and is extracted by the upward flow of the drainage duct 5. It is like that.
By the way, for example, the thin-plate-like garbage 20 such as a pull tab of can juice or a thin rubber is easy to ride on the swirling flow because the area receiving the water flow is large.
However, since the thin-plate-like garbage 20 is collected in a vertical posture by the action of the swirling flow, the area that receives the water flow becomes small with respect to the upward flow, and it becomes difficult to ride the flow. It settles from the opening part 41.
Therefore, as shown in FIG. 5, by supplying bubbles to the opening 41 of the bottom wall 4 from below and generating turbulent flow near the center of the bottom wall 4, thin plate-like shapes gathered in a vertical orientation are collected. The garbage 20 is placed in a posture other than the vertical direction in which it is easily sucked into the drainage duct 5 by turbulent flow, so that the thin plate-like dust 20 that tends to sink is sucked in the upward flow of the drainage duct 5.

次に、この砂分離洗浄装置の動作を説明する。
ジェットポンプ21から投入された汚砂混合水を、円筒型の固液分離槽1の接線方向から流入させることで旋回流を発生させる。
ここで発生させた旋回流による遠心力で砂と砂利とごみとが分散され、比重差分離されるとともに、底壁4の円錐篩で砂とごみを粒径分離する。
水流篩効果により円錐篩を通過した砂は矩形型の沈降槽2に沈降し、スクリューコンベア9で搬出される。
Next, the operation of this sand separation and cleaning apparatus will be described.
A swirling flow is generated by causing the sewage mixed water introduced from the jet pump 21 to flow from the tangential direction of the cylindrical solid-liquid separation tank 1.
Sand, gravel, and dust are dispersed by centrifugal force generated by the swirling flow generated here and separated by specific gravity, and sand and dust are separated by a conical sieve on the bottom wall 4.
The sand that has passed through the conical sieve due to the water sieve effect settles in the rectangular sedimentation tank 2 and is carried out by the screw conveyor 9.

一方、篩形状を円錐型としたことと旋回流によるスワール効果の相乗作用により、分離されたごみ及び砂利が自然に底壁4の中心付近に集まる。
そして、底壁4の中心で発生させた吸込流によりごみは排水と共に越流させ、また、砂利は底壁4の開口部41から沈降槽2に落下させ、砂と共に搬出させる。
従来の洗砂機は、砂とごみ、砂利が混在した状態で比重差分離をしていることから、砂の流出を抑えるために、排水ダクト5の吸込流速を大きくすることができなかったが、ここでは砂利とごみの重さが大きく異なるため、従来に比べて吸込流速を大きくすることが可能となり、ごみの除去効率を高めることができる。
また、排水ダクト5の吸込流により矩形型沈降槽2内にも流れを生じさせることで、篩の通過流量を増すことができ、篩効果を高めることができる。
On the other hand, the separated dust and gravel naturally gather near the center of the bottom wall 4 due to the synergistic effect of the conical shape of the sieve and the swirl effect caused by the swirling flow.
Then, the dust is caused to overflow with the drainage by the suction flow generated at the center of the bottom wall 4, and the gravel is dropped from the opening 41 of the bottom wall 4 to the settling tank 2 and carried out together with the sand.
Since the conventional sand washer separates the specific gravity in a state where sand, dust and gravel are mixed, the suction flow velocity of the drainage duct 5 could not be increased in order to suppress the outflow of sand. In this case, since the gravel and garbage are greatly different in weight, it is possible to increase the suction flow velocity as compared with the conventional case, and it is possible to increase the efficiency of removing the dust.
In addition, by causing a flow in the rectangular sedimentation tank 2 by the suction flow of the drainage duct 5, the passing flow rate of the sieve can be increased, and the sieving effect can be enhanced.

かくして、本実施例の砂分離洗浄装置の運転方法は、ジェットポンプ21により汚砂混合水を固液分離槽1に接線方向に導入し、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、逆さ裁頭円錐状の篩3により砂と砂利とを粒径分離する砂分離洗浄装置の運転方法において、ジェットポンプ21の駆動水ポンプ22から篩3の下方に逆洗管18を接続し、汚砂混合水を導入する揚砂行程と、逆洗管18を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整することから、大雨の後などにジェットポンプ21が一度に大量の沈砂を揚砂した場合でも、揚砂行程と給水逆洗行程とを任意の時間ずつ交互に繰り返すことにより、汚砂混合水の砂濃度を現場毎に調整することができ、これにより、砂分離洗浄装置の処理能力オーバーを防止することができる。
また、逆洗用のポンプが不要となり、従来の駆動水ポンプ1台で揚砂、集砂、給水及び逆洗をこなすことが可能となる。
Thus, in the operation method of the sand separation and washing apparatus of the present embodiment, the dirty sand mixed water is introduced into the solid-liquid separation tank 1 in the tangential direction by the jet pump 21, and the dirty sand and waste are dispersed by the centrifugal force by the swirl flow. In the operation method of the sand separating and washing apparatus that separates the specific gravity and separates the particle size of sand and gravel by the inverted conical sieve 3, the backwash pipe is provided below the sieve 3 from the driving water pump 22 of the jet pump 21. 18 is connected, and the sand concentration process for introducing the sewage mixed water and the water supply backwash process for supplying water through the backwash pipe 18 are alternately repeated for an arbitrary time to adjust the sand concentration of the sewage mixed water. Therefore, even when the jet pump 21 unloads a large amount of sand at a time after heavy rain, etc., the sand-mixed water sand can be obtained by alternately repeating the sand-rolling step and the water supply back-washing step each time. The concentration can be adjusted for each site. More, it is possible to prevent the throughput over the sand separator cleaning device.
Moreover, a pump for backwashing becomes unnecessary, and it becomes possible to carry out sanding, sand collection, water supply and backwashing with one conventional driving water pump.

この場合、砂分離洗浄装置が、汚砂混合水が導入される固液分離槽1と、該固液分離槽1の下に設置される沈降槽2とを備え、前記固液分離槽1が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁3と、該筒壁3の底部に配設された逆さ裁頭円錐状の篩からなる底壁4と、該底壁4の中心付近の水を外部に排出する排水ダクト5とを備えることにより、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、底壁4の篩により砂と砂利とを粒径分離し、これにより、底壁4の中心付近に比重差の大きいごみと砂利とを集め、比重の大きい砂利は底壁4中心から沈降槽2に落下させて砂と共に回収する一方、比重の小さいごみを効率よく選択的に排水ダクト5により水と共に排出することができる。
すなわち、従来では、砂とごみ、砂利が混在した状態で比重差分離をしていることから、砂の流出を抑えるために、排水ダクト5の吸込流速を大きくすることができなかったが、本実施例では、比重が大きく異なる砂利とごみを比重差分離するため、従来に比べて吸込流速を大きくすることが可能となり、ごみの除去効率を高めることができる。
また、排水ダクト5の強い吸込流で沈降槽2内の水を吸い込むことにより、底壁4の篩通過流量を増やすことができ、これにより、篩効果を高めることができる。
In this case, the sand separation and cleaning device includes a solid-liquid separation tank 1 into which the waste sand mixed water is introduced, and a sedimentation tank 2 installed under the solid-liquid separation tank 1, and the solid-liquid separation tank 1 is From the cylindrical tube wall 3 that generates a swirling flow descending along the peripheral wall by flowing the mixed sand water in the tangential direction, and an inverted conical sieve disposed at the bottom of the tube wall 3 Provided with a bottom wall 4 and a drainage duct 5 for discharging water near the center of the bottom wall 4 to disperse dirt sand and waste by centrifugal force due to swirling flow and separate the specific gravity difference. Sand and gravel are separated in particle size by the sieve of the wall 4, thereby collecting dust and gravel having a large specific gravity difference near the center of the bottom wall 4, and gravel having a large specific gravity is transferred from the center of the bottom wall 4 to the settling tank 2. While dropping and collecting with sand, waste with small specific gravity is efficiently and selectively collected with water by the drainage duct 5 It can be out.
That is, conventionally, since the specific gravity difference separation is performed in a state where sand, waste, and gravel are mixed, the suction flow velocity of the drainage duct 5 cannot be increased in order to suppress the outflow of sand. In the embodiment, gravel and waste having different specific gravities are separated by specific gravity difference, so that the suction flow rate can be increased as compared with the conventional case, and the removal efficiency of dust can be increased.
Moreover, by sucking the water in the sedimentation tank 2 with a strong suction flow of the drainage duct 5, the flow rate of the sieve wall passing through the bottom wall 4 can be increased, thereby enhancing the sieving effect.

また、前記底壁4を上下動可能に弾支することにより、汚砂混合水投入時に、砂利やごみの衝突、ごみの堆積や旋回流により常に変動する水圧等により、底壁4の篩が振動(揺動)し、篩面で捕捉された砂利には常に上下方向の慣性力が働くことになり、篩目への砂利の挟まりを防止することができる。
また、運転完了後、ドレンで水を引き抜きながら、流入管7から水を流入させると、流入水の落下エネルギーをばねのたわみエネルギーに変換することができ、流入を止めると篩は減衰振動を始めることから、この減衰振動による慣性力により逆洗による篩目清掃効果を得ることができる。
Further, by supporting the bottom wall 4 so as to be movable up and down, the sieve of the bottom wall 4 is caused by water pressure that constantly fluctuates due to gravel, dust collision, dust accumulation and swirling flow, etc. The gravitational force that is vibrated (oscillated) and trapped on the sieve surface is always subjected to an inertia force in the vertical direction, so that gravel can be prevented from being caught in the sieve mesh.
In addition, after the operation is completed, when water is introduced from the inflow pipe 7 while draining water with the drain, the falling energy of the inflowing water can be converted into the bending energy of the spring, and when the inflow is stopped, the sieve starts damped vibration. Therefore, the mesh cleaning effect by backwashing can be obtained by the inertial force due to the damped vibration.

一方、底壁4の開口部41に下方から気泡を供給し、底壁4の中心付近に乱流を発生させるエア供給装置14を設けることにより、旋回流によって縦向きの姿勢で集められる薄板状のごみ20を、乱流によって排水ダクト5に吸い込まれやすい姿勢にすることができ、これにより、沈降しやすい薄板状のごみ20を排水ダクト5で吸い込んで排出することができる。
また、エア供給装置14が、底壁4の裏面に下方から気泡を供給することにより、逆洗時に、底壁4の篩に付着したごみをエアブロー効果により浮上させることができる。
On the other hand, by providing an air supply device 14 that supplies bubbles from below to the opening 41 of the bottom wall 4 and generates turbulent flow near the center of the bottom wall 4, a thin plate shape that is collected in a vertical orientation by a swirling flow The waste 20 can be in a posture that can be easily sucked into the drainage duct 5 by turbulent flow, whereby the thin plate-like dust 20 that tends to settle can be sucked into the drainage duct 5 and discharged.
In addition, the air supply device 14 supplies air bubbles from below to the back surface of the bottom wall 4, so that dust attached to the screen of the bottom wall 4 can be lifted by the air blow effect during backwashing.

図8に、本発明の砂分離洗浄装置の運転方法の第2実施例を示す。
砂分離洗浄装置は、汚砂混合水が導入される固液分離槽1と、該固液分離槽1の下に設置される沈降槽2とを備えている。
そして、固液分離槽1が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁3と、該筒壁3の底部に配設された逆さ裁頭円錐状の篩からなる底壁4と、該底壁4の開口部41と固液分離槽1の上部とを接続する循環ダクト11と、該循環ダクト11の一部に接続されたエジェクタ12とを備えている。
本実施例の砂分離洗浄装置の運転方法は、かかる砂分離洗浄装置において、ジェットポンプ21の駆動水ポンプ22から篩3の下方に逆洗管18を接続し、汚砂混合水を導入する揚砂行程と、逆洗管18を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整する。
なお、図8において、第1実施例と同一部材は、同一符号を記すことによりその説明を省略する。
FIG. 8 shows a second embodiment of the operation method of the sand separation and cleaning apparatus of the present invention.
The sand separation and cleaning device includes a solid-liquid separation tank 1 into which dirty sand mixed water is introduced, and a sedimentation tank 2 installed under the solid-liquid separation tank 1.
The solid-liquid separation tank 1 is disposed at a cylindrical cylindrical wall 3 that generates a swirling flow that descends along the peripheral wall by allowing the sewage mixed water to flow in a tangential direction, and at the bottom of the cylindrical wall 3. Connected to a part of the circulation duct 11, a bottom wall 4 made of an inverted frustoconical sieve, a circulation duct 11 connecting the opening 41 of the bottom wall 4 and the upper part of the solid-liquid separation tank 1 And an ejector 12.
The operation method of the sand separating and cleaning apparatus of the present embodiment is as follows. In this sand separating and cleaning apparatus, the backwash pipe 18 is connected to the lower side of the sieve 3 from the driving water pump 22 of the jet pump 21 to introduce the contaminated sand mixed water. The sand process and the water supply back-washing process of supplying water through the backwash pipe 18 are alternately repeated at arbitrary times to adjust the sand concentration of the sewage-mixed water.
In FIG. 8, the same members as those in the first embodiment are designated by the same reference numerals, and the description thereof is omitted.

前記した第1実施例の砂分離洗浄装置は、底壁4の中心付近に沈降槽2に連通する開口部を設けているため、砂利と同じ比重、重量を持つレキ片、ガラス片等は砂利と共に沈降槽2に沈降する可能性がある。
本実施例では、更に高度にごみを除去する手段として、底壁中心の開口部41を、沈降槽2に連通させることなく、循環ダクト11に接続している。
このとき、篩上や循環ダクト11にはごみや砂利が溜まっていくので、エジェクタ12により一定時間毎に固液分離槽1内を再循環させ、篩動作を繰り返し、運転完了後に残ったごみと砂利を分岐管13から槽外に引き抜くようにする。
なお、砂利とごみは処分上分離する必要があるため、後工程に砂利ごみ分離機が必要となるが、砂利ごみ分離機は従来製品の上向流式分級機等を用いることができる。
また、砂利はコンテナ等に回収し、ごみは排水と共に流して、沈砂池に戻すようにする。
The sand separation and cleaning apparatus of the first embodiment described above is provided with an opening communicating with the settling tank 2 in the vicinity of the center of the bottom wall 4, so that the gravel pieces, glass pieces, etc. having the same specific gravity and weight as gravel are gravel. At the same time, there is a possibility of settling in the settling tank 2.
In this embodiment, the opening 41 at the center of the bottom wall is connected to the circulation duct 11 without communicating with the settling tank 2 as a means for removing dust at a higher level.
At this time, since dust and gravel accumulate on the sieve and the circulation duct 11, the inside of the solid-liquid separation tank 1 is recirculated by the ejector 12 every predetermined time, and the sieving operation is repeated. The gravel is pulled out of the tank from the branch pipe 13.
In addition, since it is necessary to isolate | separate gravel and waste on disposal, a gravel waste separator is required in a post process, but the upward flow type classifier etc. of a conventional product can be used for a gravel waste separator.
Gravel is collected in a container, etc., and waste is washed away with waste water and returned to the sand basin.

かくして、本実施例の砂分離洗浄装置の運転方法は、ジェットポンプ21により汚砂混合水を固液分離槽1に接線方向に導入し、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、逆さ裁頭円錐状の篩3により砂と砂利とを粒径分離する砂分離洗浄装置の運転方法において、ジェットポンプ21の駆動水ポンプ22から篩3の下方に逆洗管18を接続し、汚砂混合水を導入する揚砂行程と、逆洗管18を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整することから、大雨の後などにジェットポンプ21が一度に大量の沈砂を揚砂した場合でも、揚砂行程と給水逆洗行程とを任意の時間ずつ交互に繰り返すことにより、汚砂混合水の砂濃度を現場毎に調整することができ、これにより、砂分離洗浄装置の処理能力オーバーを防止することができる。
また、逆洗用のポンプが不要となり、従来の駆動水ポンプ1台で揚砂、集砂、給水及び逆洗をこなすことが可能となる。
Thus, in the operation method of the sand separation and washing apparatus of the present embodiment, the dirty sand mixed water is introduced into the solid-liquid separation tank 1 in the tangential direction by the jet pump 21, and the dirty sand and waste are dispersed by the centrifugal force generated by the swirling flow. In the operation method of the sand separating and washing apparatus that separates the specific gravity and separates the particle size of sand and gravel by the inverted conical sieve 3, the backwash pipe is provided below the sieve 3 from the driving water pump 22 of the jet pump 21. 18 is connected, and the sand concentration process for introducing the sewage mixed water and the water supply backwash process for supplying water through the backwash pipe 18 are alternately repeated for an arbitrary time to adjust the sand concentration of the sewage mixed water. Therefore, even when the jet pump 21 unloads a large amount of sand at a time after heavy rain, etc., the sand-mixed water sand can be obtained by alternately repeating the sand-rolling step and the water supply back-washing step each time. The concentration can be adjusted for each site. More, it is possible to prevent the throughput over the sand separator cleaning device.
Moreover, a pump for backwashing becomes unnecessary, and it becomes possible to carry out sanding, sand collection, water supply and backwashing with one conventional driving water pump.

この場合、砂分離洗浄装置が、汚砂混合水が導入される固液分離槽1と、該固液分離槽1の下に設置される沈降槽2とを備え、前記固液分離槽1が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁3と、該筒壁3の底部に配設された逆さ裁頭円錐状の篩からなる底壁4と、該底壁4の開口部41と固液分離槽1の上部とを接続する循環ダクト11と、該循環ダクト11の一部に接続されたエジェクタ12とを備えることにより、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、底壁4の篩により砂と砂利とを粒径分離して、底壁4の中心付近に比重差の大きいごみと砂利を集め、エジェクタ12及び循環ダクト11により一定時間毎に溜まったごみと砂利を固液分離槽1内を再循環させ、運転完了後に残ったごみや砂利を槽外に引き抜くことにより、砂利と共に沈降する可能性のあるレキ片やガラス片と区別し、砂のみを回収することができる。   In this case, the sand separation and cleaning device includes a solid-liquid separation tank 1 into which the waste sand mixed water is introduced, and a sedimentation tank 2 installed under the solid-liquid separation tank 1, and the solid-liquid separation tank 1 is From the cylindrical tube wall 3 that generates a swirling flow descending along the peripheral wall by flowing the mixed sand water in the tangential direction, and an inverted conical sieve disposed at the bottom of the tube wall 3 By providing the bottom wall 4, the circulation duct 11 that connects the opening 41 of the bottom wall 4 and the upper part of the solid-liquid separation tank 1, and the ejector 12 that is connected to a part of the circulation duct 11, Disperse dirt sand and waste by centrifugal force due to swirl flow and separate the specific gravity difference, and separate the particle size of sand and gravel by the sieve of the bottom wall 4 to dispose the waste having a large specific gravity near the center of the bottom wall 4 Gravel is collected, and the waste and gravel collected at regular intervals by the ejector 12 and the circulation duct 11 are separated into solid and liquid. Recirculates 1, by pulling the remaining dirt and gravel after the operation completes outside the tank, distinguished from potential gravel pieces or glass fragments to settle with gravel, it is possible to recover the sand only.

以上、本発明の砂分離洗浄装置の運転方法について、複数の実施例に基づいて説明したが、本発明は上記実施例に記載した構成に限定されるものではなく、その趣旨を逸脱しない範囲において適宜その構成を変更することができる。   As mentioned above, although the operating method of the sand separation washing | cleaning apparatus of this invention was demonstrated based on several Example, this invention is not limited to the structure described in the said Example, In the range which does not deviate from the meaning. The configuration can be changed as appropriate.

本発明の砂分離洗浄装置の運転方法は、汚砂混合水の砂濃度を現場毎に調整することにより、砂分離洗浄装置の処理能力オーバーを防止することから、例えば、汚砂を高度に洗浄することにより産業廃棄物の対象から除外するような砂分離洗浄装置に好適に適用することができる。   The operation method of the sand separation and cleaning apparatus of the present invention prevents the sand separation and cleaning apparatus from exceeding its processing capacity by adjusting the sand concentration of the contaminated sand mixed water for each site. By doing so, it can be suitably applied to a sand separation and cleaning apparatus that is excluded from the object of industrial waste.

本発明の砂分離洗浄装置の運転方法の実施例を示す説明図である。It is explanatory drawing which shows the Example of the operating method of the sand separation washing | cleaning apparatus of this invention. 同実施例の運転方法を示すチャート図である。It is a chart figure which shows the driving | running method of the Example. 同運転方法で使用する砂分離洗浄装置を示し、(a)はその断面図、(b)は底壁を弾支した断面図である。The sand separation washing | cleaning apparatus used by the operation method is shown, (a) is the sectional drawing, (b) is the sectional view which supported the bottom wall elastically. 同砂分離洗浄装置を示す全体図である。It is a general view which shows the sand separation washing | cleaning apparatus. 同砂分離洗浄装置にエア供給装置を設けた変形実施例を示す断面図である。It is sectional drawing which shows the modification which provided the air supply apparatus in the sand separation washing | cleaning apparatus. エア供給装置に逆洗ノズルを設けた変形実施例を示す断面図である。It is sectional drawing which shows the modification which provided the backwashing nozzle in the air supply apparatus. 旋回流と上向流による薄板状のごみの動きを示す説明図である。It is explanatory drawing which shows the motion of the thin-plate-like refuse by a swirl flow and an upward flow. 本発明の砂分離洗浄装置の運転方法の第2実施例で使用する砂分離洗浄装置を示す断面図である。It is sectional drawing which shows the sand separation washing | cleaning apparatus used in 2nd Example of the operating method of the sand separation washing | cleaning apparatus of this invention.

符号の説明Explanation of symbols

1 固液分離槽
2 沈降槽
3 筒壁(篩)
4 底壁
41 開口部
5 排水ダクト
6 分離ホッパ
61 越流トラフ
7 流入管
8 コイルばね
9 スクリューコンベア
10 逆洗ノズル(給水装置)
11 循環ダクト
12 エジェクタ
13 分岐管
14 エア供給装置
15 ブロア
16 配管
17 散気ノズル
18 逆洗管
19 逆洗ノズル
20 薄板状のごみ
21 ジェットポンプ
22 駆動水ポンプ
23 配管
1 Solid-liquid separation tank 2 Sedimentation tank 3 Tube wall (sieving)
4 bottom wall 41 opening 5 drainage duct 6 separation hopper 61 overflow trough 7 inflow pipe 8 coil spring 9 screw conveyor 10 backwash nozzle (water supply device)
DESCRIPTION OF SYMBOLS 11 Circulation duct 12 Ejector 13 Branch pipe 14 Air supply device 15 Blower 16 Piping 17 Air diffuser nozzle 18 Backwash pipe 19 Backwash nozzle 20 Thin plate-shaped garbage 21 Jet pump 22 Drive water pump 23 Piping

Claims (3)

ジェットポンプにより汚砂混合水を固液分離槽に接線方向に導入し、旋回流による遠心力で汚砂とごみとを分散し比重差分離するとともに、逆さ裁頭円錐状の篩により砂と砂利とを粒径分離する砂分離洗浄装置の運転方法において、ジェットポンプの駆動水ポンプから篩の下方に逆洗管を接続し、汚砂混合水を導入する揚砂行程と、逆洗管を介して給水する給水逆洗行程とを任意の時間ずつ交互に繰り返し、汚砂混合水の砂濃度を調整することを特徴とする砂分離洗浄装置の運転方法。   Sediment sand mixed water is introduced tangentially into the solid-liquid separation tank by a jet pump, and the sand and dust are separated and separated by specific gravity by centrifugal force generated by swirling flow. In the operation method of the sand separation and cleaning device for separating the particle size of the sand, the backwash pipe is connected to the lower part of the sieve from the driving water pump of the jet pump, The method for operating the sand separating and cleaning apparatus is characterized by adjusting the sand concentration of the sewage mixed water by alternately repeating a water supply backwashing process for supplying water in an arbitrary time. 前記砂分離洗浄装置が、汚砂混合水が導入される固液分離槽と、該固液分離槽の下に設置される沈降槽とを備え、前記固液分離槽が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁と、該筒壁の底部に配設された逆さ裁頭円錐状の篩からなる底壁と、該底壁の中心付近の水を外部に排出する排水ダクトとを備えたことを特徴とする請求項1記載の砂分離洗浄装置の運転方法。   The sand separation and cleaning device includes a solid-liquid separation tank into which dirty sand mixed water is introduced, and a sedimentation tank installed under the solid-liquid separation tank, and the solid-liquid separation tank is sand tangent in a tangential direction. A cylindrical tube wall that generates a swirling flow descending along the peripheral wall by flowing mixed water, a bottom wall made of an inverted frustoconical sieve disposed at the bottom of the tube wall, and the bottom wall The operation method of the sand separation washing | cleaning apparatus of Claim 1 provided with the drainage duct which discharges | emits the water of the center vicinity of this outside. 前記砂分離洗浄装置が、汚砂混合水が導入される固液分離槽と、該固液分離槽の下に設置される沈降槽とを備え、前記固液分離槽が、接線方向に汚砂混合水を流入させることにより周壁に沿い下降する旋回流を発生させる円筒状の筒壁と、該筒壁の底部に配設された逆さ裁頭円錐状の篩からなる底壁と、該底壁の開口部と固液分離槽の上部とを接続する循環ダクトと、該循環ダクトの一部に接続されたエジェクタとを備えたことを特徴とする請求項1記載の砂分離洗浄装置の運転方法。   The sand separation and cleaning device includes a solid-liquid separation tank into which dirty sand mixed water is introduced, and a sedimentation tank installed under the solid-liquid separation tank, and the solid-liquid separation tank is sand tangent in a tangential direction. A cylindrical tube wall that generates a swirling flow descending along the peripheral wall by flowing mixed water, a bottom wall made of an inverted frustoconical sieve disposed at the bottom of the tube wall, and the bottom wall The operation method of the sand separation washing | cleaning apparatus of Claim 1 provided with the circulation duct which connects the opening part of this and the upper part of a solid-liquid separation tank, and the ejector connected to a part of this circulation duct. .
JP2005308361A 2005-10-24 2005-10-24 Operation method of sand-separating washing apparatus Pending JP2007111676A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2523657A (en) * 2015-02-06 2015-09-02 Cde Global Ltd Screening apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2523657A (en) * 2015-02-06 2015-09-02 Cde Global Ltd Screening apparatus
GB2523657B (en) * 2015-02-06 2016-12-21 Cde Global Ltd Screening apparatus
US9764330B2 (en) 2015-02-06 2017-09-19 Cde Global Limited Screening apparatus

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