JP4633502B2 - Sand separation and cleaning equipment - Google Patents

Sand separation and cleaning equipment Download PDF

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JP4633502B2
JP4633502B2 JP2005057629A JP2005057629A JP4633502B2 JP 4633502 B2 JP4633502 B2 JP 4633502B2 JP 2005057629 A JP2005057629 A JP 2005057629A JP 2005057629 A JP2005057629 A JP 2005057629A JP 4633502 B2 JP4633502 B2 JP 4633502B2
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liquid separation
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JP2006239546A (en
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泰典 中野
輝一 新阜
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Hitachi Plant Technologies Ltd
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Description

本発明は、砂分離洗浄装置に関し、特に、沈砂池等から揚砂された汚砂の臭気を除去するとともに砂中に含まれる夾雑物を高度に除去することを可能とした砂分離洗浄装置に関するものである。   The present invention relates to a sand separation and cleaning device, and more particularly, to a sand separation and cleaning device capable of removing odors of dirty sand pumped from a sand basin and the like and highly removing impurities contained in the sand. Is.

従来、下水処理場や浄水場等の沈砂池から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 purification plant using a pump is solid-liquid separated by a solid-liquid separation device using specific gravity difference separation, centrifugal separation, etc., and only the sand content is recovered. I am doing so.

ところで、近年、廃棄物に関する規制が厳しくなり、夾雑物が含まれている沈砂は、産業廃棄物として取り扱われ、その処分コストが膨大となり問題となっている。
一方、沈砂を一般廃棄物として処分(又は再利用)するためには、熱灼減量が10%以下であることに加え、沈砂に含まれる夾雑物を確実に分離除去する必要がある。
By the way, in recent years, regulations regarding wastes have become stricter, and sedimentation sand containing foreign matters is handled as industrial waste, and its disposal cost has become enormous.
On the other hand, in order to dispose (or reuse) the sand sediment as general waste, it is necessary to reliably separate and remove impurities contained in the sand sediment in addition to the heat loss being 10% or less.

そこで、本件出願人は、下記の特許文献1により、沈砂池等から揚砂された汚砂の臭気を除去するとともに砂中に含まれる夾雑物を高度に除去することを可能とした砂分離洗浄装置を提案している。
この砂分離洗浄装置は、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た砂分離洗浄装置において、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ている。
この砂分離洗浄装置は、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。
Therefore, the applicant of the present invention, according to Patent Document 1 below, removes the odor of the sand that has been pumped from a sand basin and the like, and at the same time, removes impurities contained in the sand to a high degree. A device is proposed.
This sand separation and washing apparatus is a sand separation and washing apparatus comprising a solid / liquid separation tank into which sewage mixed water is introduced and a sedimentation tank installed under the solid / liquid separation tank. A bottom made up of a cylindrical tube wall that generates a swirling flow that descends along the peripheral wall by flowing sewage mixed water in a tangential direction, and an inverted frustoconical sieve disposed at the bottom of the tube wall A wall and a drainage duct for discharging water near the center of the bottom wall to the outside.
This sand separation and cleaning device disperses waste sand and dust by centrifugal force due to swirling flow and separates the specific gravity difference, and also separates the particle size of sand and gravel by the sieve of the bottom wall, thereby, near the center of the bottom wall Collecting waste and gravel with a large specific gravity, and dropping gravel with a large specific gravity into the sedimentation tank from the center of the bottom wall and recovering it together with sand, while discharging waste with a low specific gravity efficiently and selectively together with water through the drainage duct. be able to.

ところで、上記砂分離洗浄装置においては、図5に示すように、底壁4の篩を清掃する手段として、揚砂ポンプの運転完了後、底壁4の裏側から噴射形状が円錐や扇型等の洗浄ノズル13により水を噴射し、逆洗するようにしているが、洗浄ノズル13により水を噴射する際に高圧が必要となるため、逆洗水量が少なくなる。
そのため、転がり落ちるごみが篩から浮かず、排水ダクト5の上向流により吸い上げられないため、篩の開口部41から落ちたごみが砂と共に搬出されるといったデメリットがあった。
また、篩面を万遍なく清掃するためには洗浄ノズル13の数量も多くなり、必然的に高価なものとなる他、ノズルが砂で詰まる等のデメリットもあった。
特願2004−373323号
By the way, in the said sand separation washing | cleaning apparatus, as shown in FIG. 5, as a means to clean the sieve of the bottom wall 4, after the completion of the operation of the sand pump, the injection shape is a cone or a fan shape from the back side of the bottom wall 4. The water is jetted by the washing nozzle 13 and backwashed. However, since high pressure is required when water is jetted by the washing nozzle 13, the amount of backwashing water is reduced.
Therefore, there is a demerit that the dust falling from the sieve does not float up from the sieve and is not sucked up by the upward flow of the drainage duct 5, so that the dust fallen from the opening 41 of the sieve is carried out together with the sand.
In addition, in order to clean the screen surface evenly, the number of the cleaning nozzles 13 is increased, which inevitably becomes expensive, and there is a demerit such that the nozzles are clogged with sand.
Japanese Patent Application No. 2004-373323

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、安価な構造で篩面を万遍なく清掃するとともに、落としたごみを篩の開口部で滞留させ、排水ダクトの上向流により吸引し除去することができる砂分離洗浄装置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 cleans the sieve surface uniformly with an inexpensive structure, and retains the dropped dust at the opening of the sieve, so that the upward flow of the drainage duct An object of the present invention is to provide a sand separation and cleaning device that can be sucked and removed by the above.

上記目的を達成するため、本発明の砂分離洗浄装置は、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た砂分離洗浄装置において、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、前記旋回流による遠心力のみを動力として汚砂とごみとを比重差分離するとともに底壁の篩に付着したごみを浮上させて当該篩により砂と砂利とを粒径分離するようにし、前記沈降槽が、固液分離槽の底壁の下に設けられた円筒状の筒壁と、該筒壁の接線方向に逆洗浄水を流入させ、前記底壁の下で旋回流を発生させる逆洗浄水管とを備えたことを特徴とする。 In order to achieve the above object, the sand separation and washing apparatus of the present invention is a sand separation and washing device comprising a solid-liquid separation tank into which sewage mixed water is introduced and a sedimentation tank installed under the solid-liquid separation tank. In the apparatus, the solid-liquid separation tank has a cylindrical tube wall that generates a swirling flow that descends along the peripheral wall by flowing sewage mixed water in a tangential direction, and an inverted structure disposed at the bottom of the tube wall. It is equipped with a bottom wall made of a frustoconical sieve and a drainage duct that discharges water near the center of the bottom wall to the outside. In addition, the dust adhering to the sieve on the bottom wall is levitated to separate the particle size of sand and gravel by the sieve, and the settling tank is a cylindrical shape provided below the bottom wall of the solid-liquid separation tank Backwash water is allowed to flow in the tangential direction of the cylinder wall and the cylinder wall to generate a swirling flow under the bottom wall. Characterized by comprising a washing water pipe.

この場合において、前記逆洗浄水管が、固液分離槽と逆方向の旋回流を発生することができる。   In this case, the reverse washing water pipe can generate a swirling flow in the opposite direction to the solid-liquid separation tank.

本発明の砂分離洗浄装置によれば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。
一方、篩の形状を円錐形状とすると、篩の外周部にごみの付着が多くなるが、本発明の砂分離洗浄装置は、沈降槽が、固液分離槽の底壁の下に設けられた円筒状の筒壁と、該筒壁の接線方向に逆洗浄水を流入させ、前記底壁の下で旋回流を発生させる逆洗浄水管とを備えることから、接線方向から給水すると旋回流による遠心力で水は外周側が上に膨れるように力が働き、篩の外周部に付着したごみは万遍なく浮上し、排水ダクトの上向流により吸引し除去することができる。
また、篩の開口率を小さくすると、スクリーン下面はよどみ状態になるため、給水した大部分は中心の開口部からの上昇渦流となって排水され、これにより、篩から転がり落ちたごみはこの開口部付近に滞留し、排水ダクトの上向流により吸引し除去することができる。
According to the sand separation and cleaning device of the present invention, the sand and dust are dispersed and separated by specific gravity difference by centrifugal force due to the swirling flow, and the particle size of the sand and gravel is separated by the sieve of the bottom wall. Garbage and gravel with a large specific gravity are collected near the center of the wall, and gravel with a large specific gravity falls from the center of the bottom wall to the settling tank and is collected together with the sand, while garbage with a small specific gravity is efficiently and selectively collected by the drainage duct. Can be discharged with water.
On the other hand, when the shape of the sieve is a conical shape, dust adheres to the outer periphery of the sieve, but the sand separation and cleaning device of the present invention has a sedimentation tank provided below the bottom wall of the solid-liquid separation tank. Since it includes a cylindrical cylindrical wall and a reverse cleaning water pipe that allows reverse cleaning water to flow in a tangential direction of the cylindrical wall and generates a swirling flow under the bottom wall, if water is supplied from the tangential direction, the centrifugal force is generated by the swirling flow. Water exerts a force so that the outer peripheral side swells upward, and the dust adhering to the outer peripheral portion of the sieve floats up and can be sucked and removed by the upward flow of the drainage duct.
In addition, when the opening ratio of the sieve is reduced, the lower surface of the screen becomes stagnation, so most of the water supplied is drained as an upward vortex from the central opening, so that the dust that has fallen off the sieve is opened in this opening. It can be sucked and removed by the upward flow of the drainage duct.

この場合、前記逆洗浄水管が、固液分離槽と逆方向の旋回流を発生することにより、篩面に付着したごみをさらに効率よく除去することができる。   In this case, the reverse washing water pipe generates a swirling flow in the direction opposite to that of the solid-liquid separation tank, so that dust attached to the sieve surface can be more efficiently removed.

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

図1〜図4に、本発明の砂分離洗浄装置の一実施例を示す。
この砂分離洗浄装置は、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、この砂分離洗浄装置は、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とを備えるとともに、前記沈降槽2が、固液分離槽1の底壁4の下に設けられた円筒状の筒壁8と、該筒壁8の接線方向に逆洗浄水を流入させ、前記底壁4の下で旋回流を発生させる逆洗浄水管9とを備えている。
1 to 4 show an embodiment of the sand separation and cleaning apparatus of the present invention.
This 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.
And this sand separation washing | cleaning apparatus is a cylindrical cylindrical wall 3 which the solid-liquid separation tank 1 produces | generates the swirl | vortex flow which descends along a surrounding wall by injecting waste-sand mixed water in a tangential direction, and this cylindrical wall 3 And a drainage duct 5 for discharging water near the center of the bottom wall 4 to the outside, and the settling tank 2 is a solid tank. A cylindrical tube wall 8 provided below the bottom wall 4 of the liquid separation tank 1 and a reverse flow in which backwash water is introduced in the tangential direction of the tube wall 8 to generate a swirling flow under the bottom wall 4. And a washing water pipe 9.

固液分離槽1の筒壁3の上部には、反転した旋回流を流入させる分離ホッパ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。
A separation hopper 6 for allowing an inverted swirl flow to flow is provided at the upper part of the cylindrical wall 3 of the solid-liquid separation tank 1, and dirty sand is mixed so that the swirl flow passes between the separation hopper 6 and the cylindrical wall 3. A water inflow pipe 7 is connected in a tangential direction.
The inflow pipe 7 is pumped with sand mixed water from a sand pump (not shown) such as a jet pump, and an annular overflow trough that receives the overflow water of the separation hopper 6 around the separation hopper 6. 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、コイルばね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.
The bottom wall 4 can also be elastically supported by a coil spring or the like so as to be movable up and down, so that when the sewage mixed water is introduced, it constantly fluctuates due to gravel and dust collision, dust accumulation and swirling flow. The sieve of the bottom wall 4 vibrates (oscillates) due to water pressure and the like, and the gravitational force captured by the sieve surface always acts in the vertical direction, so that gravel is prevented from being caught in the sieve mesh. it can.

排水ダクト5は、底壁4の開口部41の上方に開口する管からなり、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 a pipe that opens above the opening 41 of the bottom wall 4, and the drainage is overflowed by the head difference h of the water surface caused by the height of the side wall above the drainage duct 5. A suction flow is generated so as not to suck in the settling sand, and among the gravel and dust collected near the center of the bottom wall 4, only dust having a small specific gravity is sucked together with water and discharged to the outside.

一方、沈降槽2は、図4にも示すように、固液分離槽1の下に底壁4を境として連続的に形成されており、上部に円筒状の筒壁8が形成されるとともに、下部にはスクリューコンベア10が一体に配設されている。
沈降槽2の筒壁8には、該筒壁8の接線方向に逆洗浄水を流入させ、固液分離槽の底壁4の下で固液分離槽と逆方向の旋回流を発生させる逆洗浄水管9が、筒壁8の接線方向に接続されている。
逆洗浄水管9は、図2(a)に示すように、槽の大きさにより2本〜4本又はそれ以上が等間隔に配設されており、揚砂ポンプの運転完了後、固液分離槽の底壁4の下で筒壁8の接線方向から給水することにより底壁4の篩面を清掃することができる。
On the other hand, as shown in FIG. 4, the sedimentation tank 2 is continuously formed below the solid-liquid separation tank 1 with the bottom wall 4 as a boundary, and a cylindrical tube wall 8 is formed at the top. The screw conveyor 10 is integrally disposed in the lower part.
Reverse washing water flows into the cylindrical wall 8 of the settling tank 2 in the tangential direction of the cylindrical wall 8 to generate a swirling flow in the opposite direction to the solid-liquid separation tank below the bottom wall 4 of the solid-liquid separation tank. A cleaning water pipe 9 is connected in the tangential direction of the cylindrical wall 8.
As shown in FIG. 2 (a), 2 to 4 or more reverse washing water pipes 9 are arranged at equal intervals depending on the size of the tank. After the operation of the sand pump is completed, the solid-liquid separation is performed. By supplying water from the tangential direction of the cylindrical wall 8 under the bottom wall 4 of the tank, the sieve surface of the bottom wall 4 can be cleaned.

次に、この砂分離洗浄装置の動作を説明する。
ジェットポンプ等の揚砂ポンプから投入された汚砂混合水を、図1(a)に示すように、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沈降槽2に沈降し、スクリューコンベア10で搬出される。
Next, the operation of this sand separation and cleaning apparatus will be described.
As shown in FIG. 1 (a), a swirl flow is generated by flowing in the tangential direction of the cylindrical solid-liquid separation tank 1 with the sewage mixed water introduced from a sand pump such as a jet pump.
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 settling tank 2 and is carried out by the screw conveyor 10.

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.
Moreover, by causing a flow in the 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.

他方、運転完了後には、図1(b)に示すように、底壁4を逆洗することで篩面に付着したし渣や砂利を除去するようにする。
篩の形状を円錐形状とすると、篩の外周部にごみの付着が多くなるが、筒壁8の接線方向から給水すると旋回流による遠心力で水は外周側が上に膨れるように力が働き、篩の外周部に付着したごみは万遍なく浮上し、排水ダクト5の上向流により除去される。
また、篩の開口率を小さくすると、スクリーン下面はよどみ状態になるため、給水した大部分は中心の開口部41からの上昇渦流11となって排水され、これにより、篩から転がり落ちたごみはこの開口部41付近に滞留し、排水ダクト5の上向流により吸引除去される。
このとき、旋回流の流速を確保するためには、逆洗浄水管9からの給水量は揚砂水量以上とすることが望ましい。
On the other hand, after the operation is completed, as shown in FIG. 1 (b), the bottom wall 4 is back-washed to remove residue and gravel attached to the sieve surface.
When the shape of the sieve is a conical shape, dust adheres to the outer peripheral portion of the sieve, but when water is supplied from the tangential direction of the cylindrical wall 8, the force acts so that the outer peripheral side swells upward due to the centrifugal force caused by the swirling flow, The dust adhering to the outer peripheral portion of the sieve floats up and is removed by the upward flow of the drainage duct 5.
Further, when the opening ratio of the sieve is reduced, the lower surface of the screen becomes stagnation, and most of the supplied water is drained as the rising vortex 11 from the central opening 41, and thus the dust that has fallen from the sieve is It stays in the vicinity of the opening 41 and is removed by suction by the upward flow of the drainage duct 5.
At this time, in order to ensure the flow velocity of the swirling flow, it is desirable that the amount of water supplied from the backwash water pipe 9 is equal to or greater than the amount of sand flow.

この場合、揚砂システムとしてジェットポンプシステムを採用している場合は、駆動水ポンプからの高圧水を逆洗浄水管9からの逆洗水として供給することができる。
この際、逆洗停止後、サイホン現象で水が逆流し、ポンプやタンクにごみが流入するのを防止するために、逆止弁取付等の考慮が必要である(図3(a))。
In this case, when a jet pump system is employed as the sand pumping system, high-pressure water from the drive water pump can be supplied as backwash water from the backwash water pipe 9.
At this time, after stoppage of backwashing, it is necessary to consider the installation of a check valve or the like in order to prevent water from flowing back due to the siphon phenomenon and flowing into the pump and tank (FIG. 3A).

その一方で、逆洗水ポンプを揚砂ポンプとは別に設置することもできる。
この際、逆洗水ポンプと固液分離槽用洗浄水ポンプとを兼ねるようにし、汚砂混合水投入時に、図2(b)に示すように、流入管7とは別に設けた洗浄水管12により、洗浄水を固液分離槽1の接線方向から流入させることもできる。
これにより、揚砂時の槽内攪拌能力が大きくなり、臭気除去性をさらに向上させることが可能である。
また、揚砂完了後、弁を切り替えて逆洗した後、再度弁を切り替え、篩面の上から洗浄水を流入させると、篩面の清掃効果が大きくなる。
これは、篩面の下に繊維類等が滞留していた場合、逆洗浄により、篩面の上に再度繊維類が付着するので、これを洗い流すために行うものである。
この際、逆洗停止後、サイホン現象で水が逆流し、ポンプや貯留槽等にごみが流入するのを防止するために、逆止弁取付等の考慮が必要である(図3(b))。
なお、使用する水は処理水が望ましいが、処理水源の確保が困難なポンプ場等では、自動ストレーナーを経由させることでごみを除去した汚水を供給することも可能である(図3(c))。
On the other hand, a backwash water pump can be installed separately from the sand pump.
At this time, the washing water pipe 12 provided separately from the inflow pipe 7 is used as a backwash water pump and a washing water pump for the solid-liquid separation tank, as shown in FIG. Thus, the washing water can be introduced from the tangential direction of the solid-liquid separation tank 1.
Thereby, the stirring ability in the tank at the time of sand sanding becomes large, and it is possible to further improve the odor removing property.
Further, after completion of the sanding, when the valve is switched and backwashed, the valve is switched again and the cleaning water is introduced from above the sieve surface, the cleaning effect of the sieve surface is increased.
This is performed in order to wash away the fibers, etc., which stay below the screen surface, because the fibers adhere again on the screen surface by backwashing.
At this time, after the backwash is stopped, it is necessary to consider the installation of a check valve in order to prevent water from flowing back due to the siphon phenomenon and the inflow of dust into the pump and the storage tank (FIG. 3B). ).
The treated water is preferably treated water, but in pump stations where it is difficult to secure a treated water source, it is also possible to supply sewage from which dust has been removed by way of an automatic strainer (FIG. 3 (c)). ).

かくして、本実施例の砂分離洗浄装置は、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とを備えた砂分離洗浄装置において、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とを備えることから、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。
Thus, the sand separation and washing apparatus of the present embodiment is a sand separation and washing apparatus provided with 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 flowing sewage mixed water in a tangential direction, and at the bottom of the cylindrical wall 3. In addition, a bottom wall 4 made of an inverted frustoconical sieve and a drainage duct 5 for discharging the water near the center of the bottom wall 4 to the outside are provided. While separating and separating the specific gravity difference, the sand and gravel are separated by the particle size by the sieve of the bottom wall 4, thereby collecting garbage and gravel having a large specific gravity difference near the center of the bottom wall 4. While dropping from the center of the bottom wall 4 into the sedimentation tank 2 and collecting it with sand, it efficiently selects trash with a low specific gravity. It can be discharged together with water by to drainage duct 5.
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 it is possible to increase the suction flow velocity as compared with the conventional case, and the dust removal efficiency 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.

一方、篩の形状を円錐形状とすると、篩の外周部にごみの付着が多くなるが、本発明の砂分離洗浄装置は、沈降槽2が、固液分離槽の底壁4の下に設けられた円筒状の筒壁8と、該筒壁8の接線方向に逆洗浄水を流入させ、前記底壁4の下で旋回流を発生させる逆洗浄水管9とを備えることから、接線方向から給水すると旋回流による遠心力で水は外周側が上に膨れるように力が働き、篩の外周部に付着したごみは万遍なく浮上し、排水ダクトの上向流により吸引し除去することができる。
また、篩の開口率を小さくすると、スクリーン下面はよどみ状態になるため、給水した大部分は中心の開口部41からの上昇渦流11となって排水され、これにより、篩から転がり落ちたごみはこの開口部41付近に滞留し、排水ダクト5の上向流により吸引し除去することができる。
そして、前記逆洗浄水管9が、固液分離槽1と逆方向の旋回流を発生することにより、篩面に付着したごみをさらに効率よく除去することができる。
On the other hand, when the shape of the sieve is a conical shape, dust adheres to the outer periphery of the sieve. However, in the sand separation and washing apparatus of the present invention, the sedimentation tank 2 is provided below the bottom wall 4 of the solid-liquid separation tank. Since the cylindrical cylindrical wall 8 is provided, and the reverse cleaning water pipe 9 for flowing back cleaning water in the tangential direction of the cylindrical wall 8 and generating swirling flow under the bottom wall 4, When water is supplied, the centrifugal force generated by the swirling flow causes the water to swell upward on the outer periphery, and the dust adhering to the outer periphery of the sieve floats up and can be sucked and removed by the upward flow of the drainage duct. .
Further, when the opening ratio of the sieve is reduced, the lower surface of the screen is in a stagnation state. Therefore, most of the supplied water is drained as the rising vortex 11 from the central opening 41, so that the dust that has fallen from the sieve is It stays in the vicinity of the opening 41 and can be sucked and removed by the upward flow of the drainage duct 5.
And since the said reverse washing water pipe | tube 9 generate | occur | produces the swirling flow of a reverse direction with the solid-liquid separation tank 1, the dust adhering to a sieve surface can be removed still more efficiently.

以上、本発明の砂分離洗浄装置について、そ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 sand separation washing | cleaning apparatus of this invention was demonstrated based on the Example, this invention is not limited to the structure described in the said Example, The structure is suitably comprised in the range which does not deviate from the meaning. Can be changed.

本発明の砂分離洗浄装置は、沈砂池等から揚砂された汚砂の臭気を除去するとともに砂中に含まれる夾雑物を高度に除去することができ、また、安価な構造で篩面を万遍なく清掃するとともに、落としたごみを篩の開口部で滞留させ、排水ダクトの上向流により吸引し除去することから、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場合に好適に適用することができる。   The sand separation and cleaning apparatus of the present invention can remove the odor of the sand that has been pumped up from a sand basin and the like, and can highly remove impurities contained in the sand. Since it is cleaned evenly, the dropped garbage stays at the opening of the sieve and is sucked and removed by the upward flow of the drainage duct. It can be suitably applied to the case of exclusion.

本発明の砂分離洗浄装置の一実施例を示し、(a)はその通常使用時の断面図、(b)は逆洗時の断面図である。One Example of the sand separation washing | cleaning apparatus of this invention is shown, (a) is sectional drawing at the time of the normal use, (b) is sectional drawing at the time of backwashing. (a)は図1(b)のA矢視相当図、(b)は同B矢視相当図である。(A) is an A arrow equivalent figure of FIG.1 (b), (b) is an arrow B equivalent figure. (a)〜(c)は、同実施例の砂分離洗浄装置のポンプの使用例を示す説明図である。(A)-(c) is explanatory drawing which shows the usage example of the pump of the sand separation washing | cleaning apparatus of the Example. 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. 従来の砂分離洗浄装置を示す断面図である。It is sectional drawing which shows the conventional sand separation washing | cleaning apparatus.

1 固液分離槽
2 沈降槽
3 筒壁(固液分離槽)
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 筒壁(沈降槽)
9 逆洗浄水管
10 スクリューコンベア
11 上昇渦流
12 洗浄水管
1 Solid-liquid separation tank 2 Sedimentation tank 3 Cylinder wall (solid-liquid separation tank)
4 Bottom wall 41 Opening 5 Drain duct 6 Separation hopper 61 Overflow trough 7 Inflow pipe 8 Cylindrical wall (sedimentation tank)
9 Backwash water pipe 10 Screw conveyor 11 Ascending vortex 12 Wash water pipe

Claims (2)

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た砂分離洗浄装置において、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、前記旋回流による遠心力のみを動力として汚砂とごみとを比重差分離するとともに底壁の篩に付着したごみを浮上させて当該篩により砂と砂利とを粒径分離するようにし、前記沈降槽が、固液分離槽の底壁の下に設けられた円筒状の筒壁と、該筒壁の接線方向に逆洗浄水を流入させ、前記底壁の下で旋回流を発生させる逆洗浄水管とを備えたことを特徴とする砂分離洗浄装置。 In a sand separation and washing apparatus comprising a solid / liquid separation tank into which sewage mixed water is introduced and a sedimentation tank installed under the solid / liquid separation tank, the solid / liquid separation tank is mixed with sewage sand in a tangential direction. A cylindrical tube wall that generates a swirling flow descending along the peripheral wall by flowing water, a bottom wall formed of an inverted frustoconical sieve disposed at the bottom of the tube wall, and A drainage duct that discharges water near the center to the outside, separates the specific gravity difference between the sewage sand and the dust by using only the centrifugal force generated by the swirling flow, and floats the dust adhering to the bottom wall sieve. The particle size separation of sand and gravel is performed by the above, and the settling tank has a cylindrical cylindrical wall provided under the bottom wall of the solid-liquid separation tank, and backwash water flows in the tangential direction of the cylindrical wall. And a reverse cleaning water pipe for generating a swirling flow under the bottom wall. 前記逆洗浄水管が、固液分離槽と逆方向の旋回流を発生させることを特徴とする請求項1記載の砂分離洗浄装置。   The sand separation and washing apparatus according to claim 1, wherein the reverse washing water pipe generates a swirling flow in a direction opposite to that of the solid-liquid separation tank.
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JP4798619B2 (en) * 2005-10-24 2011-10-19 株式会社日立プラントテクノロジー Sand separation and cleaning equipment
KR100716559B1 (en) * 2006-09-29 2007-05-09 양시천 Apparatus for removing deposit and water
JP5631766B2 (en) * 2011-01-28 2014-11-26 前澤工業株式会社 Sand lifting equipment
JP2021154229A (en) * 2020-03-27 2021-10-07 アクアインテック株式会社 Driving method for solid-liquid separator, and solid-liquid separator
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