JP2005095800A - Mud water treatment apparatus - Google Patents

Mud water treatment apparatus Download PDF

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JP2005095800A
JP2005095800A JP2003333834A JP2003333834A JP2005095800A JP 2005095800 A JP2005095800 A JP 2005095800A JP 2003333834 A JP2003333834 A JP 2003333834A JP 2003333834 A JP2003333834 A JP 2003333834A JP 2005095800 A JP2005095800 A JP 2005095800A
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rotating drum
water
muddy water
tank
screen
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JP3717906B2 (en
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Haruhiko Sakamoto
晴彦 阪本
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SAKAMOTO SHOKAI KK
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SAKAMOTO SHOKAI KK
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  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a mud water treatment apparatus which makes it possible to efficiently treat mud water produced upon pile driving on a construction site and, thereby, permits the reduction of a treatment cost. <P>SOLUTION: A rotating drum 3 which is rotatively driven by an oil hydraulic motor 4 is disposed on a car body 2 of a self-traveling vehicle 1 and spiral vanes 16, 17 are disposed on the outer side and the inner side of a screen 13 incorporated inside the rotating drum 3. A hopper 11 for supply is disposed on the opening 10 of the rotating drum 3. The mud water stored in a waste mud water storage tank and pH adjuster in an adjustor tank 18 mounted on the car body 2 are supplied into the screen 13 from the hopper 11 for supply and the pH of the mud water is made to be the extent of 5 - 7 by means of mixing and stirring of the spiral vanes 16, 17. At the same time, the mud water is separated into a water content, a fine particle solid content and a coarse particle solid content by using the screen 13, the water content and the fine particle solid content are sent into a turbid water tank 19 by means of a pump 22 disposed in the rotating drum 3, a coagulant is supplied into the turbid water tank 19 to perform solid-liquid separation, separated water over the muddy material deposited on the bottom plate of the turbid water tank 19 is drained and the muddy material is disposed of as it is. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

この発明は、主として基礎杭の建て込み時に発生する泥水の処理装置に関するものである。   The present invention mainly relates to an apparatus for treating muddy water generated when a foundation pile is built.

アースドリルあるいはボーリングマシンによって地面に縦孔を掘削し、その縦孔内に基礎杭を建て込むことは一般的に行なわれている。   It is a common practice to drill a vertical hole in the ground with an earth drill or a boring machine and build a foundation pile into the vertical hole.

上記のような基礎杭の建て込みに際しては地面を掘削するため、多量の泥水が発生する。この泥水は普通、廃棄泥水貯溜槽内に一旦貯溜され、その廃棄泥水貯溜槽から取り出されて、pH調整処理および減容化処理されて廃棄される。   When the foundation pile as described above is built, a large amount of muddy water is generated because the ground is excavated. This muddy water is normally once stored in a waste muddy water storage tank, taken out of the waste muddy water storage tank, and subjected to pH adjustment processing and volume reduction processing and discarded.

ところで、廃棄泥水貯溜槽内の泥水の処理に際し、従来は、廃棄泥水貯溜槽内の泥水をバキュームポンプ車によって産業廃棄物処理業者の処理場まで搬送し、その処理場においてpH調整処理および減容化処理して廃棄処理するようにしているため、処理コストが高いという問題があった。   By the way, when processing muddy water in the waste muddy water storage tank, conventionally, the muddy water in the waste muddy water storage tank is transported to a treatment plant of an industrial waste disposal contractor by a vacuum pump car, and pH adjustment processing and volume reduction are carried out at the treatment plant. However, there is a problem that the processing cost is high.

この発明の課題は、基礎杭の建て込み時に発生する泥水を建設現場で効率よく無害化処理できるようにして処理コストの大幅な低減化を図ることができるようにした泥水処理装置を提供することである。   An object of the present invention is to provide a muddy water treatment apparatus that can efficiently detoxify muddy water generated at the time of erection of foundation piles at a construction site and can greatly reduce the treatment cost. It is.

上記の課題を解決するために、この発明においては、自走式車両の車体上に、後端が開口する回転ドラムと、その回転ドラムの駆動用モータと、pH調整剤が貯溜された調整剤タンクと、濁水タンクとを搭載し、前記回転ドラムの後端開口に泥水の供給用ホッパと、粗粒固形分の排出用シュートとを接続し、前記調整剤タンク内のpH調整剤を前記ホッパ内に供給するポンプを設け、前記回転ドラム内には、その回転ドラムと一体に回転してホッパから回転ドラム内に供給される泥水を水分および微粒固形分と粗粒固形分とに分離する筒状のスクリーンを組込み、そのスクリーンの内周および外周に沿って螺旋羽根を取付け、外側螺旋羽根間には前記スクリーンを通過して回転ドラムの底部に溜る水分および微粒固形分を前記濁水タンク内に供給するポンプを組込み、前記濁水タンク内に高分子凝集剤を供給する凝集剤供給手段と、濁水タンク内において固液分離された分離水の排水手段および泥状物の排出手段を設けた構成を採用したのである。   In order to solve the above-mentioned problems, in the present invention, on the body of a self-propelled vehicle, a rotating drum whose rear end is opened, a motor for driving the rotating drum, and an adjusting agent in which a pH adjusting agent is stored A tank and a muddy water tank, a muddy water supply hopper and a coarse solids discharge chute are connected to the rear end opening of the rotating drum, and the pH adjuster in the adjuster tank is supplied to the hopper A pump for supplying the inside of the rotary drum is provided, and in the rotary drum, a cylinder that rotates integrally with the rotary drum and separates muddy water supplied from the hopper into the rotary drum into moisture and fine solids and coarse solids. A spiral blade is installed along the inner and outer peripheries of the screen, and moisture and fine solids accumulated in the bottom of the rotating drum through the screen are placed between the outer spiral blades in the muddy water tank. A structure in which a pump for feeding is incorporated, a flocculant supply means for supplying a polymer flocculant into the turbid water tank, a drainage means for separated water separated in the turbid water tank and a means for discharging mud Adopted.

上記の構成から成る泥水処理装置においては、回転ドラムを一方向に回転させた状態において、廃棄泥水貯溜槽内の泥水を供給用ホッパからスクリーン内に供給すると共に、調整剤タンクから泥水中にpH調整剤を供給して螺旋羽根の回転による混合および撹拌により泥水のpHを5〜7程度に調整すると共に、上記スクリーンによって泥水を水分および微粒固形分と粗粒固形分とに分離する。   In the muddy water treatment apparatus having the above-described configuration, the muddy water in the waste muddy water storage tank is supplied from the supply hopper into the screen while the rotary drum is rotated in one direction, and the pH from the regulator tank to the muddy water. The adjusting agent is supplied to adjust the pH of the muddy water to about 5 to 7 by mixing and stirring by the rotation of the spiral blades, and the muddy water is separated into moisture and fine solids and coarse solids by the screen.

スクリーンを通過して回転ドラム内の底部に溜る水分と微粒固形分を濁水タンク内に供給すると共に、凝集剤供給手段により濁水タンク内に高分子凝集剤を供給して、固液分離し、濁水タンク内の底部に沈殿、堆積する泥状物上の分離水を排水手段により排水し、泥状物を排出手段により濁水タンク内から取り出し、現場で集積させて仮置きし、乾燥させたのち、一般残土として処分する。   Moisture and fine solids accumulated in the bottom of the rotating drum through the screen are supplied into the turbid water tank, and the polymer flocculant is supplied into the turbid water tank by the flocculant supply means to separate into solid and liquid. After draining the separated water on the mud that settles and deposits on the bottom of the tank, drain the mud from the muddy water tank by the drain, collect it on the spot, temporarily store it, and dry it. Dispose as general residual soil.

一方、スクリーン内に残る粗粒固形分は、回転ドラムの逆回転により、その回転ドラムと共に回転するスクリーン内の螺旋羽根により、回転ドラムの後端の開口から排出シュート内に送り込んで外部に取り出し、廃棄処理する。   On the other hand, the coarse solid content remaining in the screen is taken out into the discharge chute from the opening at the rear end of the rotating drum by the spiral blade in the screen rotating together with the rotating drum by reverse rotation of the rotating drum, Dispose of it.

ここで、pH調整剤としては泥水のpHを5〜7程度とするものであればよく、そのようなpH調整剤として希硫酸を挙げることができる。   Here, any pH adjusting agent may be used as long as the pH of the muddy water is about 5 to 7, and examples of such a pH adjusting agent include dilute sulfuric acid.

以上のように、この発明に係る泥水処理装置においては、自走式車両上において、泥水のpH調整処理と、pH調整後に泥状物と分離水の分離処理とを行なうことができるため、建設現場において泥水を処理することができると共に、処理後の泥状物を一般残土として処分することができる。このため、バキュームポンプ車を用いて泥水を産業廃棄物処理場まで運び込む必要がなくなると共に、処理業者への委託業務を不要とすることができるので、泥水処理コストの大幅な削減を図ることができる。   As described above, in the muddy water treatment apparatus according to the present invention, on a self-propelled vehicle, the muddy water pH adjustment treatment and the separation treatment of muddy matter and separated water after pH adjustment can be performed. The muddy water can be treated on site, and the treated mud can be disposed of as general residual soil. For this reason, it is not necessary to carry muddy water to an industrial waste treatment plant using a vacuum pump vehicle, and it is possible to eliminate the need for outsourcing work to a processing company, thereby greatly reducing muddy water treatment costs. .

また、スクリーン内に螺旋羽根を設けたことによって、回転ドラムの逆回転によってスクリーン内に残る粗粒固形分を排出用シュートに取り出して廃棄処理することができる。   Moreover, by providing the spiral blade in the screen, the coarse solid content remaining in the screen by the reverse rotation of the rotary drum can be taken out to the discharge chute and discarded.

以下、この発明の実施の形態を図面に基づいて説明する。図1に示すように、自走式車両1の車体2上には、傾斜状に配置された回転ドラム3と、その回転ドラム3の回転駆動用の油圧モータ4とが搭載されている。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. As shown in FIG. 1, on a vehicle body 2 of a self-propelled vehicle 1, a rotating drum 3 arranged in an inclined manner and a hydraulic motor 4 for driving the rotating drum 3 are mounted.

回転ドラム3は円筒部3aの前後端に円錐筒部3b、3cを設けた構成とされ、後側円錐筒部3cの外周には軌道輪5が設けられ、その軌道輪5が前記車体2上の支持台6で支持された回転可能な複数のガイドローラ7によって回転自在に支持されている。   The rotating drum 3 has a configuration in which conical cylindrical portions 3b and 3c are provided at the front and rear ends of the cylindrical portion 3a. A race ring 5 is provided on the outer periphery of the rear conical cylindrical portion 3c. Are supported by a plurality of rotatable guide rollers 7 supported by a support base 6.

図2に示すように、前側円錐筒部3bは閉塞端を有し、その閉塞端に設けられた軸8が軸受9によって回転自在に支持され、その軸9に前記油圧モータ4が接続されている。   As shown in FIG. 2, the front conical cylinder portion 3 b has a closed end, and a shaft 8 provided at the closed end is rotatably supported by a bearing 9, and the hydraulic motor 4 is connected to the shaft 9. Yes.

一方、後側円錐筒部3cは後端に開口10を有し、その開口10に泥水の供給用ホッパ11の下端出口が臨んでいると共に、粗粒固形分の排出用シュート12の上部開口が臨んでいる。   On the other hand, the rear conical cylinder portion 3c has an opening 10 at the rear end, and the lower end of the muddy water supply hopper 11 faces the opening 10 and the upper opening of the chute 12 for discharging coarse solid matter. I'm here.

排出用シュート12は上部排出用シュート12aと下部排出用シュート12bとに分割され、上部排出用シュート12aは固定の支持とされ、一方、下部排出用シュート12bは上部排出用シュート12aの下端出口を中心に回動可能とされて下端の出口の位置を水平面上で変更し得るようになっている。   The discharge chute 12 is divided into an upper discharge chute 12a and a lower discharge chute 12b, and the upper discharge chute 12a is fixedly supported, while the lower discharge chute 12b has a lower end outlet of the upper discharge chute 12a. The position of the exit at the lower end can be changed on the horizontal plane so that it can be rotated around the center.

回転ドラム3の内部には筒状のスクリーン13が回転ドラム3と同心上に設けられている。スクリーン13は、図3および図4に示すように、軸方向に延びる複数のバー13aを円周方向に間隔をおいて設け、そのバー13aの外側に断面形状が略3角形の線材13bを螺旋状に巻付け、その線材13bの螺旋部間に微小な間隙15を設けた構成とされている。実施の形態では上記間隙15の大きさを0.5〜1.0mmの範囲としている。   A cylindrical screen 13 is provided concentrically with the rotating drum 3 inside the rotating drum 3. As shown in FIGS. 3 and 4, the screen 13 is provided with a plurality of bars 13a extending in the axial direction at intervals in the circumferential direction, and a wire 13b having a substantially triangular cross section is spiraled outside the bars 13a. It is configured such that a minute gap 15 is provided between the spiral portions of the wire 13b. In the embodiment, the size of the gap 15 is in the range of 0.5 to 1.0 mm.

上記スクリーン13は供給用ホッパ11の下端出口から排出される泥水を受け、その泥水を水分および微粒固形分と粗粒固形分とに分離するようになっている。   The screen 13 receives muddy water discharged from the lower end outlet of the supply hopper 11 and separates the muddy water into moisture and fine solids and coarse solids.

なお、スクリーン13は上記の構造のものに限定されず、泥水を水分および微粒固形分と粗粒固形分とに分離することができるようにしたものであればよい。   The screen 13 is not limited to the one having the above-described structure, and may be any screen that can separate muddy water into moisture and fine solids and coarse solids.

図2に示すように、スクリーン13は、その外周に沿って取付けた螺旋羽根16により回転ドラム3に取付けられて回転ドラム3と一体に回転するようになっている。また、スクリーン13の内側にはその内周に沿って螺旋羽根17が取付けられている。この内側の螺旋羽根17はスクリーン13の外側に設けられた前記螺旋羽根16と同方向の螺旋とされている。   As shown in FIG. 2, the screen 13 is attached to the rotating drum 3 by a spiral blade 16 attached along the outer periphery thereof and rotates integrally with the rotating drum 3. A spiral blade 17 is attached to the inside of the screen 13 along its inner periphery. The inner spiral blade 17 has a spiral in the same direction as the spiral blade 16 provided outside the screen 13.

車体2上には、調整剤タンク18と、濁水タンク19が搭載され、調整剤タンク18内には泥水のpHを5〜7程度に調整するpH調整剤が充填されている。pH調整剤として、ここでは希硫酸を用いるようにしている。   A regulator tank 18 and a muddy water tank 19 are mounted on the vehicle body 2, and the regulator tank 18 is filled with a pH regulator that adjusts the pH of the muddy water to about 5-7. Here, dilute sulfuric acid is used as the pH adjuster.

調整剤タンク18内のpH調整剤は、ポンプ20の駆動によって供給管21内に送り込まれ、その供給管21の排出端21aから供給用ホッパ11内に供給されるようになっている。   The pH adjusting agent in the adjusting agent tank 18 is fed into the supply pipe 21 by driving the pump 20, and is supplied into the supply hopper 11 from the discharge end 21 a of the supply pipe 21.

回転ドラム3内には、前側円錐筒部3b内においてスクリーン13の外側の螺旋羽根16間にポンプ22が組込まれている。ポンプ22の吐出口に接続された供給管23はスクリーン13を貫通して内側の螺旋羽根17の内側および供給用ホッパ11の出口中心部に挿通され、その供給用ホッパ11から外部に引き出されて濁水タンク19に接続されている。   In the rotating drum 3, a pump 22 is incorporated between the spiral blades 16 outside the screen 13 in the front conical cylinder portion 3b. The supply pipe 23 connected to the discharge port of the pump 22 passes through the screen 13 and is inserted into the inner spiral blade 17 and the outlet center of the supply hopper 11, and is drawn out from the supply hopper 11. The muddy water tank 19 is connected.

上記供給管23は2分割され、その分割端は供給用ホッパ11の出口中心部に配置されたロータリジョイント24を介して連結されて、回転ドラム3と共にポンプ22が自在に回転し得るようになっている。   The supply pipe 23 is divided into two parts, and the divided ends are connected via a rotary joint 24 arranged at the center of the outlet of the supply hopper 11 so that the pump 22 can freely rotate together with the rotary drum 3. ing.

図5に示すように濁水タンク19には、その内部に凝集剤を供給する凝集剤供給手段25が接続されている。凝集剤供給手段25は、濁水タンク19の上側に水溶性の高分子凝集剤が充填された凝集剤タンク26を設け、その凝集剤タンク26内の高分子凝集剤中にポンプ27を設け、このポンプ27の吐出口と濁水タンク19内とをパイプ28で連通し、上記ポンプ27の駆動によって凝集剤タンク26内の高分子凝集剤を濁水タンク19内に送り込むようにしている。   As shown in FIG. 5, the muddy water tank 19 is connected to a flocculant supply means 25 for supplying the flocculant therein. The flocculant supply means 25 is provided with a flocculant tank 26 filled with a water-soluble polymer flocculant on the upper side of the turbid water tank 19, and a pump 27 is provided in the polymer flocculant in the flocculant tank 26. The discharge port of the pump 27 and the inside of the muddy water tank 19 are connected by a pipe 28, and the polymer coagulant in the coagulant tank 26 is sent into the muddy water tank 19 by driving the pump 27.

濁水タンク19内には、回転ドラム3内に組込まれたポンプ22の駆動によってスクリーン13を通過した水分と微粒固形分とが供給され、その水分と微粒固形分は凝集剤供給手段25から送られる高分子凝集剤によって泥状の固形分(泥状物)と清澄水(分離水)とに分離され、分離水は排水手段30によって排水され、固形分は排出手段31によって外部に排出される。   The muddy water tank 19 is supplied with water and fine solids that have passed through the screen 13 by driving a pump 22 incorporated in the rotary drum 3, and the water and fine solids are sent from the flocculant supply means 25. The polymer flocculant separates into a muddy solid (mud) and clarified water (separated water), the separated water is drained by the drainage means 30, and the solid is discharged to the outside by the discharge means 31.

排水手段30は濁水タンク19内にポンプ32を組込み、そのポンプ32の吐出口に排水管33を接続し、上記ポンプ32の駆動によって濁水タンク19内の分離水を排水管33から排水するようにしている。   The drainage means 30 incorporates a pump 32 in the muddy water tank 19, connects a drain pipe 33 to the discharge port of the pump 32, and drains the separated water in the muddy water tank 19 from the drain pipe 33 by driving the pump 32. ing.

排出手段31は濁水タンク19の下部に設けられた排出口34にポンプ35の吸込口を接続し、そのポンプ35の吐出口に排出管36を接続し、上記ポンプ35の駆動によって泥状物を排出管36から排出するようにしている。   The discharge means 31 connects a suction port of a pump 35 to a discharge port 34 provided in the lower part of the muddy water tank 19, connects a discharge pipe 36 to the discharge port of the pump 35, and mud is removed by driving the pump 35. It discharges from the discharge pipe 36.

図1および図2において、40は図示省略した廃棄泥水貯溜槽と供給用ホッパ11とを連通させる泥水供給管を示し、その泥水供給管40には図示省略したポンプが接続され、そのポンプの駆動によって廃棄泥水貯溜槽内の泥水が供給用ホッパ11内に供給される。   1 and 2, reference numeral 40 denotes a muddy water supply pipe for connecting a waste muddy water storage tank (not shown) to the supply hopper 11, and a pump (not shown) is connected to the muddy water supply pipe 40 to drive the pump. Thus, the muddy water in the waste muddy water storage tank is supplied into the supply hopper 11.

また、図1において、42は各種ポンプの駆動モータの駆動源であるジェネレータを示す。   In FIG. 1, reference numeral 42 denotes a generator which is a drive source for drive motors of various pumps.

実施の形態で示す泥水処理装置は上記の構造から成り、廃棄泥水貯溜槽内に貯溜された泥水の処理に際しては、油圧モータ4の駆動により回転ドラム3を一方向に回転し、廃棄泥水貯溜槽内の泥水を泥水供給管40から供給用ホッパ11内に送り込むと共に、図1に示すポンプ20の駆動によって調整剤タンク18内のpH調整剤を供給管21から供給用ホッパ11内に供給する。   The muddy water treatment apparatus shown in the embodiment has the above-described structure. When the muddy water stored in the waste muddy water storage tank is processed, the rotating drum 3 is rotated in one direction by driving the hydraulic motor 4, and the waste muddy water storage tank. The muddy water is fed into the supply hopper 11 from the muddy water supply pipe 40, and the pH adjusting agent in the adjustment agent tank 18 is supplied from the supply pipe 21 into the supply hopper 11 by driving the pump 20 shown in FIG.

供給用ホッパ11内に供給された泥水とpH調整剤は、その供給用ホッパ11の下端出口からスクリーン13内に供給され、スクリーン13によって水分および微粒固形分と粗粒固形分とに分離されると共に、スクリーン13により捕捉された粗粒固形分はスクリーン13の内側に取付けた螺旋羽根17の回転による送り作用によって回転ドラム3の閉塞端に向けて送られる。   The muddy water and the pH adjusting agent supplied into the supply hopper 11 are supplied into the screen 13 from the lower end outlet of the supply hopper 11, and are separated into moisture and fine solids and coarse solids by the screen 13. At the same time, the coarse solid content captured by the screen 13 is sent toward the closed end of the rotating drum 3 by the feeding action by the rotation of the spiral blade 17 attached inside the screen 13.

また、泥水とpH調整剤は、スクリーン13の外側および内側に設けられた螺旋羽根16、17の回転により混合、撹拌されてpHが5〜7程度にpH調整される。   Further, the muddy water and the pH adjusting agent are mixed and stirred by the rotation of the spiral blades 16 and 17 provided on the outside and inside of the screen 13 so that the pH is adjusted to about 5 to 7.

スクリーン13を通過した水分および微粒固形分は回転ドラム3の底部に溜り、この水分および微粒固形分は、回転ドラム3と共に回転するポンプ22がドラム底部に貯溜する水分および微粒固形分中を旋回するときそのポンプ22により吸引されて濁水タンク19に送り込まれる。   The water and fine solids that have passed through the screen 13 are collected at the bottom of the rotary drum 3, and the water and fine solids are swirled in the water and fine solids that the pump 22 that rotates together with the rotary drum 3 stores at the bottom of the drum. At that time, it is sucked by the pump 22 and sent to the muddy water tank 19.

なお、回転ドラム3内に所定量の泥水とpH調整剤を供給して回転ドラム3を所定時間回転させ、撹拌羽根16、17の回転による混合、撹拌により泥水をpH調整処理したのち、ポンプ22が回転ドラム3内の底部に配置される位置で回転ドラム3を停止させ、その停止状態でポンプ22を駆動して、スクリーン13を通過した水分と微粒固形分を連続して濁水タンク19内に送り込むようにしてもよい。   A predetermined amount of muddy water and a pH adjusting agent are supplied into the rotary drum 3 to rotate the rotary drum 3 for a predetermined time, and after adjusting the pH of the muddy water by mixing and stirring by rotation of the stirring blades 16 and 17, the pump 22. The rotary drum 3 is stopped at a position where it is disposed at the bottom of the rotary drum 3, and the pump 22 is driven in the stopped state so that the water and fine solids that have passed through the screen 13 are continuously put into the muddy water tank 19. You may make it send.

濁水タンク19内に水分および微粒固形分が供給されると、凝集剤供給手段25の作動によって凝集剤タンク26内の高分子凝集剤が濁水タンク19内に送り込まれ、その高分子凝集剤によって水分および微粒固形分は固液分離され、濁水タンク19の底部に泥状物が堆積し、その泥状物上に分離水が貯溜する。   When moisture and fine solids are supplied into the turbid water tank 19, the polymer flocculant in the flocculant tank 26 is sent into the turbid water tank 19 by the operation of the flocculant supply means 25, and the polymer flocculant causes moisture to flow. The fine solid content is separated into solid and liquid, and a muddy substance is accumulated at the bottom of the turbid water tank 19, and the separated water is stored on the muddy substance.

このとき、泥状物および分離水は回転ドラム3内において予めpH調整されているため、分離水は下水等に放流することが可能であり、また、泥状物は一般残土と同様の取扱いとすることができる。   At this time, since the muddy substance and the separated water are pH adjusted in advance in the rotary drum 3, the separated water can be discharged into sewage and the like, and the muddy substance is handled in the same manner as general residual soil. can do.

そこで、濁水タンク19内に所定量の分離水が貯溜されると、排水手段30のポンプ32を駆動して排水管33から排水する。   Therefore, when a predetermined amount of separated water is stored in the muddy water tank 19, the pump 32 of the drainage means 30 is driven to drain from the drain pipe 33.

一方、泥状物は排出手段31のポンプ35を駆動して排出管36から排出し、現場に集積、仮置きして乾燥させてから一般残土として処分する。   On the other hand, the mud is discharged from the discharge pipe 36 by driving the pump 35 of the discharge means 31, collected on the site, temporarily placed and dried, and then disposed of as general residual soil.

このように、実施形態で示す泥水処理装置においては、自走式車両1上において泥水のpH調整処理と、その調整後に固液分離処理を行なうことができるので、建設現場において基礎杭の建て込み時に発生する泥水の処理を行なうことができると共に、処理後の泥状物と分離水の廃棄処理を行うことができる。   Thus, in the muddy water treatment apparatus shown in the embodiment, since the muddy water pH adjustment process on the self-propelled vehicle 1 and the solid-liquid separation process can be performed after the adjustment, the foundation pile is built at the construction site. It is possible to treat muddy water that is sometimes generated, and to dispose of muddy matter and separated water after treatment.

このため、バキュームポンプ車を用いて泥水を廃棄物処理場まで運び込む必要がなくなると共に、処理業者への委託業務を不要とすることができるので、処理コストを大幅に削減することができる。   For this reason, it is not necessary to carry muddy water to a waste disposal site using a vacuum pump vehicle, and it is possible to dispense with a contractor to a processing company, so that processing costs can be greatly reduced.

また、スクリーン13内に残る粗粒固形分も回転ドラム3を逆回転することにより内側螺旋羽根17の回転による送り作用によって回転ドラム3の後端の開口10から排出用シュート12内に取り出して廃棄処理することができる。   Further, the coarse solid content remaining in the screen 13 is also taken out from the opening 10 at the rear end of the rotating drum 3 into the discharge chute 12 by the rotating action of the inner spiral blade 17 by reversely rotating the rotating drum 3 and discarded. Can be processed.

さらに、スクリーン13の外側および内側に螺旋羽根16、17を設けたことによって、泥水とpH調整剤とを混合、撹拌することができるため、泥水をきわめて効果的にpH調整処理を行なうことができる。   Further, by providing the spiral blades 16 and 17 on the outside and inside of the screen 13, the muddy water and the pH adjusting agent can be mixed and stirred, so that the muddy water can be subjected to a pH adjustment treatment very effectively. .

この発明に係る泥水処理装置の実施形態を示す正面図Front view showing an embodiment of a muddy water treatment apparatus according to the present invention 図1の回転ドラム部を示す断面図Sectional drawing which shows the rotating drum part of FIG. スクリーンの一部分を示す断面図Sectional view showing a part of the screen 図3のIV−IV線に沿った断面図Sectional view along line IV-IV in FIG. 濁水タンク部を示す断面図Cross section showing muddy water tank

符号の説明Explanation of symbols

1 自走式車両
2 車体
3 回転ドラム
4 モータ
10 開口
11 供給用ホッパ
12 排出用シュート
13 スクリーン
16、17 螺旋羽根
18 調整剤タンク
19 濁水タンク
20 ポンプ
22 ポンプ
25 凝集剤供給手段
31 排出手段
DESCRIPTION OF SYMBOLS 1 Self-propelled vehicle 2 Car body 3 Rotating drum 4 Motor 10 Opening 11 Supply hopper 12 Discharge chute 13 Screens 16, 17 Spiral blade 18 Conditioner tank 19 Muddy water tank 20 Pump 22 Pump 25 Coagulant supply means 31 Discharge means

Claims (1)

自走式車両の車体上に、後端が開口する回転ドラムと、その回転ドラムの駆動用モータと、pH調整剤が貯溜された調整剤タンクと、濁水タンクとを搭載し、前記回転ドラムの後端開口に泥水の供給用ホッパと、粗粒固形分の排出用シュートとを接続し、前記調整剤タンク内のpH調整剤を前記ホッパ内に供給するポンプを設け、前記回転ドラム内には、その回転ドラムと一体に回転してホッパから回転ドラム内に供給される泥水を水分および微粒固形分と粗粒固形分とに分離する筒状のスクリーンを組込み、そのスクリーンの内周および外周に沿って螺旋羽根を取付け、外側螺旋羽根間には前記スクリーンを通過して回転ドラムの底部に溜る水分および微粒固形分を前記濁水タンク内に供給するポンプを組込み、前記濁水タンク内に高分子凝集剤を供給する凝集剤供給手段と、濁水タンク内において固液分離された分離水の排水手段および泥状物の排出手段を設けた泥水処理装置。   On the vehicle body of the self-propelled vehicle, a rotating drum whose rear end is opened, a motor for driving the rotating drum, an adjusting agent tank in which a pH adjusting agent is stored, and a muddy water tank are mounted. A muddy water supply hopper and a coarse solids discharge chute are connected to the rear end opening, and a pump for supplying the pH adjusting agent in the adjusting agent tank into the hopper is provided. Incorporates a cylindrical screen that rotates integrally with the rotating drum and separates the muddy water supplied from the hopper into the rotating drum into moisture and fine solids and coarse solids. A spiral blade is attached along the outer spiral blade, and a pump for supplying moisture and fine solids accumulated in the bottom of the rotating drum through the screen to the inside of the turbid water tank is incorporated between the outer spiral blades. And coagulant supply means for supplying Atsumarizai, mud processing apparatus provided with means for discharging waste water means and the slurry of separated water which is solid-liquid separated in turbid water tank.
JP2003333834A 2003-09-25 2003-09-25 Muddy water treatment equipment Expired - Lifetime JP3717906B2 (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008229446A (en) * 2007-03-19 2008-10-02 Shin Meiwa Ind Co Ltd Sludge thickening apparatus and vehicle
CN108585432A (en) * 2018-07-05 2018-09-28 鹏鹞环保股份有限公司 Integrated spiral shell presses sludge dewatering equipment
CN108585433A (en) * 2018-07-05 2018-09-28 鹏鹞环保股份有限公司 Integral sludge thickener
CN108609834A (en) * 2018-07-05 2018-10-02 鹏鹞环保股份有限公司 Waterpower driven rotary screen tube
CN114477526A (en) * 2022-01-13 2022-05-13 武汉荣牧环境工程有限公司 Industrial wastewater heat energy power device for environmental protection recycling

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008229446A (en) * 2007-03-19 2008-10-02 Shin Meiwa Ind Co Ltd Sludge thickening apparatus and vehicle
CN108585432A (en) * 2018-07-05 2018-09-28 鹏鹞环保股份有限公司 Integrated spiral shell presses sludge dewatering equipment
CN108585433A (en) * 2018-07-05 2018-09-28 鹏鹞环保股份有限公司 Integral sludge thickener
CN108609834A (en) * 2018-07-05 2018-10-02 鹏鹞环保股份有限公司 Waterpower driven rotary screen tube
CN108609834B (en) * 2018-07-05 2024-06-04 鹏鹞环保股份有限公司 Hydraulic rotary filter screen cylinder
CN108585432B (en) * 2018-07-05 2024-06-04 鹏鹞环保股份有限公司 Integrated screw press sludge dewatering machine
CN108585433B (en) * 2018-07-05 2024-06-04 鹏鹞环保股份有限公司 Integrated sludge thickener
CN114477526A (en) * 2022-01-13 2022-05-13 武汉荣牧环境工程有限公司 Industrial wastewater heat energy power device for environmental protection recycling

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