JPH0585500U - Sludge recovery truck - Google Patents
Sludge recovery truckInfo
- Publication number
- JPH0585500U JPH0585500U JP3242992U JP3242992U JPH0585500U JP H0585500 U JPH0585500 U JP H0585500U JP 3242992 U JP3242992 U JP 3242992U JP 3242992 U JP3242992 U JP 3242992U JP H0585500 U JPH0585500 U JP H0585500U
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- Prior art keywords
- sludge
- pressure water
- tank
- recovery
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- Treatment Of Sludge (AREA)
Abstract
(57)【要約】
【目的】 凝集剤を用いながらしかも混和槽やフロック
形成槽を必要とせず、それによって、装置の小型化を図
ることにより汚泥処理能力に低下をきたすことなくスラ
ッジの分離性能のみを向上させ、汚泥回収車としての効
率を高める。
【構成】 高圧水ポンプ13から送り出される高圧水を
回収ホース3の先端に設けた噴流ポンプ10に供給し、
噴流ポンプでスラッジを吸い上げると共に、これを高圧
水と共に回収ホース3を通して沈降槽2内に搬送し、沈
降槽2内においてスラッジを分離沈降させて処理回収し
た後、上澄水を再び高圧水ポンプ13で吸い出すように
した汚泥回収車において、高圧水ポンプ13の吸い込み
側に凝集剤タンク17を連接する。これにより、凝集剤
を含む高圧水が原水と一緒に噴流ポンプ10からジェッ
ト流となって回収ホース3内に噴出するのを利用して両
者を急速混和させ、かつ、回収ホース3を利用してフロ
ックの生成を行う。
(57) [Summary] [Purpose] Sludge separation performance is achieved by using a flocculant and without the need for a mixing tank or floc formation tank, thereby reducing the size of the device and without decreasing sludge treatment capacity. Improve the efficiency of the sludge recovery vehicle. [Structure] The high-pressure water sent from the high-pressure water pump 13 is supplied to a jet pump 10 provided at the tip of the recovery hose 3,
The sludge is sucked up by the jet pump and is conveyed together with the high pressure water into the settling tank 2 through the recovery hose 3, and the sludge is separated and settled in the settling tank 2 to be treated and recovered, and then the supernatant water is again supplied to the high pressure water pump 13. In the sludge recovery vehicle designed to suck out, the coagulant tank 17 is connected to the suction side of the high-pressure water pump 13. As a result, the high-pressure water containing the coagulant is rapidly mixed with the raw water as a jet flow from the jet pump 10 into the recovery hose 3, and both are rapidly mixed, and the recovery hose 3 is used. Generate flock.
Description
【0001】[0001]
この考案は、河川や湖沼或いは土木工事現場等における汚泥の浚渫、または産 業廃棄物のスラッジピット等を浚渫するための汚泥回収車に関する。 The present invention relates to a sludge recovery vehicle for dredging sludge in rivers, lakes and marshes, civil engineering sites, etc., or sludge pits for industrial waste.
【0002】[0002]
従来、この種の汚泥やスラッジピットの浚渫に使用される装置としては、例え ば平成1年特許出願公開第176500号公報にみられるようなものが知られて いる。 Conventionally, as an apparatus used for dredging of this type of sludge or sludge pit, there is known an apparatus as disclosed in, for example, Japanese Patent Application Publication No. 176500.
【0003】 すなわち、このものは高圧水ポンプから送り出される高圧水を回収ホースの途 中に設けた噴流ポンプに供給し、この噴流ポンプで汚泥やスラッジピット等のス ラッジを含む原水を吸い上げて高圧水と共に回収ホースを通して沈降槽内に搬送 し、沈降槽内においてスラッジを分離沈降させ、沈降槽に設けられたゴミ回収コ ンベヤとスラッジ回収コンベヤとでゴミとスラッジを回収した後、沈降槽内に残 った上澄水を再び高圧水ポンプに供給するという手段をとっている。That is, this product supplies high-pressure water sent from a high-pressure water pump to a jet pump provided in the middle of a recovery hose, and this jet pump sucks up raw water containing sludge such as sludge and sludge pits to obtain high pressure water. The sludge is separated and settled in the settling tank through the collection hose through the collection hose, and the dust and sludge are collected by the waste collection conveyor and sludge collection conveyor provided in the settling tank. The remaining supernatant water is supplied to the high-pressure water pump again.
【0004】 このように上記手段では、スラッジ等の固形物を含有した原水から固形物を分 離して回収するのに沈降槽を用いているが、この沈降槽だけでは比較的粗くかつ 比重の大きな粒子しか分離して回収することができず、細かな粒子は回収できな いので処理能力の点で問題がある。As described above, in the above means, the settling tank is used to separate and recover the solid matter from the raw water containing the solid matter such as sludge, but this settling tank alone is relatively coarse and has a large specific gravity. Since only particles can be separated and collected, and fine particles cannot be collected, there is a problem in processing capacity.
【0005】 勿論、これを補うための手段としては例えば浄水場などで実際に行われている ように、直列・多段に配置した混和池に原水を導いて硫酸バン土やポリ塩化アル ミ等の凝集剤を添加し、これを急速混和してアルミニウムの水酸化物を生成させ ることにより、アルミニウム水酸化物を媒体にスラッジを次第に凝集させて集塊 とし、次のフロック形成池でこれをさらに攪拌して粗くかつ密度の高いフロック にした後、沈降池で分離沈降させるという方法が知られている。Of course, as a means for compensating for this, for example, as is actually practiced in water purification plants, raw water is introduced into a mixing pond arranged in series and in multiple stages to remove vanadium sulfate, polychlorinated aluminum, etc. By adding a flocculant and rapidly mixing it to form aluminum hydroxide, sludge is gradually flocculated in the aluminum hydroxide as a medium into agglomerates, which are then further aggregated in the next floc formation pond. A known method is to stir to make coarse and dense flocs, and then separate and settle in a sedimentation basin.
【0006】[0006]
しかし、このような手段を汚泥回収車に適用するには、スラッジを含む原水に 凝集剤を急速混和してスラッジを凝集させる混和槽や、この凝集したスラッジを さらに大きな集塊にしてゆくフロック形成槽を必要とし、装置そのものがどうし ても大型化するので、車載上のスペースおよび重量制限から装置規模が制限を受 け、汚泥処理能力が低下せざるを得ないという問題があった。 However, in order to apply such a method to a sludge recovery vehicle, a mixing tank that rapidly mixes a flocculant with raw water containing sludge to agglomerate sludge, and floc formation that makes this agglomerated sludge into larger agglomerates Since a tank is required and the equipment itself becomes large, the size of the equipment is limited due to the space and weight restrictions on the vehicle, and there is a problem that the sludge treatment capacity must be reduced.
【0007】 したがって、この考案の目的は、凝集剤を用いながらしかも混和槽やフロック 形成槽を必要とせず、これによって、装置の小型化を図ることにより汚泥処理能 力に低下をきたすことなくスラッジの分離性能のみを向上させ、汚泥回収車とし ての効率を著しく高めることのできる新規な機構を備えた汚泥回収車を提供する ことである。Therefore, an object of the present invention is to use a flocculant and not to require a mixing tank or a floc formation tank, thereby making it possible to downsize the device and thereby reduce sludge treatment performance. It is to provide a sludge recovery vehicle equipped with a new mechanism that can improve only the separation performance of the sludge and significantly improve the efficiency of the sludge recovery vehicle.
【0008】[0008]
上記の目的を達成するために、この考案にあっては、高圧水ポンプから送り出 される高圧水を回収ホースの先端に設けた噴流ポンプに供給し、噴流ポンプでス ラッジを吸い上げると共に、これを高圧水と共に回収ホースを通して沈降槽内に 搬送し、沈降槽内においてスラッジを分離沈降させて処理回収した後、上澄水を 再び高圧水ポンプで吸い出すようにした汚泥回収車において、高圧水ポンプの吸 い込み側に凝集剤を供給するための凝集剤タンクを連接したのである。 In order to achieve the above object, in the present invention, high-pressure water sent from a high-pressure water pump is supplied to a jet pump provided at the tip of a recovery hose, and the jet pump sucks up sludge and Is transported together with high-pressure water through a collection hose into the settling tank, and after sludge is separated and settled in the settling tank for treatment and collection, the high-pressure water pump is used to collect the supernatant water again. The coagulant tank for supplying the coagulant to the suction side was connected.
【0009】[0009]
これにより、高圧水ポンプの吸い込み側へと供給された凝集剤は、高圧水と混 ざり合いながら噴流ポンプへと供給され、かつ、噴流ポンプのところで凝集剤の 混ざった高圧水と回収ホースへと吸い上げられてきたスラッジを含む原水とがジ ェット流となって回収ホース3内に噴出し、このところで急速に混和されて凝集 剤が働き始めスラッジを集塊させる。 As a result, the coagulant supplied to the suction side of the high-pressure water pump is supplied to the jet pump while being mixed with the high-pressure water, and at the jet pump, the high-pressure water mixed with the coagulant and the recovery hose are supplied. The raw water containing the sludge that has been sucked up becomes a jet flow and is jetted into the recovery hose 3, where it is rapidly mixed and the coagulant begins to work to agglomerate the sludge.
【0010】 また、上記のようにして急速混和された凝集剤を含む高圧水と原水は、比較的 長い回収ホース3を通る間に次第にスラッジの凝集が進行し、粗くかつ比重の大 きな粒子のフロックとなって沈降槽に送られることになる。Further, in the high-pressure water and the raw water containing the coagulant rapidly mixed as described above, the sludge agglomerates gradually while passing through the comparatively long recovery hose 3, and the coarse particles having a large specific gravity are obtained. Will be sent to the sedimentation tank.
【0011】 かくして、この考案による汚泥回収車によれば、凝集剤を使用しながらしかも 混和槽やフロック形成槽を用いずにスラッジを比較的粗くかつ比重の大きいフロ ックとして生成させることができ、したがって、同じ大きさの車両であっても汚 泥処理能力に低下をきたすことなくスラッジの分離性能のみを向上させ、汚泥回 収車としての効率を著しく高め得ることになる。[0011] Thus, according to the sludge recovery vehicle of the present invention, sludge can be generated as flocs having a relatively coarse and large specific gravity while using a flocculant and without using a mixing tank or a floc formation tank. Therefore, even with vehicles of the same size, it is possible to improve only the sludge separation performance without lowering the sludge treatment capacity and significantly improve the efficiency as a sludge recovery vehicle.
【0012】[0012]
以下、図面に基づいてこの考案を説明する。 The invention will be described below with reference to the drawings.
【0013】 図1および図2において、この考案の一実施例である汚泥回収車Aは、車体1 上に架装したスラッジ処理用の沈降槽2と、この沈降槽2内へとスラッジSを含 む原水を搬送するための回収ホース3とを備える。1 and 2, a sludge recovery vehicle A, which is an embodiment of the present invention, has a settling tank 2 for sludge treatment mounted on a vehicle body 1 and a sludge S into the settling tank 2. And a recovery hose 3 for carrying the raw water contained therein.
【0014】 沈降槽2の上部には原水受入タンク4が設けられており、かつ、この原水受入 タンク4には、供給ポンプ5をもつ凝集剤補助タンク6が備えられていて、原水 受入タンク4内へと凝集剤を供給し得るようになっている。A raw water receiving tank 4 is provided above the settling tank 2, and the raw water receiving tank 4 is provided with a coagulant auxiliary tank 6 having a supply pump 5. The flocculant can be supplied into the inside.
【0015】 また、沈降槽2内には、沈降したスラッジSを収集するためのスクリューコン ベヤ7と、このスクリューコンベヤ7に連接して収集したスラッジSを水切りし つつ外部へと運び出すスラッジ回収コンベヤ8とがそれぞれ設けられており、さ らに、車体1上にはスラッジ回収コンベヤ8で運ばれてきたスラッジSを運搬車 Bに積み込むための出し入れ自在の積み換え用コンベヤ9が設けてある。Further, in the settling tank 2, a screw conveyor 7 for collecting the settled sludge S, and a sludge recovery conveyor that is connected to the screw conveyor 7 and drains the collected sludge S to the outside while draining it. 8 is provided on the vehicle body 1, and a transfer conveyor 9 for loading and unloading the sludge S carried by the sludge recovery conveyor 8 onto the transport vehicle B is provided on the vehicle body 1.
【0016】 前記原水受入タンク4は沈降槽2内へと通じ、しかも、この原水受入タンク4 に対して回収ホース3の基端が接続され、回収ホース3を通して搬送されてきた スラッジSを含む原水を一旦原水受入タンク4で受け、ここで所定量の凝集剤を 供給して混ぜ合わせながら沈降槽2へと流入させるようになっている。The raw water receiving tank 4 communicates with the inside of the settling tank 2, and the raw water receiving tank 4 is connected to the base end of the recovery hose 3 and the raw water containing the sludge S transported through the recovery hose 3 is supplied. Is once received by the raw water receiving tank 4, and a predetermined amount of the coagulant is supplied and mixed into the raw water receiving tank 4 to flow into the settling tank 2.
【0017】 原水受入タンク4に対して基端を接続した回収ホース3は、ここから十分な長 さをもって延び、かつ、先端には噴流ポンプ10が設けられており、この噴流ポ ンプ10からはさらにサクションホース11が延びている。The recovery hose 3 whose base end is connected to the raw water receiving tank 4 extends with a sufficient length from this, and a jet pump 10 is provided at the tip, and from this jet pump 10. Furthermore, the suction hose 11 extends.
【0018】 一方、車体1上には動力用エンジン12によつて駆動される高圧水ポンプ13 が備えられており、この高圧水ポンプ13の吸い込み側は通路14を通して沈降 槽2内に通じ、かつ、吐出側は高圧ホース15により噴流ポンプ10に連通して いて、沈降槽2内の上澄水を高圧水ポンプ13で吸い上げつつこれを高圧にして 噴流ポンプ10に供給し、この高圧水で噴流ポンプ10を駆動するようになって いる。On the other hand, a high-pressure water pump 13 driven by a power engine 12 is provided on the vehicle body 1. The suction side of the high-pressure water pump 13 communicates with the settling tank 2 through a passage 14, and The discharge side is connected to the jet pump 10 by a high-pressure hose 15. The high-pressure water pump 13 sucks the supernatant water in the settling tank 2 and supplies it to the jet pump 10 at a high pressure. It is designed to drive 10.
【0019】 また、車体1上には供給ポンプ16を備えた凝集剤タンク17が設けられてお り、この凝集剤タンク17がパイプ18を通して高圧水ポンプ13の吸い込み側 通路14に通じ、高圧水ポンプ13の吸い込み側に対して凝集剤を供給し得るよ うになっている。A coagulant tank 17 equipped with a supply pump 16 is provided on the vehicle body 1. The coagulant tank 17 communicates with a suction side passage 14 of the high-pressure water pump 13 through a pipe 18 to supply high-pressure water. The coagulant can be supplied to the suction side of the pump 13.
【0020】 さらに、沈降槽2の内部上方にはストレーナ19を介して沈降槽2内へと通じ るオーバフロー室20が備えられており、このオーバフロー室20からは戻りホ ース21が外方へと延び、沈降槽2からオーバフロー室20へと溢れ出た上澄水 を戻りホース21で元のスラッジ回収現場Cへと戻すようになっている。Further, an overflow chamber 20 communicating with the inside of the settling tank 2 via a strainer 19 is provided above the inside of the settling tank 2, and from this overflow chamber 20, a return hose 21 goes outward. The supernatant water overflowing from the settling tank 2 to the overflow chamber 20 is returned to the original sludge recovery site C by the return hose 21.
【0021】 次に作用について説明する。Next, the operation will be described.
【0022】 積み換え用コンベヤ9を運搬車Bの荷台に向かって引き出した後、車体1に設 けられた制御盤22を操作して高圧水ポンプ13と供給ポンプ16とを始動し、 かつ同時に、スラッジ回収コンベヤ8と積み換えコンベヤ9をも始動させる。After pulling out the transhipment conveyor 9 toward the bed of the carrier B, the control panel 22 provided on the vehicle body 1 is operated to start the high-pressure water pump 13 and the supply pump 16, and at the same time. The sludge recovery conveyor 8 and the transshipment conveyor 9 are also started.
【0023】 前記高圧水ポンプ13と供給ポンプ16との始動に伴い沈降槽2内の上澄水が 通路14を通して高圧水ポンプ13に吸い込まれ、かつ同時に、供給ポンプ16 によって凝集剤タンク17内の凝集剤が添加される。When the high-pressure water pump 13 and the supply pump 16 are started, the supernatant water in the settling tank 2 is sucked into the high-pressure water pump 13 through the passage 14, and at the same time, the supply pump 16 causes the flocculating agent tank 17 to coagulate. Agent is added.
【0024】 かくして、凝集剤を含む高圧水が高圧ホース15から噴流ポンプ10を通して 回収ホース3に供給されることになる。Thus, the high pressure water containing the coagulant is supplied from the high pressure hose 15 to the recovery hose 3 through the jet pump 10.
【0025】 一方、この高圧水の供給により噴流ポンプ10が働いてサクションホース11 の先端から回収現場Cにある汚泥等のスラッジSを吸い上げ、高圧水とスラッジ が混ざり合った状態で回収ホース3から沈降槽2側の原水受入タンク4に向かっ て搬送される。On the other hand, the jet pump 10 operates by the supply of this high-pressure water to suck up the sludge S such as sludge at the recovery site C from the tip of the suction hose 11, and the high-pressure water and the sludge are mixed with each other from the recovery hose 3. It is transported to the raw water receiving tank 4 on the settling tank 2 side.
【0026】 このとき、凝集剤の混ざった高圧水とサクションホース11から吸い上げられ たスラッジSとは噴流ポンプ10からジェット流となって回収ホース3内に噴出 するためこのところで急速に混和され、凝集剤が働き始めてスラッジSを集塊さ せ始める。At this time, the high-pressure water mixed with the coagulant and the sludge S sucked up from the suction hose 11 become a jet flow from the jet pump 10 and are jetted into the recovery hose 3 so that they are rapidly mixed and coagulated at this point. The agent begins to work and the sludge S begins to agglomerate.
【0027】 したがって、特に混和槽を設けることなくこれら凝集剤を含む高圧水とスラッ ジSとは噴流ポンプ10によって十分に急速混和され、スラッジSが集塊し始め る。Therefore, the high pressure water containing these coagulants and the sludge S are sufficiently rapidly mixed by the jet pump 10 without providing a mixing tank, and the sludge S starts to agglomerate.
【0028】 また、上記のようにして急速混和された高圧水とスラッジSを含む原水は、比 較的長い回収ホース3を通る間に次第にスラッジSの凝集が進行し、粗くかつ比 重の大きな粒子のフロックとなって沈降槽2における原水受入タンク4に搬送さ れてくる。Further, in the raw water containing the high-pressure water and the sludge S rapidly mixed as described above, the sludge S gradually agglomerates while passing through the comparatively long recovery hose 3, resulting in a coarse and large specific gravity. The particles become flocs and are transported to the raw water receiving tank 4 in the settling tank 2.
【0029】 このことから、フロック形成槽を用いなくてもスラッジSは比較的大きなフロ ックとなって沈降槽2の原水受入タンク4に送り込まれる。From this, the sludge S becomes a relatively large floc and is sent to the raw water receiving tank 4 of the sedimentation tank 2 without using the floc formation tank.
【0030】 そして、この原水受入タンク4に送られてくる原水の性状をみながら、必要な らば制御盤22を操作して供給ポンプ5を始動し、原水に対して凝集剤補助タン ク6から必要な量の凝集剤を追加し、凝集性能を向上させながら沈降槽2へと送 り込む。Then, while observing the properties of the raw water sent to the raw water receiving tank 4, the control panel 22 is operated to start the supply pump 5 if necessary, and the coagulant auxiliary tank 6 is added to the raw water. The necessary amount of coagulant is added from the above to the settling tank 2 while improving the coagulation performance.
【0031】 かくして、比較的粗くかつ比重の大きなフロックとなって原水中に含まれてい るスラッジSは沈降槽2内において急速に沈降し、スクリューコンベヤ7で収集 されつつスラッジ回収コンベヤ8の基端部分に集められ、回収コンベヤ8で水切 りされながら運ばれて積み換えコンベヤ9に乗り移り、運搬車Bへと送られて積 み込まれる。Thus, the sludge S that is relatively coarse and has a large specific gravity and is contained in the raw water rapidly settles in the settling tank 2, and is collected by the screw conveyor 7 while being collected at the base end of the sludge recovery conveyor 8. Collected in a portion, transported while being drained by the recovery conveyor 8, transferred to the transshipment conveyor 9, and sent to the carrier B for loading.
【0032】 以上の操作を繰り返しながらスラッジ回収現場CのスラッジSを次々と回収処 理してゆくのである。The sludge S at the sludge collection site C is successively collected by repeating the above operation.
【0033】 一方、この操作の進行に伴いサクションホース11の先端からスラッジSと共 にを吸い上げられた水によって沈降槽2内の水位が上昇するが、この殖えた分の 水はストレーナ19を通してオーバフロー室20に溢れ出し、ここから戻りホー ス21を通ってスラッジ回収現場Cに戻される。On the other hand, as this operation progresses, the water level in the settling tank 2 rises due to the water sucked up together with the sludge S from the tip of the suction hose 11, but the water thus grown overflows through the strainer 19. It overflows into the chamber 20 and returns from here to the sludge collection site C through the hose 21.
【0034】[0034]
以上のように、この考案によれば、凝集剤を用いながらしかも混和槽やフロッ ク形成槽を必要とせず、したがって、同じ大きさの車両であっても汚泥処理能力 に低下をきたすことなくスラッジの分離性能のみを向上させ、汚泥回収車として の効率を著しく高めることができるという効果をもつ。 As described above, according to the present invention, a flocculating agent is used, and neither a mixing tank nor a floc formation tank is required. Therefore, even if the vehicle is the same size, the sludge treatment capacity is not deteriorated and the sludge treatment capacity is reduced. It has the effect of improving only the separation performance of the sludge and significantly increasing the efficiency as a sludge recovery vehicle.
【図1】この考案の一実施例である汚泥回収車のスラッ
ジ処理状況を示す図である。FIG. 1 is a diagram showing a sludge treatment situation of a sludge recovery vehicle according to an embodiment of the present invention.
【図2】同汚泥処理車のスラッジ処理回収機構を模式的
に示す図である。FIG. 2 is a diagram schematically showing a sludge treatment and recovery mechanism of the sludge treatment vehicle.
A 汚泥回収車 B 運搬車 C スラッジ回収現場 S スラッジ 1 車体 2 沈降槽 3 回収ホース 8 スラッジ回収コンベヤ 9 積み換え用コンベヤ 10 噴流ポンプ 11 サクションホース 13 高圧水ポンプ 14 通路 15 高圧ホース 16 供給ポンプ 17 凝集剤タンク 20 オーバフロー室 21 戻りホース A Sludge recovery vehicle B Transport vehicle C Sludge recovery site S Sludge 1 Vehicle body 2 Sedimentation tank 3 Recovery hose 8 Sludge recovery conveyor 9 Transloading conveyor 10 Jet pump 11 Suction hose 13 High pressure water pump 14 Passage 15 High pressure hose 16 Supply pump 17 Aggregation Agent tank 20 Overflow chamber 21 Return hose
Claims (1)
回収ホースの先端に設けた噴流ポンプに供給し、噴流ポ
ンプでスラッジを吸い上げると共に、これを高圧水と共
に回収ホースを通して沈降槽内に搬送し、沈降槽内にお
いてスラッジを分離沈降させて処理回収した後、上澄水
を再び高圧水ポンプで吸い出すようにした汚泥回収車に
おいて、高圧水ポンプの吸い込み側に凝集剤を供給する
ための凝集剤タンクを連接したことを特徴とする汚泥回
収車。1. The high-pressure water sent from the high-pressure water pump is supplied to a jet pump provided at the tip of the recovery hose, the sludge is sucked up by the jet pump, and the sludge is conveyed together with the high-pressure water into the settling tank through the recovery hose. After sludge is separated and settled in the settling tank, treated and collected, and in the sludge recovery vehicle where the supernatant water is sucked again by the high-pressure water pump, a coagulant tank for supplying the coagulant to the suction side of the high-pressure water pump is installed. A sludge collection vehicle characterized by being connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3242992U JP2583531Y2 (en) | 1992-04-17 | 1992-04-17 | Sludge collection vehicle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3242992U JP2583531Y2 (en) | 1992-04-17 | 1992-04-17 | Sludge collection vehicle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0585500U true JPH0585500U (en) | 1993-11-19 |
| JP2583531Y2 JP2583531Y2 (en) | 1998-10-22 |
Family
ID=12358715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3242992U Expired - Fee Related JP2583531Y2 (en) | 1992-04-17 | 1992-04-17 | Sludge collection vehicle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2583531Y2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010107845A (en) * | 2001-10-31 | 2001-12-07 | 박찬우 | A sludge treatment device |
| KR100470138B1 (en) * | 2001-10-31 | 2005-02-21 | 대보공업 주식회사 | A sludge treatment system |
| JP2013043150A (en) * | 2011-08-25 | 2013-03-04 | Kowa Kinzoku Kogyo:Kk | Sludge treatment method and sludge treatment equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5412307B2 (en) | 2010-02-01 | 2014-02-12 | 株式会社ビービーエム | Installation method of bridge support device and fixing jig used in the method |
-
1992
- 1992-04-17 JP JP3242992U patent/JP2583531Y2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010107845A (en) * | 2001-10-31 | 2001-12-07 | 박찬우 | A sludge treatment device |
| KR100470138B1 (en) * | 2001-10-31 | 2005-02-21 | 대보공업 주식회사 | A sludge treatment system |
| JP2013043150A (en) * | 2011-08-25 | 2013-03-04 | Kowa Kinzoku Kogyo:Kk | Sludge treatment method and sludge treatment equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2583531Y2 (en) | 1998-10-22 |
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