JP2012007524A - Floating matter collecting pump device and collecting ship - Google Patents

Floating matter collecting pump device and collecting ship Download PDF

Info

Publication number
JP2012007524A
JP2012007524A JP2010143413A JP2010143413A JP2012007524A JP 2012007524 A JP2012007524 A JP 2012007524A JP 2010143413 A JP2010143413 A JP 2010143413A JP 2010143413 A JP2010143413 A JP 2010143413A JP 2012007524 A JP2012007524 A JP 2012007524A
Authority
JP
Japan
Prior art keywords
floating
pump
impeller
floating matter
matter
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.)
Pending
Application number
JP2010143413A
Other languages
Japanese (ja)
Other versions
JP2012007524A5 (en
Inventor
Masa Tagome
雅 田篭
Kenji Takago
賢二 田篭
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP2010143413A priority Critical patent/JP2012007524A/en
Publication of JP2012007524A publication Critical patent/JP2012007524A/en
Publication of JP2012007524A5 publication Critical patent/JP2012007524A5/ja
Pending legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)
  • Removal Of Floating Material (AREA)

Abstract

PROBLEM TO BE SOLVED: To reliably and efficiently take floating matter by enhancing a wide and stratified suction flow in the vicinity of a water surface for improving floating matter collecting technique, to provide a mobile cruising type while taking into account of emergency and in a case of oil-spill accident, and to solve the problem that reuse is required by direct collection.SOLUTION: The floating matter collecting pump device is set on a ship and integrated therewith so that it can be used as a cruising type floating matter collecting ship. The floating matter collecting pump device collects only the floating matter by using a specific gravity difference in a floating matter separation tank connected to a suction-ejection duct after widely taking the floating matter in the vicinity of a water surface. Spilled oil is reusable because of the direct collection using the specific gravity difference without using a treatment agent in a case of oil-spill collection.

Description

本発明は水面に浮かぶ流出油やアオコ・スカムおよびゴミなどの浮遊物をポンプにより取り込み、分離タンクで浮遊物を回収する装置に関する   The present invention relates to a device that takes in floating oil such as spilled oil, water scum, and dust floating on the water surface by a pump and collects the floating material in a separation tank.

従来は、海洋において、油流出事故が発生した場合、オイルフェンスを張り、油吸着材で回収するか油処理剤などで分散・分解する方法がある。流出油の処理装置としては、双胴船の双胴間に下端が水面下に没する回転翼車(水車)を設け、ゲル化剤との混合攪拌による油物質のゲル化を促進し、回収するもの(特許文献1)もあるが、装置が大掛かりで、小回りもきかず、回収しても、再利用は難しい。また、ポンプを吸引力として利用した浮遊物を回収する方法(特許文献2)やバキュウムポンプで流出油を回収する方法(特許文献3)もあるが、吸込み流れが不安定で一様でないため、回収効率は良くない。 Conventionally, when an oil spill accident occurs in the ocean, there is a method in which an oil fence is stretched and recovered with an oil adsorbent or dispersed and decomposed with an oil treatment agent or the like. As a spilled oil treatment device, a rotary impeller (water turbine) with its lower end submerged below the surface of the water is provided between the catamarans of the catamaran to promote the gelation of the oil substance by mixing and stirring with the gelling agent. Some devices (Patent Document 1) do, but the device is large, does not turn easily, and is difficult to reuse even if collected. In addition, there are a method (Patent Document 2) that collects suspended matter using a pump as a suction force and a method (Patent Document 3) that collects spilled oil with a vacuum pump, but the suction flow is unstable and uneven. Recovery efficiency is not good.

特開昭59−156890号公報JP 59-156890 A 特開昭59−230887号公報JP 59-230887 A 特開平4−266588号公報JP-A-4-266588

浮遊物の回収技術向上のためには、水面付近において一様で幅広の層状的な吸込み流れを強めて確実に浮遊物を取り込むこと、浮遊物を取り込んだ後、浮遊物のみを効率的に分離回収する技術を必要とする。流出油事故の場合は、緊急性を考慮した小回りがきくこと、および直接回収による再利用が求められる。   In order to improve the technology for collecting suspended solids, the uniform and wide layered suction flow is strengthened near the surface of the water to ensure that the suspended matter is taken in. After the suspended matter is taken in, only the suspended matter is efficiently separated. Recover technology is required. In the case of a spilled oil accident, it is necessary to make a small turn in consideration of urgency and reuse it by direct recovery.

本発明は従来技術の問題点を解決するために、浮遊物を直接取り込むことが出来るポンプを組み込んだ比較的簡単な浮遊物回収装置で、貫流ポンプの流れの特性を生かして、水面付近に一様で幅広の層状的な吸込み流れを作り、浮遊物を効率良くポンプを通して取り込み、分離タンクで回収出来るようにした浮遊物回収装置を提供することを目的とする。   In order to solve the problems of the prior art, the present invention is a relatively simple suspended matter collecting apparatus incorporating a pump that can directly take in suspended matter. An object of the present invention is to provide a suspended matter recovery apparatus that creates a wide and stratified suction flow in a wide range, efficiently takes in suspended matter through a pump, and can be recovered by a separation tank.

請求項1に記載の発明は、貫流ポンプ(クロスフロ−ポンプ)の内部流れの特性を生かし、ポンプによる浮遊物の取り込み技術と浮遊物分離タンクの回収技術を組み合わせた効率良い浮遊物回収装置を提供するものである。即ち、羽根車形状が円筒状で多翼の貫流ポンプの外側ケ−シング形状を浮遊物回収用にアレンジしたポンプ本体を羽根車上端が水面近くに没する程度に設置し、水面付近の流れに貫流ポンプ特有の一様で幅広の層状の安定した吸込み流れを作ることによって、浮遊物を含む流れを直接ポンプに取り込む。その吐出し流れは、なお乱れの少ない層状の流れを維持しながら浮遊物分離タンクに送られる。この乱れの少ない流れの特性により、水と浮遊物の比重差を利用することによるタンク内での浮遊物の回収が容易となる。   The invention according to claim 1 provides an efficient floating substance recovery device that combines the characteristics of the internal flow of a once-through pump (cross flow pump) and combines the technique of collecting the floating substance by the pump and the technique of collecting the floating substance separation tank. To do. In other words, the pump body with the impeller shape cylindrical and the outer casing shape of the multi-blade once-through pump arranged for collecting suspended matter is installed so that the upper end of the impeller is submerged near the water surface. By creating a uniform, wide, laminar, stable suction flow characteristic of a once-through pump, a flow containing suspended solids is taken directly into the pump. The discharge flow is sent to the suspended matter separation tank while maintaining a laminar flow with little disturbance. This less turbulent flow characteristic facilitates the recovery of suspended matter in the tank by utilizing the specific gravity difference between water and suspended matter.

図1に浮遊物吸引用の貫流ポンプ50の内部構造の概略図を示す。(a)は貫流ポンプ本体の外側ケ−シング形状を浮遊物吸引用にアレンジした断面図、(b)は(a)のY−Y矢視断面図である。貫流ポンプ50の本体は、基本的には円筒状の多翼の羽根車7を収容したポンプケ−シング30と流れを制御する舌部8から構成され、羽根車回転軸2によって駆動用モ−タ12に接続されている。 FIG. 1 shows a schematic view of the internal structure of a once-through pump 50 for sucking suspended matters. (A) is sectional drawing which arranged the outer casing shape of the once-through pump main body for floating matter suction, (b) is a YY arrow sectional view of (a). The main body of the once-through pump 50 is basically composed of a pump casing 30 containing a cylindrical multi-blade impeller 7 and a tongue portion 8 for controlling the flow. The impeller rotary shaft 2 drives the motor for driving. 12 is connected.

流れは図1(a)のポンプ断面図に示すように吸込み側9から吐出し側10に向って2回羽根6を通過する。即ち流れは吸込み側9では、羽根車7の外側から内側へ、吐出し側10では内側から外側へ流出して羽根車7を横断する。羽根車7は幅方向に長くとれること、また、流れが二次元的で羽根車に接線方向に吐出されることから、吐出し流れは従来技術と異なり、幅広のシ−ト状で乱れも少なく、また拡散することなく、一様な流れとなって遠くまで達することができる。従って従来とは異なり、ポンプによって直接取り込まれた浮遊物は水と浮遊物が複雑に混濁することなく、吐出されるため、吐出し側に設置された浮遊物分離タンクにおける浮遊物の分離が容易である。 The flow passes through the blade 6 twice from the suction side 9 toward the discharge side 10 as shown in the pump sectional view of FIG. That is, the flow flows from the outside of the impeller 7 to the inside on the suction side 9 and flows out from the inside to the outside on the discharge side 10 to cross the impeller 7. The impeller 7 can be long in the width direction, and since the flow is two-dimensional and is discharged tangentially to the impeller, the discharge flow is wide sheet-like and less turbulent, unlike the prior art. Also, it can reach a long distance in a uniform flow without spreading. Therefore, unlike the conventional case, the suspended matter directly taken in by the pump is discharged without complicated turbidity of water and suspended matter, so it is easy to separate the suspended matter in the suspended matter separation tank installed on the discharge side. It is.

また、各羽根6の吸込み側における入口と出口が吐出し側では逆になるため、物が羽根間に詰まりにくい構造であることは回収に当たり、優れた強みである。例えば藻類や小さなクラゲ類および小さなゴミなども直接ポンプに取り込むことが出来る。羽根枚数を変えて羽根ピッチを変えたり、羽根内外径比を変えることによって、浮遊物の性状や大きさに応じた対応が出来るなどの特徴を持っている。 In addition, since the inlet and outlet on the suction side of each blade 6 are reversed on the discharge side, it is an excellent strength in collecting that the structure is less likely to cause clogging between the blades. For example, algae, small jellyfish and small garbage can be taken directly into the pump. By changing the number of blades, changing the blade pitch, or changing the inner / outer diameter ratio of the blades, it is possible to respond to the nature and size of the suspended matter.

請求項2に記載の発明は請求項1に記載の浮遊物回収用ポンプ装置を船にセットして一体化した走行型の浮遊物回収船を構成したもので、その中の浮遊物分離タンクの底部解放口は船の底面あるいは船尾側の外壁を通して外部へ開口していて、該浮遊物吸引用の貫流ポンプにより取り込まれた浮遊物を含む液体のうち、比重の大きい液体は低部開口部より自然に外に流出し、比重の小さい油などの浮遊物はタンク容器内の上部水面付近に集積するような構造になっている。 The invention described in claim 2 constitutes a traveling-type floating substance recovery ship in which the floating substance recovery pump device according to claim 1 is set and integrated on the ship, and the floating substance separation tank of the traveling type The bottom opening is opened to the outside through the bottom of the ship or the outer wall on the stern side. Of the liquid containing floating matter taken in by the flow-through pump for sucking the floating matter, the liquid with high specific gravity is from the lower opening. It has a structure that naturally flows out and floats such as oil with a small specific gravity accumulate near the upper water surface in the tank container.

該浮遊物分離タンクの底部解放口を船尾側に開口するようにすれば、ポンプによる吐出し流れが推進力となるため、スクリュウによる推進を不要とすることも出来る。 If the bottom opening of the floating substance separation tank is opened to the stern side, the discharge flow by the pump becomes the propulsive force, so that the propulsion by the screw can be made unnecessary.

請求項3に記載の発明は図2の浮遊物吸引用の貫流ポンプ51の羽根車7の羽根6の外径寸法を6bのように羽根車側板7bより少し外側に突き出して、吸込み口での浮遊物を掻き込みやすくしたもので、これによれば、空回りすることなく、浮遊物の種類によらず、確実に取り込むことができる。各羽根外径寸法の羽根車側板外径よりの突き出し量は羽根車直径に対し、3〜10%程度が適当である。   In the invention according to claim 3, the outer diameter dimension of the impeller 7 of the impeller 7 of the once-through pump 51 for floating substance suction in FIG. 2 protrudes slightly outside the impeller side plate 7b as shown by 6b, According to this, it is possible to reliably take in the suspended matter without depending on the type of the suspended matter. About 3 to 10% of the protrusion amount from the impeller side plate outer diameter of each blade outer diameter size is appropriate.

請求項4に記載の発明は、流出した毒性のある浮遊物の液体などをポンプ内に取込んで、羽根車中空回転軸の散気孔から処理液や微細気泡を噴出させて、液体を中和して無害化したり水質浄化を助長すること、および装置内の清掃を目的とする。 The invention according to claim 4 neutralizes the liquid by taking the toxic suspended liquid that has flowed out into the pump and ejecting the treatment liquid and fine bubbles from the air diffuser of the impeller hollow rotating shaft. The purpose is to detoxify or promote water purification and to clean the inside of the apparatus.

微細化した気泡や処理液の供給手段は図2に示すように、羽根車7内の中空回転軸3の外周面に多数の散気孔5を穿孔、あるいは多孔質材を貼り付け、中空回転軸3を通して羽根車外部のホ−ス13に接続したエアポンプ11と液体ポンプ11bにより処理液単独あるいはエアと一緒に羽根車内の流れの中に散気孔5より微粒子の状態で供給できる構造となっている。 As shown in FIG. 2, the supply means for the refined bubbles and the processing liquid has a large number of diffused holes 5 formed on the outer peripheral surface of the hollow rotary shaft 3 in the impeller 7 or a porous material attached thereto. The air pump 11 and the liquid pump 11b connected to the hose 13 outside the impeller through 3 can be supplied in the form of fine particles from the air diffuser 5 into the flow in the impeller together with the treatment liquid alone or with air. .

請求項5に記載の発明は、該貫流ポンプの吸込み側流路内の羽根車直前に吸込口に向かって水平面に対し、+3°〜+10°程度傾斜したガイドベ−ンを水面近くに没した状態で設置することを特徴とするもので、これによりポンプへの近寄り流れの水面近傍の流れが増速され、水面に淀みのない微小波を発生させることになる。これにより、水面に油膜様の幕を張らないようになり、浮遊物の取り込みを容易にすることが可能となる。 The invention according to claim 5 is a state in which a guide vane inclined by about + 3 ° to + 10 ° with respect to the horizontal plane toward the suction port immediately before the impeller in the suction side channel of the once-through pump is submerged near the water surface. In this way, the flow in the vicinity of the water surface of the approaching flow to the pump is accelerated, and a micro wave without stagnation on the water surface is generated. As a result, an oil film-like curtain is not stretched on the water surface, and it becomes possible to easily take in floating substances.

請求項6に記載の発明はポンプにより取り込んだ浮遊物を比重差を利用して分離回収するための浮遊物分離タンクの形状や構造についての技術を提供するものである。タンクは大別して矩形タイプと円形タイプに分けられ、浮遊物が浮上し易いように円形タイプでは、タンク内において流れに旋回流を与えるサイクロンタイプ、矩形タイプでは、タンク後部の高さ方向中間の位置に流れを制御して浮遊物を分離するための浮遊物分離ガイドを設置した構造となっている。 The invention described in claim 6 provides a technique regarding the shape and structure of a floating substance separation tank for separating and collecting the floating substance taken in by a pump using a difference in specific gravity. Tanks are broadly divided into rectangular types and circular types. Cyclone type that gives a swirling flow to the flow in the tank, and rectangular type in the middle of the height direction in the rear of the tank so that the suspended matter can easily float. It has a structure in which a floating material separation guide for separating the floating material by controlling the flow is installed.

請求項7に記載の発明は固定型の浮遊物回収用ポンプ装置で、藻類や浮遊ゴミなどの固形物を回収する浮遊物回収タンクの形状や設置方法についての技術を提供するものである。浮遊物回収タンクは貫流ポンプの吸込み側に接続しても吐出し側に接続してもよい。浮遊物の回収には、外部の海や河川に開放された吸込み側流路や吐出し側流路に浮遊物回収スクリ−ン設置して行う。 The invention according to claim 7 is a fixed type floating substance collection pump device, and provides a technique regarding the shape and installation method of the floating substance collection tank for collecting solid substances such as algae and floating dust. The suspended matter recovery tank may be connected to the suction side or the discharge side of the once-through pump. Floating substances are collected by installing a floating substance collection screen in the suction-side flow path and discharge-side flow path open to the outside sea or river.

本発明によれば、流出油や多様な浮遊物をポンプに直接取り込んだ後、容易に浮遊物分離タンクで回収できることから従来の技術よりも回収効率が良く、回収した油の再利用も可能となる。また、有害な浮遊物に対しても羽根車中空回転軸3の散気孔5から処理液や微細気泡を噴出することにより、対処することが可能となる。   According to the present invention, spilled oil and various floating substances can be easily collected in the floating substance separation tank after being directly taken into the pump, so that the recovery efficiency is better than conventional techniques, and the recovered oil can be reused. Become. Moreover, it becomes possible to cope with harmful floating matters by ejecting the treatment liquid and the fine bubbles from the air diffusion holes 5 of the impeller hollow rotary shaft 3.

図1は本発明の浮遊物を取り込む貫流ポンプ(クロスフロ−ポンプ)本体の基本構造を示す。(a)は貫流ポンプの断面図、(b)は(a)のY−Y矢視断面図である。FIG. 1 shows a basic structure of a main body of a cross-flow pump (cross-flow pump) for taking in floating matter of the present invention. (A) is sectional drawing of a once-through pump, (b) is a YY arrow sectional drawing of (a). 図2は図1の羽根車および流入口ケ−シング内部に新技術を加えた浮遊物吸引用の貫流ポンプの構造を示す。(a)は貫流ポンプの断面図、(b)は(a)のY−Y矢視断面図である。FIG. 2 shows the structure of a once-through pump for sucking a floating substance by adding a new technology inside the impeller and inlet casing of FIG. (A) is sectional drawing of a once-through pump, (b) is a YY arrow sectional drawing of (a). 図3は浮遊物回収用ポンプ装置を船にセットし、一体化した浮遊物回収船の構造を示す。(a)は平面図、(b)は側断面図である。(実施例1)FIG. 3 shows the structure of a floating substance recovery ship integrated with a floating substance recovery pump device set on the ship. (A) is a top view, (b) is a side sectional view. Example 1 図4は図3の第1の実施例とは浮遊物分離タンクの構造が異なる場合の浮遊物回収船の構造を示す。(a)は平面図、(b)は側断面図である。(実施例2)FIG. 4 shows the structure of a floating substance recovery ship when the structure of the floating substance separation tank is different from that of the first embodiment of FIG. (A) is a top view, (b) is a side sectional view. (Example 2) 図5は図4の第2の実施例とは浮遊物分離タンク後壁側開放口の形状が異なる場合の浮遊物回収船の構造を示す。(a)は平面図、(b)は側断面図である。(実施例3)FIG. 5 shows the structure of a suspended matter recovery ship in the case where the shape of the opening on the rear wall side of the suspended matter separation tank is different from that of the second embodiment of FIG. (A) is a top view, (b) is a side sectional view. (Example 3) 図6は図4の第2の実施例の羽根車を3連にして、より幅広く浮遊物を回収できるようにした浮遊物回収船の構造を示す平面図である。(実施例4)FIG. 6 is a plan view showing the structure of a suspended matter recovery ship in which the impeller of the second embodiment of FIG. Example 4 図7は図3の第1実施例における浮遊物分離タンクを円筒型にした場合の構造を示す。(a)は平面図、(b)は側断面図である。(実施例5)FIG. 7 shows the structure when the floating substance separation tank in the first embodiment of FIG. (A) is a top view, (b) is a side sectional view. (Example 5) 図8は貫流ポンプを縦型にして、ポンプの吐き出しダクトを円形の浮遊物分離タンクの流入口に接線方向に接続した場合の浮遊物回収船を示す。(a)は平面図、(b)は側断面図である。(実施例6)FIG. 8 shows a suspended matter recovery ship when the once-through pump is a vertical type and the discharge duct of the pump is connected tangentially to the inlet of the circular suspended matter separation tank. (A) is a top view, (b) is a side sectional view. (Example 6) 図9は図4の第2実施例とは異なる矩形型の浮遊物分離タンクを接続した場合の浮遊物回収船の構造を示す。(a)は平面図、(b)は側断面図である。(実施例7)FIG. 9 shows the structure of a floating substance recovery ship when a rectangular floating substance separation tank different from the second embodiment of FIG. 4 is connected. (A) is a top view, (b) is a side sectional view. (Example 7) 図10は図9の第7実施例の浮遊物分離タンクと異なり、浮遊ゴミなどの固形の浮遊物を回収する場合の装置を示す。(a)は平面図、(b)は側断面図である。(実施例8)FIG. 10 shows an apparatus for collecting solid floating matters such as floating dust unlike the floating matter separation tank of the seventh embodiment of FIG. (A) is a top view, (b) is a side sectional view. (Example 8) 図11は縦置きの貫流ポンプの吸込み側に浮遊物回収タンクを接続した場合の浮遊物回収用ポンプ装置の据付け状態を示す。(a)は平面図、(b)は側断面図である。(実施例9)FIG. 11 shows an installed state of the floating substance recovery pump device when a floating substance recovery tank is connected to the suction side of the longitudinal once-through pump. (A) is a top view, (b) is a side sectional view. Example 9 図12は浮遊物吸引用の貫流ポンプを筏に取り付けた場合の構造を示す。(a)は平面断面図、(b)は側断面図である。(実施例10)FIG. 12 shows a structure when a once-through pump for floating substance suction is attached to a ridge. (A) is a plane sectional view, (b) is a side sectional view. (Example 10)

以下に本発明の実施の形態を図3〜図12を参照して説明する。 Embodiments of the present invention will be described below with reference to FIGS.

図3は本発明の第1実施例で、請求項1に記載の浮遊物回収用ポンプ装置全体を船にセットし、一体化したときの浮遊物回収船40の形態を示し、流出油などの回収に利用される。(a)は平面図、(b)は側断面図である。本発明の基本的構造は貫流ポンプを中心にして、吸込み側には船首の取水口部に開閉式流入ガイド61、ポンプの直前の取水流路64に浮遊物導入ガイドベ−ン65を設置し、吐き出し側には吐出しダクト55に接続した浮遊物分離タンク81が設置されている。タンク底部の開放口70は船底を通じて外へ開口している。浮遊物のポンプへの取水口62の開口部は浮遊物のある水面側の流れを幅広く取り込むため、深さ方向を浅くした横長の矩形にし、ポンプ吸込側ケ−シング15によってポンプ吸込み口に向かってなだらかに接続している。 FIG. 3 is a first embodiment of the present invention, and shows the form of the suspended matter recovery ship 40 when the entire floating matter recovery pump device according to claim 1 is set on a ship and integrated. Used for recovery. (A) is a top view, (b) is a side sectional view. The basic structure of the present invention is centered on the once-through pump, and on the suction side, an open / close type inflow guide 61 is installed at the intake port of the bow, and a floating material introduction guide vane 65 is installed in the intake channel 64 immediately before the pump, A floating substance separation tank 81 connected to the discharge duct 55 is installed on the discharge side. An opening 70 at the bottom of the tank opens to the outside through the ship bottom. The opening of the water intake 62 to the pump of the floating substance takes a wide flow on the water surface side where there is the floating substance, so that the depth direction is made into a horizontally long rectangle, and the pump suction side casing 15 moves toward the pump suction port. Connected gently.

この実施の形態による流出油などの浮遊物回収では、まず船60の先首も兼ねた開閉式流入ガイド61を開いて水面付近に漂う流出油などの浮遊物を取水口62に導き、取水流路64において貫流ポンプの羽根車7のすぐ上流側に設置した浮遊物導入ガイドベ−ン65によって、水面14付近の流れを増速させるとともに、局部的に水面付近のみを活性化させ、微小な水面波を発生させる。この手法により、油などの浮遊物が水面に幕を張ることなく、浮遊物のポンプへの取り込みを容易にすることが出来る。 In the recovery of suspended matter such as spilled oil according to this embodiment, first, the openable inflow guide 61 that also serves as the head of the ship 60 is opened, and the suspended matter such as spilled oil drifting near the surface of the water is led to the water inlet 62, A floating material introduction guide vane 65 installed on the path 64 immediately upstream of the impeller 7 of the once-through pump accelerates the flow near the water surface 14 and locally activates only the vicinity of the water surface. Generate a wave. By this method, floating substances such as oil can be easily taken into the pump without causing a curtain on the water surface.

浮遊物吸引用の貫流ポンプ51により水とともに取り込まれた流出油などの浮遊物の吐き出し流れは前述のように乱れも少ないため、水と浮遊物は混濁せず、吐出しダクト55を通って矩形型浮遊物分離タンク81に運び込まれる。この浮遊物分離タンク81は矩形型で流入口部に水平方向導入ガイド68、後壁側に浮遊物分離ガイド69、底部に船底開放口70を設けた構造になっている。 Since the discharge flow of floating matter such as spilled oil taken together with water by the flow-through pump 51 for floating matter suction is less turbulent as described above, the water and the floating matter are not turbid and pass through the discharge duct 55 and become rectangular. It is carried into the mold floating matter separation tank 81. This floating substance separation tank 81 has a rectangular shape and is provided with a horizontal introduction guide 68 at the inlet, a floating substance separation guide 69 on the rear wall side, and a ship bottom opening 70 at the bottom.

浮遊物分離タンク81においては、流入口部において水平方向導入ガイド68によりポンプの吐出しダクト55からの流入を水平方向に向かわせ、比重の小さい浮遊物が浮上し易いようにする。タンク後壁側では、下向きの流れに含まれる浮遊物のみを水面側に戻すために流れを制御する浮遊物分離ガイド69を設置し、比重差を利用して浮遊物のみ上方に向かうようにする。余分の水は船底開放口70から外部に自然流出し、浮遊物分離タンク81の水位のバランスが保たれる。 In the floating substance separation tank 81, the inflow from the discharge duct 55 of the pump is directed in the horizontal direction by the horizontal introduction guide 68 at the inlet, so that the floating substance having a small specific gravity can easily float. On the tank rear wall side, a floating material separation guide 69 for controlling the flow to return only the floating material contained in the downward flow to the water surface side is installed, and only the floating material is directed upward using the specific gravity difference. . Excess water naturally flows out to the outside from the ship bottom opening 70, and the balance of the water level in the suspended matter separation tank 81 is maintained.

浮遊物分離タンク81の水面側に集められた油などの浮遊物は浮遊物回収導入パイプ71を通って浮遊物回収容器73に集められる。浮遊物は浮遊物分離タンク81の入口側に集まりやすいため、回収容器の位置は場所の余裕があれば、浮遊物分離タンク81の前側に置いた方がよい。あるいはフレキシブルホ−スなどによるサイホン作用を利用して直接水面側から回収容器へ回収してもよい。本発明によれば、流出油を直接回収できるため、再利用できるメリットがある。 The floating substance such as oil collected on the water surface side of the floating substance separation tank 81 is collected in the floating substance collection container 73 through the floating substance collection introduction pipe 71. Since the floating substances are likely to gather on the inlet side of the floating substance separation tank 81, the position of the recovery container should be placed on the front side of the floating substance separation tank 81 if there is room. Or you may collect | recover to a collection container directly from the water surface side using the siphon effect | action by a flexible hose. According to the present invention, since the spilled oil can be directly recovered, there is an advantage that it can be reused.

水質浄化や浮遊物の浮上を助長する手段としては、請求項4に記載の技術を利用できる。エアポンプ11により該中空回転軸3に供給された気体を前述の図2に示す散気孔5を通して羽根車内中心部に細かな気泡として噴出させ、その微細な気泡が均一に混入した状態で羽根車7の内側から外側を通ってポンプの吐出し流れと共に供給される。この気泡を伴う流れによって、水質を浄化したり、吐出し部において浮遊物の浮上を助長し、回収を容易にする。 The technique described in claim 4 can be used as means for promoting water purification and floating floating. The gas supplied to the hollow rotary shaft 3 by the air pump 11 is ejected as fine bubbles into the center of the impeller through the air diffusion holes 5 shown in FIG. 2, and the impeller 7 in a state where the fine bubbles are uniformly mixed. Supplied along with the pump discharge flow from the inside through the outside. The flow accompanied by the bubbles purifies the water quality and promotes the floating of the suspended matter at the discharge part, facilitating the recovery.

流出した浮遊物が回収できない毒性のある液体などを処理する場合には、液体ポンプ11bにより有害液を無害にするための処理液をホ−ス13を通して貫流ポンプの羽根車の中空回転軸3に供給し、回転を伴いながら該散気孔5から微粒化した処理液を羽根車内に噴出させ、取込んだ有害液などに均一に混入させることによって、無害化することができる。 In the case of processing a toxic liquid or the like that cannot be recovered from the suspended matter that has flowed out, a processing liquid for making the harmful liquid harmless by the liquid pump 11b is passed through the hose 13 to the hollow rotary shaft 3 of the impeller of the once-through pump. It can be rendered harmless by supplying and spraying the atomized treatment liquid from the diffuser hole 5 with rotation into the impeller and uniformly mixing it into the taken-in harmful liquid or the like.

ポンプのメンテナンスおよび洗浄は吸込み側水門58と吐出し側水門59を閉じることによって行う。装置の洗浄はポンプを空運転しながら、液体ポンプ11bにより洗浄液を該羽根車中空軸散気孔5の装置に供給して行う。 Maintenance and cleaning of the pump is performed by closing the suction side sluice 58 and the discharge side sluice 59. The apparatus is cleaned by supplying the cleaning liquid to the impeller hollow shaft diffuser 5 by the liquid pump 11b while the pump is idling.

図4は本発明の第2実施例の流出油などの浮遊物回収船41の形態を示す。(a)は平面図、(b)側断面図である。本装置の構造は、図3の第一の実施例と異なり、浮遊物分離タンク82の底部の開放口は船底側でなく、浮遊物分離タンク後壁側開放口74から船尾開放口80を通じて外部(海、河川)へ通じている。 FIG. 4 shows the form of a floating substance recovery ship 41 such as spilled oil according to the second embodiment of the present invention. (A) is a top view, (b) is a sectional side view. The structure of this apparatus is different from the first embodiment of FIG. 3 in that the opening at the bottom of the floating substance separation tank 82 is not on the ship bottom side, but from the floating wall separation tank rear wall side opening 74 to the outside through the stern opening 80. (Sea, river).

この実施の形態によれば、浮遊物分離ガイド69の部分で、比重差により分離された余分の水は該浮遊物分離ガイド69の下を通って船尾開放口80から外へ流出する。船外部への開放口の位置は船底側でも船尾側でも構わないが、開放口を船尾側に設ければ、排出速度により船の推進力が得られるという利点がある。 According to this embodiment, excess water separated due to the difference in specific gravity flows out from the stern opening 80 through the suspended matter separation guide 69 at the floating matter separation guide 69. The position of the opening to the outside of the ship may be on the bottom side or the stern side. However, if the opening is provided on the stern side, there is an advantage that the propulsive force of the ship can be obtained by the discharge speed.

船首入口部にあるバ−スクリ−ン63は、貫流ポンプに直接取り込むことができない大きな固形浮遊物を回収するため、および浮遊物の種類によりポンプ上流側で回収した方が良いときに対応できるようにしたものである。 The bar screen 63 at the bow entrance can be used to recover large solid suspended solids that cannot be taken directly into the once-through pump, and when it is better to collect upstream of the pump depending on the type of suspended solids. It is a thing.

図5は本発明の第3実施例の浮遊物回収船42の形態を示す。(a)は平面図、(b)は側断面図である。本装置の構造は、図4の第2の実施例と異なり、浮遊物分離タンク後壁側開放口74から船尾開放口80へ接続した排出パイプ91の途中に電動排出コントロ−ルバルブ90を設けて、バルブ開度を調節することによりタンクからの排出量や排出スピ−ドを変え、また左右のバルブ開度を変えることによって船の速度や方向変換が出来ようにしている。この方法では、スクリュウによる推進は必要とせず、ゆっくりしたスピ−ドで動くため、浮遊物回収に適している。 FIG. 5 shows the form of the suspended matter recovery ship 42 of the third embodiment of the present invention. (A) is a top view, (b) is a side sectional view. Unlike the second embodiment of FIG. 4, the structure of this apparatus is provided with an electric discharge control valve 90 in the middle of a discharge pipe 91 connected from the floating wall separation tank rear wall side opening 74 to the stern opening 80. The amount of discharge from the tank and the discharge speed are changed by adjusting the valve opening, and the speed and direction of the ship can be changed by changing the left and right valve openings. This method does not require propulsion with a screw, and moves at a slow speed, so it is suitable for collecting suspended matter.

図6は本発明の第4実施例の浮遊物回収船43の形態を示す平面図である。貫流ポンプ52の流れは2次元的であるから、吸込みの流入口幅を増やすためには、単純に羽根車7の軸方向の長さを増やせばよい。あるいは本図に示すように羽根車7を数個幅方向に連結すればよい。本実施例は羽根車7を3個接続した場合で、他の構成は図4の第2実施例の形態と同様である。 FIG. 6 is a plan view showing the form of the suspended matter recovery ship 43 of the fourth embodiment of the present invention. Since the flow of the once-through pump 52 is two-dimensional, in order to increase the suction inlet width, the axial length of the impeller 7 is simply increased. Alternatively, several impellers 7 may be connected in the width direction as shown in the figure. This embodiment is a case where three impellers 7 are connected, and the other configuration is the same as that of the second embodiment shown in FIG.

図7は本発明の第5実施例の浮遊物回収船44の形態を示す平面図(a)と側断面図(b)である。本技術は浮遊物分離タンク84の形状を矩形ではなく、円筒形にしたものである。吐出しダクト55から円筒形の浮遊物分離タンク84に流入した流れは、センタ−分離壁86によって左右に分かれ、円筒に沿う循環流を生じながら、比重差によって、浮遊物は水面側に集められる。センタ−分離壁86は油などの浮遊物の浮上を助長するために下膨らみになっている。余分の水は底部開口部より自然流出し、水位のバランスが保たれる。浮遊物回収容器73bは、仕切り板77によって、油室78と水室79に分けられている。 FIG. 7 is a plan view (a) and a side sectional view (b) showing the form of the suspended matter recovery ship 44 of the fifth embodiment of the present invention. In the present technology, the shape of the suspended matter separation tank 84 is not rectangular but cylindrical. The flow flowing into the cylindrical floating substance separation tank 84 from the discharge duct 55 is divided into left and right by the center separation wall 86, and the floating substance is collected on the water surface side due to the difference in specific gravity while generating a circulating flow along the cylinder. . The center separation wall 86 is bulged downward in order to promote the floating of floating substances such as oil. Excess water naturally flows out from the bottom opening, and the water level is balanced. The suspended matter collection container 73 b is divided into an oil chamber 78 and a water chamber 79 by a partition plate 77.

浮遊物の回収容器76を仕切り板77によって、油室78と水室79に分けたのは、次の理由による。本装置による浮遊物の回収効率は、貫流ポンプ羽根車7の没水深さに関係する船の喫水に影響されやすいので、浮遊物の回収量に応じて、水室の水量を放出調整して船の喫水を最適の位置に保つためである。 The floating material collection container 76 is divided into the oil chamber 78 and the water chamber 79 by the partition plate 77 for the following reason. The floating collection efficiency of this device is easily affected by the draft of the ship, which is related to the submergence depth of the once-through pump impeller 7, so that the amount of water in the water chamber is adjusted according to the amount of floating collected. This is to keep the draft in the optimum position.

貫流ポンプ羽根車7を適正な没水深さにする方法としては、ポンプ吸込み側ケ−シング15と吐出しダクト55の一部をフレキシブルホ−スにしてポンプ本体を上下可能にする方法もある。また、ポンプと一体の前後のフランジ25、26を上下にスライドできるようにして調節する方法もある。 As a method of making the once-through pump impeller 7 have an appropriate submerged depth, there is a method in which a part of the pump suction side casing 15 and the discharge duct 55 are made flexible hoses so that the pump body can be moved up and down. There is also a method of adjusting the front and rear flanges 25, 26 integral with the pump so that they can slide up and down.

図8は本発明の第6実施例の浮遊物回収船45の形態を示す。(a)は平面図、(b)は側断面図である。本実施例では浮遊物吸引用の貫流ポンプ53の据付けが第1〜第5の実施例とは異なり、縦置きになっているのが特徴である。ポンプケ−シング形状31はポンプと分離タンクの位置関係を考慮してアレンジしている。この実施の形態によれば円筒形の浮遊物分離タンク85は、吐出しダクト56からの流れが分離用タンクに接線方向に流入する構造であり、流れは円形のタンク内を旋回しながら、分離に要する時間を長くし、浮遊物と水を分離しやすくする。余分の水は船底開放口70bから自然流出し、タンク内の水位が保たれる。 FIG. 8 shows a form of a suspended matter collection ship 45 according to the sixth embodiment of the present invention. (A) is a top view, (b) is a side sectional view. Unlike the first to fifth embodiments, the present embodiment is characterized in that the flow-through pump 53 for floating matter suction is installed vertically. The pump casing shape 31 is arranged in consideration of the positional relationship between the pump and the separation tank. According to this embodiment, the cylindrical floating substance separation tank 85 has a structure in which the flow from the discharge duct 56 flows tangentially into the separation tank, and the flow is separated while swirling in the circular tank. It takes longer time to make it easier to separate suspended matter and water. Excess water naturally flows out from the ship bottom opening 70b, and the water level in the tank is maintained.

縦置きでは、横置きのように幅方向に長く取れないが、駆動用モ−タ12bが水面上に設置できることから、据付およびメンテナンスが容易である。縦置きは小規模の浮遊物回収に対して有効である。また、水面近くの流れのみの流入が得られるので浮遊物を確実に取り込むことが出来る。 In the vertical installation, it cannot be taken long in the width direction as in the horizontal installation, but since the driving motor 12b can be installed on the water surface, installation and maintenance are easy. Vertical installation is effective for small-scale suspended matter collection. In addition, since only an inflow near the water surface can be obtained, suspended matters can be reliably taken in.

図9は本発明の第7実施例の浮遊物回収船46の形態を示す。(a)は平面断面図、(b)は側断面図である。本発明は第6実施例と同じく、浮遊物吸引用の貫流ポンプ54の据付けは縦置きであるが、浮遊物分離タンク83は矩形で、タンクの船尾側は全面的に開放されていて、外海や河川と通じている。ポンプケ−シング形状32はポンプと分離タンクの中心位置がほぼ一致するようにアレンジしている。 FIG. 9 shows the form of a suspended matter recovery ship 46 according to the seventh embodiment of the present invention. (A) is a plane sectional view, (b) is a side sectional view. In the present invention, as in the sixth embodiment, the flow-through suction flow-through pump 54 is installed vertically, but the float separation tank 83 is rectangular, and the stern side of the tank is fully open. And the river. The pump casing shape 32 is arranged so that the center positions of the pump and the separation tank substantially coincide.

この実施の形態によれば、浮遊物分離タンク83に取り込まれた浮遊物を含む流れは、浮遊物分離板92によって水面近くの流れをせき止めることによって、比重の小さい油などの浮遊物を回収し、比重の大きい水は浮遊物分離板92の下を通過して後方に流出する構造になっている。他の構成は図8の第6実施例の形態と基本的には同様である。 According to this embodiment, the flow containing the suspended matter taken into the suspended matter separation tank 83 collects suspended matter such as oil having a small specific gravity by blocking the flow near the water surface by the suspended matter separation plate 92. The water having a large specific gravity passes under the suspended matter separating plate 92 and flows backward. The other configuration is basically the same as that of the sixth embodiment shown in FIG.

図10は本発明の第8実施例の浮遊物回収船47の形態を示す。(a)は平面断面図、(b)は側断面図である。本発明は主にアオコや浮遊ゴミなどの小浮遊物を対象にしたもので、油類の回収装置に比べるとシンプルな装置となる。ダム湖などでの浮遊物回収の使用にも適している。 FIG. 10 shows the form of a suspended matter collection ship 47 according to the eighth embodiment of the present invention. (A) is a plane sectional view, (b) is a side sectional view. The present invention is mainly intended for small floating substances such as aquatic or floating dust, and is a simpler apparatus than an oil recovery apparatus. It is also suitable for the use of suspended matter collection in dam lakes.

この実施の形態では、図9の第7実施例と同じく、浮遊物回収タンク87の船尾側は全面的に開放されていて外海や河川と通じている。浮遊物回収タンク87に取り込まれた浮遊物を含む流れは、浮遊物回収スクリ−ン94において浮遊物のみ回収される。 In this embodiment, as in the seventh example of FIG. 9, the stern side of the suspended matter collection tank 87 is fully open and communicates with the open sea and rivers. The flow containing the suspended matter taken into the suspended matter collection tank 87 is collected only in the suspended matter collection screen 94 by the suspended matter collection screen 94.

図11は本発明の第9実施例で、縦置きの浮遊物吸引用の貫流ポンプ54を池20に設置した場合の状態を示す。(a)は平面断図、(b)はポンプ縦置き型浮遊物回収装置47の側断面図である。本実施例では固定据付け型なのでポンプの吸込み側に浮遊物回収タンク88を接続した構成になっている。また、図2に示す羽根車中空回転軸の散気孔5から微小気泡を噴出すれば水質の浄化にもなる。 FIG. 11 is a ninth embodiment of the present invention, and shows a state in which a vertically placed flow-through pump 54 for suctioning floating matter is installed in the pond 20. (A) is a plan sectional view, and (b) is a side sectional view of the pump vertical floating substance recovery device 47. In this embodiment, since it is a fixed installation type, a floating substance recovery tank 88 is connected to the suction side of the pump. Moreover, if a micro bubble is ejected from the diffuser hole 5 of an impeller hollow rotating shaft shown in FIG. 2, it will also purify water quality.

この実施の形態によれば、貫流ポンプの流れは乱れが少なく、吐出し流れが遠くまで達する特性により池全体の水面付近の流れの循環を活性化させることができるため、水質を浄化とともにアオコなども発生し難くなる。アオコなどの藻類やゴミなどの浮遊物は、ポンプの吸込側に設置した浮遊物回収スクリ−ン94によって回収できる。池が広い場合はポンプ台数を増やした方が良い。ゴルフ場などに配置されている池にも利用できる。 According to this embodiment, the flow of the once-through pump is less turbulent, and the circulation of the flow near the water surface of the entire pond can be activated by the characteristic that the discharge flow reaches far away, so that the water quality is purified and aquatic etc. Is less likely to occur. Floating matters such as algae such as blue seaweed and garbage can be collected by a floating matter collection screen 94 installed on the suction side of the pump. If the pond is large, it is better to increase the number of pumps. It can also be used for ponds located in golf courses.

図12は本発明の第10実施例で、筏95に浮遊物吸引用の貫流ポンプ54を取り付けて、移動可能にしたものである。この場合はアオコなどの藻類や浮遊ゴミなどを直接貫流ポンプに取り込んだ後、ポンプ吐出口89に接続したフレキシブルホ−ス96により、離れた場所で浮遊物を分離用タンクで回収するかそのまま放流する場合を示す。 FIG. 12 shows a tenth embodiment of the present invention, in which a trough 95 is provided with a once-through pump 54 for sucking a floating substance so as to be movable. In this case, after taking algae such as sea cucumbers and floating dust directly into the once-through pump, the floating hose connected to the pump discharge port 89 is used to collect the suspended matter in a separation tank or release it as it is. Indicates when to do.

この実施の形態によれば、筏に貫流ポンプが設置されていることからポンプの吸込み口が水位によらず一定になるため、ダム湖やポンプ機場の前池など水位が大きく変動する所での使用に適している。また、本ポンプは前述のように物が詰りにくいこと、および羽根車7の羽根ピッチを変えることによって羽根間の間隔を容易に変えることができるので、多様でサイズの異なる浮遊物に対応できることが特徴である。例えば、発電所取水口における小クラゲ対策なども考えられる。 According to this embodiment, since the once-through pump is installed in the reed, the suction port of the pump becomes constant regardless of the water level, so in places where the water level fluctuates greatly, such as a dam lake or the front pond of the pump station. Suitable for use. In addition, the pump is difficult to clog as described above, and the interval between the blades can be easily changed by changing the blade pitch of the impeller 7, so that it can cope with various and different floating matters. It is a feature. For example, measures against small jellyfish at the intake of a power plant can be considered.

本発明の浮遊物回収用ポンプ装置で使用する浮遊物吸引用の貫流ポンプは構造的に物が詰りにくいことから、浮遊物を直接ポンプに取り込み回収できるため、流出油やアオコおよび浮遊ゴミなどの多様な浮遊物回収に適している。特に本装置を船にセットして一体化した走行型の浮遊物回収船は、流出油を直接回収して再利用できるなど優れたメリットがある。 Since the flow-through pump used for the suspended matter recovery pump device of the present invention is structurally resistant to clogging, the suspended matter can be directly taken into the pump and recovered. Suitable for collecting various suspended matters. In particular, a traveling float collection ship in which the present apparatus is integrated on a ship has an excellent merit in that the spilled oil can be directly recovered and reused.

2 羽根車回転軸
3 散気孔を有する羽根車中空回転軸
5 散気孔
6 貫流ポンプの羽根
6b 羽根先端が羽根車の側板外径より外側に突き出した部分
7 羽根車
7b 貫流ポンプ羽根車の側板
8 ケ−シング舌部
9 ポンプ吸込側
10 ポンプ吐出側
11 エアポンプ
11b 液体ポンプ
12 駆動用モ−タ
12b 縦型駆動用モ−タ
13 ホ−ス
14 水面
14b 液面
15 ポンプ吸込み側ケ−シング
20 池
25、26 フランジ
30,31,32,33,
ポンプケ−シング
40,41,42,43,44, 浮遊物回収船
45、46、47 ポンプ縦置き型浮遊物回収船
48 浮遊物回収筏
50,51,52 貫流ポンプ
53,54 縦置きの貫流ポンプ
55、56、57 吐出しダクト
58 吸込み側水門
59 吐出し側水門
60 船
61、61b、61C 開閉式流入ガイド
62 取水口
63 バ‐スクリ‐ン
64 取水流路
65 浮遊物導入ガイドベ‐ン
68 水平方向導入ガイド
69 浮遊物分離ガイド
70,70b 船底開放口
71 浮遊物回収導入パイプ
72 バルブ
73, 73b 浮遊物回収容器
74 浮遊物分離タンク後壁側開放口
77 仕切り板
78 油類回収室
79 水室
80 船尾開放口
81,82,83 矩形型浮遊物分離タンク
84, 85 円筒型浮遊物分離タンク
86 センタ−分離壁
87、88 浮遊物回収タンク
89 ポンプ吐出口
90 電動排出コントロ−ルバルブ
91 排出パイプ
92 浮遊物分離板
94 浮遊物回収スクリ−ン
95 筏
96 フレキシブルホ−ス
97 ポンプ取付架台
B 微細気泡
2 Impeller rotating shaft
3 Impeller hollow rotating shaft with air diffuser holes 5 Air diffuser holes 6 Blades of once-through pump
6b A portion where the tip of the blade protrudes outside the outer diameter of the side plate of the impeller 7 Impeller 7b Side plate 8 of the once-through pump impeller 8 Casing tongue
9 Pump suction side 10 Pump discharge side
11 Air pump 11b Liquid pump 12 Motor for driving
12b Motor for vertical drive 13 hose
14 Water surface 14b Liquid surface 15 Pump suction side casing
20 Pond 25, 26 Flange
30, 31, 32, 33,
Pump casing 40, 41, 42, 43, 44, float collection vessel 45, 46, 47 Pump vertical type float collection vessel 48 Float collection tank 50, 51, 52 Cross flow pump 53, 54 Vertical flow through pump 55, 56, 57 Discharge duct 58 Suction side sluice 59 Discharge side sluice 60 Ship
61, 61b, 61C Open / close type inflow guide 62 Water intake
63 Bar screen
64 Intake channel
65 Floating material introduction guide van 68 Horizontal introduction guide
69 Floating material separation guides 70, 70b
71 Floating material collection introduction pipe 72 Valve
73, 73b Floating substance collection container 74 Floating substance separation tank rear wall side open port 77 Partition plate
78 Oil recovery room
79 Water chamber 80 Stern opening
81, 82, 83 Rectangular floating substance separation tank
84, 85 Cylindrical float separation tank
86 Center separation walls 87, 88 Floating substance recovery tank 89 Pump discharge port
90 Electric discharge control valve 91 Discharge pipe 92 Floating material separator
94 Floating material collection screen 95 筏
96 Flexible hose 97 Pump mount
B fine bubbles

Claims (7)

羽根車形状が円筒状で多翼の貫流ポンプ(クロスフロ−ポンプ)の外側ケ−シング形状を浮遊物回収用にアレンジしたポンプを羽根車上端が水面近くに没する程度に設置し、水面近くに浮遊する油や浮遊ゴミなどをポンプで吸引して取り込んだ後、吐出しダクトに接続した浮遊物回収用分離タンク(底部に外部への開放口あり)へ導き、浮遊物を水との比重差を利用して分離し、浮遊物のみをまとめて回収することを特徴とする浮遊物回収用ポンプ装置 Install a pump with an impeller shape that is cylindrical and the outer casing of a multi-blade once-through pump (cross flow pump) arranged to collect suspended matter so that the upper end of the impeller is submerged near the water surface. After sucking floating oil or floating dust with a pump and taking it in, it is led to a separation tank for collecting floating matter connected to the discharge duct (there is an opening to the outside at the bottom), and the floating matter has a specific gravity difference from water Floating substance collection pump device characterized by separating using float and collecting only floating substances 請求項1に記載の浮遊物回収用ポンプ装置を船や筏と一体化してセットし、前記浮遊物回収用分離タンクの底部の開放口を船の底や船尾の外壁を通して外へ開口するようにして、貫流ポンプにより取り込まれた浮遊物を含む液体のうち、比重の大きい余分の液体はタンク低部の開口部より船外に自然流出させ、比重の小さい油などの浮遊物は浮遊物回収用分離タンク内の上部水面付近に集積するようにし、それを浮遊物回収容器にまとめて回収することを特徴とする走行型の浮遊物回収船(筏) The suspended matter collecting pump device according to claim 1 is set integrally with a ship or a dredger, and the opening at the bottom of the floating matter collecting separation tank is opened to the outside through the bottom of the ship or the outer wall of the stern. Of the liquid containing suspended matter taken in by the once-through pump, excess liquid with a large specific gravity is allowed to flow out of the ship through the opening in the lower part of the tank. A floating floating recovery vessel (回収) that accumulates near the upper water surface in the separation tank and collects it in a floating recovery container. 請求項1に記載の貫流ポンプの各羽根外径寸法を羽根車側板の外径より少し外側に突き出した構造にし、浮遊物を吸込み口へ掻き込みやすくしたことを特徴とする浮遊物回収用ポンプ装置 A pump for collecting floating matter, characterized in that each blade outer diameter of the once-through pump according to claim 1 has a structure projecting slightly outside the outer diameter of the impeller side plate, and the floating matter is easily scraped into the suction port. apparatus 請求項1に記載の貫流ポンプの羽根車回転軸を多数の散気孔を有する中空回転軸にし、羽根車外部より該中空回転軸を通して羽根車内に処理液や洗浄液を供給、あるいは同時にエアも供給し、該散気孔よりそれらを微粒化して流れの中に噴出させることにより、水質の浄化、装置内の洗浄および微細気泡による浮遊物の浮上助長などが出来るようにしたことを特徴とする浮遊物回収用ポンプ装置 The impeller rotary shaft of the once-through pump according to claim 1 is a hollow rotary shaft having a large number of air diffusion holes, and processing liquid and cleaning liquid are supplied into the impeller from the outside of the impeller through the hollow rotary shaft, or air is also supplied simultaneously. Floating matter recovery, characterized by being able to purify water quality, clean the inside of the device, and promote the floating of floating matter by fine bubbles by atomizing them from the air holes and ejecting them into the flow Pump equipment 請求項1乃至2に記載の貫流ポンプの吸込み側流路内の羽根車直前に吸込口に向かって水平面に対し、+3°〜+10°程度傾斜させたガイドベ−ンを水面近くに没した状態で設置することによって、吸込み口へ向う水面近傍の流れを増速し、浮遊物の取り込みを容易にしたことを特徴とする浮遊物回収用ポンプ装置 A guide vane inclined by about + 3 ° to + 10 ° with respect to the horizontal plane toward the suction port immediately before the impeller in the suction side flow path of the once-through pump according to claim 1 or 2 in a state where the guide vane is immersed near the water surface. Floating matter collection pump device characterized by accelerating the flow in the vicinity of the water surface toward the suction port and facilitating uptake of suspended matter by installing 請求項1乃至2に記載のポンプ吐出しケ−シングに接続した該浮遊物分離タンクの形状は大別して矩形タイプと円形タイプに分けられ、比重差を利用して浮遊物が浮上し易いように円形タイプでは、タンク内において旋回流を与えるサイクロンタイプ、矩形タイプでは、タンク後壁側の高さ方向中間の位置に流れを制御して浮遊物を分離するための浮遊物分離ガイドを設置した構造を特徴とする浮遊物回収用ポンプ装置 The shape of the floating substance separation tank connected to the pump discharge casing according to claim 1 is roughly divided into a rectangular type and a circular type so that the floating substance can easily float by using a specific gravity difference. In the circular type, a cyclone type that gives a swirling flow in the tank, and in the rectangular type, a structure that installs a floating material separation guide to separate the floating material by controlling the flow at the middle position in the height direction on the tank rear wall side. Floating matter collection pump device characterized by 請求項1に記載の貫流ポンプの吸込み側あるいは吐出し側に浮遊物回収タンクを接続し、
その回収タンクの外部の海や河川に開放された吸込み側流路や吐出し側流路に藻類やゴミなどの浮遊物を回収するためのスクリ−ンを設置したことを特徴とする浮遊物回収用ポンプ装置
A float collection tank is connected to the suction side or the discharge side of the once-through pump according to claim 1,
Floating matter collection, characterized by installing a screen to collect floating matter such as algae and garbage in the suction-side flow path and discharge-side flow path open to the sea and river outside the collection tank Pump equipment
JP2010143413A 2010-06-24 2010-06-24 Floating matter collecting pump device and collecting ship Pending JP2012007524A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2010143413A JP2012007524A (en) 2010-06-24 2010-06-24 Floating matter collecting pump device and collecting ship

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2010143413A JP2012007524A (en) 2010-06-24 2010-06-24 Floating matter collecting pump device and collecting ship

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2014240702A Division JP5983963B2 (en) 2014-11-28 2014-11-28 Floating matter recovery pump device and recovery vessel

Publications (2)

Publication Number Publication Date
JP2012007524A true JP2012007524A (en) 2012-01-12
JP2012007524A5 JP2012007524A5 (en) 2013-07-25

Family

ID=45538347

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010143413A Pending JP2012007524A (en) 2010-06-24 2010-06-24 Floating matter collecting pump device and collecting ship

Country Status (1)

Country Link
JP (1) JP2012007524A (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012005947A (en) * 2010-06-24 2012-01-12 Masa Tagome Pump aeration device
JP2013022477A (en) * 2011-07-15 2013-02-04 Masa Tagome Microbubble generation flowing pump
CN103072674A (en) * 2013-01-29 2013-05-01 扬州唐人实业有限公司 On-water waste cleaning ship
CN103241863A (en) * 2012-02-01 2013-08-14 李大华 Shipborne water area purifying system and water area purifying method
JP2014015793A (en) * 2012-07-10 2014-01-30 Masa Tagome Floating object recovery pump device and configuration of suction passage on recovery boat
JP2014097449A (en) * 2012-11-14 2014-05-29 Masa Tagome Through-flow pump ultrafine bubble flow supply device
JP2015030455A (en) * 2013-08-05 2015-02-16 ホ イ、ジョン Oil recovery device
CN104554642A (en) * 2014-11-03 2015-04-29 杭州盛吉金属塑料有限公司 Floating object cleaning ship
JP2016060309A (en) * 2014-09-17 2016-04-25 大成建設株式会社 Floating matter collection ship
KR101728209B1 (en) 2014-05-07 2017-04-18 남정호 Oil spill prevention vessel and oil recovery vessel
JP2017109155A (en) * 2015-12-15 2017-06-22 真一 本村 Water bloom recovery device
KR101857434B1 (en) * 2016-11-18 2018-05-14 서울대학교 산학협력단 Oil recovery device
CN112551615A (en) * 2020-12-23 2021-03-26 黄送华 River channel treatment intake pool and integrated sewage treatment system
CN112919583A (en) * 2021-01-14 2021-06-08 江苏济冠通环保科技股份有限公司 Intelligent mobile blue algae collecting and disposing complete device with telescopic surrounding arms
WO2021171502A1 (en) * 2020-02-27 2021-09-02 ヤマハ発動機株式会社 Marine trash collection device
CN114876832A (en) * 2022-04-26 2022-08-09 安徽理工大学 Cyclone air inlet centrifugal fan
CN116854270A (en) * 2023-09-05 2023-10-10 呼和浩特市生态环境监控中心 Mode-adjustable sewage energy-saving processor based on water environment ecological monitoring

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57176677U (en) * 1981-05-02 1982-11-08
JPH04266588A (en) * 1991-02-20 1992-09-22 Masateru Niimura Floating crude oil recovering ship
JPH09177651A (en) * 1995-12-26 1997-07-11 Toshiba Eng Co Ltd Cross flow turbine
JP2001271781A (en) * 2000-03-24 2001-10-05 Awamura Mfg Co Ltd Gate built-in type pump equipment

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57176677U (en) * 1981-05-02 1982-11-08
JPH04266588A (en) * 1991-02-20 1992-09-22 Masateru Niimura Floating crude oil recovering ship
JPH09177651A (en) * 1995-12-26 1997-07-11 Toshiba Eng Co Ltd Cross flow turbine
JP2001271781A (en) * 2000-03-24 2001-10-05 Awamura Mfg Co Ltd Gate built-in type pump equipment

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012005947A (en) * 2010-06-24 2012-01-12 Masa Tagome Pump aeration device
JP2013022477A (en) * 2011-07-15 2013-02-04 Masa Tagome Microbubble generation flowing pump
CN103241863A (en) * 2012-02-01 2013-08-14 李大华 Shipborne water area purifying system and water area purifying method
CN103241863B (en) * 2012-02-01 2014-04-09 李大华 Shipborne water area purifying system and water area purifying method
JP2014015793A (en) * 2012-07-10 2014-01-30 Masa Tagome Floating object recovery pump device and configuration of suction passage on recovery boat
JP2014097449A (en) * 2012-11-14 2014-05-29 Masa Tagome Through-flow pump ultrafine bubble flow supply device
CN103072674A (en) * 2013-01-29 2013-05-01 扬州唐人实业有限公司 On-water waste cleaning ship
CN103072674B (en) * 2013-01-29 2015-12-23 扬州唐人实业有限公司 A kind of water rubbish clean-up vessel
JP2015030455A (en) * 2013-08-05 2015-02-16 ホ イ、ジョン Oil recovery device
KR101728209B1 (en) 2014-05-07 2017-04-18 남정호 Oil spill prevention vessel and oil recovery vessel
JP2016060309A (en) * 2014-09-17 2016-04-25 大成建設株式会社 Floating matter collection ship
CN104554642A (en) * 2014-11-03 2015-04-29 杭州盛吉金属塑料有限公司 Floating object cleaning ship
JP2017109155A (en) * 2015-12-15 2017-06-22 真一 本村 Water bloom recovery device
KR101857434B1 (en) * 2016-11-18 2018-05-14 서울대학교 산학협력단 Oil recovery device
WO2021171502A1 (en) * 2020-02-27 2021-09-02 ヤマハ発動機株式会社 Marine trash collection device
CN112551615A (en) * 2020-12-23 2021-03-26 黄送华 River channel treatment intake pool and integrated sewage treatment system
CN112551615B (en) * 2020-12-23 2023-11-24 黄送华 River course treatment intake pool and integrated sewage treatment system
CN112919583A (en) * 2021-01-14 2021-06-08 江苏济冠通环保科技股份有限公司 Intelligent mobile blue algae collecting and disposing complete device with telescopic surrounding arms
CN114876832A (en) * 2022-04-26 2022-08-09 安徽理工大学 Cyclone air inlet centrifugal fan
CN114876832B (en) * 2022-04-26 2023-09-26 安徽理工大学 Rotational flow air inlet centrifugal fan
CN116854270A (en) * 2023-09-05 2023-10-10 呼和浩特市生态环境监控中心 Mode-adjustable sewage energy-saving processor based on water environment ecological monitoring

Similar Documents

Publication Publication Date Title
JP2012007524A (en) Floating matter collecting pump device and collecting ship
JP2012007524A5 (en)
JP5983963B2 (en) Floating matter recovery pump device and recovery vessel
JP5717104B2 (en) Floating matter recovery pump device and shape of suction passage of recovery vessel
JP2018199949A (en) Floating matter collecting boat
CN101182053A (en) Backflow air-floating device for water-arrangement optimization multi-phase flow pump
JP4538404B2 (en) Water purification apparatus, water pollution organism recovery ship, and water pollution organism treatment method
JP5652758B2 (en) Pump aeration device
JP2012005947A5 (en)
CN103880231B (en) A kind of Zero discharge treatment method of ship oil wastewater
WO2007125996A1 (en) Water quality improving unit and water quality improving device
KR101870404B1 (en) Micro-algae collection and separation device
WO2013042197A1 (en) Waste water treatment equipment in flue gas desulfurization facility
CN108069525A (en) A kind of self-propelled micro-nano oxygen increasing equipment
JP6176689B2 (en) Float collection ship
JP6779475B2 (en) Blue-green algae concentration and recovery device
JP4059346B2 (en) Water purification system and water flow generating stirring mixer
CN207294249U (en) A kind of industrial waste water disposal device
JP2017099347A (en) Swirling flow gas-liquid mixer for aquaculture
KR101315242B1 (en) Wastewater treatment system using venturi tube
KR101163971B1 (en) Aeration device for water treatment
WO2017094373A1 (en) Floating object recovery vessel
CN210825513U (en) High-efficient prereaction pressurization dissolved air flotation machine
KR101662430B1 (en) Conduit type apparatus for treating wastewater
CN207891137U (en) A kind of self-propelled micro-nano oxygen increasing equipment

Legal Events

Date Code Title Description
A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130606

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20140129

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20140225

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20140321

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20140409

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20140930

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20150306