WO2017094373A1 - Floating object recovery vessel - Google Patents

Floating object recovery vessel Download PDF

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Publication number
WO2017094373A1
WO2017094373A1 PCT/JP2016/080774 JP2016080774W WO2017094373A1 WO 2017094373 A1 WO2017094373 A1 WO 2017094373A1 JP 2016080774 W JP2016080774 W JP 2016080774W WO 2017094373 A1 WO2017094373 A1 WO 2017094373A1
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Prior art keywords
chamber
floating
separation tank
suspended matter
flow
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PCT/JP2016/080774
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French (fr)
Japanese (ja)
Inventor
雅 田篭
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雅 田篭
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Priority claimed from JP2016097665A external-priority patent/JP6176689B2/en
Application filed by 雅 田篭 filed Critical 雅 田篭
Publication of WO2017094373A1 publication Critical patent/WO2017094373A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63BSHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B35/00Vessels or similar floating structures specially adapted for specific purposes and not otherwise provided for
    • B63B35/32Vessels or similar floating structures specially adapted for specific purposes and not otherwise provided for for collecting pollution from open water
    • EFIXED CONSTRUCTIONS
    • E02HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02BHYDRAULIC ENGINEERING
    • E02B15/00Cleaning or keeping clear the surface of open water; Apparatus therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/70Suction grids; Strainers; Dust separation; Cleaning

Definitions

  • the present invention relates to a device that takes in floating oil such as oil spills, water scum, and dust floating on the water surface by a floating material collecting device incorporating a suction pump, and separates and collects various drifting floating materials in a floating material separation tank. .
  • Patent Document 2 As a method for recovering a floating substance using a vacuum pump as a suction force, there is Patent Document 2, but there is a problem that the suction flow into the pump is unstable and it is difficult to take in the floating substance smoothly.
  • patent document 3 and patent document 4 although a suspended
  • the flow near the surface of the intake channel that takes in the float floating on the surface of the water is controlled, the flow containing the float is taken in by the suction pump, and the pump is discharged.
  • a technique for efficiently separating and recovering various drifting floating substances in a floating substance separation tank connected to the mouth channel is required.
  • FIG. 5 shows the structure of the suction side introduction passage 64 and a part of the floating substance separation tank 90 in the vicinity of the pump of the conventional floating substance collecting apparatus incorporating the drift pump 50 for taking in floating floating substances.
  • (A) is a top view
  • (b) is sectional drawing.
  • 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 8 for controlling the flow, and is connected to the drive motor 12 by the impeller rotating shaft 2.
  • the floating substance inflow guide plate 22 is installed across the flow path width below the water surface of the suction side introduction path 64 as shown in the sectional view in the vicinity of the pump in FIG.
  • the suspended matter can be reliably taken into the impeller together with a stable suction flow on the water surface side.
  • the flow in the pump section passes through the blades 6 twice from the suction side 9 toward the discharge side 10 and toward the discharge port.
  • the discharge flow of the once-through pump has a wide two-dimensional flow with little turbulence and is sent to the floating substance separation tank 90 connected to the pump discharge side introduction path 65.
  • the floating substance separation tank 90 In the floating substance separation tank 90, the floating substance is collected by utilizing the difference in specific gravity with water. Conventionally, in the floating substance separation tank 90, it is difficult to collect the floating substance because of various kinds and properties of the floating substance. There was also a problem with floating objects.
  • the object of the present invention is to solve the problems in the structure of such a conventional suspended matter recovery tank.
  • the invention described in claim 1 provides a novel suspended matter separation tank for efficiently collecting various suspended matters.
  • This floating substance separation tank is divided into two parts by a partition plate.
  • the upstream side is a first chamber and the downstream side is a second chamber.
  • An opening is provided between the lower end of the partition plate and the bottom of the tank.
  • an opening (outlet) that leads from the bottom side outlet at the rear of the second chamber to the outside of the stern side (sea, river, lake).
  • suspended matter is collected on the water surface side of both chambers due to the difference in specific gravity with the water, and the excess water in the tank is allowed to flow naturally from the stern opening, and the water level between the tank and the outside of the tank The balance is maintained so that the suspended matter can be collected continuously.
  • a first guide or guide vane inclined slightly upward is installed at the inlet of the first chamber of the floating substance separation tank, and the water flow containing the floating substance flowing in is made to flow slightly upward toward the water surface.
  • Floating substances are likely to float on the surface of the water, and by utilizing the specific gravity difference, floating substances (such as oil) having a specific gravity smaller than 1 are collected on the water surface side.
  • a second guide made of a curved plate curved slightly upward is installed toward the front of the first chamber, thereby flowing into the first chamber. The flow in the vicinity of the water surface including suspended matter U-turns downward on the rear wall side of the first chamber, is guided to the second guide, is reversed, and flows toward the outlet. Part of the flow becomes a circulating flow toward the water surface, making it easier to float floating objects.
  • Floats that could not be recovered immediately in the first chamber such as those with specific gravity close to 1 or minute floats, that cannot be immediately lifted to the surface of the water, pass under the second guide and below the communicating partition plate. Flows into the second chamber through the opening.
  • a third guide inclined upward is installed at the bottom of the inlet of the second chamber so that the flow flows slightly upward, and the flow is directed from the bottom side to the water surface side. In this way, it makes it easier for floating objects to float on the water surface. Since the flow flowing into the second chamber through the opening under the partition plate is a slow and stable flow, suspended matter having a specific gravity close to 1 is likely to rise to the surface of the water and cannot be collected in the first chamber. The suspended matter can be recovered.
  • the first chamber can be efficiently recovered in a state where spilled oil having a small specific gravity can be reused.
  • the second chamber has a function of collecting various suspended matters having a specific gravity close to 1 and plastic particles that have recently become a problem in the ocean.
  • the specific gravity of the suspended matter to be collected is close to 1 and difficult to collect on the water surface side, attach a suspended matter collection net to the outlet of the bottom of the second chamber and collect the suspended matter.
  • the mesh size is selected according to the size and properties of the suspended matter to be collected. When collecting minute suspended matter, attach a filter instead of a net. If a net is not required, it may not be installed.
  • the present invention by dividing the structure in the suspended matter separation tank into two chambers, the first chamber and the second chamber, various drifting suspended matters can be efficiently collected, so that the efficiency of the collecting operation can be improved.
  • FIG. 1 shows the overall configuration of the suspended matter recovery ship apparatus of the present invention.
  • (A) is a top view
  • (b) is sectional drawing (Example 1).
  • FIG. 2 is an enlarged cross-sectional view of the suspended matter separation tank portion of FIG.
  • FIG. 3 shows an overall configuration of a floating matter recovery ship apparatus different from that shown in FIG. (A) is a top view
  • (b) is sectional drawing (Example 2).
  • FIG. 4 shows an example of the structure of a conventional floating object recovery ship apparatus.
  • (A) is a top view
  • (b) is sectional drawing.
  • FIG. 5 shows a part of a floating substance separation tank and an introduction path for taking in floating substances before and after the once-through pump of the floating substance recovery ship.
  • (A) is a top view
  • (b) is sectional drawing.
  • FIG. 1 is a first embodiment relating to the invention described in claim 1 and claim 2 and shows the entire structure of a floating substance recovery ship 40 incorporating a new floating substance separation tank 90.
  • FIG. 4A is a plan view
  • FIG. FIG. 2 is an enlarged view showing the internal structure of the suspended matter separation tank 90.
  • the structure of the suspended matter recovery ship 40 is a cylindrical multi-blade once-through pump 50, and the suction side includes a wide suction-side introduction passage 64 that roughly matches the side wall width of the once-through pump.
  • the floating inflow guide plate 22 is installed below the water surface of the inlet / outlet guide 60 and the introduction path 64 just before the pump at the water intake, and the floating side of the drift taken in with the water is separated and recovered on the pump discharge side.
  • This is a configuration in which a suspended matter separation tank 90 is connected to a discharge side introduction path 65 having substantially the same width as the suction side introduction path.
  • the floating substance separation tank 90 is divided into two parts by a partition plate 93.
  • the upstream side is a first chamber 95 and the downstream side is a second chamber 96.
  • a predetermined opening is provided between the lower end of the partition plate 93 and the tank bottom surface.
  • the first chamber 95 and the second chamber 96 are in communication with each other, and the flow in the suspended matter separation tank passes from the first chamber 95 through the opening h, It is configured to flow into the chamber 96.
  • a first guide 67 inclined slightly upward at the inlet portion, and a second guide curved slightly upward toward the front portion of the first chamber near the lower end of the rear partition plate 93. 69 is installed, and a third guide 87 inclined upward is installed at the bottom of the second chamber inlet.
  • floating substances drifting in the vicinity of the water surface are taken into the suction once-through pump 50 together with water from the intake port of the bow through the suction side introduction path 64.
  • the discharge flow of the once-through pump has a wide and less turbulent flow characteristic, and water and suspended matter are fed into the suspended matter separation tank 90 without becoming turbid.
  • the flow that includes the floating material that has been sent flows in as a slightly upward flow due to the first guide 67 installed at the inlet of the first chamber.
  • suspended matter (oil, etc.) having a specific gravity smaller than 1 is collected on the water surface side.
  • the flow in the vicinity of the water surface including suspended matter flowing into the first chamber makes a U-turn downward on the rear wall side of the first chamber, is guided to the second guide 69, and goes to the outlet. Since a part of the flow forms a circulating flow toward the water surface side, the suspended matter easily floats, and the suspended matter is collected on the water surface side.
  • the flow including the remaining suspended matter that could not rise to the water surface side in the first chamber passes under the second guide 69, goes to the second chamber 96 through the communicating opening h, and is collected in the first chamber 95.
  • the suspended matter that could not be removed is collected in the second chamber 96.
  • a third guide 87 is installed at the bottom of the second chamber inlet so that the inflow flows upward from the bottom surface toward the water surface. As a result, the suspended matter easily floats on the water surface. Floating substances such as oil collected on the water surface side are collected in floating substance collection containers 73 and 74 through the floating substance collection introduction pipe 71.
  • the position in the height direction of the suspended matter separation guide 69 should be adjusted according to the type and properties of the suspended matter.
  • the excess water after separating from the floating substance in the floating substance separation tank naturally flows out from the outflow port 80 at the bottom of the second chamber to the outside of the ship (sea, river, lake) through the stern opening 82 to separate the floating substance.
  • the water level balance between the tank and the outside of the tank is maintained. Thereby, floating substance collection operation can be performed continuously.
  • the suspended matter collection net or filter 85 is attached to the second chamber outlet 80 and collected. In this embodiment, since the outlet is on the stern side, it contributes slightly to the propulsion of the ship.
  • the impeller rotating shaft 2 shown in FIG. 5 is a diffused hole hollow rotating shaft having a number of small holes, and the air pump 11 shown in FIG. Gas is supplied into the diffuser hole hollow rotary shaft through the supply hose 13 connected to the hermetic bracket, and is blown into the rotating impeller as finer bubbles than the diffuser hole.
  • the fine bubbles are supplied with the discharge flow of the pump from the inside to the outside of the impeller 7 in a state where the fine bubbles are uniformly mixed.
  • the floating substance can be promoted in the first chamber and can be easily recovered. It also contributes to water purification by fine bubbles.
  • a treatment liquid for making the harmful suspended matter (liquid) harmless by the liquid pump 11b shown in FIG. It is made harmless by supplying it into the hollow rotating shaft of the air diffuser hole of the impeller, spraying the processing liquid atomized from the air diffuser hole into the impeller while rotating, and evenly mixing it with the harmful liquid taken in. be able to.
  • FIG. 3 shows the form of the suspended matter recovery ship 41 in the second embodiment.
  • FIG. 1A is a plan view
  • FIG. Unlike the first embodiment of FIG. 1, the present floating substance recovery ship has a structure in which an outlet 81 that leads to a ship bottom opening 83 is provided on the bottom side of the second chamber of the floating substance separation tank.
  • Other configurations and floating substance collection functions are the same as those of the first embodiment shown in FIG.
  • FIG. 4 shows an example of the device configuration of a conventional suspended matter collection ship 45.
  • the floating substance separation tank is a single chamber. Drifting floating substance taken in by the pump flows into the floating substance separation tank 92 connected to the pump discharge port. In the floating substance separation tank, the floating substance gathers on the water surface side due to the difference in specific gravity, and excess water is collected in the tank. The water naturally flows out from the bottom rear wall side outlet 78 to the outside through the stern opening 82, and the water level balance in the suspended matter separation tank 92 is maintained.
  • the inflow direction at the tank inlet is horizontal, but the effect of floating the floating substance in the horizontal flow is Inferior.
  • the first guide 67 inclined slightly upward is installed and the inflow direction is slightly upward, the floating substance is likely to float.
  • the suspended matter recovery ship of the present invention takes in a flow containing suspended matter by a once-through pump and then sends it to a suspended matter separation tank connected to a discharge side flow path.
  • the floating separation tank is divided into two chambers, a first chamber and a second chamber, by a partition plate with the bottom of the tank in communication. It can be efficiently collected in the chamber. In addition, it has excellent functions such as direct recovery and reuse of spilled oil.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Health & Medical Sciences (AREA)
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  • Combustion & Propulsion (AREA)
  • Ocean & Marine Engineering (AREA)
  • Removal Of Floating Material (AREA)

Abstract

[Problem] To provide a device that, after taking in drifting floating objects with a cross-flow pump, efficiently recovers various floating objects using the difference in specific gravity between the floating objects and water in a floating object separation tank that is connected to the pump discharge-side flow path. [Solution] The internal structure of a floating object separation tank 90 of the present invention is such that the floating object separation tank 90 is divided by a partition plate 93 into two chambers, namely, a first chamber 95 and a second chamber 96, the bottom surface sides of which communicate to each other, an upwardly inclined first guide 67 is placed at the inflow port of the first chamber, an upwardly curved second guide 69 is placed near the lower end of the rear partition plate 93, and an upwardly inclined third guide is placed at the inflow port of the second chamber 96, the internal structure controlling the flow in the vicinity of a water surface that flows into the first chamber and enabling floating objects to be accumulated on the water surface side. The second chamber 96 recovers a floating object that the first chamber has failed to recover, and superfluous water flows out naturally through a stern release port 82. The water level balance between the inside of the floating object separation tank and the outside of the vessel is thus maintained to enable the continuous work of floating object recovery.

Description

浮遊物回収船Float collection ship クロスリファレンスCross reference
 本出願は、2015年11月30日に日本国において出願された特願2015-232621および2016年5月16日に日本国において出願された特願2016-097665に基づき優先権を主張し、上記両出願に記載された内容は、本明細書に援用する。また、本願において引用した特許、特許出願及び文献に記載された内容は、本明細書に援用する。 This application claims priority based on Japanese Patent Application No. 2015-232621 filed in Japan on November 30, 2015 and Japanese Patent Application No. 2016-097665 filed in Japan on May 16, 2016, and The contents described in both applications are incorporated herein by reference. Moreover, the content described in the patent quoted in this application, a patent application, and literature is used for this specification.
 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、吸引ポンプを組込んだ浮遊物回収装置により取り込み、浮遊物分離タンクで多様な漂流浮遊物を分離回収する装置に関する。 TECHNICAL FIELD The present invention relates to a device that takes in floating oil such as oil spills, water scum, and dust floating on the water surface by a floating material collecting device incorporating a suction pump, and separates and collects various drifting floating materials in a floating material separation tank. .
 従来は、海洋において、流出油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、バキュームポンプを吸引力として利用した浮遊物を回収する方法として、特許文献2があるが、ポンプへの吸込み流れが不安定で浮遊物をスムーズに取り込み難いなどの問題がある。また、特許文献3および特許文献4では、吸引ポンプにより浮遊物を安定して取り込めるが、浮遊物分離タンクにおいて、多様な浮遊物の種類や性状により、回収し難い浮遊物も存在することが問題となる。 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 / decomposed with an oil treatment agent. 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. Moreover, as a method for recovering a floating substance using a vacuum pump as a suction force, there is Patent Document 2, but there is a problem that the suction flow into the pump is unstable and it is difficult to take in the floating substance smoothly. Moreover, in patent document 3 and patent document 4, although a suspended | floating matter can be taken in stably with a suction pump, there exists a problem that the suspended | floating matter which is hard to collect | recover exists in a suspended | floating matter isolation | separation tank by various kinds and characteristics of a suspended | floating matter. It becomes.
特開昭59-156890号公報JP 59-156890 A 特開平4-266588号公報JP-A-4-266588 特開2012-7524号公報JP 2012-7524 A 特開2014-015793号公報JP 2014-015793 A
 浮遊物回収船による浮遊物回収技術の向上のためには、水面に漂流する浮遊物を取り込む取水路の水面近傍の流れを制御して、浮遊物を含む流れを吸引ポンプにより取り込み、ポンプ吐出し口流路に接続した浮遊物分離タンクにおいて、多様な漂流浮遊物を、効率よく分離して回収する技術を必要とする。 In order to improve the float collection technology by the float collection ship, the flow near the surface of the intake channel that takes in the float floating on the surface of the water is controlled, the flow containing the float is taken in by the suction pump, and the pump is discharged. A technique for efficiently separating and recovering various drifting floating substances in a floating substance separation tank connected to the mouth channel is required.
 図5に、漂流浮遊物を取り込む貫流ポンプ50を組込んだ従来の浮遊物回収装置のポンプ付近の吸込側導入路64の構造と浮遊物分離タンク90の一部を示す。(a)は平面図、(b)は断面図である。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ーシング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によって駆動用モータ12に接続されている。漂流浮遊物を取り込む導入路では、図5(b)のポンプ近傍の断面図に示すように吸込側導入路64の水面下に浮遊物流入ガイドプレート22を流路幅に渡って設置することにより、浮遊物を水面側の安定した吸込み流れと共に確実に羽根車へ取り込むことができるようにしている。ポンプ部における流れは図5(b)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を通過して吐出口へ向かう。貫流ポンプの吐出し流れは、乱れの少ない幅広の二次元的な流れを有し、ポンプ吐出側導入路65に接続した浮遊物分離タンク90に送られる。 FIG. 5 shows the structure of the suction side introduction passage 64 and a part of the floating substance separation tank 90 in the vicinity of the pump of the conventional floating substance collecting apparatus incorporating the drift pump 50 for taking in floating floating substances. (A) is a top view, (b) is sectional drawing. 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 8 for controlling the flow, and is connected to the drive motor 12 by the impeller rotating shaft 2. Has been. In the introduction path for taking in drifting floating substances, the floating substance inflow guide plate 22 is installed across the flow path width below the water surface of the suction side introduction path 64 as shown in the sectional view in the vicinity of the pump in FIG. The suspended matter can be reliably taken into the impeller together with a stable suction flow on the water surface side. As shown in the pump cross-sectional view of FIG. 5B, the flow in the pump section passes through the blades 6 twice from the suction side 9 toward the discharge side 10 and toward the discharge port. The discharge flow of the once-through pump has a wide two-dimensional flow with little turbulence and is sent to the floating substance separation tank 90 connected to the pump discharge side introduction path 65.
 浮遊物分離タンク90内では、漂流浮遊物を水との比重差を利用して浮遊物を回収するが、従来は浮遊物分離タンク90において、多様な浮遊物の種類や性状により、回収し難い浮遊物も存在する問題があった。 In the floating substance separation tank 90, the floating substance is collected by utilizing the difference in specific gravity with water. Conventionally, in the floating substance separation tank 90, it is difficult to collect the floating substance because of various kinds and properties of the floating substance. There was also a problem with floating objects.
 本発明は、このような従来の浮遊物回収タンクの構造上の問題点を解決することを目的としたものである。 The object of the present invention is to solve the problems in the structure of such a conventional suspended matter recovery tank.
 請求項1に記載の発明は、多様な浮遊物を効率よく回収するための新規の浮遊物分離タンクを提供するものである。本浮遊物分離タンク内は、仕切板により二つに分けて上流側を第1チャンバー、下流側を第2チャンバーとし、該仕切板の下端とタンク底面との間に開口部を設けて連通構造にし、第2チャンバー後部の底面側流出口から船尾の底面側外部(海、川、湖沼)に通じる開放口(流出口)を設けた構成である。タンク内では、水との比重差により、浮遊物を両チャンバーの水面側で回収し、タンク内の余分の水は、船尾開放口より、自然流出させて、タンク内と船外との水位のバランスが保たれるようにし、連続して浮遊物の回収作業ができるようにしている。 The invention described in claim 1 provides a novel suspended matter separation tank for efficiently collecting various suspended matters. This floating substance separation tank is divided into two parts by a partition plate. The upstream side is a first chamber and the downstream side is a second chamber. An opening is provided between the lower end of the partition plate and the bottom of the tank. And an opening (outlet) that leads from the bottom side outlet at the rear of the second chamber to the outside of the stern side (sea, river, lake). In the tank, suspended matter is collected on the water surface side of both chambers due to the difference in specific gravity with the water, and the excess water in the tank is allowed to flow naturally from the stern opening, and the water level between the tank and the outside of the tank The balance is maintained so that the suspended matter can be collected continuously.
 浮遊物分離タンクの第1チャンバー流入口には、少し上向きに傾斜させた第1ガイド、又はガイドベ-ンを設置し、流入した浮遊物を含む水流を水面側に向かって少し上向きの流れにして、浮遊物が水面に浮上しやすくし、比重差を利用して、比重が1より小さい浮遊物(油など)を水面側に集めるようにする。第1チャンバー後部の前記仕切板の下端近くには、第1チャンバーの前部に向けて、少し上向きに湾曲させた平面曲板からなる第2ガイドを設置することにより、第1チャンバーへ流入する浮遊物を含む水面近傍の流れが、第1チャンバー後壁側で下方へUタ-ンして、第2ガイドに誘導され、反転して出口へ向かう流れとなる。その流れの一部が水面側へ向かう循環流れとなり、浮遊物を浮上しやすくする。 A first guide or guide vane inclined slightly upward is installed at the inlet of the first chamber of the floating substance separation tank, and the water flow containing the floating substance flowing in is made to flow slightly upward toward the water surface. Floating substances are likely to float on the surface of the water, and by utilizing the specific gravity difference, floating substances (such as oil) having a specific gravity smaller than 1 are collected on the water surface side. Near the lower end of the partition plate at the rear of the first chamber, a second guide made of a curved plate curved slightly upward is installed toward the front of the first chamber, thereby flowing into the first chamber. The flow in the vicinity of the water surface including suspended matter U-turns downward on the rear wall side of the first chamber, is guided to the second guide, is reversed, and flows toward the outlet. Part of the flow becomes a circulating flow toward the water surface, making it easier to float floating objects.
 比重が1に近いものや微小な浮遊物など、すぐには水面側に浮上できないなど、第1チャンバーで回収できなかった浮遊物は、該第2ガイドの下を通り、連通した前記仕切板下の開口部を通って第2チャンバーへ流入する。 Floats that could not be recovered immediately in the first chamber, such as those with specific gravity close to 1 or minute floats, that cannot be immediately lifted to the surface of the water, pass under the second guide and below the communicating partition plate. Flows into the second chamber through the opening.
 請求項2に記載の発明は、前記第2チャンバーの流入口底部に、上向きに傾斜した第3ガイドを設置し、流れが少し上向きに流入するようにして、流れが底面側から水面側に向かうようにして、浮遊物が水面に浮上しやすくする。該仕切板下の開口部を通って第2チャンバーへ流入する流れは、速度も遅く安定した流れなので、比重が1に近い浮遊物も水面側に浮上しやすいので、第1チャンバーで回収できなかった浮遊物も回収可能となる。 According to a second aspect of the present invention, a third guide inclined upward is installed at the bottom of the inlet of the second chamber so that the flow flows slightly upward, and the flow is directed from the bottom side to the water surface side. In this way, it makes it easier for floating objects to float on the water surface. Since the flow flowing into the second chamber through the opening under the partition plate is a slow and stable flow, suspended matter having a specific gravity close to 1 is likely to rise to the surface of the water and cannot be collected in the first chamber. The suspended matter can be recovered.
 浮遊物分離タンク内を上記のように、二室の構造にすることにより、第1チャンバーでは、比重の小さい流出油などを再利用できる状態で効率よく回収可能となる。第2チャンバーでは、比重が1に近い多様な浮遊物や最近海洋で問題となっているプラスチック粒子も回収できる機能を有する。 By using a two-chamber structure in the floating substance separation tank as described above, the first chamber can be efficiently recovered in a state where spilled oil having a small specific gravity can be reused. The second chamber has a function of collecting various suspended matters having a specific gravity close to 1 and plastic particles that have recently become a problem in the ocean.
 回収する浮遊物の比重が1に近く、水面側で回収し難い場合は、第2チャンバーの底部の流出口に浮遊物回収網を取り付けて、浮遊物を回収する。網目の大きさは、回収する浮遊物の大きさや性状によって選定する。微小な浮遊物を回収する場合は網の替わりにフィルタを取り付ける。網は不要であれば、設置しなくてもよい。 If the specific gravity of the suspended matter to be collected is close to 1 and difficult to collect on the water surface side, attach a suspended matter collection net to the outlet of the bottom of the second chamber and collect the suspended matter. The mesh size is selected according to the size and properties of the suspended matter to be collected. When collecting minute suspended matter, attach a filter instead of a net. If a net is not required, it may not be installed.
 本発明は、浮遊物分離タンク内の構造を第1チャンバーと第2チャンバーの二室に分けることにより、多様な漂流浮遊物を効率よく回収できることから、回収作業の能率を高めることができる。 In the present invention, by dividing the structure in the suspended matter separation tank into two chambers, the first chamber and the second chamber, various drifting suspended matters can be efficiently collected, so that the efficiency of the collecting operation can be improved.
図1は、本発明の浮遊物回収船の装置の全体構成を示す。(a)は平面図、(b)は断面図である(実施例1)。FIG. 1 shows the overall configuration of the suspended matter recovery ship apparatus of the present invention. (A) is a top view, (b) is sectional drawing (Example 1). 図2は、図1の浮遊物分離タンク部の拡大断面図である。FIG. 2 is an enlarged cross-sectional view of the suspended matter separation tank portion of FIG. 図3は、図1とは異なる別形態の浮遊物回収船の装置の全体構成を示す。(a)は平面図、(b)は断面図である(実施例2)。FIG. 3 shows an overall configuration of a floating matter recovery ship apparatus different from that shown in FIG. (A) is a top view, (b) is sectional drawing (Example 2). 図4は、従来の浮遊物回収船の装置の構造の一例を示す。(a)は平面図、(b)は断面図である。FIG. 4 shows an example of the structure of a conventional floating object recovery ship apparatus. (A) is a top view, (b) is sectional drawing. 図5は、浮遊物回収船の貫流ポンプ前後における浮遊物を取り込む導入路と浮遊物分離タンクの一部を示す。(a)は平面図、(b)は断面図である。FIG. 5 shows a part of a floating substance separation tank and an introduction path for taking in floating substances before and after the once-through pump of the floating substance recovery ship. (A) is a top view, (b) is sectional drawing.
2  羽根車回転軸
6  貫流ポンプの羽根
7  羽根車
8  ケーシング舌部
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  駆動用モータ
13  供給ホース
14  水面
22  浮遊物導入ガイドプレ-ト
30  ポンプケーシング
40,41  浮遊物回収船
45  浮遊物回収船(従来型)
50  貫流ポンプ
58  船
59  水門
60  開閉式流入ガイド
63  バースクリーン
64  吸込側導入路
65  吐出側導入路
67  第1ガイド
68  水平方向導入ガイド
69  第2ガイド
70  浮遊物分離ガイド
71  浮遊物回収導入パイプ
72  バルブ
73,74  浮遊物回収容器
78  タンク後壁側流出口
80  第2チャンバー後壁側流出口
81  第2チャンバー底面側流出口
82  船尾開放口(流出口)
83  船底面開放口(流出口)
85,86  浮遊物回収網又はフィルタ
87  第3ガイド
90,91  浮遊物分離タンク
92   浮遊物分離タンク(従来型)
93  仕切板
95  第1チャンバー
96  第2チャンバー
98  スクリュウ
 F  浮遊物
 h  仕切板下端と浮遊物分離タンク底面との間の開口高さ
2 impeller rotary shaft 6 cross-flow pump blade 7 impeller 8 casing tongue 9 pump suction side 10 pump discharge side 11 air pump 11b liquid pump 12 drive motor 13 supply hose 14 water surface 22 floating material introduction guide plate 30 pump casing 40, 41 Float recovery ship 45 Float recovery ship (conventional type)
50 Cross-flow pump 58 Ship 59 Sluice 60 Opening and closing type inflow guide 63 Bar screen 64 Suction side introduction path 65 Discharge side introduction path 67 First guide 68 Horizontal introduction guide 69 Second guide 70 Floating substance separation guide 71 Floating substance collection introduction pipe 72 Valves 73 and 74 Floating substance recovery container 78 Tank rear wall side outlet 80 Second chamber rear wall side outlet 81 Second chamber bottom side outlet 82 Stern opening (outlet)
83 Ship bottom opening (outlet)
85, 86 Floating substance collection network or filter 87 Third guide 90, 91 Floating substance separation tank 92 Floating substance separation tank (conventional type)
93 Partition plate 95 First chamber 96 Second chamber 98 Screw F Floating substance h Opening height between lower end of partition plate and bottom of floating substance separation tank
 以下に、本発明の実施の形態を、図1及至図3を参照して説明する。 Hereinafter, embodiments of the present invention will be described with reference to FIGS.
 図1は、請求項1および請求項2に記載の発明に関する第1実施例で、新規の浮遊物分離タンク90を組込んだ浮遊物回収船40の全体構成を示す。同図(a)は平面図、図(b)は断面図である。図2は、浮遊物分離タンク90の内部構造を示す拡大図である。本浮遊物回収船40の構造は、円筒状で多翼の貫流ポンプ50を中心にして、吸込側には、貫流ポンプの側壁幅に概略合わせた幅広の吸込側導入路64を備え、船首の取水口部に開閉式流入ガイド60、ポンプ直前の導入路64の水面下に浮遊物流入ガイドプレート22を設置し、ポンプ吐出側には、水と共に取り込んだ漂流浮遊物を分離回収するために、吸込側導入路と略同幅の吐出側導入路65に浮遊物分離タンク90を接続した構成である。 FIG. 1 is a first embodiment relating to the invention described in claim 1 and claim 2 and shows the entire structure of a floating substance recovery ship 40 incorporating a new floating substance separation tank 90. FIG. 4A is a plan view, and FIG. FIG. 2 is an enlarged view showing the internal structure of the suspended matter separation tank 90. The structure of the suspended matter recovery ship 40 is a cylindrical multi-blade once-through pump 50, and the suction side includes a wide suction-side introduction passage 64 that roughly matches the side wall width of the once-through pump. The floating inflow guide plate 22 is installed below the water surface of the inlet / outlet guide 60 and the introduction path 64 just before the pump at the water intake, and the floating side of the drift taken in with the water is separated and recovered on the pump discharge side. This is a configuration in which a suspended matter separation tank 90 is connected to a discharge side introduction path 65 having substantially the same width as the suction side introduction path.
 浮遊物分離タンク90内は、仕切板93により二つに分けて、上流側を第1チャンバー95、下流側を第2チャンバー96とし、仕切板93の下端とタンク底面との間は所定の開口高さhを有する開口部を有し、第1チャンバー95と第2チャンバー96の間を連通状態にし、浮遊物分離タンク内の流れが第1チャンバー95から該開口部hを通って、第2チャンバー96へと流れる構成になっている。第1チャンバーでは、流入口部に少し上向きに傾斜させた第1ガイド67、後部の仕切板93の下端付近には、第1チャンバーの前部に向けて、少し上向きに湾曲させた第2ガイド69を設置し、第2チャンバー入口底部には、上向きに傾斜した第3ガイド87を設置した構成である。 The floating substance separation tank 90 is divided into two parts by a partition plate 93. The upstream side is a first chamber 95 and the downstream side is a second chamber 96. A predetermined opening is provided between the lower end of the partition plate 93 and the tank bottom surface. The first chamber 95 and the second chamber 96 are in communication with each other, and the flow in the suspended matter separation tank passes from the first chamber 95 through the opening h, It is configured to flow into the chamber 96. In the first chamber, a first guide 67 inclined slightly upward at the inlet portion, and a second guide curved slightly upward toward the front portion of the first chamber near the lower end of the rear partition plate 93. 69 is installed, and a third guide 87 inclined upward is installed at the bottom of the second chamber inlet.
 この実施の形態によれば、水面付近に漂う浮遊物が船首部の取水口から吸込側導入路64を通って水と共に吸引用の貫流ポンプ50に取り込まれる。貫流ポンプの吐出し流れは幅広で乱れの少ない流れ特性を有し、水と浮遊物は混濁せずに浮遊物分離タンク90に送り込まれる。送り込まれた浮遊物を含む流れは、第1チャンバー流入口に設置された第1ガイド67により、少し上向きの流れとなって流入するため、浮遊物が水面に浮上しやすくなり、比重差を利用して、比重が1より小さい浮遊物(油など)を水面側に集める。 According to this embodiment, floating substances drifting in the vicinity of the water surface are taken into the suction once-through pump 50 together with water from the intake port of the bow through the suction side introduction path 64. The discharge flow of the once-through pump has a wide and less turbulent flow characteristic, and water and suspended matter are fed into the suspended matter separation tank 90 without becoming turbid. The flow that includes the floating material that has been sent flows in as a slightly upward flow due to the first guide 67 installed at the inlet of the first chamber. As a result, suspended matter (oil, etc.) having a specific gravity smaller than 1 is collected on the water surface side.
 図2の拡大図に示すように、第1チャンバーへ流入する浮遊物を含む水面近傍の流れは、第1チャンバー後壁側で下方へUターンして、第2ガイド69に誘導され、出口へと向かう流れとなり、その流れの一部が水面側に向かう循環流れを形成するため、浮遊物は浮上しやすくなり、水面側に浮遊物が集められる。第1チャンバーで水面側に浮上できなかった残りの浮遊物を含む流れは、第2ガイド69の下を通り、連通した開口部hを通って第2チャンバー96へ向かい、第1チャンバー95で取りきれなかった浮遊物を第2チャンバー96で回収することになる。 As shown in the enlarged view of FIG. 2, the flow in the vicinity of the water surface including suspended matter flowing into the first chamber makes a U-turn downward on the rear wall side of the first chamber, is guided to the second guide 69, and goes to the outlet. Since a part of the flow forms a circulating flow toward the water surface side, the suspended matter easily floats, and the suspended matter is collected on the water surface side. The flow including the remaining suspended matter that could not rise to the water surface side in the first chamber passes under the second guide 69, goes to the second chamber 96 through the communicating opening h, and is collected in the first chamber 95. The suspended matter that could not be removed is collected in the second chamber 96.
 仕切板93の底部の開口部hを通って第2チャンバーへ流入する流れは、速度も遅く安定した流れなので、比重が1に近い浮遊物も水面側に浮上しやすいので回収しやすい。また、第2チャンバー入口底部には、第3ガイド87が設置され、流入流れが底面側から水面側に向けて上向きになるようにしている。これにより、浮遊物は、水面に浮上しやすくなる。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及び74に回収される。浮遊物分離ガイド69の高さ方向位置は、浮遊物の種類や性状により、調整できるようにした方がよい。 Since the flow flowing into the second chamber through the opening h at the bottom of the partition plate 93 is a slow and stable flow, suspended matter having a specific gravity close to 1 easily floats on the water surface side and is easy to collect. A third guide 87 is installed at the bottom of the second chamber inlet so that the inflow flows upward from the bottom surface toward the water surface. As a result, the suspended matter easily floats on the water surface. Floating substances such as oil collected on the water surface side are collected in floating substance collection containers 73 and 74 through the floating substance collection introduction pipe 71. The position in the height direction of the suspended matter separation guide 69 should be adjusted according to the type and properties of the suspended matter.
 浮遊物分離タンク内の浮遊物から分離した後の余分の水は第2チャンバー底部の流出口80から船尾の開放口82を通じて船外(海、川、湖沼)へ自然流出して、浮遊物分離タンク内と船外との水位のバランスが保たれるようになっている。これにより、浮遊物回収作業を連続して行うことができる。両チャンバーの水面側で回収できなかった浮遊物も回収する場合は、第2チャンバー流出口80に浮遊物回収網やフィルタ85を取り付けて回収する。この実施例では、流出口を船尾側にしているので、船の推進に若干寄与する。 The excess water after separating from the floating substance in the floating substance separation tank naturally flows out from the outflow port 80 at the bottom of the second chamber to the outside of the ship (sea, river, lake) through the stern opening 82 to separate the floating substance. The water level balance between the tank and the outside of the tank is maintained. Thereby, floating substance collection operation can be performed continuously. When the suspended matter that could not be collected on the water surface side of both chambers is also collected, the suspended matter collection net or filter 85 is attached to the second chamber outlet 80 and collected. In this embodiment, since the outlet is on the stern side, it contributes slightly to the propulsion of the ship.
 水質浄化や浮遊物の浮上を助長する手段としては、図5に示す羽根車回転軸2を多数の小孔を有する散気孔中空回転軸にして、図1に示すエアポンプ11により、軸受け後端の密閉ブラケットに接続した供給ホース13を通して散気孔中空回転軸内に気体を供給し、回転する羽根車内に散気孔より細かな気泡として噴出させる。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、第1チャンバー内において浮遊物の浮上を助長し、回収を容易にすることができる。また、微細気泡による水質の浄化にも寄与する。 As a means for promoting water purification and floating floating, the impeller rotating shaft 2 shown in FIG. 5 is a diffused hole hollow rotating shaft having a number of small holes, and the air pump 11 shown in FIG. Gas is supplied into the diffuser hole hollow rotary shaft through the supply hose 13 connected to the hermetic bracket, and is blown into the rotating impeller as finer bubbles than the diffuser hole. The fine bubbles are supplied with the discharge flow of the pump from the inside to the outside of the impeller 7 in a state where the fine bubbles are uniformly mixed. By the flow accompanied with the bubbles, the floating substance can be promoted in the first chamber and can be easily recovered. It also contributes to water purification by fine bubbles.
 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、図1に示す液体ポンプ11bにより有害浮遊物(液)を無害にするための処理液を、供給ホース13を通して貫流ポンプの羽根車の散気孔中空回転軸内に供給し、回転を伴いながら該散気孔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 that cannot be recovered from the suspended matter that has flowed out, a treatment liquid for making the harmful suspended matter (liquid) harmless by the liquid pump 11b shown in FIG. It is made harmless by supplying it into the hollow rotating shaft of the air diffuser hole of the impeller, spraying the processing liquid atomized from the air diffuser hole into the impeller while rotating, and evenly mixing it with the harmful liquid taken in. be able to.
 図3は、第2実施例で、浮遊物回収船41の形態を示す。図(a)は平面図、図(b)は断面図である。本浮遊物回収船の構造は、図1の第1実施例と異なり、浮遊物分離タンクの第2チャンバーの底面側に、船底開放口83に通じる流出口81を設けた構造である。他の構成や浮遊物回収機能は、図1の第1実施例の形態と同様である。 FIG. 3 shows the form of the suspended matter recovery ship 41 in the second embodiment. FIG. 1A is a plan view, and FIG. Unlike the first embodiment of FIG. 1, the present floating substance recovery ship has a structure in which an outlet 81 that leads to a ship bottom opening 83 is provided on the bottom side of the second chamber of the floating substance separation tank. Other configurations and floating substance collection functions are the same as those of the first embodiment shown in FIG.
 図4には、従来の浮遊物回収船45の装置構成の一例を示す。この例では、浮遊物分離タンク内は、単室である。ポンプにより取り込まれた漂流浮遊物がポンプ吐出し口に接続した浮遊物分離タンク92内へ流入し、浮遊物分離タンク内では、比重差により浮遊物は水面側に集まり、余分の水は、タンク底部の後壁側流出口78から船尾開放口82を通じて外部へ自然流出し、浮遊物分離タンク92内の水位バランスが保たれる。 FIG. 4 shows an example of the device configuration of a conventional suspended matter collection ship 45. In this example, the floating substance separation tank is a single chamber. Drifting floating substance taken in by the pump flows into the floating substance separation tank 92 connected to the pump discharge port. In the floating substance separation tank, the floating substance gathers on the water surface side due to the difference in specific gravity, and excess water is collected in the tank. The water naturally flows out from the bottom rear wall side outlet 78 to the outside through the stern opening 82, and the water level balance in the suspended matter separation tank 92 is maintained.
 この形状を持つ構成では、原油のように比重が1より明らかに小さいものは浮遊物分離タンク92の水面側に浮上して集められるが、比重が1付近の浮遊物やプラスチック粒子などの微小な浮遊物は、浮上速度が小さいために、分離タンク内の循環流れに乗って、分離タンクの後部流出口78から船外に放出されることになり、多様な浮遊物に対しては、効果的に回収できない場合がある。原油流出においても、流出して時間がたつと、海水と混じって原油の性状が変わり、比重が1近くになることもあり、浮遊物の回収効率が低下する問題が生じることになる。 In the configuration having this shape, those having specific gravity smaller than 1 such as crude oil are floated and collected on the water surface side of the floating substance separation tank 92, but the specific gravity is very small such as suspended matter and plastic particles. Since the floating speed is low, the floating speed rides on the circulating flow in the separation tank and is discharged from the rear outlet 78 of the separation tank to the outside of the ship, which is effective for various floating substances. May not be recovered. Even in the case of a crude oil spill, as time passes, the properties of the crude oil change as it mixes with seawater, and the specific gravity may be close to 1, resulting in a problem that the recovery efficiency of suspended solids is reduced.
 また、浮遊物分離タンク92の流入口部に設置された水平方向導入ガイド68においては、タンク入口部での流入方向が水平方向になるが、水平方向の流れでは、浮遊物を浮上させる効果は劣る。図1の本発明の実施例1に示すように、少し上向きに傾斜させた第1ガイド67を設置して、流入方向を少し上向きにすれば、浮遊物は浮上しやすくなる。 In addition, in the horizontal introduction guide 68 installed at the inlet of the floating substance separation tank 92, the inflow direction at the tank inlet is horizontal, but the effect of floating the floating substance in the horizontal flow is Inferior. As shown in the first embodiment of the present invention in FIG. 1, if the first guide 67 inclined slightly upward is installed and the inflow direction is slightly upward, the floating substance is likely to float.
 本発明の浮遊物回収船は、貫流ポンプにより浮遊物を含む流れを取り込んだ後、吐出側流路に接続した浮遊物分離タンクに送り込まれる。浮遊物分離タンク内は、タンク底面部を連通にした仕切板により、第1チャンバーと第2チャンバーの二室に分けることにより流出油や浮遊ゴミなどの多様な浮遊物の性状に応じて、両チャンバーに効率よく回収出来る。また、流出油を直接回収して再利用できるなど、優れた機能を有する。 The suspended matter recovery ship of the present invention takes in a flow containing suspended matter by a once-through pump and then sends it to a suspended matter separation tank connected to a discharge side flow path. The floating separation tank is divided into two chambers, a first chamber and a second chamber, by a partition plate with the bottom of the tank in communication. It can be efficiently collected in the chamber. In addition, it has excellent functions such as direct recovery and reuse of spilled oil.

Claims (2)

  1.  取水口から浮遊物分離タンクまでの流路幅が略一定である導入路の途中に、円筒状で多翼の羽根車を有する貫流ポンプを流路幅方向にわたって設置し、該貫流ポンプの吐出し側導入路に前記浮遊物分離タンクを接続した構成の浮遊物回収装置を組込んだ浮遊物回収船において、
     前記浮遊物分離タンクの内部構造を、仕切板により、上流側を第1チャンバー、下流側を第2チャンバーの二室に分け、前記仕切板の下端とタンク底面との間に開口部を有する連通構造にし、前記第2チャンバー底部の後壁側流出口から船尾の底面側外部に通じる流出開放口を設け、該第1チャンバーの流入口には、上向きに傾斜させた第1ガイドを設置し、該第1チャンバー後部の前記仕切板の下端近くには、第1チャンバー前部に向けて上向きに湾曲させた第2ガイドを設置したことを特徴とする浮遊物回収船。
    A cross-flow pump having a cylindrical and multi-blade impeller is installed in the flow path width direction in the middle of the introduction path where the flow path width from the intake port to the suspended matter separation tank is substantially constant, and the discharge of the cross-flow pump In the suspended matter recovery ship incorporating the suspended matter recovery device configured to connect the suspended matter separation tank to the side introduction path,
    The internal structure of the floating substance separation tank is divided into two chambers, a first chamber on the upstream side and a second chamber on the downstream side by a partition plate, and a communication having an opening between the lower end of the partition plate and the tank bottom surface. And having an outflow opening that leads from the rear wall side outlet at the bottom of the second chamber to the outside at the bottom of the stern, and a first guide inclined upward is installed at the inlet of the first chamber, A float collection ship, wherein a second guide curved upward toward the front of the first chamber is installed near the lower end of the partition plate at the rear of the first chamber.
  2.  前記浮遊物分離タンクの前記第2チャンバーの流入口底面部に、上向きに傾斜した第3ガイドを設け、前記第2チャンバーへの流入流れを上向きにして、底面側から水面側に向かう流れを得ることを特徴とする請求項1に記載の浮遊物回収船。 A third guide inclined upward is provided at the bottom of the inlet of the second chamber of the floating substance separation tank, and the flow from the bottom to the water surface is obtained with the inflow to the second chamber facing upward. The suspended matter collection ship according to claim 1.
PCT/JP2016/080774 2015-11-30 2016-10-18 Floating object recovery vessel WO2017094373A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP2015-232621 2015-11-30
JP2015232621 2015-11-30
JP2016097665A JP6176689B2 (en) 2015-11-30 2016-05-16 Float collection ship
JP2016-097665 2016-05-16

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WO2019073107A1 (en) * 2017-10-12 2019-04-18 Suomen Merituote Oy Arrangement for collecting plastic waste from water bodies

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Publication number Priority date Publication date Assignee Title
JP2004098044A (en) * 2002-09-11 2004-04-02 Kondo Kogyo Kk Oil separator
JP2010247144A (en) * 2009-03-27 2010-11-04 Tokyo Electric Power Co Inc:The Oil separation tank
JP2014015793A (en) * 2012-07-10 2014-01-30 Masa Tagome Floating object recovery pump device and configuration of suction passage on recovery boat

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004098044A (en) * 2002-09-11 2004-04-02 Kondo Kogyo Kk Oil separator
JP2010247144A (en) * 2009-03-27 2010-11-04 Tokyo Electric Power Co Inc:The Oil separation tank
JP2014015793A (en) * 2012-07-10 2014-01-30 Masa Tagome Floating object recovery pump device and configuration of suction passage on recovery boat

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019073107A1 (en) * 2017-10-12 2019-04-18 Suomen Merituote Oy Arrangement for collecting plastic waste from water bodies

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