JP4263032B2 - Vacuum suction oil recovery system - Google Patents

Vacuum suction oil recovery system Download PDF

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Publication number
JP4263032B2
JP4263032B2 JP2003182388A JP2003182388A JP4263032B2 JP 4263032 B2 JP4263032 B2 JP 4263032B2 JP 2003182388 A JP2003182388 A JP 2003182388A JP 2003182388 A JP2003182388 A JP 2003182388A JP 4263032 B2 JP4263032 B2 JP 4263032B2
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oil
suction
water
pipe
recovery system
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JP2005013880A (en
Inventor
正佳 佐野
宗生 吉江
勇 藤田
英夫 三浦
雅光 辰口
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INDEPENDENT ADMINISTRATIVE INSTITUTION PORT AND AIRPORT RESEARCH INSTITUTE
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INDEPENDENT ADMINISTRATIVE INSTITUTION PORT AND AIRPORT RESEARCH INSTITUTE
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/204Keeping clear the surface of open water from oil spills

Description

【0001】
【発明の属する技術分野】
本発明は、事故を起こした船舶等から流出した油を真空吸引して回収する真空吸引油回収システムに関し、更に詳しくは、上記船舶の近傍で作業を行う油回収船に搭載され、海上を浮遊している油を効率的に真空吸引して回収する真空吸引油回収システムに関する。
【0002】
【従来の技術】
1997年1月2日未明、大しけの日本海(島根県隠岐島沖)で暖房用のC重油約19,000klを積んで上海からペトロパブロフスクへ航行中のロシア船籍の老朽タンカー「ナホトカ号」の破断事故が発生し、船体は浸水し、乗員はボートで避難するが、船長は行方不明となり、後日、福井県の海岸に漂着した事故があった。
【0003】
上記船体は、水深約2,500mの海底に沈没し、その船体から分離した船首部分は、強い北西の季節風にあおられて漂流し、対馬海岸を横断して越前加賀海岸国立公園内の福井県三国町安島沖に座礁した。そして、積み荷の重油は、約6,240klが流出し、海底に沈んだ船体の油タンクに残る重油約12,500klの一部は、その後も流出し続けている。
【0004】
海上に流出した重油は、福井県をはじめ、日本海沿岸の多数の府県に及ぶ海岸に漂着して環境に大打撃を与えたが、この流出重油の一部は、多数の関係者やボランティアの働きによって回収されたことは記憶に新しい。
【0005】
上記のような海難事故は、冬の極寒の風の強い時に発生することが多いが、この時期の流出重油の回収作業は過酷なものである。つまり、流出重油は、冷たい海面に浮上しながら長時間にわたって波浪に揉まれた結果、次第に硬度を増して30万センチポイズ以上になり、それは柔らかいアスフアルトのように変質している。
【0006】
従って、回収船の甲板から下ろした吸入ホースで真空吸引しようとしても吸入ホースが閉止され、簡単に吸引することができない。そこで、上記のように塊り状に変化している重油に高圧水を噴射して小塊に分離させ、これを船上から伸ばしたヒシャクで掬い上げて回収する方法も採用されたが、この作業には、柄の長さが3.5m以上のヒシャクが必要であり、この柄の先に設けた汲取り部に重油を掬った重量は、手には10kg以上に感じられる。
【0007】
従って、ヒシャクの汲取り部を海面から船上まで持ち上げて船上のドラム缶に投入する作業は、体力を必要とし、体力のある若い人でも僅か15分程度の作業が限度であったとのことである。この杓による汲取り作業は、海岸の岩場の足場の悪い場所で行なわれたが、一人の人の1日の作業で、せいぜいドラム缶1本分が限度の非能率さであったという。
【0008】
このようなタンカーの油流出事故がしばしば発生することから、流出油の回収には、種々な装置や方法が提案されている(例えば、特許文献1参照。)。
【0009】
【特許文献1】
特開2000−8354号公報(第2〜3頁、図1)
【0010】
【発明が解決しようとする課題】
ところが、上記のように、ポンプで吸引・圧送する方法では、重油などのように高粘度に変質する油は、簡単に真空吸引できないという本質的な問題がある。また、水中ポンプで油を吸い込む方法もあるが、水中ポンプ等の装置はかなりの重量があるので、波に追従し難く、水面の油よりも水ばかりを吸い易い。
【0011】
更に、回収船の船上より海面に下ろした吸引ホースで海面に浮上している粘性の比較的小さい油膜を吸引する時は、波浪の動きにホース先を追従させて上下させる必要があるが、重量のあるホースを波の動きに追従させて操作することは大変な作業である。
【0012】
従って、実際の作業では、ホースの先端が海水中に潜って多量の海水を吸引したり、あるいは先端が浮きあがって真空が途切れ、海面に浮き沈みしている油を効率的に吸引が困難である。
【0013】
一方、ネットコンベアで流出油を回収する方法も提案されているが、無端形のネットコンベアがある程度の回動スピードを持っていれば、高粘度油の場合には、ネットの網目から油が垂れ落ちないが、低粘度油の場合には、ネットの網目から油が垂れ落ちるため、回収できないという問題があった。
【0014】
本発明は、竜巻の原理に着目し、高速ジェット気流の周囲に発生する負圧を利用して水面上に浮遊している油を高濃度で吸引、回収する真空吸引油回収システムを提供するものである。
【0015】
【課題を解決するための手段】
係る目的を達成するため、本発明の真空吸引油回収システムは、次のように構成されている。
【0016】
(1)先端部に波の上下運動に追随する吸引口を設けた油吸引管によって水面に浮遊している油を真空吸引、即ち真空吸引装置によって空気吸引管、サイクロン式気液分離器、油吸引管及び吸引口を介して空気を吸引して回収する真空吸引油回収システムであって、前記吸引口の胴部に空気吸引管を設け、該空気吸引管の開口部を蓋体によって開閉することを特徴とする真空吸引油回収システムである。
【0017】
(2) 前記油吸引管に注水管を設ける一方、前記油吸引管とサイクロン式気液分離器及び油水粗分離装置を介して間接的に接続している分離油排出管に注水管を設け、各注水管より各管内に潤滑用の水を注入することを特徴とする(1)記載の真空吸引油回収システムである。
【0020】
前記油水粗分離装置は、その本体内に静置・重力分離方式の分離素子を備えており、該分離素子は、多段に配した複数の水平板と、その前後に配した整流板により構成され、且つ、前記水平板をポリプロピレンやポリエチレン板等の合成樹脂板、或いは合成樹脂コートで表面処理した金属板により構成してなる(2)記載の真空吸引油回収システムである。
【0022】
) 前記吸引口の進行方向前方に、斜め下方に向けて湾曲した波返し部を有する波高制限板を設け、該波高制限板により、短周期の三角波を消去するようにしたことを特徴とする()記載の真空吸引油回収システムである。
【0023】
【発明の実施の形態】
以下、本発明の実施の形態を図面を用いて説明する。
【0024】
図1に示すように、油回収船50は、本発明の真空吸引油回収システムに適用する真空吸引油回収装置48を搭載している。この真空吸引油回収装置48は、図3に示すように、主として、油吸引管2、サイクロン式気液分離器3、空気吸引管4、真空吸引装置5、油水粗分離装置6、分離油排出管(排油管)7、排水ポンプ8、排油ポンプ10、貯油タンク11、注水管12及び13から構成されている。
【0025】
高速気流による吸引では、移送管、つまり、油吸引管2が水平の場合、管長が長くなると、管路の中に多数のプラグ(油の塊による管路閉塞)が発生して圧力損失が急激に上昇し、やがて油の移送が不可能になるため、本発明では、上記油吸引管2を、図2及び図3に示すように、ほぼ垂直に立ち上げてプラグの発生を防止するようにしている。
【0026】
また、油吸引管2の先端部に取り付けられているラッパ状の吸引口1は、図3に示すように、油吸収管2の先端屈曲部に設けた可撓部17と、吸引口1の下部に取り付けた中空円筒形の浮体(フロート)18によって波の上下運動に追随する所謂「波乗り機構」となっている。
【0027】
実験によると、油吸引口1が、常に油の中に埋没しているより、間欠的に油の中に浸かる方が油回収力が強くなることが分かっている。これは、油を吸引し、次に、空気を吸引して吹き飛ばすことにより、平均輸送量を高めることができるためである。図4は、周期的に空気を吸引させる機構である。空気吸引管25の開口部に摺動蓋26があり、この摺動蓋26を油圧シリンダー27にて周期的に開閉するようになっている。
【0028】
図2に示すように、油吸引口1は、フロート18で支持され、スイベル32が回転中心になって波に追従するようになっている。油回収しないときには、油圧シリンダ33により油吸引口1を海面よりはね上げておくことができる。
【0029】
上記の油吸引管2の上端は、図3に示すように、サイクロン式気液分離器3に接続されている。このサイクロン式気液分離器3は、図5(a)に示すように、円筒形をしており、油吸引管2は、円筒形のサイクロン本体14の接線方向に接続されている。
【0030】
従って、真空吸引装置5により、空気吸引管4、サイクロン式気液分離器3、油吸引管2及び吸引口1を介して空気dを吸引すると、油吸引管2及び吸引口1内が負圧になり、図6に示すように、高速ジェット気流jによって水面の浮遊油aが吸引される。
【0031】
この油水bは、図5(b)に示すように、サイクロン式気液分離器3の中で遠心力により円筒形のサイクロン本体14の内周面に押し付けられ、その下部に降下する。一方、空気dは、密度が小さいため、サイクロン本体14の中心部にある空気吸引管4を通って大気中に排気される。垂直な油吸引管2内では、実験的にプラグが発生しないので、海面に浮遊している高粘度の浮遊油aは、サイクロン式気液分離器3に回収される。
【0032】
このサイクロン式気液分離器3に回収された油水bは、図3に示すように、排水ポンプ8および排油ポンプ10により油水粗分離装置6を介して吸引される。そして、油水粗分離装置6を通過する間に油水bは、油a’と水wとに粗分離される。
【0033】
分離水wは、その一部が排水管9の先端に取り付けた放水ノズル15から集油や、浮遊油aを小さな塊に破砕するために海面へ向けて放水される(図2及び図3参照)。残りの分離水wは、図3に示すように、注水管12から油吸引管2内に供給され、管内輸送する吸引油の潤滑剤としてリサイクル利用される。
【0034】
油水粗分離装置6で粗分離された分離油a’は、分離油排出管7から貯油タンク11に移送される。高粘度油では、排油管7を通過する摩擦抵抗が高くなるので、図3及び図9に示すように、注水管13から排油管7内に5〜10%の水wを添加する。このように、注水管13から排油管7内に水wを添加すると、この水wが潤滑剤として作用して摩擦抵抗が非常に小さくなり、分離油a’をスムーズに移送することができる。
【0035】
注水管13から排油管7内に注入される注水量が5%に満たないと、注水による潤滑効果が得られないし、注水量が10%を超えると、その分、貯油タンク11内の貯油量が少なくなり、逆効果になる。
【0036】
上記油水粗分離装置6は、重力分離方式であり、本体16内に静置・重力分離方式の分離素子(分離ユニット)35を備えている。この分離素子35は、図7のように、多段に配した複数の水平板(分離促進板)24と、その前後に配した整流板22により構成されている。この水平板24は、移動中に浮上する油滴を付着させて捕集できるポリプロピレンやポリエチレン板等の合成樹脂板、或いは合成樹脂コート等で表面処理した金属板が用いられている。上記整流板22は、多数の孔23を有している(図8参照)。
【0037】
図7に示すように、サイクロン式気液分離器3の下端出口21から油水粗分離装置6の本体16内に導入された油水混合液bは、同本体16内を通過する間に油粒子a’が浮上し、水wは、分離素子35の水平板24の間を通過して下方の排水口20から排水される。その際、油の微粒子a”は、分離素子35の水平板24の下面に付着して水wから分離される。上部に浮上した油a’は、排油口19から排油管7を経て排油ポンプ10により吸引排出される。
【0038】
また、上記本体16の上層位置には、油水境界面センサー37が設けられ、油水混合体bより分離された油の状態が、常時、検査され、その信号は、適当な場所、例えば、油水粗分離装置本体16に設けたメーター(図示せず)に表示され、作業者がこれを時々監視しながら真空吸引装置5を調整できるようになっている。また、油水境界面センサー37の信号によって排水ポンプ8と排油ポンプ10の回転数を電気的に制御することによって油水粗分離装置6の自動運転が可能になる。尚、38、39及び40は、バルブである。
【0039】
図1に示すように、上記油回収船50は、双胴船であり、二つの胴体51の間にオイルフェンス28を張り、海面の漂流油aを集めて、その中で油aを回収する方式を採用している。この方が単胴船より効率が良い。双胴船形の油回収船50の波を沈静化するには、図10に示すような波高制限板44が効果的である。
【0040】
尚、46は、ごみ除去格子である。
【0041】
この波高制限板44は、鋼、或いは、アルミニュームなどの剛性の高い部分29にゴムなどの柔軟な部分30から構成される。この波高制限板44により、短周期の三角波Cを消去しておくと、長周期の波に対しては、フロート18の波乗り性能により油吸引口1を海面の動きに容易に追従させることができる。尚、31は、波返し部、Aは、油回収船50の前進方向を示している。
【0042】
また、油吸引口1の形状は、特定の形状に限定されるものでなく、図11( a)に示すような垂直管1a、同図(b)に示すようなL形管1b、同図(c)に示すように、絞り部41にスリット42を持つU字管1c、同図(d)のスリット42付き管1dなど各種のものが考えられる。
【0043】
また、フロート18の形状は、波乗り性が良く、しかも、油の流れを妨げない形状が良く、図12乃至図15のように各種のものが考えられる。例えば、図12のフロート18は、円板形に形成され、かつ、車の両輪のように吸引口1の両側に設けられている。また、図13のフロート18は、偏平体形に形成され、かつ、車の前輪のように縦軸52を中心にして回動可能に設けられている。また、図14のフロート18は、偏平体形に形成され、かつ、三角枠(平面視)53の三方に設けられている。更に、図15のフロート18は、円筒形に形成され、かつ、コ字形枠(平面視)54の四隅に設けられている。尚、図12(b)乃至図15(b)中、iは波形形状を示している。
【0044】
【発明の効果】
上記のように、本発明は、水面に浮遊している油を真空吸引して回収する真空吸引油回収システムであって、真空吸引装置によって空気吸引管、サイクロン式気液分離器、油吸引管及び吸引口を介して空気を吸引し、前記吸引口より吸引された空気の高速ジェット気流に乗せて水面の浮遊油を吸引するようにしたことを特徴とする真空吸引油回収システムである。
【0045】
従って、例えば、冬季の冷たい海水に揉まれて硬度が増した油塊や低粘度油でも、吸引口より吸引された空気の高速ジェット気流に乗せて効率的に吸引することができる。
【0046】
特に、前記油吸引管を略鉛直に立ち上げて吸引された油のプラグ流の発生を防止するとともに、前記油吸引管内に水を積極的に注入して管内を移動中の油の潤滑剤として使用するようにしたので、油吸引管が目詰まりすることなく、効率的に回収することができる。
【0047】
また、本発明は、前記吸引口に浮体(フロート)を設け、前記吸引口を波の上下運動に追随させるようにしたので、波浪により大きく上下する海面に浮上する流出油でも波浪の状態に関係なく、効率的に回収することができる。
【0048】
また、本発明は、前記油吸引管の上端にサイクロン式気液分離器を接続し、該サイクロン式気液分離器によって油吸引管で吸引した空気と油水とを分離し、分離後の空気を大気中に放出する一方、分離後の油水を油水分離装置に送出するようにしたので、最終的に油水の分離のみを行うことができる。
【0049】
また、本発明の前記油水粗分離装置は、その本体内に静置・重力分離方式の分離素子を備えており、該分離素子は、多段に配した複数の水平板と、その前後に配した整流板により構成されているので、油と水の比重差を利用して油と水とを簡単に分離することができる。
【0050】
また、本発明は、前記吸引口の進行方向前方に、斜め下方に向けて湾曲した波返し部を有する波高制限板を設け、該波高制限板により、短周期の三角波を消去するようにしたので、吸引口が波の荒い三角波に翻弄されることがなくなり、水面の浮遊油を効率的に吸引できる。
【図面の簡単な説明】
【図1】(a)本発明の真空吸引油回収システムに適用した油回収船の平面図、(b)同油回収船の側面図である。
【図2】同油回収船の腰部拡大斜視図である。
【図3】本発明の真空吸引油回収システムの構造図である。
【図4】油吸引管に設けた空気取入手段の説明図である。
【図5】(a)サイクロン式気液分離器の平面図、(b)同サイクロン式気液分離器の側面図である。
【図6】油吸引管の作用説明図である。
【図7】油水粗分離装置の側面図である。
【図8】清流板の正面図である。
【図9】排油管の説明図である。
【図10】波高制限板の側面図である。
【図11】(a)〜(d)各吸引口の側面図である。
【図12】(a)フロートの他の実施形態を示す平面図、(b)同フロートの作動図である。
【図13】(a)フロートの他の実施形態を示す平面図、(b)同フロートの作動図である。
【図14】(a)フロートの他の実施形態を示す平面図、(b)同フロートの作動図である。
【図15】(a)フロートの他の実施形態を示す平面図、(b)同フロートの作動図である。
【符号の説明】
a 水面に浮遊している油
d 空気
j 高速ジェット気流
1 吸引口
2 油吸引管
3 サイクロン式気液分離器
4 空気吸引管
5 真空吸引装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a vacuum suction oil recovery system that recovers by vacuum suction of oil that has flowed out of a ship or the like that has caused an accident. More specifically, the present invention is mounted on an oil recovery ship that operates near the ship and floats on the sea. The present invention relates to a vacuum suction oil recovery system that efficiently recovers and collects the oil being vacuumed.
[0002]
[Prior art]
Early on January 2, 1997, a Russian-registered old tanker, Nakhodka, sailed from Shanghai to Petropavlovsk with approximately 19,000 kl of C heavy oil for heating in the Great Sea of Japan (off Oki Island, Shimane Prefecture) No. ”breakage occurred, the hull was flooded, and the crew evacuated by boat, but the captain was missing, and at a later date there was an accident that arose on the coast of Fukui Prefecture.
[0003]
The above-mentioned hull sinks to the bottom of the sea about 2,500m in depth, and the bow part separated from the hull drifts under the strong northwest seasonal wind and crosses the Tsushima coast in Fukui Prefecture in the Echizen Kaga Coast National Park. Grounded off Mt. Then, about 6,240 kl of heavy oil in the cargo flows out, and a part of about 12,500 kl of heavy oil remaining in the oil tank of the hull sinking to the seabed continues to flow out.
[0004]
The heavy oil that spilled to the sea drifted to the coasts of Fukui Prefecture and many other prefectures on the coast of the Japan Sea, and had a huge impact on the environment. What was recovered by work is new to memory.
[0005]
The maritime accidents described above often occur when the wind is extremely cold in winter, but the recovery operation of the spilled heavy oil at this time is severe. In other words, the spilled heavy oil floated on the cold sea surface and was engulfed by waves over a long period of time, and as a result, gradually increased in hardness to 300,000 centipoise or more, and it was altered like soft asphalt.
[0006]
Therefore, even if the suction hose lowered from the deck of the recovery ship is used for vacuum suction, the suction hose is closed and cannot be easily suctioned. Therefore, a method was adopted in which high-pressure water was injected into the heavy oil that changed into a lump shape as described above, and separated into small lumps, which were scooped up and collected with a cypress stretched from the ship. For this, a handle with a handle length of 3.5 m or more is required, and the weight of heavy oil applied to the pumping part provided at the tip of the handle feels 10 kg or more.
[0007]
Therefore, the work of lifting the ladle pumping part from the sea surface to the ship and putting it into the drum can on the ship requires physical strength, and even a young person with physical strength can only work for about 15 minutes. The dredging work was carried out in a poor place on the coastal rocky ground, but it was said that the work of one person per day was at most inefficient as much as one drum can.
[0008]
Since such tanker oil spill accidents often occur, various apparatuses and methods have been proposed for collecting spilled oil (see, for example, Patent Document 1).
[0009]
[Patent Document 1]
JP 2000-8354 A (pages 2 to 3, FIG. 1)
[0010]
[Problems to be solved by the invention]
However, as described above, in the method of sucking and pumping with a pump, there is an essential problem that oil having a high viscosity, such as heavy oil, cannot be easily vacuumed. There is also a method of sucking oil with a submersible pump, but a device such as a submersible pump has a considerable weight, so it is difficult to follow a wave, and it is easier to suck only water than oil on the water surface.
[0011]
Furthermore, when sucking an oil film with relatively low viscosity floating on the surface of the sea with a suction hose that is lowered from the surface of the recovery vessel, it is necessary to make the hose tip follow the wave motion and move it up and down. It is a hard work to operate a hose with a wave following the movement of a wave.
[0012]
Therefore, in actual work, the tip of the hose is submerged in seawater to suck in a large amount of seawater, or the tip floats up and the vacuum is interrupted, making it difficult to efficiently suck up the oil floating on the sea surface. .
[0013]
On the other hand, a method of collecting spilled oil with a net conveyor has also been proposed. However, if the endless net conveyor has a certain rotation speed, in the case of high-viscosity oil, the oil drips from the net of the net. However, in the case of low-viscosity oil, the oil drips from the net of the net, and there is a problem that it cannot be recovered.
[0014]
The present invention provides a vacuum suction oil recovery system that focuses on the principle of tornado and sucks and recovers oil floating on the water surface at a high concentration by using negative pressure generated around a high-speed jet stream. It is.
[0015]
[Means for Solving the Problems]
In order to achieve the object, the vacuum suction oil recovery system of the present invention is configured as follows.
[0016]
(1) Vacuum suction of oil floating on the water surface by an oil suction pipe provided with a suction port that follows the vertical movement of the wave at the tip, that is , air suction pipe, cyclone gas-liquid separator, oil by a vacuum suction device A vacuum suction oil recovery system that sucks and recovers air through a suction tube and a suction port , wherein an air suction tube is provided in a body portion of the suction port, and an opening of the air suction tube is opened and closed by a lid. This is a vacuum suction oil recovery system.
[0017]
(2) While providing a water injection pipe in the oil suction pipe , a water injection pipe is provided in a separated oil discharge pipe that is indirectly connected to the oil suction pipe via a cyclone-type gas-liquid separator and an oil / water rough separator, The vacuum suction oil recovery system according to (1) , wherein water for lubrication is injected into each pipe from each water injection pipe .
[0020]
( 3 ) The oil / water coarse separation device includes a stationary / gravity separation type separation element in its main body, and the separation element includes a plurality of horizontal plates arranged in multiple stages, and a rectifying plate arranged before and after the horizontal plates. The vacuum suction oil recovery system according to (2), wherein the horizontal plate is made of a synthetic resin plate such as polypropylene or polyethylene plate or a metal plate surface-treated with a synthetic resin coat .
[0022]
( 4 ) A wave height limiting plate having a wave return portion curved obliquely downward is provided in front of the suction port in the traveling direction, and the short wave triangular wave is erased by the wave height limiting plate. The vacuum suction oil recovery system according to ( 1 ).
[0023]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0024]
As shown in FIG. 1, the oil recovery ship 50 is equipped with a vacuum suction oil recovery device 48 that is applied to the vacuum suction oil recovery system of the present invention. As shown in FIG. 3, the vacuum suction oil recovery device 48 mainly includes an oil suction tube 2, a cyclone gas-liquid separator 3, an air suction tube 4, a vacuum suction device 5, an oil / water rough separation device 6, and a separated oil discharge. It comprises a pipe (oil drain pipe) 7, a drain pump 8, a drain oil pump 10, an oil storage tank 11, and water injection pipes 12 and 13.
[0025]
In the suction by high-speed air flow, when the transfer pipe, that is, the oil suction pipe 2 is horizontal, when the pipe length becomes long, a large number of plugs (pipe blockage due to a lump of oil) are generated in the pipe and the pressure loss suddenly increases. In the present invention, the oil suction pipe 2 is raised almost vertically as shown in FIGS. 2 and 3 to prevent the occurrence of plugs. ing.
[0026]
Further, the trumpet-shaped suction port 1 attached to the distal end portion of the oil suction tube 2 includes a flexible portion 17 provided at the distal end bent portion of the oil absorption tube 2 and the suction port 1 as shown in FIG. This is a so-called “wave riding mechanism” that follows the vertical movement of a wave by a hollow cylindrical floating body (float) 18 attached to the lower part.
[0027]
According to experiments, it has been found that the oil recovery force is stronger when the oil suction port 1 is immersed in the oil intermittently than when the oil suction port 1 is always buried in the oil. This is because the average transport amount can be increased by sucking oil and then sucking and blowing air. FIG. 4 shows a mechanism for periodically sucking air. A sliding lid 26 is provided at the opening of the air suction pipe 25, and the sliding lid 26 is periodically opened and closed by a hydraulic cylinder 27.
[0028]
As shown in FIG. 2, the oil suction port 1 is supported by the float 18, and the swivel 32 follows the wave with the swivel 32 serving as a rotation center. When oil is not recovered, the oil suction port 1 can be lifted from the sea surface by the hydraulic cylinder 33.
[0029]
The upper end of the oil suction pipe 2 is connected to a cyclone type gas-liquid separator 3 as shown in FIG. As shown in FIG. 5A, the cyclone gas-liquid separator 3 has a cylindrical shape, and the oil suction pipe 2 is connected in a tangential direction of the cylindrical cyclone main body 14.
[0030]
Therefore, when the air d is sucked by the vacuum suction device 5 through the air suction tube 4, the cyclone gas-liquid separator 3, the oil suction tube 2 and the suction port 1, the oil suction tube 2 and the suction port 1 have a negative pressure. Then, as shown in FIG. 6, the floating oil a on the water surface is sucked by the high-speed jet air flow j.
[0031]
As shown in FIG. 5 (b), the oil water b is pressed against the inner peripheral surface of the cylindrical cyclone main body 14 by the centrifugal force in the cyclone gas-liquid separator 3 and falls to the lower part thereof. On the other hand, since the density of the air d is small, it passes through the air suction pipe 4 at the center of the cyclone body 14 and is exhausted into the atmosphere. Since no plug is experimentally generated in the vertical oil suction pipe 2, the high-viscosity floating oil a floating on the sea surface is collected by the cyclone gas-liquid separator 3.
[0032]
As shown in FIG. 3, the oil water b collected in the cyclone type gas-liquid separator 3 is sucked through the oil / water coarse separator 6 by the drain pump 8 and the drain pump 10. The oil water b is roughly separated into oil a ′ and water w while passing through the oil / water rough separation device 6.
[0033]
The separated water w is discharged toward the sea surface in order to crush oil collection or floating oil a into a small lump from a discharge nozzle 15 that is partly attached to the tip of the drain pipe 9 (see FIGS. 2 and 3). ). As shown in FIG. 3, the remaining separated water w is supplied from the water injection pipe 12 into the oil suction pipe 2 and recycled as a lubricant for suction oil transported in the pipe.
[0034]
The separated oil a ′ roughly separated by the oil / water coarse separation device 6 is transferred from the separated oil discharge pipe 7 to the oil storage tank 11. In the case of high-viscosity oil, the frictional resistance passing through the oil drain pipe 7 becomes high, so 5 to 10% of water w is added from the water injection pipe 13 into the oil drain pipe 7 as shown in FIGS. In this way, when water w is added from the water injection pipe 13 into the oil discharge pipe 7, the water w acts as a lubricant, the frictional resistance becomes very small, and the separated oil a ′ can be smoothly transferred.
[0035]
If the amount of water injected from the water injection pipe 13 into the oil discharge pipe 7 is less than 5%, the lubrication effect by water injection cannot be obtained. If the amount of water injection exceeds 10%, the oil storage amount in the oil storage tank 11 is increased accordingly. Will be less effective.
[0036]
The oil / water coarse separation device 6 is of a gravity separation type and includes a stationary / gravity separation type separation element (separation unit) 35 in the main body 16. As shown in FIG. 7, the separation element 35 includes a plurality of horizontal plates (separation promoting plates) 24 arranged in multiple stages, and a rectifying plate 22 arranged before and after the horizontal plates. The horizontal plate 24 is made of a synthetic resin plate such as polypropylene or polyethylene plate that can collect oil droplets that float while moving, or a metal plate that has been surface-treated with a synthetic resin coat. The rectifying plate 22 has a large number of holes 23 (see FIG. 8).
[0037]
As shown in FIG. 7, the oil / water mixture b introduced into the main body 16 of the oil / water coarse separation device 6 from the lower end outlet 21 of the cyclone type gas-liquid separator 3 passes through the main body 16 with oil particles a 'Floats up and the water w passes between the horizontal plates 24 of the separation element 35 and is drained from the lower drainage port 20. At that time, the oil fine particles a ″ adhere to the lower surface of the horizontal plate 24 of the separation element 35 and are separated from the water w. The oil a ′ floating above the oil is discharged from the oil discharge port 19 through the oil discharge pipe 7. The oil pump 10 sucks and discharges.
[0038]
In addition, an oil / water boundary surface sensor 37 is provided at the upper layer position of the main body 16, and the state of the oil separated from the oil / water mixture b is constantly inspected, and the signal is sent to an appropriate place, for example, an oil / water coarse sensor. It is displayed on a meter (not shown) provided in the separation device main body 16 so that the operator can adjust the vacuum suction device 5 while monitoring this occasionally. Further, the oil / water rough separation device 6 can be automatically operated by electrically controlling the rotational speeds of the drainage pump 8 and the drainage pump 10 by the signal of the oil / water boundary surface sensor 37. Reference numerals 38, 39 and 40 are valves.
[0039]
As shown in FIG. 1, the oil recovery ship 50 is a catamaran, and an oil fence 28 is stretched between the two bodies 51 to collect the drifting oil a on the sea surface and recover the oil a therein. The method is adopted. This is more efficient than monohulls. In order to calm the waves of the catamaran-shaped oil recovery ship 50, a wave height limiting plate 44 as shown in FIG. 10 is effective.
[0040]
Reference numeral 46 denotes a dust removal grid.
[0041]
The wave height limiting plate 44 includes a highly rigid portion 29 such as steel or aluminum and a flexible portion 30 such as rubber. If the short period triangular wave C is eliminated by the wave height limiting plate 44, the oil suction port 1 can easily follow the movement of the sea surface due to the wave riding performance of the float 18 for long period waves. . Reference numeral 31 denotes a wave return portion, and A denotes a forward direction of the oil recovery ship 50.
[0042]
Further, the shape of the oil suction port 1 is not limited to a specific shape, but a vertical tube 1a as shown in FIG. 11 (a), an L-shaped tube 1b as shown in FIG. As shown in (c), various types such as a U-shaped tube 1c having a slit 42 in the throttle part 41 and a tube 1d with a slit 42 in FIG.
[0043]
Moreover, the shape of the float 18 has good wave riding characteristics, and also has a shape that does not obstruct the flow of oil, and various types are conceivable as shown in FIGS. For example, the float 18 in FIG. 12 is formed in a disk shape and is provided on both sides of the suction port 1 like both wheels of a car. Further, the float 18 of FIG. 13 is formed in a flat body shape, and is provided so as to be rotatable about the longitudinal axis 52 like a front wheel of a vehicle. Further, the float 18 in FIG. 14 is formed in a flat body shape, and is provided on three sides of a triangular frame (plan view) 53. Furthermore, the float 18 of FIG. 15 is formed in a cylindrical shape and provided at the four corners of a U-shaped frame (plan view) 54. In FIG. 12B to FIG. 15B, i indicates a waveform shape.
[0044]
【The invention's effect】
As described above, the present invention is a vacuum suction oil recovery system that recovers the oil floating on the water surface by vacuum suction. The vacuum suction device uses an air suction pipe, a cyclone gas-liquid separator, and an oil suction pipe. The vacuum suction oil recovery system is characterized in that air is sucked through the suction port, and the floating oil on the water surface is sucked on the high-speed jet stream of the air sucked from the suction port.
[0045]
Therefore, for example, even a lump of oil or low-viscosity oil that has been hardened by cold seawater in winter can be efficiently sucked on a high-speed jet stream of air sucked from the suction port.
[0046]
In particular, the oil suction pipe is raised substantially vertically to prevent the generation of sucked oil plug flow, and water is actively injected into the oil suction pipe as a lubricant for oil moving in the pipe. Since it is used, the oil suction pipe can be efficiently recovered without clogging.
[0047]
Further, according to the present invention, a floating body (float) is provided at the suction port, and the suction port is made to follow the vertical movement of the wave. And can be recovered efficiently.
[0048]
In the present invention, a cyclone type gas-liquid separator is connected to the upper end of the oil suction pipe, the air sucked in the oil suction pipe and the oil water are separated by the cyclone type gas-liquid separator, and the separated air is While being released into the atmosphere, the separated oil and water are sent to the oil / water separator, so that only the oil and water can be finally separated.
[0049]
Moreover, the oil / water rough separation device of the present invention includes a stationary / gravity separation type separation element in the main body, and the separation elements are arranged in a plurality of horizontal plates and in front and behind the horizontal plates. Since it is constituted by a current plate, oil and water can be easily separated using the difference in specific gravity between oil and water.
[0050]
Further, according to the present invention, a wave height limiting plate having a wave returning portion curved obliquely downward is provided in front of the suction port in the traveling direction, and the triangular wave having a short period is erased by the wave height limiting plate. The suction port is not swayed by a rough triangular wave, and the floating oil on the water surface can be sucked efficiently.
[Brief description of the drawings]
FIG. 1A is a plan view of an oil recovery ship applied to a vacuum suction oil recovery system of the present invention, and FIG. 1B is a side view of the oil recovery ship.
FIG. 2 is an enlarged perspective view of a waist portion of the oil recovery ship.
FIG. 3 is a structural diagram of a vacuum suction oil recovery system of the present invention.
FIG. 4 is an explanatory diagram of air intake means provided in the oil suction pipe.
5A is a plan view of a cyclone gas-liquid separator, and FIG. 5B is a side view of the cyclone gas-liquid separator.
FIG. 6 is an operation explanatory diagram of an oil suction pipe.
FIG. 7 is a side view of the coarse oil / water separator.
FIG. 8 is a front view of a clear plate.
FIG. 9 is an explanatory diagram of an oil drain pipe.
FIG. 10 is a side view of a wave height limiting plate.
FIGS. 11A to 11D are side views of suction ports. FIGS.
12A is a plan view showing another embodiment of the float, and FIG. 12B is an operation diagram of the float.
13A is a plan view showing another embodiment of the float, and FIG. 13B is an operation diagram of the float.
14A is a plan view showing another embodiment of the float, and FIG. 14B is an operation diagram of the float.
15A is a plan view showing another embodiment of the float, and FIG. 15B is an operation diagram of the float.
[Explanation of symbols]
a Oil floating on the water surface d Air j High-speed jet stream 1 Suction port 2 Oil suction tube 3 Cyclone gas-liquid separator 4 Air suction tube 5 Vacuum suction device

Claims (4)

先端部に波の上下運動に追随する吸引口を設けた油吸引管によって水面に浮遊している油を真空吸引、即ち真空吸引装置によって空気吸引管、サイクロン式気液分離器、油吸引管及び吸引口を介して空気を吸引して回収する真空吸引油回収システムであって、前記吸引口の胴部に空気吸引管を設け、該空気吸引管の開口部を蓋体によって開閉することを特徴とする真空吸引油回収システム。Vacuum suction of oil floating on the water surface by an oil suction tube provided with a suction port that follows the vertical movement of the wave at the tip, that is , an air suction tube, a cyclone gas-liquid separator, an oil suction tube and A vacuum suction oil recovery system that sucks and collects air through a suction port, wherein an air suction tube is provided in a body portion of the suction port, and an opening of the air suction tube is opened and closed by a lid. Vacuum suction oil recovery system. 前記油吸引管に注水管を設ける一方、前記油吸引管とサイクロン式気液分離器及び油水粗分離装置を介して間接的に接続している分離油排出管に注水管を設け、各注水管より各管内に潤滑用の水を注入することを特徴とする請求項1記載の真空吸引油回収システム。The oil suction pipe is provided with a water injection pipe, while the oil suction pipe is provided with a separate oil discharge pipe that is indirectly connected to the oil suction pipe via a cyclone type gas-liquid separator and an oil / water rough separation device. The vacuum suction oil recovery system according to claim 1 , wherein water for lubrication is poured into each pipe . 前記油水粗分離装置は、その本体内に静置・重力分離方式の分離素子を備えており、該分離素子は、多段に配した複数の水平板と、その前後に配した整流板により構成され、且つ、前記水平板をポリプロピレンやポリエチレン板等の合成樹脂板、或いは合成樹脂コートで表面処理した金属板により構成してなる請求項記載の真空吸引油回収システム。 The oil / water coarse separation device includes a stationary / gravity separation type separation element in its main body, and the separation element is composed of a plurality of horizontal plates arranged in multiple stages and rectifying plates arranged before and after the horizontal plates. The vacuum suction oil recovery system according to claim 2 , wherein the horizontal plate is formed of a synthetic resin plate such as polypropylene or polyethylene plate or a metal plate surface-treated with a synthetic resin coat . 前記吸引口の進行方向前方に、斜め下方に向けて湾曲した波返し部を有する波高制限板を設け、該波高制限板により、短周期の三角波を消去するようにしたことを特徴とする請求項記載の真空吸引油回収システム。 A wave height limiting plate having a wave return portion curved obliquely downward is provided in front of the suction port in the traveling direction, and the short wave triangular wave is erased by the wave height limiting plate. 1 vacuum oil recovery system according.
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JP5770776B2 (en) * 2012-04-27 2015-08-26 眞一 渡部 Oil Exceptioner
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CN104671487B (en) * 2013-11-27 2016-06-08 中国石油化工股份有限公司 A kind of point water-purification plant and purifying method thereof
CN103922497B (en) * 2014-04-14 2015-04-08 中国石油大学(华东) Three-stage pressure-reducing V-shaped hydraulic cyclone air floatation device
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