JP2009061376A - Oil spill recovery treatment apparatus - Google Patents

Oil spill recovery treatment apparatus Download PDF

Info

Publication number
JP2009061376A
JP2009061376A JP2007230361A JP2007230361A JP2009061376A JP 2009061376 A JP2009061376 A JP 2009061376A JP 2007230361 A JP2007230361 A JP 2007230361A JP 2007230361 A JP2007230361 A JP 2007230361A JP 2009061376 A JP2009061376 A JP 2009061376A
Authority
JP
Japan
Prior art keywords
oil
emulsion
steam ejector
oil recovery
spilled
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.)
Granted
Application number
JP2007230361A
Other languages
Japanese (ja)
Other versions
JP4780503B2 (en
Inventor
Isamu Fujita
勇 藤田
Muneo Yoshie
宗生 吉江
Kenji Takezaki
健二 竹崎
Yosuke Hayashi
洋介 林
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.)
National Institute of Maritime Port and Aviation Technology
Original Assignee
National Institute of Maritime Port and Aviation Technology
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 National Institute of Maritime Port and Aviation Technology filed Critical National Institute of Maritime Port and Aviation Technology
Priority to JP2007230361A priority Critical patent/JP4780503B2/en
Publication of JP2009061376A publication Critical patent/JP2009061376A/en
Application granted granted Critical
Publication of JP4780503B2 publication Critical patent/JP4780503B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Removal Of Floating Material (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an oil spill recovery treatment apparatus which can obtain a high oil recovery efficiency and enables the dispersion treatment of high viscosity oil as well as treatment of oil spill while staying on the spot for a long time. <P>SOLUTION: The oil spill recovery treatment apparatus comprises an oil spill suction means 1 equipped with a steam ejector 2 sucking an emulsion of the oil spill drifting on the water surface, an oil recovery means 11 separating and recovering oil from the emulsion sucked by the oil spill suction means 1, an oil collection means 16 installed around the steam ejector 1, water guns 21 releasing water toward the steam ejector 2, a chemical injection means 24 injecting a chemical, such as an emulsion breaking agent or dispersing agent, or the like, into at least either the steam ejector 2 or the water guns 21, and three-way switching valves 28a, 28b as an operation mode switching means switching an oil recovery mode and an emulsion dispersion mode. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

この発明は、流出油回収処理装置、特に、高温高圧の蒸気エゼクタを使用することによって、高い油回収効率が得られると共に、気液分離器や油水分離器等の各種機器の閉塞を防止でき、さらに、高粘度油の分散処理が可能となり、しかも、油回収モードとエマルジョン分散処理モードとを切り替えできるので、回収油タンクの容量に制限されることなく、長時間現場に留まっての流出油の処理が可能となる流出油回収処理装置に関するものである。   This invention is capable of obtaining high oil recovery efficiency by using a spilled oil recovery processing device, particularly a high-temperature and high-pressure steam ejector, and can prevent clogging of various devices such as a gas-liquid separator and an oil-water separator, Furthermore, it is possible to disperse high-viscosity oil, and the oil recovery mode and emulsion dispersion processing mode can be switched. The present invention relates to a spilled oil recovery processing apparatus that can be processed.

タンカーによる油流出事故は、小規模なものを含めて毎年発生しており、事故発生件数をゼロにすることは不可能に近い。従って、万一、油流出事故が発生した場合には、流出油による環境汚染を最小限に留める対策が極めて重要である。   Tanker oil spills occur every year, including small ones, and it is almost impossible to reduce the number of accidents to zero. Therefore, in the unlikely event that an oil spill accident occurs, it is extremely important to take measures to minimize environmental pollution caused by the spilled oil.

海面に流出した油は、波浪等により海水と混合されて、W/O型エマルジョンを形成する。このようにして形成されたエマルジョンは、非常に高い粘度を示すと共に、取り込まれた水の量だけ体積が増加している。   Oil that has flowed out to the sea surface is mixed with seawater by waves or the like to form a W / O type emulsion. The emulsion thus formed exhibits a very high viscosity and increases in volume by the amount of water taken up.

エマルジョン化した流出油の対処法には、回収処理法および拡散処理法等がある。回収処理法は、ポンプ等により流出油のエマルジョンを吸引して回収油タンクに回収する方法であり、拡散処理法は、分散剤等の化学薬剤により流出油のエマルジョンを乳化し、微細な油滴にして分散させ、酸素や紫外線等の接触による自然浄化作用により流出油を無害化する方法である。   Methods for dealing with emulsified spilled oil include recovery processing and diffusion processing. The recovery treatment method is a method in which the spilled oil emulsion is sucked with a pump or the like and collected in a recovery oil tank. The diffusion treatment method emulsifies the spilled oil emulsion with a chemical agent such as a dispersant, and fine oil droplets. The spilled oil is detoxified by natural purification by contact with oxygen or ultraviolet rays.

従来、水面上の油を吸引する技術が特許文献1(特開平10−151455号公報)に開示されている。この技術は、エゼクタを利用して水面上の油を吸引するものである。エゼクタは、運動部分がなく耐食性材料が使用可能であるので耐久力に富み、しかも、構造が簡単であるので、保守・点検が容易であり、さらに、電力の消費量が少なく経済的である等の利点を有している。従って、流出油の回収処理にエゼクタを利用することは好ましい。   Conventionally, a technique for sucking oil on a water surface is disclosed in Patent Document 1 (Japanese Patent Laid-Open No. 10-151455). This technique uses an ejector to suck oil on the water surface. The ejector has no moving parts and can use corrosion-resistant materials, so it has excellent durability, and since the structure is simple, it is easy to maintain and inspect, and it is economical because it consumes less power. Has the advantage of Therefore, it is preferable to use an ejector for the recovery process of the spilled oil.

特開平10−151455号公報JP-A-10-151455

上述したように、流出油の回収処理にエゼクタを利用することは好ましいが、エゼクタによる流出油回収処理装置を船舶に搭載して、流出油回収処理を行った場合、以下のような問題がある。   As described above, it is preferable to use the ejector for the recovery process of the spilled oil. However, when the spilled oil recovery processing device by the ejector is mounted on the ship and the spilled oil recovery process is performed, there are the following problems. .

(1)回収された流出油は、依然エマルジョン化しているので、油水分離器等の機器が閉塞する恐れがあった。
(2)取り込まれた水の量だけ体積が増加しているので、回収油タンクの容量が不足する。
(3)回収油タンクが満杯になった場合には、一旦、帰港せざるを得ず、回収能率が悪い。
(1) Since the recovered spilled oil is still emulsified, equipment such as an oil-water separator may be clogged.
(2) Since the volume is increased by the amount of taken-in water, the capacity of the recovered oil tank is insufficient.
(3) When the recovered oil tank is full, it is forced to return to the port once and the recovery efficiency is poor.

従って、この発明の目的は、高温高圧の蒸気エゼクタを使用することによって、高い油回収効率が得られると共に、気液分離器や油水分離器等の各種機器の閉塞を防止でき、さらに、高粘度油の分散処理が可能となる。しかも、油回収モードとエマルジョン分散処理モードとを切り替えできるので、回収油タンクの容量に制限されることなく、長時間現場に留まっての流出油の処理が可能となる流出油回収処理装置を提供することにある。   Accordingly, the object of the present invention is to obtain a high oil recovery efficiency by using a high-temperature and high-pressure steam ejector, and to prevent clogging of various devices such as a gas-liquid separator and an oil-water separator. Oil dispersion processing is possible. In addition, since the oil recovery mode and the emulsion dispersion processing mode can be switched, there is provided a spilled oil recovery processing device that can process the spilled oil for a long time without being limited by the capacity of the recovered oil tank. There is to do.

この発明は、上記目的を達成するためになされたものであって、下記を特徴とするものである。   The present invention has been made to achieve the above object, and is characterized by the following.

請求項1記載の発明は、水面上に漂流する流出油のエマルジョンを吸引する蒸気エゼクタを備えた流出油吸引手段と、前記流出油吸引手段により吸引された前記エマルジョンから油を分離回収する油回収手段と、前記蒸気エゼクタの周囲に配される集油手段と、前記蒸気エゼクタに向けて水を放出する放水手段と、エマルジョン解消剤または分散剤等の薬剤を前記蒸気エゼクタおよび前記放水手段の少なくとも一方に注入する薬剤注入手段と、油回収モードとエマルジョン分散処理モードとを切り替える運転モード切替手段とを備え、油回収モードの場合には、前記薬剤注入手段から前記エマルジョン解消剤が前記蒸気エゼクタおよび前記放水手段の少なくとも一方に注入され、分離処理された油は、前記油回収手段により回収され、エマルジョン分散処理モードの場合には、前記薬剤注入手段から前記分散剤が前記蒸気エゼクタおよび前記放水手段の少なくとも一方に注入され、分散処理された処理液は、排出されることに特徴を有するものである。   The invention according to claim 1 is a spilled oil suction means having a steam ejector for sucking an emulsion of the spilled oil drifting on the water surface, and an oil recovery for separating and recovering the oil from the emulsion sucked by the spilled oil suction means. Means, oil collecting means disposed around the steam ejector, water discharge means for discharging water toward the steam ejector, and an agent such as an emulsion remover or a dispersing agent at least in the steam ejector and the water discharge means. A medicine injection means for injecting into one side, and an operation mode switching means for switching between an oil recovery mode and an emulsion dispersion treatment mode. In the case of the oil recovery mode, the emulsion canceling agent is supplied from the drug injection means to the vapor ejector and The oil injected into and separated from at least one of the water discharge means is recovered by the oil recovery means and emulsified. In the dispersion dispersion processing mode, the dispersion agent is injected from the chemical injection means into at least one of the steam ejector and the water discharge means, and the treated treatment liquid is discharged. It is.

請求項2記載の発明は、請求項1記載の発明において、前記薬剤注入手段と前記運転モード切替手段とは連動していることに特徴を有するものである。   The invention according to claim 2 is characterized in that, in the invention according to claim 1, the medicine injection means and the operation mode switching means are interlocked.

請求項3記載の発明は、請求項1または2記載の発明において、前記油回収手段は、気液分離器と油水分離器とを備えていることに特徴を有するものである。   The invention described in claim 3 is characterized in that, in the invention described in claim 1 or 2, the oil recovery means comprises a gas-liquid separator and an oil-water separator.

請求項4記載の発明は、請求項1から3の何れか1つに記載の発明において、前記蒸気エゼクタおよび前記集油手段は、波浪に追従して移動することに特徴を有するものである。   A fourth aspect of the invention is characterized in that, in the invention according to any one of the first to third aspects, the steam ejector and the oil collecting means move following a wave.

請求項5記載の発明は、請求項1から4の何れか1つに記載の流出油回収処理装置は、船舶に搭載されていることに特徴を有するものである。   The invention according to claim 5 is characterized in that the oil spill recovery processing device according to any one of claims 1 to 4 is mounted on a ship.

この発明によれば、高温高圧の蒸気エゼクタを使用することによって、高い油回収効率が得られると共に、気液分離器や油水分離器等の各種機器の閉塞を防止でき、さらに、高粘度油の分散処理が可能となる。しかも、油回収モードとエマルジョン分散処理モードとを切り替えできるので、回収油タンクの容量に制限されることなく、長時間現場に留まっての流出油の処理が可能となる。   According to the present invention, by using a high-temperature and high-pressure steam ejector, high oil recovery efficiency can be obtained, and blockage of various devices such as a gas-liquid separator and an oil-water separator can be prevented. Distributed processing is possible. In addition, since the oil recovery mode and the emulsion dispersion processing mode can be switched, it is possible to process the spilled oil staying on site for a long time without being limited by the capacity of the recovery oil tank.

この発明の流出油回収処理装置を船舶に搭載した場合の一実施態様を、図面を参照しながら説明する。   An embodiment when the spilled oil recovery processing device of the present invention is mounted on a ship will be described with reference to the drawings.

図1は、この発明の流出油回収処理装置を示す概略構成図、図2は、流出油吸引手段を示す概略側面図、図3は、流出油吸引手段を示す概略平面図、図4は、図3のA方向矢視図である。   1 is a schematic configuration diagram showing a spilled oil recovery processing apparatus of the present invention, FIG. 2 is a schematic side view showing a spilled oil suction means, FIG. 3 is a schematic plan view showing a spilled oil suction means, and FIG. It is an A direction arrow directional view of FIG.

図1から図3において、1は、流出油吸引手段であり、蒸気エゼクタ2と、蒸気エゼクタ2に高圧蒸気を供給する蒸気供給手段3とを備えている。
蒸気供給手段3は、清水タンク4、給水ポンプ5、ボイラ6、蒸気流量計7、調圧弁8および供給ポンプ9から構成されている。給水ポンプ5により清水タンク4内の水は、ボイラ6に送られて高圧蒸気となる。高圧蒸気は、蒸気流量計7および調圧弁8により所定の流量および圧力に調整された後、供給ポンプ9によって蒸気エゼクタ2の蒸気供給管10に送られる。
In FIG. 1 to FIG. 3, reference numeral 1 denotes spilled oil suction means, which includes a steam ejector 2 and a steam supply means 3 for supplying high-pressure steam to the steam ejector 2.
The steam supply means 3 includes a fresh water tank 4, a water supply pump 5, a boiler 6, a steam flow meter 7, a pressure regulating valve 8, and a supply pump 9. The water in the fresh water tank 4 is sent to the boiler 6 by the feed pump 5 and becomes high-pressure steam. The high-pressure steam is adjusted to a predetermined flow rate and pressure by the steam flow meter 7 and the pressure regulating valve 8, and then sent to the steam supply pipe 10 of the steam ejector 2 by the supply pump 9.

11は、蒸気エゼクタ2により吸引された流出油のエマルジョンから油を分離回収する油回収手段である。油回収手段11は、気液分離器12と油水分離器13とから構成されている。蒸気エゼクタ2により吸引された流出油のエマルジョンは、油水吸引管14から気液分離器12に送られ、ここで遠心力により気体と液体とに分離された後、油水分離器13により油と水とに分離される。分離された油は、回収油タンク15内に貯留され、水は、排出管13aから船外に排出される。   Reference numeral 11 denotes oil recovery means for separating and recovering oil from the spilled oil emulsion sucked by the steam ejector 2. The oil recovery means 11 includes a gas / liquid separator 12 and an oil / water separator 13. The emulsion of the spilled oil sucked by the steam ejector 2 is sent from the oil / water suction pipe 14 to the gas / liquid separator 12 where it is separated into gas and liquid by centrifugal force, and then oil and water are separated by the oil / water separator 13. And separated. The separated oil is stored in the recovered oil tank 15, and the water is discharged out of the ship through the discharge pipe 13a.

なお、エゼクタ2の作動液体として、高温高圧の蒸気を使用することによって、流出油のエマルジョンの吸引と同時に、エマルジョンの粘度を飛躍的に低下させることができる。この結果、回収油の付着による油水分離器等の機器の閉塞の問題は起こらない。しかも、エマルジョン解消剤によるエマルジョンの分解が容易に行われる。さらに、従来の分散剤散布法では、高粘度油の分散は困難であったが、高温高圧の蒸気エゼクタ2を使用することによってこれが可能となる。   By using high-temperature and high-pressure steam as the working liquid of the ejector 2, the viscosity of the emulsion can be drastically reduced simultaneously with the suction of the spilled oil emulsion. As a result, there is no problem of blockage of equipment such as an oil / water separator due to adhesion of recovered oil. Moreover, the emulsion can be easily decomposed by the emulsion remover. Furthermore, although it has been difficult to disperse high-viscosity oil by the conventional dispersant spraying method, this can be achieved by using the high-temperature and high-pressure steam ejector 2.

16は、集油手段としての集油板であり(図2から図4参照)、蒸気エゼクタ2の後方に蒸気エゼクタ2を取り囲むように配されている。集油板16には、オイルブーム17が接続されている。   Reference numeral 16 denotes an oil collecting plate as oil collecting means (see FIGS. 2 to 4), and is arranged behind the steam ejector 2 so as to surround the steam ejector 2. An oil boom 17 is connected to the oil collecting plate 16.

蒸気供給管10の途中は、可撓性に富んだゴム管10aにより構成され、蒸気エゼクタ2側の蒸気供給管10は、自在継手18を介してゴム管10aに接続されている。油水吸引管14の途中は、可撓性に富んだゴム管14aにより構成され、蒸気エゼクタ2側の油水吸引管14は、自在継手18を介してゴム管14aに接続されている。蒸気エゼクタ2近傍の蒸気供給管10および油水吸引管14には、フロート19が取り付けられている。ゴム管10a、14aおよび自在継手18の作用によって、蒸気エゼクタ2および集油板16は、波浪に追従して移動する。なお、蒸気供給管10と油水吸引管14との途中間には、蒸気エゼクタ2を逆洗する際に開かれる逆洗弁20が取り付けられている。   In the middle of the steam supply pipe 10, a rubber pipe 10 a having high flexibility is configured, and the steam supply pipe 10 on the steam ejector 2 side is connected to the rubber pipe 10 a via a universal joint 18. In the middle of the oil / water suction tube 14, a rubber tube 14 a having a high flexibility is formed. The oil / water suction tube 14 on the steam ejector 2 side is connected to the rubber tube 14 a via a universal joint 18. A float 19 is attached to the steam supply pipe 10 and the oil / water suction pipe 14 in the vicinity of the steam ejector 2. By the action of the rubber tubes 10a and 14a and the universal joint 18, the steam ejector 2 and the oil collecting plate 16 move following the waves. A backwash valve 20 that is opened when the steam ejector 2 is backwashed is attached between the steam supply pipe 10 and the oil / water suction pipe 14.

21は、放水手段としての複数本の放水銃であり、海水ポンプ22によって蒸気エゼクタ2に向けて海水を放出する。23は、ゴミよけネットであり、放水銃21から放水された海水により海面上のゴミが蒸気エゼクタ2に吸引されるのを防止する。   Reference numeral 21 denotes a plurality of water discharge guns as water discharge means, and discharges seawater toward the steam ejector 2 by the seawater pump 22. Reference numeral 23 denotes a dust net, which prevents the sea surface waste from being sucked into the steam ejector 2 by seawater discharged from the water discharge gun 21.

24は、薬剤注入手段であり、エマルジョン解消剤タンク25内のエマルジョン解消剤または分散剤タンク26内の分散剤を供給ポンプ27によって、後述する三方切替弁を介して蒸気エゼクタ2および放水銃21の少なくとも一方に注入する。   Reference numeral 24 denotes a medicine injecting means for supplying the emulsion remover in the emulsion remover tank 25 or the dispersant in the dispersant tank 26 to the steam ejector 2 and the water discharge gun 21 via a supply pump 27 via a three-way switching valve described later. Inject into at least one.

28a、28bは、運転モード切替手段としての三方切替弁である。三方切替弁28aは、油回収モード、すなわち、エマルジョン解消剤の添加により流出油のエマルジョンから油を回収する場合には、気液分離器12からの流路を油水分離器13側に切り替える。一方、エマルジョン分散処理モード、すなわち、分散剤により流出油のエマルジョンを分散処理する場合には、気液分離器12からの流路を排水管13a側に切り替える。三方切替弁28bは、上記運転モードに応じて、供給ポンプ27に送る薬剤をエマルジョン解消剤タンク25内のエマルジョン解消剤か分散剤タンク26内の分散剤かに切り替える。上記2つの三方切替弁28a、28bは、運転モードに応じて自動的に切り替わるようにしても良い。   28a and 28b are three-way switching valves as operation mode switching means. The three-way switching valve 28a switches the flow path from the gas-liquid separator 12 to the oil-water separator 13 side in the oil recovery mode, that is, when oil is recovered from the emulsion of the spilled oil by adding an emulsion canceling agent. On the other hand, in the emulsion dispersion processing mode, that is, when the emulsion of the spilled oil is dispersed with the dispersant, the flow path from the gas-liquid separator 12 is switched to the drain pipe 13a side. The three-way switching valve 28b switches the medicine to be supplied to the supply pump 27 to the emulsion eliminating agent in the emulsion eliminating agent tank 25 or the dispersing agent in the dispersing agent tank 26 according to the operation mode. The two three-way switching valves 28a and 28b may be automatically switched according to the operation mode.

このように構成されている、この発明の流出油回収処理装置によれば、以下のようにして、海面上に漂流する流出油を回収処理することができる。   According to the spilled oil recovery processing device of the present invention configured as described above, the spilled oil drifting on the sea surface can be recovered and processed as follows.

油回収モードの場合には、三方切替弁28aを油水分離器13側に、そして、三方切替弁28bをエマルジョン解消剤タンク25側にそれぞれ切り替え、蒸気供給手段3から高圧蒸気を蒸気供給管10に送る。これにより、蒸気エゼクタ2が作動して、集油板16およびオイルブーム17内の流出油のエマルジョンが吸引される。流出油は、放水銃21から放出される海水によって、ゴミよけネット23を介して蒸気エゼクタ2側に集められる。蒸気エゼクタ2および集油板16は、フロート19の浮力により波浪に追従して移動するので、流出油のエマルジョンは、蒸気エゼクタ2によって確実に吸引される。   In the case of the oil recovery mode, the three-way switching valve 28a is switched to the oil / water separator 13 side, and the three-way switching valve 28b is switched to the emulsion eliminating agent tank 25 side, and high-pressure steam from the steam supply means 3 is transferred to the steam supply pipe 10. send. As a result, the steam ejector 2 is operated, and the oil spilled oil in the oil collecting plate 16 and the oil boom 17 is sucked. The spilled oil is collected on the steam ejector 2 side by the seawater discharged from the water discharge gun 21 through the dust net 23. Since the steam ejector 2 and the oil collecting plate 16 move following the waves by the buoyancy of the float 19, the emulsion of the spilled oil is reliably sucked by the steam ejector 2.

エマルジョン解消剤タンク25内のエマルジョン解消剤は、供給ポンプ27によって蒸気供給管10に送られると同時に、放水銃21に送られる。エマルジョン解消剤は、蒸気供給管10および放水銃21の何れか一方に供給しても良い。これによって、流出油のエマルジョンは、分解され、油水吸引管14を通って気液分離器12に送られ、ここで、遠心力により気体と液体とに分離される。この後、分離された液体分は、三方切替弁28aを通って油水分離器13に送られ、ここで、油と水とに分離される。分離された油は、回収油タンク15内に貯留され、水は、排出管13aから船外に排出される。   The emulsion remover in the emulsion remover tank 25 is sent to the steam supply pipe 10 by the supply pump 27 and simultaneously to the water discharge gun 21. The emulsion eliminating agent may be supplied to one of the steam supply pipe 10 and the water discharge gun 21. As a result, the spilled oil emulsion is decomposed and sent to the gas-liquid separator 12 through the oil / water suction pipe 14, where it is separated into gas and liquid by centrifugal force. Thereafter, the separated liquid is sent to the oil / water separator 13 through the three-way switching valve 28a, where it is separated into oil and water. The separated oil is stored in the recovered oil tank 15, and the water is discharged out of the ship through the discharge pipe 13a.

このようにして、流出油のエマルジョンから油が回収されるが、蒸気エゼクタ2によって吸引された流出油のエマルジョンから水が分離除去されるので、その体積分だけ、余計に油を回収油タンク15に回収することができる。   In this way, oil is recovered from the spilled oil emulsion, but water is separated and removed from the spilled oil emulsion sucked by the steam ejector 2, so that extra oil is recovered by the volume of the oil tank 15. Can be recovered.

さらに油の回収が進んで、回収油タンク15が満杯になったら、三方切替弁28aを排出管13a側に、そして、三方切替弁28bを分散剤タンク26側にそれぞれ切り替える。これにより、分散剤タンク26内の分散剤は、供給ポンプ27によって蒸気供給管10に送られると同時に、放水銃21に送られる。分散剤は、蒸気供給管10および放水銃21の何れか一方に供給しても良い。この分散処理によって、流出油のエマルジョンは、無害化され、油水吸引管14を通って気液分離器12に送られ、ここで、遠心力により気体と液体とに分離される。この後、分離された液体分は、三方切替弁28aを通って排出管13aから船外に排出される。   When the oil recovery further proceeds and the recovered oil tank 15 is full, the three-way switching valve 28a is switched to the discharge pipe 13a side, and the three-way switching valve 28b is switched to the dispersant tank 26 side. As a result, the dispersant in the dispersant tank 26 is sent to the steam supply pipe 10 by the supply pump 27 and simultaneously to the water discharge gun 21. The dispersant may be supplied to either the steam supply pipe 10 or the water discharge gun 21. By this dispersion treatment, the spilled oil emulsion is rendered harmless and sent to the gas-liquid separator 12 through the oil / water suction pipe 14 where it is separated into gas and liquid by centrifugal force. Thereafter, the separated liquid is discharged out of the ship from the discharge pipe 13a through the three-way switching valve 28a.

なお、蒸気エゼクタ2を逆洗する場合には、逆洗弁20を開いて蒸気を油水吸引管14側から蒸気エゼクタ2に流す。   When the steam ejector 2 is backwashed, the backwash valve 20 is opened and the steam flows from the oil / water suction pipe 14 side to the steam ejector 2.

このように、高温高圧の蒸気エゼクタを使用することによって、高い油回収効率が得られると共に、気液分離器や油水分離器等の各種機器の閉塞を防止でき、さらに、高粘度油の分散処理が可能となる。しかも、油回収モードとエマルジョン分散処理モードとを切り替えできるので、タンクの容量分だけの流出油の回収が終了した後も、船外に排出可能な分散処理による流出油の処理が行える。従って、回収油タンクの容量に制限されることなく、長時間現場に留まっての流出油の処理が可能となる。   In this way, by using a high-temperature and high-pressure steam ejector, high oil recovery efficiency can be obtained, and blockage of various devices such as a gas-liquid separator and an oil-water separator can be prevented. Is possible. In addition, since the oil recovery mode and the emulsion dispersion processing mode can be switched, the spilled oil can be processed by the dispersion process that can be discharged out of the ship even after the recovery of the spilled oil corresponding to the capacity of the tank is completed. Therefore, it is possible to treat the spilled oil staying on site for a long time without being limited by the capacity of the recovered oil tank.

この発明の流出油回収処理装置を示す概略構成図である。It is a schematic block diagram which shows the spilled oil collection | recovery processing apparatus of this invention. 流出油吸引手段を示す概略側面図である。It is a schematic side view which shows a spilled oil suction means. 流出油吸引手段を示す概略平面図である。It is a schematic plan view which shows a spilled oil suction means. 図3のA方向矢視図である。It is an A direction arrow directional view of FIG.

符号の説明Explanation of symbols

1:流出油吸引手段
2:蒸気エゼクタ
3:蒸気供給手段
4:清水タンク
5:給水ポンプ
6:ボイラ
7:蒸気流量計
8:調圧弁
9:供給ポンプ
10:蒸気供給管
10a:ゴム管
11:油回収手段
12:気液分離器
13:油水分離器
13a:排出管
14:油水吸引管
14a:ゴム管
15:回収油タンク
16:集油板
17:オイルブーム
18:自在継手
19:フロート
20:逆洗弁
21:放水銃
22:海水ポンプ
23:ゴミよけネット
24:薬剤注入手段
25:エマルジョン解消剤タンク
26:分散剤タンク
27:供給ポンプ
28a、28b:三方切替弁
1: Spilled oil suction means 2: Steam ejector 3: Steam supply means 4: Fresh water tank 5: Water supply pump 6: Boiler 7: Steam flow meter 8: Pressure regulating valve 9: Supply pump 10: Steam supply pipe 10a: Rubber pipe 11: Oil recovery means 12: gas-liquid separator 13: oil / water separator 13a: discharge pipe 14: oil / water suction pipe 14a: rubber pipe 15: recovered oil tank 16: oil collecting plate 17: oil boom 18: universal joint 19: float 20: Backwash valve 21: Water spray gun 22: Seawater pump 23: Garbage prevention net 24: Drug injection means 25: Emulsification agent tank 26: Dispersant tank 27: Supply pumps 28a, 28b: Three-way switching valve

Claims (5)

水面上に漂流する流出油のエマルジョンを吸引する蒸気エゼクタを備えた流出油吸引手段と、前記流出油吸引手段により吸引された前記エマルジョンから油を分離回収する油回収手段と、前記蒸気エゼクタの周囲に配される集油手段と、前記蒸気エゼクタに向けて水を放出する放水手段と、エマルジョン解消剤または分散剤等の薬剤を前記蒸気エゼクタおよび前記放水手段の少なくとも一方に注入する薬剤注入手段と、油回収モードとエマルジョン分散処理モードとを切り替える運転モード切替手段とを備え、油回収モードの場合には、前記薬剤注入手段から前記エマルジョン解消剤が前記蒸気エゼクタおよび前記放水手段の少なくとも一方に注入され、分離処理された油は、前記油回収手段により回収され、エマルジョン分散処理モードの場合には、前記薬剤注入手段から前記分散剤が前記蒸気エゼクタおよび前記放水手段の少なくとも一方に注入され、分散処理された処理液は、排出されることを特徴とする流出油回収処理装置。   An spilled oil suction means having a steam ejector for sucking an emulsion of the spilled oil drifting on the water surface, an oil recovery means for separating and recovering oil from the emulsion sucked by the spilled oil suction means, and a periphery of the steam ejector Oil collecting means disposed on the steam ejector, water discharge means for discharging water toward the steam ejector, and drug injection means for injecting an agent such as an emulsion desorbing agent or a dispersant into at least one of the steam ejector and the water discharge means. And an operation mode switching means for switching between an oil recovery mode and an emulsion dispersion treatment mode. In the case of the oil recovery mode, the emulsion eliminating agent is injected from the chemical injection means into at least one of the steam ejector and the water discharge means. The separated oil is recovered by the oil recovery means, and is in an emulsion dispersion processing mode. Expediently, the medicament from said injecting means dispersing agent is injected into at least one of the steam ejector and the water discharge means, distributed treated process liquid is spilled oil recovery treatment apparatus, characterized in that it is discharged. 前記薬剤注入手段と前記運転モード切替手段とは連動していることを特徴とする、請求項1記載の流出油回収処理装置。   The spilled oil recovery processing apparatus according to claim 1, wherein the medicine injection means and the operation mode switching means are interlocked. 前記油回収手段は、気液分離器と油水分離器とを備えていることを特徴とする、請求項1または2記載の流出油回収処理装置。   The spilled oil recovery processing apparatus according to claim 1 or 2, wherein the oil recovery means includes a gas-liquid separator and an oil-water separator. 前記蒸気エゼクタおよび前記集油手段は、波浪に追従して移動することを特徴とする、請求項1から3の何れか1つに記載の流出油回収処理装置。   The spilled oil recovery processing apparatus according to any one of claims 1 to 3, wherein the steam ejector and the oil collecting means move following waves. 船舶に搭載されていることを特徴とする、請求項1から4の何れか1つに記載の流出油回収処理装置。   The spilled oil recovery processing apparatus according to any one of claims 1 to 4, wherein the spilled oil recovery processing apparatus is mounted on a ship.
JP2007230361A 2007-09-05 2007-09-05 Spilled oil recovery processor Expired - Fee Related JP4780503B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007230361A JP4780503B2 (en) 2007-09-05 2007-09-05 Spilled oil recovery processor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007230361A JP4780503B2 (en) 2007-09-05 2007-09-05 Spilled oil recovery processor

Publications (2)

Publication Number Publication Date
JP2009061376A true JP2009061376A (en) 2009-03-26
JP4780503B2 JP4780503B2 (en) 2011-09-28

Family

ID=40556479

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007230361A Expired - Fee Related JP4780503B2 (en) 2007-09-05 2007-09-05 Spilled oil recovery processor

Country Status (1)

Country Link
JP (1) JP4780503B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10208210B2 (en) 2014-07-30 2019-02-19 Mitsubishi Materials Corporation Hydrophilic oil repellent and production method of same, surface coating material, coating film, resin composition, oil-water separation filter material, and porous body
US10294125B2 (en) 2014-07-30 2019-05-21 Mitsubishi Materials Corporation Filter medium, method for producing filter medium, water treatment module, and water treatment device
US10364360B2 (en) 2014-07-30 2019-07-30 Mitsubishi Materials Corporation Surface coating material, coating film, and hydrophilic oil repellent member
US10399868B2 (en) 2014-07-30 2019-09-03 Mitsubishi Materials Corporation Oil-water separation apparatus and drainage system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10208210B2 (en) 2014-07-30 2019-02-19 Mitsubishi Materials Corporation Hydrophilic oil repellent and production method of same, surface coating material, coating film, resin composition, oil-water separation filter material, and porous body
US10294125B2 (en) 2014-07-30 2019-05-21 Mitsubishi Materials Corporation Filter medium, method for producing filter medium, water treatment module, and water treatment device
US10364360B2 (en) 2014-07-30 2019-07-30 Mitsubishi Materials Corporation Surface coating material, coating film, and hydrophilic oil repellent member
US10399868B2 (en) 2014-07-30 2019-09-03 Mitsubishi Materials Corporation Oil-water separation apparatus and drainage system

Also Published As

Publication number Publication date
JP4780503B2 (en) 2011-09-28

Similar Documents

Publication Publication Date Title
KR102162348B1 (en) Ship using fuel having low sulphur
JP4780503B2 (en) Spilled oil recovery processor
WO2021210192A1 (en) Floating-oil recovery processing apparatus
CN201729726U (en) High-efficiency dissolved air flotation system
KR101691425B1 (en) Complex Purification System of Oil-polluted Underground Water by Physical and Chemical
EP4058218B1 (en) Treatment of hydrocarbon-contaminated materials
US7905192B1 (en) Integrated underwater surface cleaning and effluent treatment system
KR102036190B1 (en) Buoyant body unit for recovery of spill oil and spill oil recovery system using this
US5957665A (en) Jet system total fluids recovery system
CN108658286A (en) A kind of wastewater treatment equipment of marine exhaust washing system
CN117090259A (en) Floating table type river and lake sewage bottom mud treatment device
CN217726628U (en) System for restoring complex contaminated land parcel by combining in-situ leaching and multiphase extraction
JP2014151318A (en) Oil floatation device, oil recovery apparatus and oil recovery method
CN106007075A (en) Fracturing waste fluid treatment device and method
KR200396223Y1 (en) Dissolved airfloatation system
CN206069576U (en) Fracturing outlet liquid processing meanss
KR20090107224A (en) Oil removal system and the removal method of the soil which the coast be imbrued
KR20090078094A (en) Marine pollution(red water,oil)control purifier ship
KR101639072B1 (en) Apparatus for removing pollutant in water using charged micro bubbles
US6659290B1 (en) Oil water separator with air sparging array for in-situ cleaning
CN107226562A (en) A kind of chemical industry purifying sewage quickly device
KR100501795B1 (en) A dredging system and apparatus of accamulated sludge using pressure floataition method in water area such as the sea,lakes,and rivers
KR100985064B1 (en) Movable real time water purification apparatus
JP2011218306A (en) Scum removing apparatus and method
KR101839584B1 (en) Apparatus for dredging underwater polluted deposit

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20100826

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20110526

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20110614

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20110624

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140715

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4780503

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R371 Transfer withdrawn

Free format text: JAPANESE INTERMEDIATE CODE: R371

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees