JP2007160264A - Oil/water separator - Google Patents

Oil/water separator Download PDF

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JP2007160264A
JP2007160264A JP2005362361A JP2005362361A JP2007160264A JP 2007160264 A JP2007160264 A JP 2007160264A JP 2005362361 A JP2005362361 A JP 2005362361A JP 2005362361 A JP2005362361 A JP 2005362361A JP 2007160264 A JP2007160264 A JP 2007160264A
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oil
water
tank
treated
filter
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JP5229764B2 (en
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Koichi Ueda
浩一 上田
Hiroshi Yamanouchi
博 山之内
Kenji Yamane
健次 山根
Kazuo Hatori
和夫 羽鳥
Nobuo Iijima
伸雄 飯島
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NATIONAL INSTITUTE FOR SEA TRAINING
National Maritime Research Institute
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NATIONAL INSTITUTE FOR SEA TRAINING
National Maritime Research Institute
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<P>PROBLEM TO BE SOLVED: To provide an oil/water separator capable of sufficiently reducing oil concentration in drainage by circulating fine oil particles in oily water through fiber materials, preferably cotton wool which is compressed to fill a tank, and further making them pass through a fine mesh filter, and also reducing burden of maintenance. <P>SOLUTION: The water W to be treated containing oil is treated by getting oil particles B separated by a coarse particle board 6 in a first pre-treatment tank 1, and the oil content further separated by a coarse particle filter 7 in a second pre-treatment tank 2. The treated water from which the oil content is coarsely separated is further treated by getting fine oil content removed by an exchangeable cartridge 3A for oil adsorption in a first tank 3, and ultrafine oil particles removed by a fine mesh filter A of 0.1-5 microns in a second tank 4. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、船舶の機関室などで生じる油を含んだビルジ水や、工場などで生じる油を含んだ汚水について、その外部への排出の際に、環境保全のため予め油分を分離するのに適した油水分離装置に関する。   In the present invention, bilge water containing oil generated in the engine room of a ship or sewage containing oil generated in a factory or the like is separated in advance for environmental protection when discharged to the outside. The present invention relates to a suitable oil-water separator.

従来、水に混入した油は、油と水との比重差による重力分離方式により分離することが行われていた。そして、平行板やフィルターを備えた水路を通過させることにより、油粒を造塊させ浮上速度を速くして分離することが行われていた。
しかしながら、油水混合物に界面活性剤や微細なゴミが混入した場合、油粒が小さくなったり、水と油粒との比重差が小さくなったりして、油粒の浮上速度が遅くなるため、比重差による油粒の分離が難しくなるという不具合がある。また、単に目の細かいフィルターを用いただけでは、目詰まりを起こして、分離性能が低下するという不具合がある。そして、目詰まりしたフィルターの交換は、同フィルターが油で汚れているため容易ではなかった。
さらに、繊維材からなるパッドやシートを用いて、液面に浮かぶ油分を吸着したり濾過により油分を除去したりすることも行われているが、このような手段では多量の油水について油分の分離を効率よく行うことは困難とされている。
一般に、界面活性剤等の混入により微細化された油粒を除去できれば、油水分離器の性能を向上させ、排水中の油分濃度を大幅に低減させることができる。従来の油水分離器では、この微粒化した油分が除去できなかったり、また目の細かいフィルターを使用した場合には目詰まりによる頻繁なフィルター交換が必要となったりして、メンテナンス上の負担の増大を招いていた。
特開2003−24705号公報 特開2005−288435号公報
Conventionally, oil mixed in water has been separated by a gravity separation method based on a difference in specific gravity between oil and water. And by passing the water channel provided with the parallel plate and the filter, the oil particles are agglomerated and separated by increasing the floating speed.
However, when surfactants and fine dust are mixed in the oil / water mixture, the oil particles become smaller, the difference in specific gravity between water and oil particles becomes smaller, and the floating speed of the oil particles becomes slower. There is a problem that it becomes difficult to separate the oil particles due to the difference. In addition, if only a fine filter is used, there is a problem that clogging occurs and the separation performance deteriorates. And replacement of a clogged filter is not easy because the filter is dirty with oil.
In addition, using a pad or sheet made of fiber material, it is also possible to adsorb the oil floating on the liquid surface or remove the oil by filtration. It is considered difficult to carry out this efficiently.
In general, if oil particles refined by mixing with a surfactant or the like can be removed, the performance of the oil / water separator can be improved and the oil concentration in the waste water can be greatly reduced. With conventional oil-water separators, this fine oil cannot be removed, and when a fine filter is used, frequent filter replacement due to clogging is required, increasing the maintenance burden. Was invited.
JP 2003-24705 A JP 2005-288435 A

本発明は、油水中の微細な油粒をタンク内に圧縮充填された繊維材、好ましくは脱脂綿に流通させてから、さらに微小メッシュのフィルターを通過させることにより、排水中の油分濃度を十分に低減できるようにするとともに、メンテナンスの負担も軽減できるようにした油水分離装置を提供することを課題とする。   According to the present invention, fine oil particles in oil water are circulated through a fiber material compressed in a tank, preferably absorbent cotton, and then passed through a fine mesh filter, so that the oil concentration in the waste water is sufficiently increased. It is an object of the present invention to provide an oil / water separator that can reduce the maintenance load.

本発明は、油分を含む被処理水を導入し通過させて上記油分の捕捉分離を行う第1タンクと、同第1タンクを通過した被処理水を導入し通過させて残余の油分の捕捉分離を行う第2タンクとを備え、上記第1タンクには、予め繊維材に水分を含ませて同繊維材を圧縮充填した油分吸着用カートリッジが交換可能に設けられるとともに、上記第2タンクには上記被処理水中の残余の油分を捕捉するための微小メッシュのフィルターが装填されていることを特徴としている。   The present invention includes a first tank that introduces and passes water to be treated containing oil, and captures and separates the oil, and the water to be treated that has passed through the first tank is introduced and passed to capture and separate the remaining oil. The first tank is provided with a replaceable oil adsorbing cartridge in which the fiber material is preliminarily compressed and filled with the fiber material, and the second tank includes a second tank. A fine mesh filter for capturing the remaining oil in the water to be treated is loaded.

また、本発明は、上記繊維材が脱脂綿であることを特徴としている。   In addition, the present invention is characterized in that the fiber material is absorbent cotton.

さらに、本発明は、上記フィルターが膜分離型フィルターとして構成されて、同フィルターのメッシュが0.1〜5ミクロンに設定されるとともに、同フィルターを逆流により洗浄するための配管が施されていることを特徴としている。   Furthermore, in the present invention, the filter is configured as a membrane separation filter, the mesh of the filter is set to 0.1 to 5 microns, and piping for cleaning the filter by backflow is provided. It is characterized by that.

また、本発明は、上記第1タンクへ導かれる上記被処理水について同被処理水中の油分を予め減少させておくための前処理装置を備え、同前処理装置が、初めに上記被処理水中の油分の粗分離を粗粒化板により行う第1前処理タンクと、同第1前処理タンクを通過した上記被処理水を導いて同被処理水中の油分の造塊分離を粗粒化フィルターにより行う第2前処理タンクとで構成されたことを特徴としている。   The present invention further includes a pretreatment device for reducing in advance the oil content in the treated water with respect to the treated water guided to the first tank, and the pretreatment device initially includes the treated water. A first pretreatment tank that performs coarse separation of oil using a coarse grained plate, and a coarsening filter that guides the water to be treated that has passed through the first pretreatment tank to separate ingots of oil in the treated water. And a second pretreatment tank performed by

本発明の油水分離装置では、油分を含む被処理水が、第1タンクにおいて同第1タンク内のカートリッジに圧縮充填された繊維材を通過する際に、微細な油分も効率よく捕捉されるようになり、このようにして第1タンクを通過した濾過水は、次に通過する第2タンク内の微小メッシュのフィルターにより、残余の油分を十分に捕捉されるようになる。   In the oil / water separator according to the present invention, when the water to be treated containing the oil passes through the fiber material compressed and filled in the cartridge in the first tank in the first tank, the fine oil is efficiently captured. Thus, the filtered water that has passed through the first tank in this way can be sufficiently captured by the fine mesh filter in the second tank that passes next.

そして、上記繊維材の上記カートリッジ内への圧縮充填は、同繊維材を予め濡らしてから行われるので、同繊維材の充填密度は著しく高められており、これにより同繊維材の間を通過する上記被処理水中の油分の捕捉が、上記繊維材の圧密化された表面への付着により十分に行われるようになる。   The compression filling of the fiber material into the cartridge is performed after the fiber material is wetted in advance, so that the filling density of the fiber material is remarkably increased, thereby passing between the fiber materials. The oil content in the water to be treated is sufficiently captured by the adhesion of the fiber material to the consolidated surface.

このようにして、第1タンクにおける上記繊維材で油分の捕捉が所要程度まで行われた後は、同繊維材を充填された前記カートリッジの交換により、直ちに第1タンクにおける油分捕捉機能の回復を図ることができる。   In this way, after the oil is captured to the required level by the fiber material in the first tank, the oil content capturing function in the first tank is immediately recovered by replacing the cartridge filled with the fiber material. You can plan.

また、本発明の油水分離装置では、上記繊維材として脱脂綿が採用されることにより、同繊維材を濡らして上記油分吸着用カートリッジ内へ圧縮充填する操作が容易に且つ十分に行われるとともに、脱脂綿は被処理水の流通抵抗が他の繊維材と比べて少ないため、同繊維材(脱脂綿)による油分の吸着捕捉が能率よく一層的確に行われるようになる。   Further, in the oil / water separator according to the present invention, the use of absorbent cotton as the fiber material facilitates and sufficiently performs the operation of wetting the fiber material and compressing and filling it into the oil adsorption cartridge. Since the flow resistance of water to be treated is less than that of other fiber materials, the adsorption and capture of oil by the fiber material (absorbent cotton) can be performed more efficiently and accurately.

さらに、第2タンクにおける微小メッシュの上記フィルターが膜分離型フィルターとして構成されて、同フィルターのメッシュが0.1〜5ミクロンに設定されていると、同フィルターにより微細な油粒の捕捉も容易に行われ、しかも上記フィルターを逆流により洗浄するための配管が施されているため、同フィルターの面倒な交換を必要とせずに同フィルターの油分捕捉機能を常時高めておくことができる。   Furthermore, if the fine mesh filter in the second tank is configured as a membrane separation filter, and the filter mesh is set to 0.1 to 5 microns, the filter can easily capture fine oil particles. In addition, since the piping for washing the filter by backflow is provided, the oil content capturing function of the filter can be constantly improved without requiring troublesome replacement of the filter.

被処理水中の油分含有量が著しく多い場合は、上記の第1タンクおよび第2タンクによる油水分離に先立って、予め被処理水中の油分を減少させておくことが望ましいが、本装置では、初めに第1前処理タンクで粗粒化板による被処理水中の油分の粗分離が行われ、ついで第2前処理タンクにおける粗粒化フィルターで被処理水中の油分の造塊分離が行われた後、被処理水が前記の第1タンクおよび第2タンクにおいて更に油分の分離が行われるものであり、このようにして被処理水中の油分分離が十分に且つ適切に行われるようになる。   When the oil content in the water to be treated is extremely high, it is desirable to reduce the oil content in the water to be treated in advance prior to the oil / water separation by the first tank and the second tank. In addition, after the first pretreatment tank is subjected to rough separation of the oil in the water to be treated by the coarsening plate, and then the ingot is separated from the water to be treated by the coarsening filter in the second pretreatment tank. The water to be treated is further separated in the first tank and the second tank, and thus the oil in the water to be treated is sufficiently and appropriately separated.

図1は本発明の一実施例としての油水分離装置を模式的に示す系統図であり、図2は油水分離のメカニズムを示す説明図で、その(a)図は吸着による油水分離のメカニズムを示す説明図、(b)図は膜分離方式による油水分離のメカニズムを示す説明図である。   FIG. 1 is a system diagram schematically showing an oil-water separator as one embodiment of the present invention, FIG. 2 is an explanatory diagram showing the mechanism of oil-water separation, and FIG. 1 (a) shows the mechanism of oil-water separation by adsorption. Explanatory drawing shown, (b) figure is explanatory drawing which shows the mechanism of the oil-water separation by a membrane separation system.

図1に示すように、船舶のビルジタンクから導かれた油分を含む被処理水Wが、同被処理水中の油分を予め減少させておくため、第1前処理タンク1に、図示しない圧入用ポンプで圧入されるようになっている。そして、第1前処理タンク1内へ流入する被処理水Wにおける大量の油分は直ちに上方へ集められてバルブ1b付き排出管1aから排出され、また比較的粒径の大きい油分は粗粒化板6により粗粒化されて、その油分もタンク1内の上方の排出管1aから排出される。
なお、図1における符号Aは水の流れ方向を示し、Bは油粒を模式的に示している。
As shown in FIG. 1, the water to be treated W including oil contained in the bilge tank of the ship reduces the oil content in the water to be treated in advance. It comes to be press-fitted with. A large amount of oil in the water to be treated W flowing into the first pretreatment tank 1 is immediately collected upward and discharged from the discharge pipe 1a with valve 1b, and oil having a relatively large particle size is coarsened. 6 is coarsened, and the oil is also discharged from the upper discharge pipe 1 a in the tank 1.
In addition, the code | symbol A in FIG. 1 shows the flow direction of water, B has shown the oil grain typically.

また、第1前処理タンク1には、同タンク内の油水界面を検出するための油水界面センサー5a,5bが設けられている。   The first pretreatment tank 1 is provided with oil / water interface sensors 5a and 5b for detecting the oil / water interface in the tank.

上述のごとく、第1前処理タンク1では、大量に流入する油や比較的粒径の大きい油分の分離が行われるが、被処理水中に猶も残存する油分の分離を行うため、第1前処理タンク1から接続管2cを介してコアレッサーとしての第2前処理タンク2へ導かれた被処理水は、同タンク2内の粗粒化フィルター7により油分を粗粒化されて分別され、このようにして粗粒化された油分は同タンク上部のバルブ2b付き排出管2aより排出される。   As described above, in the first pretreatment tank 1, oil that flows in a large amount or oil having a relatively large particle diameter is separated. However, in order to separate the oil that remains in the water to be treated, The water to be treated guided from the treatment tank 1 to the second pretreatment tank 2 as a coalescer through the connecting pipe 2c is coarsened and separated by the coarsening filter 7 in the tank 2. The oil thus coarsened is discharged from a discharge pipe 2a with a valve 2b at the top of the tank.

油分を含む被処理水Wが上述の第1前処理タンク1および第2前処理タンク2を経由することにより、その油分をかなり除去されるが、本装置では第2前処理タンク2で前処理された被処理水が、さらに微細油粒の除去処理を施されるため、第1タンク3および第2タンク4へ順次送給される。   The treated water W containing the oil passes through the first pretreatment tank 1 and the second pretreatment tank 2 described above, so that the oil is considerably removed. In this apparatus, the pretreatment is performed in the second pretreatment tank 2. Since the treated water is further subjected to the removal process of fine oil particles, it is sequentially fed to the first tank 3 and the second tank 4.

すなわち、第2前処理タンク2の出口フィルター7aを経由した被処理水は、接続管3aおよびバルブ8を介し第1タンク3の頂部へ導かれ、同第1タンク3における交換可能の油分吸着用カートリッジ3Aにおいて、図2(a)に示すごとく、微細な油粒Bを吸着除去される。
ついで、被処理水は、第1タンク3の底部の第1バルブ3Vおよび第2タンク4の底部の第2バルブ4Vを介し、同第2タンク4内へ導かれる。
That is, the water to be treated that has passed through the outlet filter 7a of the second pretreatment tank 2 is guided to the top of the first tank 3 via the connecting pipe 3a and the valve 8, and is used for oil exchange that can be exchanged in the first tank 3. In the cartridge 3A, as shown in FIG. 2A, fine oil particles B are adsorbed and removed.
Then, the water to be treated is introduced into the second tank 4 through the first valve 3V at the bottom of the first tank 3 and the second valve 4V at the bottom of the second tank 4.

そして、第2タンク4の内部における微小メッシュ(0.1〜5ミクロン)のフィルター4Aにより、図2(b)に示すごとく、被処理水中に含まれる超微細の油粒Bの捕捉除去が行われる。   Then, the ultrafine oil particles B contained in the water to be treated are captured and removed by the fine mesh (0.1 to 5 micron) filter 4A inside the second tank 4 as shown in FIG. 2 (b). Is called.

第1タンク3における交換可能のカートリッジ3Aは、予め繊維材に水分を含ませて同繊維材を十分に圧縮充填されており、この繊維材としては好ましくは脱脂綿が用いられる。
また、第2タンク4におけるフィルター4Aについては、同フィルター4Aの目詰まりの程度を流量計などで検知する手段が設けられる。
The replaceable cartridge 3 </ b> A in the first tank 3 is preliminarily compressed and filled with moisture contained in a fiber material. Absorbent cotton is preferably used as the fiber material.
The filter 4A in the second tank 4 is provided with means for detecting the degree of clogging of the filter 4A with a flow meter or the like.

そして、フィルター4Aを逆流により洗浄するための配管として、第2タンク4の頂部に接続された排出管10に、切換バルブ12を介して洗浄水導入管13が接続される。また、第1バルブ3Vと第2バルブ4Vとの間の配管11aに、洗浄水排出用の排水管11が接続されている。このようにして、第2タンク4の内部で、逆流により微小メッシュのフィルター4Aの洗浄が行われるようになっている。
なお、切換バルブ12および洗浄水導入管13を設ける代わりに、単に排水管10に逆流用ポンプを設けるようにしてもよい。
Then, a washing water introduction pipe 13 is connected to the discharge pipe 10 connected to the top of the second tank 4 via a switching valve 12 as a pipe for washing the filter 4A by backflow. Further, a drain pipe 11 for discharging cleaning water is connected to a pipe 11a between the first valve 3V and the second valve 4V. In this way, the fine mesh filter 4A is cleaned by backflow inside the second tank 4.
Instead of providing the switching valve 12 and the cleaning water introduction pipe 13, a drain pump may be simply provided in the drain pipe 10.

図1に示すように、第1前処理タンク1および第2前処理タンク2の各底部には、重い不純物を含んだ水の排水を行うためのバルブ1e,2e付き排出管1d,2dが接続されている。また、符号9は接続用フランジを示している。   As shown in FIG. 1, discharge pipes 1d and 2d with valves 1e and 2e for draining water containing heavy impurities are connected to the bottoms of the first pretreatment tank 1 and the second pretreatment tank 2, respectively. Has been. Reference numeral 9 denotes a connecting flange.

上述の本実施例の油水分離装置では、油分を含む被処理水Wが、第1タンク3において同第1タンク3内のカートリッジ3Aに圧縮充填された繊維材を通過する際に、微細な油分も効率よく吸着捕捉されるようになり、このようにして第1タンク3を通過した濾過水は、次に通過する第2タンク4内の微小メッシュのフィルター4Aにより、残余の油分を十分に捕捉除去されるようになる。   In the oil / water separator of the above-described embodiment, when the water to be treated W containing oil passes through the fiber material compressed and filled in the cartridge 3A in the first tank 3 in the first tank 3, the fine oil content is reduced. The filtered water that has passed through the first tank 3 in this way is sufficiently trapped by the fine mesh filter 4A in the second tank 4 that passes next. It will be removed.

そして、上記繊維材のカートリッジ3A内への圧縮充填は、同繊維材を予め濡らしてから行われるので、同繊維材の充填密度は著しく高められており、これにより同繊維材の間を通過する被処理水W中の油分の吸着捕捉が、上記繊維材の圧密化された表面への付着により十分に行われるようになる。   Then, the compression filling of the fiber material into the cartridge 3A is performed after the fiber material is wetted in advance, so that the filling density of the fiber material is remarkably increased, thereby passing between the fiber materials. Adsorption and capture of oil in the water to be treated W is sufficiently performed by adhering to the compacted surface of the fiber material.

このようにして、第1タンク3における上記繊維材で油分の捕捉が所要程度まで行われた後は、同繊維材を充填されたカートリッジ3Aの交換により、直ちに第1タンク3における油分捕捉機能の回復を図ることができる。   In this way, after the oil is captured by the fiber material in the first tank 3 to the required level, the oil content capturing function in the first tank 3 is immediately replaced by replacing the cartridge 3A filled with the fiber material. Recovery can be achieved.

また、本実施例の油水分離装置では、上記繊維材として脱脂綿が採用されることにより、同繊維材を濡らして油分吸着用カートリッジ3A内へ圧縮充填する操作が容易に且つ十分に行われるとともに、脱脂綿は被処理水の流通抵抗が他の繊維材と比べて少ないため、同繊維材(脱脂綿)による油分の吸着捕捉が能率よく一層的確に行われるようになる。   Further, in the oil / water separator of this embodiment, the use of absorbent cotton as the fiber material facilitates and sufficiently performs the operation of wetting the fiber material and compressing and filling it into the oil adsorption cartridge 3A. Since the absorbent cotton has less flow resistance of the water to be treated than other fiber materials, the oil material can be more efficiently adsorbed and captured by the fiber material (absorbent cotton).

さらに、第2タンク4における微小メッシュのフィルター4Aが膜分離型フィルターとして構成されて、同フィルター4Aのメッシュが0.1〜5ミクロンに設定されているので、同フィルター4Aにより超微細な油粒の捕捉除去も容易に行われ、しかもフィルター4Aを逆流により洗浄するための配管が施されているため、同フィルター4Aの面倒な交換を必要とせずに同フィルター4Aの油分捕捉機能を常時高めておくことができる。   Furthermore, the fine mesh filter 4A in the second tank 4 is configured as a membrane separation type filter, and the mesh of the filter 4A is set to 0.1 to 5 microns. Since the filter 4A is easily removed and piping for washing the filter 4A by backflow is provided, the oil trapping function of the filter 4A can be constantly improved without the need for troublesome replacement of the filter 4A. I can leave.

被処理水中の油分含有量が著しく多い場合は、第1タンク3および第2タンク4による油水分離に先立って、予め被処理水中の油分を減少させておくことが望ましいが、本装置では、初めに第1前処理タンク1で粗粒化板6による被処理水W中の油分の粗分離が行われ、ついで第2前処理タンク2における粗粒化フィルター7で被処理水中の油分の造塊分離が行われた後、被処理水Wが第1タンク3および第2タンク4において更に油分の分離が行われるものであり、このようにして被処理水中の油分分離が十分に且つ適切に行われるようになる。   When the oil content in the water to be treated is remarkably high, it is desirable to reduce the oil content in the water to be treated in advance prior to the oil / water separation by the first tank 3 and the second tank 4. In the first pretreatment tank 1, the oil content in the water to be treated W is roughly separated by the coarsening plate 6, and then the agglomeration of the oil in the water to be treated is performed by the coarsening filter 7 in the second pretreatment tank 2. After the separation, the water to be treated W is further separated in the first tank 3 and the second tank 4, and thus the oil in the treated water is sufficiently and appropriately separated. Will come to be.

本発明の一実施例としての油水分離装置を模式的に示す系統図である。1 is a system diagram schematically showing an oil-water separator as one embodiment of the present invention. 油水分離のメカニズムを示す説明図で、(a)図は吸着による油水分離のメカニズムを示す断面図、(b)図は膜分離方式による油水分離のメカニズムを示す断面図である。It is explanatory drawing which shows the mechanism of oil-water separation, (a) A figure is sectional drawing which shows the mechanism of oil-water separation by adsorption, (b) Figure is sectional drawing which shows the mechanism of oil-water separation by a membrane separation system.

符号の説明Explanation of symbols

1 第1前処理タンク
1a 排出管
1b バルブ
1d 排出管
1e バルブ
2 第2前処理タンク
2a 排出管
2b バルブ
2c 接続管
2d 排出管
2e バルブ
3 第1タンク
3A 油分吸着用カートリッジ
3a 接続管
3V 第1バルブ
4 第2タンク
4A フィルター
4V 第2バルブ
5a,5b 油水界面センサー
6 粗粒化板
7 粗粒フィルター
7a 出口フィルター
8 バルブ
9 接続用フランジ
10 排出管
11 排水管
11a 配管
12 切換バルブ
13 洗浄水導入管
A 水の流れ方向
B 油粒
W 被処理水
1 First Pretreatment Tank 1a Discharge Pipe 1b Valve 1d Discharge Pipe 1e Valve 2 Second Pretreatment Tank 2a Discharge Pipe 2b Valve 2c Connection Pipe 2d Discharge Pipe 2e Valve 3 First Tank 3A Oil Content Adsorption Cartridge 3a Connection Pipe 3V First Valve 4 Second tank 4A Filter 4V Second valve 5a, 5b Oil / water interface sensor 6 Coarse grain plate 7 Coarse grain filter 7a Outlet filter 8 Valve 9 Flange for connection
10 discharge pipe
11 Drain pipe
11a Piping
12 Switching valve
13 Washing water introduction pipe A Water flow direction B Oil grain W Water to be treated

Claims (4)

油分を含む被処理水を導入し通過させて上記油分の捕捉分離を行う第1タンクと、同第1タンクを通過した被処理水を導入し通過させて残余の油分の捕捉分離を行う第2タンクとを備え、上記第1タンクには、予め繊維材に水分を含ませて同繊維材を圧縮充填した油分吸着用カートリッジが交換可能に設けられるとともに、上記第2タンクには上記被処理水中の残余の油分を捕捉するための微小メッシュのフィルターが装填されていることを特徴とする、油水分離装置。   A first tank that introduces and passes through the water to be treated containing oil and captures and separates the oil, and a second tank that introduces and passes the water to be treated that has passed through the first tank and captures and separates the remaining oil. An oil-adsorbing cartridge in which moisture is preliminarily contained in the fiber material and compressed and filled with the fiber material, and the second tank is provided with a replaceable water in the first tank. An oil-water separator, which is equipped with a fine mesh filter for capturing the remaining oil. 上記繊維材が脱脂綿であることを特徴とする、請求項1に記載の油水分離装置。   The oil-water separator according to claim 1, wherein the fiber material is absorbent cotton. 上記フィルターが膜分離型フィルターとして構成されて、同フィルターのメッシュが0.1〜5ミクロンに設定されるとともに、同フィルターを逆流により洗浄するための配管が施されていることを特徴とする、請求項1または2に記載の油水分離装置。   The filter is configured as a membrane separation filter, the mesh of the filter is set to 0.1 to 5 microns, and piping for cleaning the filter by backflow is provided. The oil-water separator according to claim 1 or 2. 上記第1タンクへ導かれる上記被処理水について同被処理水中の油分を予め減少させておくための前処理装置を備え、同前処理装置が、初めに上記被処理水中の油分の粗分離を粗粒化板により行う第1前処理タンクと、同第1前処理タンクを通過した上記被処理水を導いて同被処理水中の油分の造塊分離を粗粒化フィルターにより行う第2前処理タンクとで構成されたことを特徴とする、請求項1〜3のいずれか1つに記載の油水分離装置。
A pretreatment device is provided for preliminarily reducing the oil content in the treated water with respect to the treated water guided to the first tank, and the pretreatment device first performs rough separation of the oil content in the treated water. A first pretreatment tank that uses a coarse grained plate and a second pretreatment that guides the water to be treated that has passed through the first pretreatment tank and that separates the agglomerates of oil in the treated water using a coarse filter. The oil-water separator according to any one of claims 1 to 3, wherein the oil-water separator is composed of a tank.
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Cited By (7)

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Publication number Priority date Publication date Assignee Title
WO2010139462A2 (en) 2009-06-03 2010-12-09 Hoppal R&D Sa Device for decontamination of aqueous effluent by separation of immiscible phases and germicidal and/or oxidising treatment in order to reduce bod and/or cod
CN102120653A (en) * 2011-01-04 2011-07-13 西安皓海嘉水处理科技有限责任公司 Treatment device and method of low-permeability high-salt oil field extracted wastewater
WO2015156118A1 (en) * 2014-04-11 2015-10-15 住友電気工業株式会社 Oil-water separation treatment system and oil-water separation treatment method
WO2016092643A1 (en) * 2014-12-10 2016-06-16 住友電気工業株式会社 Oil-water separation system, oil-water separation method, and spiral separation membrane element
JP2018525215A (en) * 2015-07-24 2018-09-06 ベコー テヒノロギース ゲーエムベーハーBeko Technologies Gmbh Oil / water separator with compressed air supply
JP2021137702A (en) * 2020-03-03 2021-09-16 住友金属鉱山株式会社 Oil separator and refining method of scandium using the same
JP7464905B2 (en) 2020-03-03 2024-04-10 住友金属鉱山株式会社 Oil-water separation device and method for refining scandium using the same

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JPH08206404A (en) * 1995-02-06 1996-08-13 Nok Corp Oil/water separator
JP2004098047A (en) * 2002-07-19 2004-04-02 Heisei Takara Shokai:Kk Apparatus for purifying/regenerating oil-containing waste treating liquid

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JPS5432869A (en) * 1977-08-19 1979-03-10 Nippon Esu Aaru Esu Kk Deeoiler
JPS6230506A (en) * 1985-07-31 1987-02-09 Toshiba Corp Filter apparatus
JPH06269606A (en) * 1993-03-17 1994-09-27 Tokyo Yogyo Co Ltd Filtration adsorber
JPH08206404A (en) * 1995-02-06 1996-08-13 Nok Corp Oil/water separator
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010139462A2 (en) 2009-06-03 2010-12-09 Hoppal R&D Sa Device for decontamination of aqueous effluent by separation of immiscible phases and germicidal and/or oxidising treatment in order to reduce bod and/or cod
CN102120653A (en) * 2011-01-04 2011-07-13 西安皓海嘉水处理科技有限责任公司 Treatment device and method of low-permeability high-salt oil field extracted wastewater
WO2015156118A1 (en) * 2014-04-11 2015-10-15 住友電気工業株式会社 Oil-water separation treatment system and oil-water separation treatment method
WO2016092643A1 (en) * 2014-12-10 2016-06-16 住友電気工業株式会社 Oil-water separation system, oil-water separation method, and spiral separation membrane element
JP2018525215A (en) * 2015-07-24 2018-09-06 ベコー テヒノロギース ゲーエムベーハーBeko Technologies Gmbh Oil / water separator with compressed air supply
JP2021137702A (en) * 2020-03-03 2021-09-16 住友金属鉱山株式会社 Oil separator and refining method of scandium using the same
JP7464905B2 (en) 2020-03-03 2024-04-10 住友金属鉱山株式会社 Oil-water separation device and method for refining scandium using the same

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