JP3700471B2 - Oil content treatment plant and oil content treatment method - Google Patents

Oil content treatment plant and oil content treatment method Download PDF

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Publication number
JP3700471B2
JP3700471B2 JP14960499A JP14960499A JP3700471B2 JP 3700471 B2 JP3700471 B2 JP 3700471B2 JP 14960499 A JP14960499 A JP 14960499A JP 14960499 A JP14960499 A JP 14960499A JP 3700471 B2 JP3700471 B2 JP 3700471B2
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tank
oil
water
mixed
separation
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JP2000334436A (en
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公明 阪本
宏治 野口
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Obayashi Corp
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Obayashi Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、例えば、油分処理プラント及びこの油分処理プラントを用いて好適な油分処理方法に関する。
【0002】
【従来の技術】
石油化学工場、石油備蓄施設、その他の油類を取扱う工場において、経年の稼働により油類出し入れ時の散逸や、構造物の損傷部からの漏洩により、油が敷地内地盤中に浸透し、土壌汚染や、地下水汚染の原因となることがある。従って、これらの汚染された跡地を再利用する際には、何らかの浄化対策が不可欠である。
【0003】
この種の浄化対策としては、油分に汚染された土壌を掘削し、また油分が染みついたコンクリートガラなどを破砕撤去し、これを管理型埋立処分場に搬送し、埋立てする方法や、工場用地内に例えばオイルセパレータ施設などの固定式の油分処理施設を構築し、この施設を用いて土壌浄化を行う方法がある。
【0004】
【発明が解決しようとする課題】
しかしながら、前者の埋立て方法にあっては、環境問題や、用地不足などにより、用地そのものの取得が問題となる。また、後者の固定式油分処理施設は、通常はコンクリート構造物であって、これら施設のない場所に新たに建設するとなると、手間と時間が必要であるばかりでなく、建設用地も確保する必要があり、一旦処理を終了した場合の撤去作業も面倒となる。さらに、オイルセパレータ施設による処理方式は、薬剤の添加装置を使用し、その後エアーを投入することによって油分を浮上分離させるため、土砂と油分の分離処理が困難であった。また上層に浮上した油分は、最終的にはオイルマットなどによって吸着していたが、連続処理作業が出来ない欠点があった。
【0005】
本発明は、以上の課題を解決するものであって、仮設設備として設置及び撤去作業が容易で、油分処理及び濁水処理を連続して行えるようにした油分処理プラント及びこの油分処理プラントを用いて好適な油分処理方法を提供するものである。
【0006】
以上の目的を達成するため、本発明の油分処理プラントは、油分混じりの土砂及び水が投入混合される貯槽と、該貯槽から供給される懸濁水を貯留するとともに油水及び泥土分離用の各種薬液が注入混合される薬液処理槽と、該薬液処理槽に接続され薬液処理された混合液を静置状態で一時貯留するとともに油分フロックとなる上層、水層及び下層に沈殿する泥土混じりの濁水に分離する静置槽、及び静置槽の下層に接続された水分分離槽とを備え、前記静置槽の上層より油分フロックを取出し、前記水分分離槽内の水層を中和処理して放流し、残部泥土として除去処理するものであり、前記静置槽及び水分分離槽は、前記薬液処理槽に対して一対配置され、一方の水分分離槽を静置貯留状態とし、他方の水分分離槽を分離処理状態に交互に稼働することを特徴とするものである。従って、本発明によれば、各槽はプレハブ材料等の簡易な構造により構築できるため、設置及び油分除去後の撤去作業が簡単に行え、処理場所に応じて転用できる。また、本発明における前記分離槽は、薬液処理槽に対して一対配置され、配管切替により一方の分離槽を静置貯留状態とし、他方の分離槽を分離処理状態に交互に稼働することによって、連続処理が可能となる。
【0007】
また、本発明の油分処理プラントは、油分混じりの土砂及び水が投入混合される貯槽と、該貯槽から供給される懸濁水を貯留するとともに油水及び泥土分離用の各種薬液が注入混合される薬液処理槽と、該薬液処理槽に接続され薬液処理された混合液を静置状態で一時貯留するとともに油分フロックとなる上層、水層及び下層に沈殿する泥土混じりの濁水に分離する静置槽、及び静置槽の下層に接続された水分分離槽とを備え、前記静置槽の上層より油分フロックを取出し、前記水分分離槽内の水層を中和処理して放流し、残部泥土として除去処理するものである油分処理プラントであって、前記薬液処理貯槽は、アルカリ剤が投入混合される第一区画と、該第一区画からオーバフローしたコロイド化懸濁水を貯留するとともに、凝集剤が投入混合される第二区画と、第三の貯槽からオーバフローした凝集物混合懸濁水を貯留するともに、高分子凝集剤が投入混合される第三区画とに仕切られていることを特徴とするものである。これにより、一つの槽内で薬液処理を順次おこなうことが出来る。
【0008】
また、本発明の油分処理方法は、上記油分処理プラントを用いた油分処理方法であって、油分混じりの懸濁水をコロイド化する工程と、コロイド化された懸濁水を凝集させ、それぞれの比重差により油分、水分及び濁水の三層に分離する工程と、分離されたそれぞれの層を分別回収処理する工程とからなることを特徴とする。従って、本発明方法によれば、従来のオイルセパレータによる方法に比べて、エアーを用いないため、土砂と水の分別回収も可能である。
【0009】
【発明の実施の形態】
以下、本発明の好ましい実施の形態につき、添付図面を参照して詳細に説明する。まず、図1は本発明方法の概略手順を示している。本発明方法では、油分を含む土砂あるいは破砕などにより細粒化されたコンクリートガラなどの建築廃材と水が懸濁した原水を槽内に投入し、次いでアルカリ剤として消石灰を投入し、攪拌操作を行うことで、そのpHを10以上に上げ、コロイド化物質にする。
【0010】
次いで、このコロイド状となった処理液に凝集剤(PAC:ポリ塩化アルミニウム、以下PACと称する)を投入攪拌することで、荷電の中和と物理化学的な吸着により、懸濁液中の固形分を凝集させる。この後、高分子凝集剤、例えばクリフロック(商品名)、ポリアクリル酸ナトリウム、ポリアクリルアミドを投入して攪拌することで、油分または固形分のフロックの結合力の強化により、粒径を拡大させる。
【0011】
以上の処理後は、処理液を静置することで、油分フロックは浮上し、また固形分、すなわち土砂、あるいは破砕コンクリート成分は沈殿し、分離する。分離後は、上層部分の油分を分別回収する。また、沈殿物及び水はさらに沈殿させて、両者を分離する。分離後の水はpH処理により中和し、排水溝などに放流する。また槽内に沈殿した土砂は、水の放流後槽内をさらうなどにより排土する。処理後の土砂は、通常の建設残土と同様な性状であるため、埋立用土砂等として活用することが出来る。
【0012】
図2は以上の手順を具体化するための油分処理プラントの平面図及び側面図、図3は、同処理プラントの詳細なフローシートである。同図において、この処理プラントは、油分が浸透した前述した工場跡などの建設用敷地内に仮設置されるものであって、油分混じりの掘削土砂及び水からなる懸濁液が投入され、これを貯留する貯槽1と、貯槽1の下流側に配置された薬液処理槽2と、薬液処理槽2の下流側に配置された一対の静置槽3と、各静置槽3の下流側に配置された水分分離槽4と、各水分分離槽4の下流に配置された緩衝タンク5と、緩衝タンク5の近傍に配置され、静置槽3で分離された油分フロックを回収する回収槽6及びフロック回収枠7とを備え、配管類を介して上流側から下流側へと連続的かつ直線的に接続されている。
【0013】
また、以上に加え、本実施形態に係る油分処理プラントは、PCAタンク8、高分子高濃度タンク9、同希釈タンク10、同貯留タンク11、希硫酸タンク12、消石灰定量投入装置13など薬液添加のための周辺装置類及び電源、制御盤14が配置されている。
【0014】
以上の各槽及び装置類は図1,2に図示するごとくプレハブ式であり、配管類の接続解体により、それぞれの集合分離が可能であり、処理現場にそれぞれを搬入して配管接続するだけで、簡単に組立て出来る。また、処理が終了したならば、配管を取外すことによって個々に分離して搬出でき、この種の処理を必要とする場所への転用が可能である。
【0015】
貯留槽1内に投入された処理懸濁液は、図3に示すように中央に設けた仕切の下側より下流側に流れ、配管を通じて薬液処理槽2に入り込む。薬液処理槽2は3枚の仕切り堰板15により上流から下流にかけて区画され、それぞれが仕切り堰板15をオーバフローすることで順次上流側から下流側へと流れる。
【0016】
上流に位置する第一の区画内には消石灰定量投入装置15を通じて消石灰が投入され、攪拌用ポンプPにより攪拌混合され、その液性をpH10以上とされることでコロイド状となる。次いで、第二の区画内にはPACが投入され、同じく攪拌用ポンプにより攪拌混合される。さらに第三の区画内には高分子凝集剤が投入され、同じく攪拌用ポンプPにより混合攪拌される。
【0017】
以上の薬液により処理された懸濁液は第四区画より配管を介して静置槽3に導入され、ここに一時ほぼ静止状態に貯留されることで、薬液処理された懸濁液は上層の油分フロックと、水分と土砂が入り混じった懸濁液とに分離される。この静置槽の中央には仕切り堰板16が配置され、その上流側よりオーバフローした表層の油分フロックを多く含む液は順次下流側区画内に入り込み、表面に油分フロックを浮べた状態で蓄積される。
【0018】
また、下流側区画の液面近くには回収板17が配置され、回収板17を通じて油分フロックを回収槽6及びフロック回収枠7側に供給し、ここに回収される。なお、符号18は下流側区画の水面に浮べた油分吸着用のオイルシートである。さらに、下流側区画の下層側は、配管を通じて水分分離槽4に接続され、下層に溜った土砂混じりの懸濁水を水分分離槽4に供給される。
【0019】
水分分離槽4は多孔板19で二つの区画に仕切られ、その上流側区画にはpH計20が、下流側区画には攪拌装置21が配置されているとともに、希硫酸タンク12から希硫酸が投入され、液性を中和するようになっている。この中和により、懸濁状態から土砂は凝集沈殿し、槽内の底部に堆積する。また上澄み、すなわち中和水は緩衝タンク5を介して外部に放流される。なお、この緩衝タンク5にも仕切り堰板22及びpH計23が設けられ、放流直前の最終チェックを行っている。
【0020】
また、以上の水分分離槽4での中和処理及び底部に溜った泥土の排土作業はバッチ式で行わなけれており、そのため、薬液処理槽2に接続される静置槽3及び分離槽4を二系統とし、一方のバッチ処理を行っている間は配管を他方側に切替えることで、連続操業を可能としている。
【0021】
【発明の効果】
以上の説明により明らかなように、本発明による油分処理プラントにあっては、仮設設備として設置及び撤去作業が容易で、油分処理及び濁水処理を連続して行うことができる。また、本発明の油分処理方法では、エアーによる懸濁液の攪拌がないため、油分分離後に水分と泥土も分離回収できる。
【図面の簡単な説明】
【図1】本発明方法の処理手順の概略を示すフローチャートである。
【図2】同処理手順を適用した本発明の油分処理プラントの平面及び側面図である。
【図3】同処理プラントの詳細なフローシートである。
【符号の説明】
1 貯槽
2 薬液処理槽
3 静置槽
4 水分分離槽
8 PACタンク
9 高分子高濃度タンク
10 希釈タンク
11 貯留タンク
12 希硫酸タンク
13 消石灰定量供給装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an oil content processing plant and an oil content processing method suitable for use with the oil content processing plant, for example.
[0002]
[Prior art]
In petrochemical factories, oil storage facilities, and other factories that handle oil, the oil permeates into the ground in the site due to dissipation during the operation of oil over time and leakage from damaged parts of the structure. Contamination and groundwater contamination may occur. Therefore, some remedial measures are indispensable when reusing these contaminated sites.
[0003]
This type of purification includes excavating soil that is contaminated with oil, crushing and removing concrete rags that are soaked in oil, transporting them to a managed landfill site, landfilling, etc. For example, there is a method of building a fixed oil treatment facility such as an oil separator facility and performing soil purification using this facility.
[0004]
[Problems to be solved by the invention]
However, in the former landfill method, the acquisition of the site itself becomes a problem due to environmental problems or lack of site. In addition, the latter fixed oil treatment facility is usually a concrete structure, and when it is newly constructed in a place without these facilities, it is necessary not only for labor and time but also to secure a construction site. Yes, once the process is completed, the removal work becomes troublesome. Furthermore, the treatment method by the oil separator facility uses a chemical addition device and then introduces air to float and separate the oil, so that it is difficult to separate the earth and sand from the oil. In addition, although the oil component floating on the upper layer was finally adsorbed by an oil mat or the like, there was a drawback that continuous processing work could not be performed.
[0005]
The present invention solves the above-described problems, and uses an oil component treatment plant and an oil component treatment plant that can be easily installed and removed as temporary equipment, and can continuously perform oil component treatment and muddy water treatment. A suitable oil content processing method is provided.
[0006]
In order to achieve the above object, the oil treatment plant of the present invention comprises a storage tank into which soil and sand mixed with oil are introduced and mixed, and suspension water supplied from the storage tank and various chemicals for separating oil and mud. Into the turbid water mixed with mud that settles in the upper layer, the water layer and the lower layer that are temporarily stored in a stationary state and are oily flocs A stationary tank to be separated, and a water separation tank connected to a lower layer of the stationary tank, and an oil floc is taken out from the upper layer of the stationary tank, and the water layer in the moisture separation tank is neutralized and discharged. and state, and are not to remove process the balance mud, the electrostatic置槽and water separation tank, a pair arranged relative to the chemical treatment bath, one water separating tank to the static置貯cut state, the other water separation Alternate tanks to separate processing And it is characterized in work to Rukoto. Therefore, according to the present invention, each tank can be constructed with a simple structure such as a prefabricated material, so that the installation and removal work after oil removal can be easily performed, and can be diverted depending on the processing place. In addition, the separation tank in the present invention is arranged in a pair with respect to the chemical treatment tank, and by switching one pipe, the one separation tank is placed in a stationary storage state, and the other separation tank is operated alternately in the separation treatment state. Continuous processing is possible.
[0007]
The oil treatment plant of the present invention is a chemical solution in which earth and sand mixed with oil and water are charged and mixed, and suspended water supplied from the storage tank is stored and various chemicals for separating oil and mud are injected and mixed. A stationary tank that separates the turbid water mixed with mud that settles in the treatment tank and the chemical liquid treatment tank connected to the chemical liquid treatment tank and temporarily stores the liquid mixture in a stationary state and becomes an oily floc; And a water separation tank connected to the lower layer of the stationary tank, take out the oil floc from the upper layer of the stationary tank, discharge the neutralized water layer in the moisture separation tank, and remove it as the remaining mud a oil treatment plant is intended to be processed, the chemical processing reservoir comprises a first compartment alkaline agent is introduced mixed with storing the colloid suspension water overflowed from the first compartment, flocculant throw A second compartment to be mixed together to store the aggregate mixture suspended water overflows from the third tank, characterized in that it partitioned into the third compartment polymer flocculant is introduced mixed is there. Thereby , a chemical | medical solution process can be performed sequentially in one tank.
[0008]
Further, the oil content treatment method of the present invention is an oil content treatment method using the above oil content treatment plant , the step of colloiding the suspension water mixed with the oil content, and agglomerating the colloidal suspension water, the specific gravity difference of each Is characterized by comprising a step of separating oil, water and turbid water into three layers and a step of separating and collecting each separated layer. Therefore, according to the method of the present invention, compared with the conventional method using an oil separator, since air is not used, it is possible to separate and collect earth and sand and water.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. First, FIG. 1 shows a schematic procedure of the method of the present invention. In the method of the present invention, building waste materials such as soil containing sand containing oil, or concrete galvanized by crushing, and raw water in which water is suspended are placed in a tank, and then slaked lime is added as an alkaline agent, followed by a stirring operation. By doing so, the pH is raised to 10 or more to make a colloidal material.
[0010]
Next, a flocculant (PAC: polyaluminum chloride, hereinafter referred to as PAC) is added to the colloidal treatment liquid and stirred, so that solids in the suspension are obtained by neutralization of charge and physicochemical adsorption. Aggregate the minutes. Thereafter, a polymer flocculant such as Cliff Rock (trade name), sodium polyacrylate, polyacrylamide is added and stirred to increase the particle size by strengthening the binding force of oil or solid floc. .
[0011]
After the above treatment, the treatment liquid is allowed to stand to float the oil floc, and solids, that is, earth and sand or crushed concrete components are precipitated and separated. After separation, the oil in the upper layer is separated and recovered. Further, the precipitate and water are further precipitated to separate them. The separated water is neutralized by pH treatment and discharged into a drain. In addition, the sediment that has settled in the tank is drained by draining the tank after the water is discharged. Since the soil after treatment has the same properties as ordinary construction residual soil, it can be used as landfill sand.
[0012]
FIG. 2 is a plan view and a side view of the oil processing plant for embodying the above procedure, and FIG. 3 is a detailed flow sheet of the processing plant. In this figure, this treatment plant is temporarily installed in a construction site such as the above-mentioned factory ruins where oil has permeated, and a suspension of excavated soil and water mixed with oil is introduced. Are stored in the storage tank 1, the chemical treatment tank 2 disposed downstream of the storage tank 1, the pair of stationary tanks 3 disposed downstream of the chemical treatment tank 2, and the downstream of each stationary tank 3. The arranged water separation tank 4, the buffer tank 5 arranged downstream of each water separation tank 4, and the collection tank 6 arranged in the vicinity of the buffer tank 5 and collecting the oil content floc separated in the stationary tank 3. And a flock collection frame 7, which are continuously and linearly connected from the upstream side to the downstream side via piping.
[0013]
In addition to the above, the oil processing plant according to the present embodiment includes a chemical solution addition such as the PCA tank 8, the polymer high-concentration tank 9, the dilution tank 10, the storage tank 11, the dilute sulfuric acid tank 12, and the slaked lime metering device 13. Peripheral devices and power supply for the control, and the control panel 14 are arranged.
[0014]
The above tanks and devices are prefabricated as shown in FIGS. 1 and 2 and can be separated from each other by connecting and disassembling the pipes. Easy to assemble. Further, when the processing is completed, the pipes can be removed and removed separately, and can be diverted to a place that requires this type of processing.
[0015]
As shown in FIG. 3, the processing suspension charged into the storage tank 1 flows downstream from the lower side of the partition provided at the center, and enters the chemical processing tank 2 through the piping. The chemical treatment tank 2 is partitioned from the upstream side to the downstream side by the three partition dam plates 15, and each of them sequentially flows from the upstream side to the downstream side by overflowing the partition dam plate 15.
[0016]
In the first compartment located upstream, slaked lime is charged through the slaked lime quantitative charging device 15 and stirred and mixed by the stirring pump P, and the liquid property is adjusted to pH 10 or more, so that it becomes colloidal. Next, PAC is introduced into the second compartment, and is similarly stirred and mixed by the stirring pump. Further, a polymer flocculant is charged into the third compartment, and mixed and stirred by the stirring pump P.
[0017]
The suspension treated with the above chemical solution is introduced into the stationary tank 3 from the fourth section through a pipe, and temporarily stored in a substantially stationary state, whereby the suspension treated with the chemical solution is an upper layer. It is separated into an oily floc and a suspension containing water and earth and sand. A partition weir plate 16 is disposed in the center of the stationary tank, and a liquid containing a large amount of surface oil floc overflowing from the upstream side sequentially enters the downstream compartment and accumulates with the oil floc floating on the surface. The
[0018]
Further, a recovery plate 17 is disposed near the liquid level in the downstream section, and the oil component flock is supplied to the recovery tank 6 and the flock recovery frame 7 side through the recovery plate 17 and recovered there. Reference numeral 18 denotes an oil sheet for adsorbing oil that floats on the water surface in the downstream section. Furthermore, the lower layer side of the downstream section is connected to the water separation tank 4 through a pipe, and suspended water mixed with earth and sand collected in the lower layer is supplied to the water separation tank 4.
[0019]
The water separation tank 4 is divided into two compartments by a perforated plate 19, a pH meter 20 is arranged in the upstream compartment, a stirrer 21 is arranged in the downstream compartment, and dilute sulfuric acid is supplied from the dilute sulfuric acid tank 12. The liquid is neutralized. By this neutralization, the earth and sand are coagulated from the suspended state and deposited on the bottom of the tank. Further, the supernatant, that is, the neutralized water is discharged to the outside through the buffer tank 5. The buffer tank 5 is also provided with a partition weir plate 22 and a pH meter 23 to perform a final check immediately before discharge.
[0020]
Moreover, the neutralization process in the above-mentioned water separation tank 4 and the soil removal work of the mud accumulated at the bottom have not been carried out in a batch manner. Is made into two systems, and while one batch processing is being performed, the piping is switched to the other side, thereby enabling continuous operation.
[0021]
【The invention's effect】
As is apparent from the above description, the oil treatment plant according to the present invention can be easily installed and removed as a temporary facility, and can perform oil treatment and muddy water treatment continuously. In the oil treatment method of the present invention, since the suspension is not stirred by air, moisture and mud can be separated and recovered after oil separation.
[Brief description of the drawings]
FIG. 1 is a flowchart showing an outline of a processing procedure of a method of the present invention.
FIG. 2 is a plan view and a side view of an oil content processing plant of the present invention to which the processing procedure is applied.
FIG. 3 is a detailed flow sheet of the processing plant.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Storage tank 2 Chemical treatment tank 3 Stationary tank 4 Moisture separation tank 8 PAC tank 9 High polymer concentration tank 10 Dilution tank 11 Storage tank 12 Dilute sulfuric acid tank 13 Slaked lime fixed quantity supply apparatus

Claims (3)

油分混じりの土砂及び水が投入混合される貯槽と、該貯槽から供給される懸濁水を貯留するとともに油水及び泥土分離用の各種薬液が注入混合される薬液処理槽と、該薬液処理槽に接続され薬液処理された混合液を静置状態で一時貯留するとともに油分フロックとなる上層、水層及び下層に沈殿する泥土混じりの濁水に分離する静置槽、及び静置槽の下層に接続された水分分離槽とを備え、
前記静置槽の上層より油分フロックを取出し、前記水分分離槽内の水層を中和処理して放流し、残部泥土として除去処理するものであり、
前記静置槽及び水分分離槽は、前記薬液処理槽に対して一対配置され、一方の水分分離槽を静置貯留状態とし、他方の水分分離槽を分離処理状態に交互に稼働することを特徴とする油分処理プラント。
A storage tank into which soil and sand mixed with oil are mixed, a chemical treatment tank for storing suspension water supplied from the storage tank and injecting and mixing various chemicals for oil and mud separation, and a connection to the chemical treatment tank The liquid mixture that has been treated with chemicals is temporarily stored in a stationary state and is separated into muddy water mixed with mud that settles in an upper layer, an aqueous layer, and a lower layer that become oily flocs, and connected to a lower layer of the stationary tank A water separation tank,
Wherein from the upper layer of the electrostatic置槽extraction of oil flocs, and released by neutralizing the aqueous layer of the water separation tank state, and are not to remove process the balance mud,
The electrostatic置槽and water separation tank, a pair arranged relative to the chemical treatment bath, one water separating tank to the static置貯distillation conditions, that you run alternately the other water separation tank for the separation processing state A characteristic oil processing plant.
油分混じりの土砂及び水が投入混合される貯槽と、該貯槽から供給される懸濁水を貯留するとともに油水及び泥土分離用の各種薬液が注入混合される薬液処理槽と、該薬液処理槽に接続され薬液処理された混合液を静置状態で一時貯留するとともに油分フロックとなる上層、水層及び下層に沈殿する泥土混じりの濁水に分離する静置槽、及び静置槽の下層に接続された水分分離槽とを備え、
前記静置槽の上層より油分フロックを取出し、前記水分分離槽内の水層を中和処理して放流し、残部泥土として除去処理するものである油分処理プラントであって、
前記薬液処理貯槽は、アルカリ剤が投入混合される第一区画と、該第一区画からオーバフローしたコロイド化懸濁水を貯留するとともに、凝集剤が投入混合される第二区画と、第三の貯槽からオーバフローした凝集物混合懸濁水を貯留するともに、高分子凝集剤が投入混合される第三区画とに仕切られていることを特徴とする油分処理プラント。
A storage tank into which soil and sand mixed with oil are mixed, a chemical treatment tank for storing suspension water supplied from the storage tank and injecting and mixing various chemicals for oil and mud separation, and a connection to the chemical treatment tank The liquid mixture that has been treated with chemicals is temporarily stored in a stationary state and is separated into muddy water mixed with mud that settles in an upper layer, an aqueous layer, and a lower layer that become oily flocs, and connected to a lower layer of the stationary tank A water separation tank,
An oil content processing plant that takes out the oil floc from the upper layer of the stationary tank, neutralizes and discharges the water layer in the water separation tank, and removes it as a residual mud,
The chemical treatment storage tank includes a first section into which an alkaline agent is charged and mixed, a second section into which a coagulant is charged and mixed while storing colloidal suspension water overflowed from the first section, and a third storage tank. The oil content processing plant is characterized in that the agglomerate mixed suspension water overflowing from the tank is stored and partitioned into a third section into which the polymer flocculant is charged and mixed.
請求項1または2に記載の油分処理プラントを用いた油分処理方法であって、
油分混じりの土砂懸濁水をコロイド化する工程と、コロイド化された懸濁水を凝集させてそれぞれの比重差により油分、水分及び濁水の三層に分離する工程と、分離されたそれぞれの層を分別回収処理する工程とからなることを特徴とする油分処理方法。
An oil content processing method using the oil content processing plant according to claim 1 or 2,
Colloidalization of oil-mixed sediment suspension water, agglomeration of colloidal suspension water and separation into three layers of oil, moisture and turbid water by each specific gravity difference, and separation of each separated layer An oil content processing method comprising a step of collecting and processing.
JP14960499A 1999-05-28 1999-05-28 Oil content treatment plant and oil content treatment method Expired - Fee Related JP3700471B2 (en)

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