JP2001269659A - Treatment method of soil contaminated with oil - Google Patents

Treatment method of soil contaminated with oil

Info

Publication number
JP2001269659A
JP2001269659A JP2000087350A JP2000087350A JP2001269659A JP 2001269659 A JP2001269659 A JP 2001269659A JP 2000087350 A JP2000087350 A JP 2000087350A JP 2000087350 A JP2000087350 A JP 2000087350A JP 2001269659 A JP2001269659 A JP 2001269659A
Authority
JP
Japan
Prior art keywords
soil
oil
particles
contaminated
oily components
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.)
Pending
Application number
JP2000087350A
Other languages
Japanese (ja)
Inventor
Akio Tango
堯雄 反後
Hiroshi Ito
洋 伊藤
Kenji Kawaguchi
謙治 川口
Yutaka Shinoda
豊 信太
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.)
Shinroku Seiki KK
Yoyu Shigen KK
Kumagai Gumi Co Ltd
Original Assignee
Shinroku Seiki KK
Yoyu Shigen KK
Kumagai Gumi Co Ltd
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 Shinroku Seiki KK, Yoyu Shigen KK, Kumagai Gumi Co Ltd filed Critical Shinroku Seiki KK
Priority to JP2000087350A priority Critical patent/JP2001269659A/en
Publication of JP2001269659A publication Critical patent/JP2001269659A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To efficiently separate and remove oily components from a soil contaminated with oil. SOLUTION: The soil contaminated with oily components are made fine grains by a fine grinning device 20 and after the oily components sticking to the surfaces of the soil particles of the soil contaminated with oil are separated from the soil particles, the particles are supplied to a liquid cyclone 41 where the oily components are removed. The soil particles of large grain sizes which are discharged from the lower discharge port of the liquid cyclone 4 and from which the oily components are removed, are classified by a classifying device, such as a vibration screen 43 or dehydrating vibration screen 44.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、油性分で汚染され
た土壌から油性分を効率的に分離する方法に関するもの
である。
The present invention relates to a method for efficiently separating oily components from soil contaminated with oily components.

【0002】[0002]

【従来の技術】海難事故等により海に流出した原油で汚
染された海浜の土壌や、原油存在地盤のトンネル掘削に
伴い搬出される掘削土には原油が付着して汚染されてい
るため、その処理が困難となることがしばしばある。従
来、このような油汚染土壌は、処理場に集積され、薬品
処理等により油性分を凝縮固化したのち、最終処分場に
廃棄されていた。
2. Description of the Related Art Crude oil adheres to and contaminates beach soil contaminated with crude oil spilled into the sea due to a marine accident and excavated soil carried out in connection with the excavation of a tunnel in the ground where crude oil exists. Processing is often difficult. Conventionally, such oil-contaminated soil has been accumulated in a treatment plant, and after condensing and solidifying oily components by chemical treatment or the like, it has been disposed of at a final disposal site.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記処
理方法では、処理に手間がかかるうえ、処理土壌の廃棄
量が多くなってしまうといった問題点があった。そこ
で、このような油汚染土壌から油性分を除去し、油汚染
土壌に含まれている礫,砂,微粒分等を抽出して再利用
する技術の確立が望まれている。
However, the above-mentioned treatment method has problems that the treatment is troublesome and the disposal amount of the treated soil is increased. Therefore, it is desired to establish a technology for removing oily components from such oil-contaminated soil, extracting gravel, sand, fine particles, and the like contained in the oil-contaminated soil for reuse.

【0004】本発明は、従来の問題点に鑑みてなされた
もので、油汚染土壌から油性分を効率的に分離して除去
し、更に、上記油性分が分離された無害な土粒子を再利
用することのできる油汚染土壌の処理方法を提供するこ
とを目的とする。
The present invention has been made in view of the conventional problems, and efficiently separates and removes oily components from oil-contaminated soil, and further recycles the harmless soil particles from which the oily components have been separated. An object of the present invention is to provide a method for treating oil-contaminated soil that can be used.

【0005】[0005]

【課題を解決するための手段】本発明の請求項1に記載
の油汚染土壌の処理方法は、油性分で汚染された土壌を
処理空隙内に投入し、加水しながら、上記土壌の土粒子
に圧縮及び粒子相互間の擦り合わせの力を作用させて、
上記土壌を細粒化するとともに、上記土粒子の表面に付
着している油性分を上記土粒子から分離する細粒化装置
により上記土壌を細粒化した後、上記細粒化装置から排
出されたスラリーを液体サイクロンに供給して、上記油
成分を除去するようにしたことを特徴とする。
According to a first aspect of the present invention, there is provided a method for treating oil-contaminated soil, wherein the soil contaminated with an oily component is introduced into a treatment space, and water is added thereto while adding water. By applying the force of compression and rubbing between particles,
After the soil is refined, the soil is refined by a refiner that separates oily components attached to the surface of the soil particles from the soil particles, and then discharged from the refiner. The slurry is supplied to a liquid cyclone to remove the oil component.

【0006】請求項2に記載の油汚染土壌の処理方法
は、液体サイクロンの後段に、液体サイクロンの下部排
出口から排出される粒径の大きな土粒子を分級する分級
手段を設け、上記土粒子を分級したことを特徴とする。
According to a second aspect of the present invention, in the method for treating oil-contaminated soil, a classifying means is provided downstream of the hydrocyclone for classifying soil particles having a large particle diameter discharged from a lower discharge port of the hydrocyclone. Is classified.

【0007】[0007]

【発明の実施の形態】以下、本発明の実施の形態につい
て、図面に基づき説明する。図1は、本発明の実施の形
態に係わる油汚染土壌の処理システムの処理フローを示
す図で、この油汚染土壌の処理システムは、油汚染土壌
を細粒化装置20に投入して土粒子の表面に付着してい
る油性分を分離した後、分級手段40により、上記細粒
化装置20から排出されたスラリーを分級し、油汚染土
壌に含まれている礫,砂,微粒分等を抽出して再利用で
きるようにしたものである。図1において、20は受け
入れホッパ11を介して投入された油汚染土壌に加水し
ながら、上記油汚染土壌の土粒子に圧縮及び粒子相互間
の擦り合わせの力を作用させて、上記土壌を細粒化する
とともに、上記土粒子の表面に付着している油性分を上
記土粒子から分離して処理水中に浮遊させる細粒化装
置、30は上記細粒化装置20から排出されたスラリー
を一時貯蔵するとともに、上記スラリーを分級手段40
の液体サイクロン41に供給するための液体供給槽(以
下、フィードサンプという)、40は液体サイクロン4
1,振動スクリーン43,脱水振動スクリーン44等の
分級装置を備え、上記フィードサンプ30から供給され
る中に含まれる土粒子を種々の大きさの土粒子に分級す
る分級手段、50は上記分級手段40から排出される油
性分を含んだ処理水を浄化する水処理部、60は上記細
粒化装置20やフィードサンプ30に処理水を供給する
給水部である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a diagram showing a processing flow of an oil-contaminated soil treatment system according to an embodiment of the present invention. After separating the oily component adhering to the surface of the oil, the slurry discharged from the fine-granulating device 20 is classified by the classification means 40 to remove the gravels, sand, fine particles, etc. contained in the oil-contaminated soil. It can be extracted and reused. In FIG. 1, reference numeral 20 denotes a method of compressing and rubbing between soil particles of the oil-contaminated soil while adding water to the oil-contaminated soil input through the receiving hopper 11, thereby finely dividing the soil. A fine-granulating device which granulates and separates oily substances adhering to the surface of the above-mentioned soil particles from the above-mentioned soil particles and floats them in treated water. While storing, the slurry is classified
A liquid supply tank (hereinafter, referred to as a feed sump) for supplying the liquid cyclone 41 with the liquid cyclone 4.
1, a classifying device including a classifying device such as a vibrating screen 43, a dewatering vibrating screen 44, and the like, classifying means for classifying soil particles contained in the material supplied from the feed sump 30 into soil particles of various sizes; A water treatment section for purifying treated water containing oily components discharged from 40, and a water supply section 60 for supplying treated water to the granulating device 20 and the feed sump 30.

【0008】図2(a)は細粒化装置20の構成を示す
図で、(b)図は(a)図のA−A断面図である。細粒
化装置20は、内周面に軸方向に沿って取付けられ、中
心方向に突出する複数の外羽根1Wを有する円筒状の回
転ドラム1と、外周面に軸方向に沿って取付けられ、径
方向に突出する複数の内羽根2Wを有し、上記回転ドラ
ム1の内部に偏心して取付けられたロータ2とを備え、
回転ドラム1の外周に設けられた環状歯車3をモータ4
により、ロータ2に取付けられた回転軸5を駆動機構6
により、それぞれ互いに逆方向に回転させ、細粒化装置
20の材料投入口7に投入された処理材料である油汚染
土壌に圧縮及びすべり応力を作用させ、塊状となった土
粒子を、ほぼ独立した粒子に分離して細粒化するととも
に、上記細粒化された土粒子に対して、主に粒子相互間
の擦り合わせの力を作用させて、粒子同士の摩擦による
相互研磨を行わせ、上記土粒子の表面に付着している油
性分等の異物を分離するものである。なお、上記処理材
料に作用する応力の大きさは、主に、回転ドラム1とロ
ータ2との間隔(ロータ2の偏心度)と、回転ドラム1
及びロータ2のそれぞれの回転速度により調整する。
FIG. 2A is a view showing the configuration of the grain refiner 20, and FIG. 2B is a sectional view taken along line AA of FIG. The grain refiner 20 is attached to the inner peripheral surface along the axial direction, and is attached to the cylindrical rotary drum 1 having a plurality of outer blades 1W protruding in the center direction, and attached to the outer peripheral surface along the axial direction, A rotor 2 having a plurality of radially projecting inner blades 2W and eccentrically mounted inside the rotary drum 1;
The ring gear 3 provided on the outer periphery of the rotary drum 1 is
As a result, the rotating shaft 5 attached to the rotor 2 is
Respectively, thereby rotating the oil contaminated soil, which is the processing material charged into the material input port 7 of the grain refiner 20, in a direction opposite to each other, and exerting a compressive and sliding stress on the oil-contaminated soil. Separated into fine particles and refined, the finely-divided soil particles, by mainly applying the force of rubbing between the particles, to perform mutual polishing by friction between the particles, It is for separating foreign substances such as oily substances adhering to the surface of the soil particles. The magnitude of the stress acting on the processing material mainly depends on the distance between the rotating drum 1 and the rotor 2 (the eccentricity of the rotor 2) and the rotating drum 1
And the rotation speed of the rotor 2.

【0009】次に、油汚染土壌の処理フローについて説
明する。まず、受け入れホッパ11に投入された油汚染
土壌を、細粒化装置20の材料投入口7に投入する。細
粒化装置20では、給水部60から供給された処理水を
上記油汚染土壌に加水し、上記油汚染土壌の塊状となっ
ている土粒子を細粒化するとともに、上記細粒化された
土粒子の表面に付着している油性分を上記処理水中に浮
遊した状態で離脱させつつ、上記油汚染土壌を下流側に
移動させ、排出口20aから排出する。このとき、上記
油汚染土壌に混入している大型の金属類や挟雑物等の固
形物は、上記排出口20aに設けられた約30mmの捕
獲用の網20bにより捕獲されて除去され、約30mm
以下の土粒子を含むスラリーがフィードサンプ30に送
られる。フィードサンプ30に貯蔵されたスラリー状の
油汚染土壌のうち、底部に貯蔵されている比較的粒径の
大きな粒状体を含むスラリーは、フィードポンプ30P
により分級手段40の液体サイクロン41に送られ分級
される。液体サイクロン41は、筒状の本体内壁に、種
々の大きさの粒状体を含んだ液体を高速で噴射して、上
記液体に含まれる粒径の小さな粒状体を分離する装置
で、上記液体が一次回転流と呼ばれる渦を形成しながら
本体内壁に沿って下部方向に移動する時に、本体の中央
部の気圧が減少し、上記液体が二次回転流と呼ばれる渦
を形成しながら上記一次回転流の内側から本体を上昇す
る現象を利用したものである。すなわち、液体サイクロ
ン41に導入されたスラリーに含まれている粒径の小さ
な粒状体は上記二次回転流に運ばれて本体の上部方向に
移動し、液体サイクロン上部の図示しない上昇管を通っ
て排出される。なお、本実施の形態では、上記上部から
排出された粒径の小さな粒状体を含むスラリーはフィー
ドサンプ30に戻される。一方、上記スラリーに含まれ
ている粒径の大きな粒状体(例えば、74μm以上の粒
状体)は、本体内壁に衝突しながら下方に移動させら
れ、液体の一部とともに図示しない下部排出口から排出
される。
Next, a processing flow of the oil-contaminated soil will be described. First, the oil-contaminated soil put into the receiving hopper 11 is put into the material inlet 7 of the grain refiner 20. In the grain refiner 20, the treated water supplied from the water supply unit 60 is added to the oil-contaminated soil, and the agglomerated soil particles of the oil-contaminated soil are refined. The oily soil adhering to the surface of the soil particles is removed while floating in the treated water, and the oil-contaminated soil is moved downstream and discharged from the outlet 20a. At this time, solids such as large metals and contaminants mixed into the oil-contaminated soil are captured and removed by a capture net 20b of about 30 mm provided at the outlet 20a, and are removed. 30mm
A slurry containing the following soil particles is sent to the feed sump 30. Among the slurry-like oil-contaminated soil stored in the feed sump 30, the slurry containing relatively large-diameter particles stored at the bottom is fed to the feed pump 30P.
Is sent to the hydrocyclone 41 of the classification means 40 and classified. The liquid cyclone 41 is a device that injects liquid containing various-sized particles at a high speed onto the inner wall of a cylindrical main body to separate small-particles having a small particle diameter contained in the liquid. When moving downward along the inner wall of the main body while forming a vortex called a primary rotating flow, the pressure in the center of the main body decreases, and the liquid forms a vortex called a secondary rotating flow while the primary rotating flow moves. This utilizes the phenomenon that the body rises from the inside. That is, the granular material having a small particle diameter contained in the slurry introduced into the hydrocyclone 41 is carried by the secondary rotation flow and moves toward the upper part of the main body, and passes through a rising pipe (not shown) above the hydrocyclone. Is discharged. In the present embodiment, the slurry containing the particulate matter having a small particle diameter discharged from the upper portion is returned to the feed sump 30. On the other hand, the granular material having a large particle diameter (for example, a granular material of 74 μm or more) contained in the slurry is moved downward while colliding with the inner wall of the main body, and is discharged together with a part of the liquid from a lower discharge port (not shown). Is done.

【0010】したがって、液体サイクロン41に投入さ
れたスラリー状の油汚染土壌のうち、細粒化装置で分離
され、処理水中に浮遊している油性分の大部分は、上記
処理水とともにフィードサンプ30に戻され、油性分が
分離された74μm以上の土粒子は、下部排出口からス
ピゴットタンク42に送られた後、分級装置である振動
スクリーン43及び脱水振動スクリーン44に送られ、
種々の大きさの粒状体に分級される。スピゴットタンク
42から送られてきたスラリーから、まず、振動スクリ
ーン43により、5mm以上の礫を主とした粒状体(土
粒子)が篩い分けされ、次に、脱水振動スクリーン44
により、74μm〜5mmの砂礫を主とした粒状体(土
粒子)が分級される。なお、上記脱水振動スクリーン4
4を通過した、約74μm以下の微粒子(シルト分)を
含んだスラリーは、再びフィードサンプ30に戻され
る。
Therefore, of the oil-contaminated soil in the slurry state charged into the liquid cyclone 41, most of the oily components separated by the granulation device and floating in the treated water are supplied to the feed sump 30 together with the treated water. The soil particles of 74 μm or more from which the oily component has been separated are sent to the spigot tank 42 from the lower outlet, and then sent to the vibrating screen 43 and the dewatering vibrating screen 44, which are classification devices,
Classified into granules of various sizes. From the slurry sent from the spigot tank 42, first, a granular material (soil particles) mainly composed of gravel of 5 mm or more is sieved by a vibrating screen 43, and then a dewatering vibrating screen 44
Thereby, a granular material (soil particles) mainly composed of sand and gravel of 74 μm to 5 mm is classified. The dehydration vibrating screen 4
The slurry containing fine particles (silt content) of about 74 μm or less that passed through 4 is returned to the feed sump 30 again.

【0011】一方、油性分の多くが浮遊しているフィー
ドサンプ30の上澄み液は、シックナータンク45に送
られる。シックナータンク45では、油性分と上記約7
4μm以下の微粒子を含んだ処理水をタンク内でゆっく
りと回転させ、粒状体等の固形物を凝集沈殿させる固液
分離を行う。上記シックナータンク45の上澄み液に
は、上述したように、油性分が浮遊しているので、水処
理部50の処理水槽51に送られ処理される。この処理
水槽51では、薬品処理等により上記油性分を凝縮固化
して上記処理液から分離し、液体濾過装置52に送る。
一方、シックナータンク45の底部に沈殿したスラリー
は、スラリータンク46に一時貯蔵される。このスラリ
ーは、油性分が除去されているので、脱水機47に送
り、このスラリーから、図示しないフィルタプレスによ
り脱水ケーキを作製し、最終処分場へ搬出する。また、
脱水機47で脱水された水は、上記処理水槽51で処理
された後、液体濾過装置52に送られる。液体濾過装置
52では、上記処理水を活性炭等の吸着材で濾過して固
化して油性分等を除去して浄化する。この浄化された処
理水は再利用するかあるいは放流し、上記油性分等を吸
着した吸着材は最終処分場に廃棄される。
On the other hand, the supernatant of the feed sump 30 in which much of the oily component is suspended is sent to the thickener tank 45. In the thickener tank 45, the oil content and
The treated water containing fine particles of 4 μm or less is slowly rotated in a tank to perform solid-liquid separation for coagulating and sedimenting solids such as particulates. As described above, the supernatant liquid of the thickener tank 45 contains an oily component, and is sent to the treated water tank 51 of the water treatment section 50 for treatment. In the treated water tank 51, the oily component is condensed and solidified by chemical treatment or the like, separated from the treatment liquid, and sent to the liquid filtration device 52.
On the other hand, the slurry precipitated at the bottom of the thickener tank 45 is temporarily stored in the slurry tank 46. Since the oily component has been removed from the slurry, the slurry is sent to a dehydrator 47, and a dewatered cake is prepared from the slurry by a filter press (not shown) and carried out to a final disposal site. Also,
The water dehydrated by the dehydrator 47 is sent to the liquid filtration device 52 after being treated in the treated water tank 51. In the liquid filtration device 52, the treated water is filtered with an adsorbent such as activated carbon and solidified to remove oily components and purify the treated water. The purified treated water is reused or discharged, and the adsorbent that has adsorbed the oily components is discarded at a final disposal site.

【0012】このように、本実施の形態によれば、細粒
化装置20により、油性分で汚染された土壌を細粒化す
るとともに、油汚染土壌の土粒子の表面に付着している
油性分を上記土粒子から分離した後、液体サイクロン4
1に供給して、上記油成分を除去するようにしたので、
油汚染土壌から油性分を効率的に分離して除去すること
ができる。すなわち、細粒化装置20から排出された油
性分を含むスラリーを分級する際に、例えば振動スクリ
ーンなどの網を用いた分級装置を用いた場合には、上記
油性分が網に付着してしまうため、上記油性分が再び土
粒子に付着してしまうが、液体サイクロン41を用いる
ことにより、比較的質量の小さい油性分を、砂礫等のあ
る程度(例えば、74μm)以上の粒径の粒子から効率
良く分離して排除することができる。更に、上記液体サ
イクロン41の下部排出口から排出される、油性分が除
去された粒径の大きな土粒子を、振動スクリーン43や
脱水振動スクリーン44により分級するようにしたの
で、油汚染土壌から砂礫や細粒砂などの再利用可能な粒
状体を得ることができ、油汚染土壌の減容化を図ること
ができる。
As described above, according to the present embodiment, the soil contaminated by the oily component is refined by the granulating device 20 and the oily soil adhering to the surface of the soil particles of the oil-contaminated soil is reduced. After the separation from the soil particles, the hydrocyclone 4
1 so as to remove the oil component,
The oily component can be efficiently separated and removed from the oil-contaminated soil. In other words, when classifying the slurry containing the oily component discharged from the grain refiner 20, when using a classifier using a net such as a vibrating screen, the oily component adheres to the net. Therefore, the oily component adheres to the soil particles again. However, by using the liquid cyclone 41, the oily component having a relatively small mass can be efficiently removed from particles such as gravel or the like having a particle size of a certain size (for example, 74 μm) or more. It can be well separated and eliminated. Furthermore, since the soil particles having a large particle diameter from which oily components have been removed and discharged from the lower outlet of the liquid cyclone 41 are classified by the vibrating screen 43 or the dewatering vibrating screen 44, sand and gravel are removed from the oil-contaminated soil. And reusable granular material such as fine sand and fine sand can be obtained, and the volume of oil-contaminated soil can be reduced.

【0013】なお、上記実施の形態では、液体サイクロ
ン41の上部から排出された粒径の小さな粒状体を含む
スラリーを、フィードサンプ30に戻すようにしたが、
直接シックナータンク45に送るようにしてもよい。
In the above-described embodiment, the slurry containing the particulate matter having a small particle diameter discharged from the upper part of the liquid cyclone 41 is returned to the feed sump 30.
You may make it send directly to the thickener tank 45.

【0014】[0014]

【発明の効果】以上説明したように、請求項1に記載の
発明によれば、油性分で汚染された土壌を処理空隙内に
投入し、加水しながら、上記土壌の土粒子に圧縮及び粒
子相互間の擦り合わせの力を作用させて、上記土壌を細
粒化するとともに、上記土粒子の表面に付着している油
性分を上記土粒子から分離した後、上記細粒化装置から
排出されたスラリーを液体サイクロンに供給して、上記
油成分を除去するようにしたので、油汚染土壌から油性
分を効率的にかつ確実に分離して除去することができ、
油性分が分離された比較的粒径の大きな土粒子を得るこ
とができる。
As described above, according to the first aspect of the present invention, the soil contaminated with the oily component is put into the treatment space, and is compressed into the soil particles of the soil while adding water. By applying the force of mutual rubbing, the soil is refined, and the oily component attached to the surface of the soil particles is separated from the soil particles, and then discharged from the refiner. The slurry is supplied to a liquid cyclone to remove the oil component, so that oily components can be efficiently and reliably separated and removed from oil-contaminated soil,
Soil particles having a relatively large particle diameter from which oily components have been separated can be obtained.

【0015】請求項2に記載の発明によれば、液体サイ
クロンの後段に、液体サイクロンの下部排出口から排出
される粒径の大きな土粒子を分級する分級手段を設け、
上記土粒子を分級したので、再利用可能な油性分が分離
された土粒子を確実に分級することができるとともに、
油汚染土壌の減容化を実現することができる。
According to the second aspect of the present invention, a classification means is provided downstream of the hydrocyclone for classifying soil particles having a large particle diameter discharged from the lower discharge port of the hydrocyclone,
Since the above-mentioned soil particles have been classified, the reusable oily component can reliably classify the separated soil particles,
Volume reduction of oil-contaminated soil can be realized.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の実施の形態に係わる油汚染土壌の処
理システムの構成と処理フローを示す図である。
FIG. 1 is a diagram showing a configuration and a processing flow of a system for treating oil-contaminated soil according to an embodiment of the present invention.

【図2】 本実施の形態に係わる細粒化装置の構成を示
す図である。
FIG. 2 is a diagram showing a configuration of a grain refiner according to the present embodiment.

【符号の説明】[Explanation of symbols]

1 回転ドラム、1W 外羽根、2 ロータ、2W 内
羽根、3 環状歯車、4 モータ、5 ロータの回転
軸、6 ロータの駆動機構、7 材料投入口、11 受
け入れホッパ、20 細粒化装置、20a 材料排出
口、20b 捕獲用の網、30 フィードサンプ、30
P フィードポンプ、40 分級手段、41 液体サイ
クロン、42 スピゴットタンク、43 振動スクリー
ン、44 脱水振動スクリーン、45 シックナータン
ク、46 スラリータンク、47 脱水機、50 水処
理部、51 処理水槽,52液体濾過装置、60 給水
部。
Reference Signs List 1 rotating drum, 1W outer blade, 2 rotor, 2W inner blade, 3 ring gear, 4 motor, 5 rotor rotating shaft, 6 rotor driving mechanism, 7 material input port, 11 receiving hopper, 20 grain refiner, 20a Material outlet, 20b Capture net, 30 Feed sump, 30
P feed pump, 40 classifying means, 41 liquid cyclone, 42 spigot tank, 43 vibrating screen, 44 dehydrating vibrating screen, 45 thickener tank, 46 slurry tank, 47 dehydrator, 50 water treatment section, 51 treated water tank, 52 liquid filtration device , 60 water supply department.

フロントページの続き (72)発明者 反後 堯雄 東京都新宿区新宿2丁目3番13号 溶融資 源株式会社内 (72)発明者 伊藤 洋 東京都新宿区津久戸町2番1号 株式会社 熊谷組東京本社内 (72)発明者 川口 謙治 東京都新宿区津久戸町2番1号 株式会社 熊谷組東京本社内 (72)発明者 信太 豊 埼玉県大里郡寄居町桜沢265番地 新六精 機株式会社内 Fターム(参考) 4D004 AA32 AA41 AB02 CA01 CA04 CA10 CA13 CA14 CA50 CB09 CB11 CB42 CB43 CB44 CB50 CC03 Continued on the front page (72) Inventor Takao Tango 2-3-13-1 Shinjuku, Shinjuku-ku, Tokyo Melting Resources Co., Ltd. (72) Inventor Hiroshi Ito 2-1 Tsukudo-cho, Shinjuku-ku, Tokyo Kumagaya Co., Ltd. Gumi Tokyo Head Office (72) Inventor Kenji Kawaguchi 2-1 Tsukudo-cho, Shinjuku-ku, Tokyo Kumagaya Gumi Tokyo Head Office (72) Inventor Yutaka Shinta 265 Sakurazawa, Yorii-cho, Osato-gun, Saitama F term (reference) 4D004 AA32 AA41 AB02 CA01 CA04 CA10 CA13 CA14 CA50 CB09 CB11 CB42 CB43 CB44 CB50 CC03

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 油性分で汚染された土壌を処理空隙内に
投入し、加水しながら、上記土壌の土粒子に圧縮及び粒
子相互間の擦り合わせの力を作用させて、上記土壌を細
粒化するとともに、上記土粒子の表面に付着している油
性分を上記土粒子から分離する細粒化装置により上記土
壌を細粒化した後、上記細粒化装置から排出されたスラ
リーを液体サイクロンに供給して、上記油成分を除去す
るようにしたことを特徴とする油汚染土壌の処理方法。
1. A method in which soil contaminated with an oily component is introduced into a treatment space, and the soil particles of the soil are subjected to a compressive force and a rubbing force between the particles while adding water to the soil so that the soil is finely divided. After the soil is finely divided by a fine-granulating device for separating oily components attached to the surface of the soil particles from the soil particles, the slurry discharged from the fine-granulation device is subjected to liquid cyclone A method for treating oil-contaminated soil, wherein the oil component is supplied to the soil to remove the oil component.
【請求項2】 液体サイクロンの後段に、液体サイクロ
ンの下部排出口から排出される粒径の大きな土粒子を分
級する分級手段を設け、上記土粒子を分級したことを特
徴とする請求項1記載の油汚染土壌の処理方法。
2. The method according to claim 1, wherein a classifying means is provided downstream of the hydrocyclone for classifying soil particles having a large particle diameter discharged from a lower discharge port of the hydrocyclone, and the soil particles are classified. Treatment method of oil contaminated soil.
JP2000087350A 2000-03-27 2000-03-27 Treatment method of soil contaminated with oil Pending JP2001269659A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000087350A JP2001269659A (en) 2000-03-27 2000-03-27 Treatment method of soil contaminated with oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000087350A JP2001269659A (en) 2000-03-27 2000-03-27 Treatment method of soil contaminated with oil

Publications (1)

Publication Number Publication Date
JP2001269659A true JP2001269659A (en) 2001-10-02

Family

ID=18603371

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000087350A Pending JP2001269659A (en) 2000-03-27 2000-03-27 Treatment method of soil contaminated with oil

Country Status (1)

Country Link
JP (1) JP2001269659A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100599222B1 (en) * 2004-04-03 2006-07-12 금광개발 주식회사 The process for recovering petroleum-contaminated soil
JP2011255261A (en) * 2010-06-07 2011-12-22 Taihei Sangyo Co Ltd Treatment method of construction sludge and reclaimed sand from construction sludge

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100599222B1 (en) * 2004-04-03 2006-07-12 금광개발 주식회사 The process for recovering petroleum-contaminated soil
JP2011255261A (en) * 2010-06-07 2011-12-22 Taihei Sangyo Co Ltd Treatment method of construction sludge and reclaimed sand from construction sludge

Similar Documents

Publication Publication Date Title
JP6399325B1 (en) Soil purification system
JP4256505B2 (en) How to treat dredged soil
JP6358520B1 (en) Soil purification system
JP6399326B1 (en) Soil purification system
KR20000052354A (en) Method and system for carrying out treatment of granular substances with pollutants adhered
JP4970756B2 (en) Crushing and polishing apparatus and method for treating contaminated soil using this apparatus
JP6027921B2 (en) Treatment method of contaminated soil
JP5912525B2 (en) Cleaning and volume reduction of radioactive material contaminated earth and sand
JP4190669B2 (en) Method and apparatus for processing particulate matter with contaminants attached
JP4338825B2 (en) Fine grain processing method
US6156083A (en) Coal reclamation systems
JP4132413B2 (en) Method for treating particulate matter with contaminants attached
JP2620120B2 (en) Method and apparatus for collecting mud used for mud pressurized shield drilling
JP2001269659A (en) Treatment method of soil contaminated with oil
JP2020065975A (en) Method for recovering dihydrate gypsum from waste gypsum board
JP4335369B2 (en) Method for treating particulate matter with contaminants attached
JP4286990B2 (en) Processing equipment for particulate matter with contaminants
JP2000197878A (en) Apparatus for treating particulate material to which pollutant is adhered
JP4137291B2 (en) Method for treating particulate matter with contaminants attached
JP2001327953A (en) Aggregate for asphalt and production of aggregate for asphalt
JP2005262076A (en) Method for cleaning soil contaminated with oil
JP6678353B2 (en) Soil purification system
JP2002011434A (en) Process and equipment for treating incineration ash
JP6678354B2 (en) Soil purification system
JP6425170B2 (en) Muddy water treatment system and muddy water treatment method

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20061211

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20090126

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090210

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20090609