JP2006116397A - Washing method and washing apparatus of contaminated soil - Google Patents

Washing method and washing apparatus of contaminated soil Download PDF

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JP2006116397A
JP2006116397A JP2004305570A JP2004305570A JP2006116397A JP 2006116397 A JP2006116397 A JP 2006116397A JP 2004305570 A JP2004305570 A JP 2004305570A JP 2004305570 A JP2004305570 A JP 2004305570A JP 2006116397 A JP2006116397 A JP 2006116397A
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sand
soil
earth
contaminants
contaminated soil
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Mitsuo Mori
光男 毛利
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Shimizu Construction Co Ltd
Shimizu Corp
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Shimizu Construction Co Ltd
Shimizu Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a washing method and a washing apparatus of contaminated soil stripping and separating contaminants firmly adhering on surface of earth and sand, and improving quality of washed soil. <P>SOLUTION: In this washing method of contaminated soil, contaminated soil containing toxic contaminants is washed and separated into washed soil and condensed residue containing condensed contaminants, the washed soil is recycled, and the condensed residue is recovered for treatment. The method comprises processes for: adding water to the contaminated soil, classifying it by wet screening to separate gravel and coarse sand to form slurry earth and sand; adding a dispersant to the slurry earth and sand, mixing and agitating to strip the contaminants from the surface of the earth and sand; treating the slurry earth and sand by a hydrocyclone to classify into sand/fine sand and fine particles containing the contaminants; separating metal contaminants by gravity type separation of the classified sand/fine sand; obtaining washed earth and sand through dewatering process of the sand/fine sand and separating separated fine particles into settled sludge and water by coagulation settling; dewatering the settled sludge and separating into the condensed residue and water, to obtain the condensed residue. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、有害な汚染物質を含有する汚染土壌の洗浄方法及びこの洗浄方法に用いられる洗浄装置に関するものであり、特に、鉱物油、多環芳香族炭化水素(PAHs)、重金属、シアン等の有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と汚染物質の濃縮した濃縮残渣とに分離し、洗浄処理土を再利用に供し、濃縮残渣を回収処理に供する汚染土壌の洗浄方法及び洗浄装置に関するものである。   The present invention relates to a method for cleaning contaminated soil containing harmful pollutants and a cleaning device used in this cleaning method, and in particular, mineral oil, polycyclic aromatic hydrocarbons (PAHs), heavy metals, cyan and the like. A method for cleaning contaminated soil in which contaminated soil containing harmful pollutants is washed, separated into washed soil and concentrated residue of pollutants, the treated soil is reused, and the concentrated residue is recovered. And a cleaning apparatus.

一般に、汚染土壌の浄化・修復には、汚染物質の種類によって様々な浄化技術が適用される。浄化コストは、対象とする汚染物質に最も適した浄化技術を選択した場合に最小となる。しかしながら、実際のサイトでは、複数の化学物質(例えば、油と重金属)によって汚染されている場合も多い。このため、低コストで、かつ適用範囲の広い浄化技術が望まれている。   In general, various purification techniques are applied to the purification and repair of contaminated soil depending on the type of the pollutant. The cost of purification is minimized when the most appropriate purification technology is selected for the subject pollutant. However, actual sites are often contaminated with multiple chemicals (eg oil and heavy metals). For this reason, a purification technique with low cost and wide application range is desired.

そのなかでも、土壌洗浄法は、揮発性有機化合物(VOCs)、PCB、農薬、重金属、シアン等の多くの物質に幅広く適用可能であることが報告されている(例えば、非特許文献1参照)。この土壌洗浄技術は、(1)洗浄効率が高い、(2)処理能力が大きい、(3)鉱物油、PAHs、重金属、シアン等の多くの物質に幅広く適用が可能、(4)汚染洗浄処理後の土壌の再利用率が約70%と非常に高いため、低コスト処理が可能といった優れた能力を有している。
田中仁志、毛利光男、熊本進誠、羽田義治、今沢正樹、高効率土壌洗浄プラント(MRP)による汚染土壌の浄化、土壌環境センター技術ニュース、2003年9月、No.7、p.36−38
Among them, it has been reported that the soil washing method is widely applicable to many substances such as volatile organic compounds (VOCs), PCBs, agricultural chemicals, heavy metals, and cyan (see, for example, Non-Patent Document 1). . This soil cleaning technology can be applied to many substances such as (1) high cleaning efficiency, (2) high processing capacity, (3) mineral oil, PAHs, heavy metals, cyanide, etc. (4) Contamination cleaning processing Since the re-use rate of the later soil is as high as about 70%, it has an excellent ability such as low-cost treatment.
Hitoshi Tanaka, Mitsuo Mori, Shinsei Kumamoto, Yoshiharu Haneda, Masaki Imazawa, Purification of Contaminated Soil by High Efficiency Soil Cleaning Plant (MRP), Soil Environment Center Technical News, September 2003, No. 7, p. 36-38

しかしながら、静電気的な相互作用等によって、土砂表面に強固に付着している汚染物質については、非特許文献1に係る土壌洗浄方法によっても、土砂表面から剥離・除去することができず、洗浄処理土に最後まで付着していることが多かった。このため、洗浄処理土の品質が低下するという問題があった。   However, contaminants that are firmly attached to the surface of the earth and sand due to electrostatic interaction or the like cannot be separated or removed from the surface of the earth and sand even by the soil washing method according to Non-Patent Document 1, and the washing process It was often attached to the soil until the end. For this reason, there existed a problem that the quality of the washing process soil fell.

本発明は、上記従来技術の問題点に鑑み、土砂表面に強固に付着している汚染物質を剥離・分離し、洗浄処理土の品質の向上した汚染土壌の洗浄方法及びこの洗浄方法に用いられる洗浄装置を提供することを目的とする。   In view of the above-mentioned problems of the prior art, the present invention is used in a method for cleaning contaminated soil, which peels and separates contaminants firmly attached to the surface of the soil and improves the quality of the cleaned soil, and this cleaning method. An object is to provide a cleaning device.

かかる課題を解決するため、
請求項1にかかる発明は、有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄方法であって、前記汚染土壌に水を添加し、湿式ふるい分級処理して礫・粗砂を分離して、スラリー状の土砂とする工程(A−1)と、このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する工程(A−2)と、このスラリー状の土砂を、ハイドロサイクロン処理して砂・細砂と、汚染物質を含む細粒子とに分級処理する工程(A−3)と、分級処理した前記砂・細砂を重力式分離処理して、さらに金属汚染物質を分離する工程(A−6)と、この砂・細砂を脱水処理する工程(A−7)とを経て、前記洗浄処理土を得ると共に、前記工程(A−3)で分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する工程(B−1)と、この沈殿汚泥を脱水処理し、前記濃縮残渣と水とに分離する工程(B−2)とを経て、前記濃縮残渣を得ることを特徴とする汚染土壌の洗浄方法である。
To solve this problem,
The invention according to claim 1 is for cleaning contaminated soil containing harmful pollutants, separating the soil into wash-treated soil and a concentrated residue obtained by concentrating the pollutants, supplying the washed-treated soil for reuse, and concentrating the soil. A method for cleaning contaminated soil in which a residue is subjected to a recovery process, wherein water is added to the contaminated soil, and wet sieving classification is performed to separate gravel and coarse sand to form slurry-like soil (A-1 ), Adding a dispersant to the slurry-like earth and sand, mixing and stirring, separating the contaminants from the surface of the earth and sand (A-2), and hydrolyzing the slurry-like earth and sand, A step of classifying fine sand and fine particles containing contaminants (A-3), a step of separating the classified sand and fine sand by gravity, and further separating metal contaminants (A- 6) and step (A-7) of dehydrating the sand / fine sand Then, while obtaining the said washing process soil, the process (B-1) which carries out the aggregation precipitation of the said fine particle isolate | separated at the said process (A-3), and isolate | separates it into a precipitated sludge and water, and dehydrates this precipitated sludge. It is the washing | cleaning method of the contaminated soil characterized by obtaining the said concentration residue through the process (B-2) which processes and isolate | separates into the said concentration residue and water.

請求項2にかかる発明は、有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄方法であって、前記汚染土壌に水を添加し、湿式ふるい分級処理して礫・粗砂を分離して、スラリー状の土砂とする工程(A−1)と、このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する工程(A−2)と、このスラリー状の土砂を、ハイドロサイクロン処理して砂・細砂と、汚染物質を含む細粒子とに分級処理する工程(A−3)と、分級処理した前記砂・細砂に捕集剤を添加して混合・攪拌する工程(A−4)と、混合・攪拌した前記砂・細砂を、泡浮遊式分離処理して汚染物質を分離する工程(A−5)と、分離した前記砂・細砂を重力式分離処理して、さらに金属汚染物質を分離する工程(A−6)と、この砂・細砂を脱水処理とする工程(A−7)とを経て、前記洗浄処理土を得ると共に、前記工程(A−3)で分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する工程(B−1)と、この沈殿汚泥を脱水処理し、前記濃縮残渣と水とに分離する工程(B−2)とを経て、前記濃縮残渣を得ることを特徴とする汚染土壌の洗浄方法である。   According to a second aspect of the present invention, contaminated soil containing harmful pollutants is washed, separated into washed treated soil and concentrated residue of the pollutants, the washed treated soil is reused, and the concentrated A method for cleaning contaminated soil in which a residue is subjected to a recovery process, wherein water is added to the contaminated soil, and wet sieving classification is performed to separate gravel and coarse sand to form slurry-like soil (A-1 ), Adding a dispersant to the slurry-like earth and sand, mixing and stirring, separating the contaminants from the surface of the earth and sand (A-2), and hydrolyzing the slurry-like earth and sand, A step of classifying fine sand and fine particles containing contaminants (A-3), a step of adding a collecting agent to the classified sand and fine sand, and mixing and stirring (A-4); The mixed and agitated sand and fine sand are separated by foam floating method to remove contaminants. Separating step (A-5), separating the sand / fine sand separated by gravity and further separating metal contaminants (A-6), and dehydrating the sand / fine sand. The step (A-7) is followed by the step (B-1) of obtaining the washing treated soil and coagulating and precipitating the fine particles separated in the step (A-3) into separated sludge and water. ) And the step (B-2) of dehydrating the precipitated sludge and separating the concentrated sludge into water and the concentrated residue to obtain the concentrated residue.

請求項3にかかる発明は、有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄装置であって、水を添加した前記汚染土壌から礫・粗砂を分離して、スラリー状の土砂とする湿式ふるい装置(10)と、このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する混合攪拌装置(20)と、このスラリー状の土砂を、砂・細砂と、汚染物質を含む細粒子とに分級処理するハイドロサイクロン装置(30)と、分級処理した前記砂・細砂からさらに金属汚染物質を分離する重力式分離装置(60)と、この砂・細砂を脱水処理し、前記洗浄処理土を得る脱水サイクロン装置(70)とを備え、かつ、分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する凝集沈殿装置(100)と、この沈殿汚泥を脱水処理し、前記濃縮残渣を得るプレス脱水装置(200)とを備えたことを特徴とする汚染土壌の洗浄装置である。   According to a third aspect of the present invention, contaminated soil containing harmful pollutants is washed, separated into washed treated soil and concentrated residue of the pollutants, the washed treated soil is reused, and the concentrated A device for cleaning contaminated soil for collecting residue, a wet sieving device (10) for separating gravel and coarse sand from the contaminated soil to which water has been added to form slurry-like soil, and the slurry-like soil Mixing and stirring device (20) for adding a dispersing agent to the earth and sand, mixing and stirring to separate the contaminants from the surface of the earth and sand, and the slurry-like earth and sand into sand and fine sand and fine particles containing the contaminants Hydrocyclone device (30) for classifying treatment, gravity type separation device (60) for further separating metal contaminants from the classified sand and fine sand, dewatering the sand and fine sand, and the washing treated soil Dehydration cyclone equipment (7 And a coagulating sedimentation device (100) for coagulating and precipitating the separated fine particles to separate the separated sludge and water, and a press dehydrating device for dehydrating the precipitated sludge to obtain the concentrated residue (200). A cleaning apparatus for contaminated soil.

請求項4にかかる発明は、有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄装置であって、水を添加した前記汚染土壌から礫・粗砂を分離して、スラリー状の土砂とする湿式ふるい装置(10)と、このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する混合攪拌装置(20)と、さらにこのスラリー状の土砂を、砂・細砂と、汚染物質を含む細粒子とに分級処理するハイドロサイクロン装置(30)と、分級処理した前記砂・細砂に捕集剤を添加して混合・攪拌する混合攪拌装置(40)と、混合・攪拌した前記砂・細砂から汚染物質を分離する泡浮遊式分離装置(50)と、分離した前記砂・細砂からさらに金属汚染物質を分離する重力式分離装置(60)と、前記砂・細砂を脱水処理し、前記洗浄処理土を得る脱水サイクロン装置(70)とを備え、かつ、分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する凝集沈殿装置(100)と、この沈殿汚泥を脱水処理し、前記濃縮残渣を得るプレス脱水装置(200)とを備えたことを特徴とする汚染土壌の洗浄装置である。   According to a fourth aspect of the present invention, contaminated soil containing harmful pollutants is washed, separated into washed treated soil and concentrated residue of the pollutants, the washed treated soil is reused, and the concentrated A device for cleaning contaminated soil for collecting residue, a wet sieving device (10) for separating gravel and coarse sand from the contaminated soil to which water has been added to form slurry-like soil, and the slurry-like soil A mixing and stirring device (20) for adding a dispersant to the earth and sand, mixing and stirring, and separating the contaminants from the surface of the earth and sand, and further adding the slurry-like earth and sand to the sand and fine sand and fine particles containing the contaminants From the hydrocyclone device (30) for classifying into the sand, the mixing and stirring device (40) for adding and collecting the collecting agent to the classified sand and fine sand, and the mixed and stirred sand and fine sand Bubble floating separator for separating pollutants 50), a gravity separator (60) for further separating metal contaminants from the separated sand / fine sand, and a dewatering cyclone device (70) for dehydrating the sand / fine sand to obtain the washed soil And a coagulating sedimentation device (100) for coagulating and precipitating the separated fine particles and separating them into a precipitated sludge and water, and a press dehydrating device for dehydrating the precipitated sludge to obtain the concentrated residue ( 200), and a contaminated soil cleaning apparatus.

本発明の汚染土壌の洗浄方法及び洗浄装置によれば、土砂に分散剤を添加して混合・攪拌することにより、土砂表面に強固に付着している汚染物質を剥離・分離することができ、洗浄処理土の品質を向上することができる。   According to the method and apparatus for cleaning contaminated soil of the present invention, by adding a dispersant to the sand and mixing and stirring, the contaminants firmly attached to the surface of the sand can be separated and separated, The quality of the cleaning soil can be improved.

以下、本発明の実施の形態に係る汚染土壌の洗浄方法及びこの洗浄方法に用いられる洗浄装置について、図面に基づき詳細に説明する。   Hereinafter, a cleaning method for contaminated soil and a cleaning device used in the cleaning method according to an embodiment of the present invention will be described in detail with reference to the drawings.

[第1の実施形態]
図1は、第1の実施形態に係る汚染土壌の洗浄装置の概略図である。本実施形態に係る洗浄装置は、請求項3に記載の発明に対応するものであり、洗浄方法は、請求項1に記載の発明に対応するものである。
[First Embodiment]
FIG. 1 is a schematic view of a contaminated soil cleaning apparatus according to the first embodiment. The cleaning apparatus according to the present embodiment corresponds to the invention described in claim 3, and the cleaning method corresponds to the invention described in claim 1.

また、本実施形態に係る汚染土壌の洗浄装置は、有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と汚染物質の濃縮した濃縮残渣とに分離し、洗浄処理土を再利用に供し、濃縮残渣を回収処理に供するものである。この装置は、水を添加した汚染土壌から礫・粗砂を分離して、スラリー状の土砂とする湿式ふるい装置(10)と、このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する混合攪拌装置(20)と、このスラリー状の土砂を、砂・細砂と、汚染物質を含む細粒子とに分級処理するハイドロサイクロン装置(30)と、分級処理した砂・細砂からさらに金属汚染物質を分離する重力式分離装置(60)と、この砂・細砂を脱水処理し、洗浄処理土を得る脱水サイクロン装置(70)と、分離した細粒子を凝集沈殿して、沈殿汚泥と水とに分離する凝集沈殿装置(100)と、この沈殿汚泥を脱水処理し、濃縮残渣を得るプレス脱水装置(200)とから、概略構成されている。   In addition, the contaminated soil cleaning apparatus according to the present embodiment cleans contaminated soil containing harmful pollutants, separates the soil into cleaned treated soil and concentrated residues of pollutants, and reuses the cleaned soil. The concentrated residue is subjected to a recovery process. This device separates gravel and coarse sand from contaminated soil to which water has been added to form a slurry-like sand, and adds a dispersant to the slurry-like sand and mixes and stirs. A mixing and stirring device (20) for separating contaminants from the surface of the soil, a hydrocyclone device (30) for classifying the slurry-like soil into sand / fine sand and fine particles containing the contaminant, and classification Gravity type separation device (60) that further separates metal contaminants from the treated sand / fine sand, dehydration cyclone device (70) that dehydrates the sand / fine sand to obtain washed soil, and separated fine particles The coagulation sedimentation apparatus (100) which coagulates and precipitates and isolate | separates into precipitation sludge and water, and the press dehydration apparatus (200) which dehydrates this precipitation sludge and obtains a concentrated residue is comprised roughly.

洗浄対象となる汚染土壌は、有害な汚染物質を含有するものである。このような有害な汚染物質としては、鉱物油、多環芳香族炭化水素(PAHs)、揮発性有機化合物(VOCs)、PCB、ダイオキシン、農薬、重金属、シアン等の有機性汚染物質及び無機性汚染物質が挙げられる。また、汚染土壌は、農業用地、工業用地、市街地、住宅地等のすべての土地の土壌である。有害な汚染物質により人工的に高濃度に汚染された工場跡地のような土壌であっても構わないし、自然汚染の農地のような土壌であってもよい。   Contaminated soil to be cleaned contains harmful pollutants. Such harmful pollutants include organic pollutants such as mineral oil, polycyclic aromatic hydrocarbons (PAHs), volatile organic compounds (VOCs), PCBs, dioxins, pesticides, heavy metals, cyanides, and inorganic pollution. Substances. Moreover, the contaminated soil is soil of all land such as agricultural land, industrial land, urban area, residential area and the like. It may be a soil such as a factory site that is artificially contaminated with harmful pollutants at a high concentration, or may be a soil such as a naturally contaminated farmland.

まず、汚染土壌は、水を添加した後、湿式ふるい装置(10)に送られる。この湿式ふるい装置(10)は、振動ふるいや超音波ふるい、比重選別等により、異物を選別して、2mmを超える礫・粗砂とそれ以下のスラリー状の土砂とに分級するものであり、網面を内部に備えている。この湿式ふるい装置(10)には、市販の公知の装置を使用することができる。汚染土壌は水を添加した後、この湿式ふるい装置(10)で分級処理し、2mmを超える礫・粗砂と2mm以下のスラリー状の土砂とに分級する(工程(A−1))。有害な汚染物質のほとんどが細粒子に付着・吸着しているおり、2mmを超える大きな礫・粗砂に含まれる汚染物質の量は、環境基準値以下であるため、2mmを超える礫・粗砂は分離後、洗浄処理土と共に再利用に供することができる。また、2mmを超える礫・粗砂をあらかじめ分離しておくことにより、土砂の洗浄効率を向上することができる。汚染土壌への水の添加量は、スラリー化する点から、土壌の2.5〜5倍(質量比)であるのが好ましい。   First, after adding water, the contaminated soil is sent to a wet sieving device (10). This wet sieving device (10) sorts foreign matter by vibration sieving, ultrasonic sieving, specific gravity sorting, etc., and classifies it into gravel / crude sand exceeding 2 mm and slurry-like earth and sand below it, It has a mesh surface inside. A commercially available well-known apparatus can be used for this wet sieving apparatus (10). After adding water, the contaminated soil is classified by the wet sieving apparatus (10) and classified into gravel / crude sand exceeding 2 mm and slurry earth and sand of 2 mm or less (step (A-1)). Most harmful pollutants adhere to and adsorb on fine particles, and the amount of pollutants contained in large gravel and coarse sand exceeding 2 mm is below the environmental standard value. Can be reused together with the washed soil after separation. Further, by separating in advance gravel / crude sand exceeding 2 mm, the washing efficiency of earth and sand can be improved. The amount of water added to the contaminated soil is preferably 2.5 to 5 times (mass ratio) that of the soil from the viewpoint of slurrying.

分級したスラリー状の土砂は、混合攪拌装置(20)に送られる。この混合攪拌装置(20)には、攪拌槽と攪拌羽根とが設けられている。この装置は、スラリー状の土砂に分散剤を添加した上で、攪拌羽根等を用いて機械的に混合・攪拌してスラリー状の土砂を相互に擦り合わせることにより、土砂表面に強固に付着した汚染物質を剥離し、分離するためのものである。この混合攪拌装置(20)には、市販の公知の装置を使用することができる。前記工程(A−1)で分級したスラリー状の土砂は、分散剤を添加して、この混合攪拌装置(20)にて混合・攪拌して、汚染物質を土砂表面から剥離する(工程(A−2))。分散剤としては、界面活性剤が好ましく、そのなかでも、ポリリン酸系の界面活性剤がより好ましい。また、分散剤の添加量は、汚染物質の存在量によって変わるが、全体に対して、0.01〜0.1質量%であるのが好ましい。分散剤を添加せずに、単にスラリー状の土砂を機械的に混合・攪拌しても、汚染物質を土砂表面から剥離することは難しい。これは、汚染物質と土砂表面との表面電荷が異なり、汚染物質は静電気的な相互作用によって、土砂表面に強固に付着しているためである。分散剤を添加することにより、これらの表面電荷が変化するため、汚染物質を容易に剥離することができる。この剥離した汚染物質は、次工程において、細粒子と共にオーバーフローとして分級するため、洗浄処理土には残らない。   The classified slurry-like earth and sand is sent to the mixing and stirring device (20). The mixing and stirring device (20) is provided with a stirring tank and a stirring blade. In this apparatus, after adding a dispersant to the slurry-like earth and sand, the slurry-like earth and sand are rubbed together by mechanically mixing and stirring using a stirring blade or the like, thereby firmly attaching to the surface of the earth and sand. It is for exfoliating and separating contaminants. A commercially available well-known apparatus can be used for this mixing and stirring apparatus (20). The slurry-like earth and sand classified in the step (A-1) is added with a dispersant, mixed and stirred by the mixing and stirring device (20), and the contaminants are separated from the surface of the earth and sand (step (A -2)). As the dispersant, a surfactant is preferable, and among them, a polyphosphate-based surfactant is more preferable. Moreover, although the addition amount of a dispersing agent changes with the abundance of a contaminant, it is preferable that it is 0.01-0.1 mass% with respect to the whole. Even if the slurry-like soil is simply mechanically mixed and stirred without adding the dispersant, it is difficult to peel the contaminants from the surface of the soil. This is because the surface charge of the pollutant is different from that of the earth and sand, and the pollutant is firmly attached to the earth and sand surface by electrostatic interaction. By adding a dispersing agent, these surface charges change, so that contaminants can be easily peeled off. The separated contaminants are classified as an overflow together with fine particles in the next step, so that they do not remain in the cleaning soil.

次いで、このスラリー状の土砂は、ハイドロサイクロン装置(30)に送られる。このハイドロサイクロン装置(30)は、円筒底部が円錐型をした構造の容器からなり、土砂と水を混ぜたスラリーを導入する上部流入口と、アンダーフローを取り出す下部流出口と、オーバーフローを取り出す上部流出口とを備えている。上部流入口から入ったスラリー状の土砂は、円筒容器の円周方向に高速で供給されることにより、回転運動を起こし、回転流となって、円錐頂部に向かって進む。この時、スラリー中の比重の重い粒子は遠心力により周壁に集まり、次第にアンダーフロー出口(下部流出口)に向かい、濃縮して排出される。一方、液体と比重の軽い粒子は、円筒容器の中央部を渦流となって上昇し、オーバーフロー出口(上部流出口)から排出される。具体的には、63μm〜2mmの砂・細砂はアンダーフローとして分級され、63μm未満の細粒子と汚染物質はオーバーフローとして上方に分級される(工程(A−3))。このハイドロサイクロン装置(30)には、市販の公知の装置を使用することができる。汚染物質は細粒子に付着・吸着しているため、ハイドロサイクロン装置(30)で分級することにより、ほとんどの汚染物質を洗浄処理土から除去することができる。この分級処理は、1回以上行うのが好ましい。   Then, this slurry-like earth and sand is sent to a hydrocyclone apparatus (30). This hydrocyclone device (30) is composed of a container having a conical structure at the bottom of the cylinder, and includes an upper inlet for introducing slurry mixed with earth and sand, a lower outlet for taking out underflow, and an upper part for taking out overflow. And an outlet. The slurry-like earth and sand that has entered from the upper inflow port is rotated at a high speed in the circumferential direction of the cylindrical container, thereby causing a rotational motion, which becomes a rotational flow and proceeds toward the top of the cone. At this time, particles having a high specific gravity in the slurry gather on the peripheral wall due to centrifugal force, gradually move toward the underflow outlet (lower outlet), and are concentrated and discharged. On the other hand, particles having a low specific gravity with the liquid rise as a vortex in the center of the cylindrical container and are discharged from the overflow outlet (upper outlet). Specifically, sand / fine sand of 63 μm to 2 mm is classified as underflow, and fine particles and contaminants of less than 63 μm are classified upward as an overflow (step (A-3)). A commercially available well-known apparatus can be used for this hydrocyclone apparatus (30). Since the contaminants adhere to and adsorb on the fine particles, most of the contaminants can be removed from the cleaning soil by classification with the hydrocyclone device (30). This classification treatment is preferably performed once or more.

分級した砂・細砂は、重力式分離装置(60)に送られる。この重力式分離装置(60)は、水と共に土砂を上方から下方へと螺旋状に流す構造になっており、粒子が液体中を重力によって沈降する際の速度の差によって分級する。比重の重い金属汚染物質は、螺旋の内側に集まり、軽い砂・細砂は、水と共に螺旋の外側に分離し、砂・細砂が下方から取り出される。この重力式分離装置(60)には、市販の公知の装置を使用することができる。砂・細砂から、重力式分離装置(60)により、金属汚染物質が分離される(工程(A−6))。このような金属汚染物質としては、例えば、散弾銃の銃弾等がある。また金属汚染物質と水は、汚染物質を含んでいるため、凝集沈殿装置(100)に送られる。   The classified sand / fine sand is sent to the gravity separation device (60). This gravitational separation device (60) has a structure in which soil and sand together with water are spirally flowed from above to below, and is classified by the difference in speed when particles settle in the liquid by gravity. Heavy metal contaminants gather inside the spiral, light sand / fine sand separates with the water to the outside of the spiral, and the sand / fine sand is taken out from below. A commercially available well-known apparatus can be used for this gravity-type separation apparatus (60). Metal contaminants are separated from the sand / fine sand by a gravity separator (60) (step (A-6)). Examples of such metal contaminants include shotgun bullets. Moreover, since a metal contaminant and water contain the contaminant, they are sent to the coagulation sedimentation apparatus (100).

砂・細砂は、脱水サイクロン装置(70)に送られる。この脱水サイクロン装置(70)は、上記ハイドロサイクロン装置(30)と同じ構造からなっている。砂・細砂は、脱水サイクロン装置(70)で洗浄処理土と水に分離される(工程(A−7))。得られた洗浄処理土は、汚染物質の残留濃度を分析して、環境基準値以下になっていることを確認する。この洗浄処理土は、汚染物質の濃度が環境基準値以下であるため、埋め戻し等に再利用することができる。また水は、貯留水槽に送られて、循環水として、湿式ふるい装置(10)に添加する水として再利用される。   Sand and fine sand are sent to a dehydration cyclone device (70). The dehydration cyclone device (70) has the same structure as the hydrocyclone device (30). Sand and fine sand are separated into washing soil and water by a dehydration cyclone device (70) (step (A-7)). Analyze the residual concentration of pollutants in the washed soil obtained and confirm that it is below the environmental standard value. This cleaning soil can be reused for backfilling and the like because the concentration of contaminants is below the environmental standard value. Moreover, water is sent to a storage tank and reused as water added to the wet sieving apparatus (10) as circulating water.

一方、ハイドロサイクロン装置(30)で分離した汚染物質を含む細粒子は、凝集沈殿装置(100)に送られる。この凝集沈殿装置(100)は、沈殿槽を備え、細粒子を含んだ懸濁水に凝集剤を添加・撹拌し、水中の微細な浮遊物を大きな沈殿汚泥として沈殿させ、清澄な処理水を分離するものである(工程(B−1))。この凝集沈殿装置(100)には、市販の公知の装置を使用することができる。このような凝集剤としては、無機系凝集剤、有機系凝集剤を単独又は組合わせて用いることができる。無機系凝集剤としては、例えば、硫酸アルミニウム、ポリ塩化アルミニウム、鉄塩等が挙げられ、有機系凝集剤としては、例えば、ポリアクリルアミド、ポリアクリル酸等が挙げられる。凝集剤の添加量は、懸濁水の懸濁質(SS)濃度に応じて調整する。また、沈殿汚泥から分離した水は、貯留水槽に送られて、循環水として、湿式ふるい装置(10)に添加する水として再利用される。   On the other hand, fine particles containing contaminants separated by the hydrocyclone device (30) are sent to the coagulation sedimentation device (100). This coagulation sedimentation device (100) is equipped with a sedimentation tank, and aggregating agent is added to and stirred in suspension water containing fine particles, and fine suspended matter in water is precipitated as a large sedimentation sludge to separate clear treated water. (Step (B-1)). A commercially available well-known apparatus can be used for this coagulation sedimentation apparatus (100). As such flocculants, inorganic flocculants and organic flocculants can be used alone or in combination. Examples of the inorganic flocculant include aluminum sulfate, polyaluminum chloride, and iron salt. Examples of the organic flocculant include polyacrylamide and polyacrylic acid. The addition amount of the flocculant is adjusted according to the suspended solid (SS) concentration of the suspension water. Moreover, the water isolate | separated from the sedimentation sludge is sent to a storage water tank, and is reused as water added to a wet sieving apparatus (10) as circulating water.

この沈殿汚泥は、水分を多量に含有しているため、プレス脱水装置(200)に送られ、脱水される。このプレス脱水装置(200)は、公知の加圧式濾過装置(ベルトフィルタープレス)等であり、濾布等からなるフィルターとプレス機を備えている。沈殿汚泥をプレス脱水装置(200)で濾過して脱水処理することで、フィルター上に含水率40〜50質量%の濃縮残渣を得ることができる(工程(B−2))。この濃縮残渣は、63μm未満の細粒子からなり、汚染物質が濃縮しているため、外部へ搬出して処分される。元の汚染土壌の粒度構成(乾燥重量比)が、礫・粗砂分25%、砂・細砂分50%、細粒子分25%であると、得られる洗浄処理土が75%、濃縮残渣が25%となり、洗浄処理土の再利用率を高くすることができる。   Since this precipitated sludge contains a large amount of moisture, it is sent to the press dewatering device (200) and dehydrated. The press dewatering device (200) is a known pressure filtration device (belt filter press) or the like, and includes a filter made of a filter cloth or the like and a press machine. By filtering the precipitated sludge with a press dehydrator (200) for dehydration, a concentrated residue having a water content of 40 to 50% by mass can be obtained on the filter (step (B-2)). This concentrated residue consists of fine particles of less than 63 μm, and since the contaminants are concentrated, they are taken out and disposed of. If the particle size composition (dry weight ratio) of the original contaminated soil is gravel / crude sand 25%, sand / fine sand 50%, fine particle 25%, the resulting washed soil is 75%, concentrated residue Becomes 25%, and the reuse rate of the cleaning soil can be increased.

また、本実施形態では、装置全体で使用する水を循環させて再利用しているため、排水による二次汚染も発生せず、また水処理のコストを低下することができる。   Moreover, in this embodiment, since the water used by the whole apparatus is circulated and reused, the secondary pollution by waste_water | drain does not generate | occur | produce and the cost of water treatment can be reduced.

本実施形態では、分散剤を添加して混合・攪拌する混合攪拌装置(20)を設けたことにより、土砂表面に強固に付着している汚染物質を剥離・分離することができ、洗浄処理土の品質を向上することができる。   In this embodiment, by providing a mixing and stirring device (20) for adding and mixing and stirring a dispersing agent, it is possible to peel and separate contaminants firmly attached to the surface of the earth and sand. Can improve the quality.

また、本実施形態では、サイズを2mmを超える礫・粗砂、63μm〜2mmの砂・細砂、63μm未満の細粒子とに分級して処理することにより、4mmまでのほとんどの土壌粒子を洗浄処理することができる。   Moreover, in this embodiment, most soil particles up to 4 mm are washed by classification and processing into gravel / coarse sand exceeding 2 mm, sand / fine sand of 63 μm to 2 mm, and fine particles of less than 63 μm. Can be processed.

[第2の実施形態]
図2は、第2の実施形態に係る汚染土壌の洗浄装置の概略図である。本実施形態に係る洗浄装置は、請求項4に記載の発明に対応するものであり、洗浄方法は、請求項2に記載の発明に対応するものである。本実施形態では、ハイドロサイクロン装置(30)と重力式分離装置(60)との間に、分級処理した砂・細砂に捕集剤を添加して混合・攪拌する混合攪拌装置(40)と、この砂・細砂から汚染物質を分離する泡浮遊式分離装置(50)とを設けたこと以外は第1の実施の形態と同様であるので、その説明は省略する。
[Second Embodiment]
FIG. 2 is a schematic view of a contaminated soil cleaning apparatus according to the second embodiment. The cleaning apparatus according to the present embodiment corresponds to the invention described in claim 4, and the cleaning method corresponds to the invention described in claim 2. In this embodiment, between the hydrocyclone device (30) and the gravity separation device (60), a mixing and stirring device (40) for adding and collecting and stirring a collecting agent to the classified sand and fine sand Since it is the same as that of the first embodiment except that the foam floating type separation device (50) for separating contaminants from the sand / fine sand is provided, the description thereof is omitted.

この混合攪拌装置(40)は、上記混合攪拌装置(20)と同じ構造からなっているが、添加する薬剤は分散剤ではなく、捕集剤(コレクター)である。この混合攪拌装置(40)では、汚染物質と土砂表面との表面電荷が異なることを利用して、汚染物質のみに選択的に付着する捕集剤を砂・細砂に添加し、機械的に混合・攪拌して、汚染物質に捕集剤を付着させるものである(工程(A−4))。この汚染物質は、次の泡浮遊式分離装置(50)において土砂から分離される。捕集剤の種類及び濃度は、対象とする汚染物質に応じて適宜選択される。   The mixing and stirring device (40) has the same structure as the mixing and stirring device (20), but the added drug is not a dispersant but a collecting agent (collector). In this mixing and stirring device (40), a trapping agent that selectively adheres only to the contaminant is added to the sand / fine sand by utilizing the fact that the surface charges of the contaminant and the sand surface are different. Mixing and stirring are performed to attach the scavenger to the contaminant (step (A-4)). This pollutant is separated from the earth and sand in the next bubble floating separator (50). The type and concentration of the collection agent are appropriately selected according to the target contaminant.

この砂・細砂は泡浮遊式分離装置(50)に送られる。この泡浮遊式分離装置(50)は、フローテーションセルとその内部にローターとを備え、セルの上部液面には、液面と水平方向を回転軸とした泡かき取り用の回転羽根からなるスクレーパーを備えている。砂・細砂を含んだスラリーを泡浮遊式分離装置(50)のフローテーションセルに導入し、気泡剤を添加して、ローターを回転してセル底部に空気を導入する。ローターから発生した気泡は、捕集剤の付着した汚染物質を捕らえて気泡と共にセル上部の液面へと上昇し、液面から泡と共にフロスとしてスクレーパーによりかき取られて除去される(工程(A−5))。この泡と水は凝集沈殿装置(100)に送られ、分離した砂・細砂は、重力式分離装置(60)に送られる。   This sand / fine sand is sent to the bubble floating separator (50). This bubble floating type separation device (50) includes a flotation cell and a rotor therein, and the upper liquid surface of the cell is composed of a rotating blade for removing bubbles with the liquid surface and the horizontal direction as a rotation axis. A scraper is provided. The slurry containing sand and fine sand is introduced into the flotation cell of the foam floating separator (50), the foaming agent is added, and the rotor is rotated to introduce air into the cell bottom. Bubbles generated from the rotor trap the contaminants with the trapping agent and rise to the liquid level at the top of the cell together with the bubbles, and are scraped off by the scraper as froth together with the bubbles from the liquid level (step (A -5)). The foam and water are sent to the coagulation sedimentation device (100), and the separated sand / fine sand is sent to the gravity separation device (60).

本実施形態では、ハイドロサイクロン装置(30)と重力式分離装置(60)との間に、捕集剤混合攪拌装置(40)と泡浮遊式分離装置(50)とを設けたことにより、残存する汚染物質を除去することができ、洗浄処理土の品質をさらに向上することができる。   In this embodiment, by providing the collection agent mixing and stirring device (40) and the bubble floating separation device (50) between the hydrocyclone device (30) and the gravity separation device (60), the remaining The contaminants to be removed can be removed and the quality of the cleaning soil can be further improved.

第1の実施形態に係る汚染土壌の洗浄装置の概略図である。It is the schematic of the cleaning apparatus of the contaminated soil which concerns on 1st Embodiment. 第2の実施形態に係る汚染土壌の洗浄装置の概略図である。It is the schematic of the cleaning apparatus of the contaminated soil which concerns on 2nd Embodiment.

符号の説明Explanation of symbols

10 湿式ふるい装置
20、40 混合攪拌装置
30 ハイドロサイクロン装置
50 泡浮遊式分離装置
60 重力式分離装置
70 脱水サイクロン装置
100 凝集沈殿装置
200 プレス脱水装置


DESCRIPTION OF SYMBOLS 10 Wet sieving apparatus 20, 40 Mixing and stirring apparatus 30 Hydrocyclone apparatus 50 Foam floating type separation apparatus 60 Gravity type separation apparatus 70 Dehydration cyclone apparatus 100 Coagulation sedimentation apparatus 200 Press dehydration apparatus


Claims (4)

有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄方法であって、
前記汚染土壌に水を添加し、湿式ふるい分級処理して礫・粗砂を分離して、スラリー状の土砂とする工程(A−1)と、
このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する工程(A−2)と、
このスラリー状の土砂を、ハイドロサイクロン処理して砂・細砂と、汚染物質を含む細粒子とに分級処理する工程(A−3)と、
分級処理した前記砂・細砂を重力式分離処理して、さらに金属汚染物質を分離する工程(A−6)と、
この砂・細砂を脱水処理する工程(A−7)とを経て、前記洗浄処理土を得ると共に、
前記工程(A−3)で分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する工程(B−1)と、
この沈殿汚泥を脱水処理し、前記濃縮残渣と水とに分離する工程(B−2)とを経て、前記濃縮残渣を得ることを特徴とする汚染土壌の洗浄方法。
Contaminated soil that cleans contaminated soil containing harmful pollutants, separates it into washed treated soil and concentrated residue of the pollutant, recycles the washed soil, and collects the concentrated residue for recovery processing Cleaning method,
Adding water to the contaminated soil, separating the gravel and coarse sand by wet sieving classification (A-1),
A step of adding a dispersant to the slurry-like earth and sand, mixing and stirring, and peeling the contaminant from the earth and sand surface (A-2);
The slurry-like earth and sand is subjected to a hydrocyclone treatment to classify it into sand / fine sand and fine particles containing contaminants (A-3),
A step (A-6) of separating the metallic contaminants by subjecting the classified sand and fine sand to a gravity separation treatment;
Through the step (A-7) of dehydrating the sand and fine sand, the washing soil is obtained,
A step (B-1) of coagulating and precipitating the fine particles separated in the step (A-3) and separating them into precipitated sludge and water;
A method for washing contaminated soil, characterized in that the precipitated residue is obtained through a step (B-2) in which the precipitated sludge is dehydrated and separated into the concentrated residue and water.
有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄方法であって、
前記汚染土壌に水を添加し、湿式ふるい分級処理して礫・粗砂を分離して、スラリー状の土砂とする工程(A−1)と、
このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する工程(A−2)と、
このスラリー状の土砂を、ハイドロサイクロン処理して砂・細砂と、汚染物質を含む細粒子とに分級処理する工程(A−3)と、
分級処理した前記砂・細砂に捕集剤を添加して混合・攪拌する工程(A−4)と、
混合・攪拌した前記砂・細砂を、泡浮遊式分離処理して汚染物質を分離する工程(A−5)と、
分離した前記砂・細砂を重力式分離処理して、さらに金属汚染物質を分離する工程(A−6)と、
この砂・細砂を脱水処理とする工程(A−7)とを経て、前記洗浄処理土を得ると共に、
前記工程(A−3)で分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する工程(B−1)と、
この沈殿汚泥を脱水処理し、前記濃縮残渣と水とに分離する工程(B−2)とを経て、前記濃縮残渣を得ることを特徴とする汚染土壌の洗浄方法。
Contaminated soil that cleans contaminated soil containing harmful pollutants, separates it into washed treated soil and concentrated residue of the pollutant, recycles the washed soil, and collects the concentrated residue for recovery processing Cleaning method,
Adding water to the contaminated soil, separating the gravel and coarse sand by wet sieving classification (A-1),
A step of adding a dispersant to the slurry-like earth and sand, mixing and stirring, and peeling the contaminant from the earth and sand surface (A-2);
The slurry-like earth and sand is subjected to a hydrocyclone treatment to classify it into sand / fine sand and fine particles containing contaminants (A-3),
A step (A-4) of adding a collecting agent to the classified sand and fine sand and mixing and stirring;
A step (A-5) of separating the contaminants by subjecting the mixed and stirred sand / fine sand to a foam floating type separation treatment;
A step (A-6) of subjecting the separated sand / fine sand to a gravity separation process to further separate metal contaminants;
Through the step (A-7) of dehydrating the sand and fine sand, the washing soil is obtained,
A step (B-1) of coagulating and precipitating the fine particles separated in the step (A-3) and separating them into precipitated sludge and water;
A method for washing contaminated soil, characterized in that the precipitated residue is obtained through a step (B-2) in which the precipitated sludge is dehydrated and separated into the concentrated residue and water.
有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄装置であって、
水を添加した前記汚染土壌から礫・粗砂を分離して、スラリー状の土砂とする湿式ふるい装置(10)と、
このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する混合攪拌装置(20)と、
このスラリー状の土砂を、砂・細砂と、汚染物質を含む細粒子とに分級処理するハイドロサイクロン装置(30)と、
分級処理した前記砂・細砂からさらに金属汚染物質を分離する重力式分離装置(60)と、
この砂・細砂を脱水処理し、前記洗浄処理土を得る脱水サイクロン装置(70)とを備え、
かつ、分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する凝集沈殿装置(100)と、
この沈殿汚泥を脱水処理し、前記濃縮残渣を得るプレス脱水装置(200)とを備えたことを特徴とする汚染土壌の洗浄装置。
Contaminated soil that cleans contaminated soil containing harmful pollutants, separates it into washed treated soil and concentrated residue of the pollutant, recycles the washed soil, and collects the concentrated residue for recovery processing A cleaning device of
A wet sieving device (10) for separating gravel and coarse sand from the contaminated soil to which water has been added to form slurry-like soil;
A mixing and stirring device (20) for adding a dispersing agent to the slurry-like earth and sand, mixing and stirring, and separating contaminants from the surface of the earth and sand;
A hydrocyclone apparatus (30) for classifying the slurry-like earth and sand into sand / fine sand and fine particles containing contaminants;
A gravity separator (60) for further separating metal contaminants from the classified sand and fine sand;
A dehydration cyclone device (70) for dehydrating the sand and fine sand to obtain the washed soil;
And the coagulation sedimentation apparatus (100) which coagulates and precipitates the separated fine particles and separates it into sedimentation sludge and water,
An apparatus for cleaning contaminated soil, comprising: a press dewatering apparatus (200) for dewatering the precipitated sludge to obtain the concentrated residue.
有害な汚染物質を含有する汚染土壌を洗浄し、洗浄処理土と前記汚染物質の濃縮した濃縮残渣とに分離し、前記洗浄処理土を再利用に供し、前記濃縮残渣を回収処理に供する汚染土壌の洗浄装置であって、
水を添加した前記汚染土壌から礫・粗砂を分離して、スラリー状の土砂とする湿式ふるい装置(10)と、
このスラリー状の土砂に分散剤を添加して混合・攪拌し、汚染物質を土砂表面から剥離する混合攪拌装置(20)と、
さらにこのスラリー状の土砂を、砂・細砂と、汚染物質を含む細粒子とに分級処理するハイドロサイクロン装置(30)と、
分級処理した前記砂・細砂に捕集剤を添加して混合・攪拌する混合攪拌装置(40)と、
混合・攪拌した前記砂・細砂から汚染物質を分離する泡浮遊式分離装置(50)と、
分離した前記砂・細砂からさらに金属汚染物質を分離する重力式分離装置(60)と、
前記砂・細砂を脱水処理し、前記洗浄処理土を得る脱水サイクロン装置(70)とを備え、
かつ、分離した前記細粒子を凝集沈殿して、沈殿汚泥と水とに分離する凝集沈殿装置(100)と、
この沈殿汚泥を脱水処理し、前記濃縮残渣を得るプレス脱水装置(200)とを備えたことを特徴とする汚染土壌の洗浄装置。


Contaminated soil that cleans contaminated soil containing harmful pollutants, separates it into washed treated soil and concentrated residue of the pollutant, recycles the washed soil, and collects the concentrated residue for recovery processing A cleaning device of
A wet sieving device (10) for separating gravel and coarse sand from the contaminated soil to which water has been added to form slurry-like soil;
A mixing and stirring device (20) for adding a dispersing agent to the slurry-like earth and sand, mixing and stirring, and separating contaminants from the surface of the earth and sand;
Furthermore, the hydrocyclone apparatus (30) for classifying the slurry-like earth and sand into sand / fine sand and fine particles containing contaminants;
A mixing and stirring device (40) for adding and mixing and stirring a collecting agent to the classified sand and fine sand;
A bubble floating separation device (50) for separating contaminants from the mixed and stirred sand and fine sand;
A gravity separator (60) for further separating metal contaminants from the separated sand and fine sand;
A dehydration cyclone device (70) for dehydrating the sand and fine sand to obtain the washed soil;
And the coagulation sedimentation apparatus (100) which coagulates and precipitates the separated fine particles and separates it into sedimentation sludge and water,
An apparatus for cleaning contaminated soil, comprising: a press dewatering apparatus (200) for dewatering the precipitated sludge to obtain the concentrated residue.


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Cited By (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009202089A (en) * 2008-02-27 2009-09-10 Shimizu Corp Reclamation treatment method and reclamation treatment system of earth and sand-waste mixture
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JP2013248559A (en) * 2012-05-31 2013-12-12 Shimizu Corp Method for cleaning heavy metal contaminated soil
JP2014018774A (en) * 2012-07-23 2014-02-03 Toa Harbor Works Co Ltd Method and system for processing earth and sand
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06343948A (en) * 1990-05-25 1994-12-20 Westinghouse Electric Corp <We> Method and apparatus for treating contaminated particulate substance
JPH1110131A (en) * 1997-06-20 1999-01-19 Dowa Mining Co Ltd Method for recovery of heavy metals from soil
JP2004261795A (en) * 2003-02-10 2004-09-24 Kankyo Eng Co Ltd Method of removing nonvolatile contaminant in soil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06343948A (en) * 1990-05-25 1994-12-20 Westinghouse Electric Corp <We> Method and apparatus for treating contaminated particulate substance
JPH1110131A (en) * 1997-06-20 1999-01-19 Dowa Mining Co Ltd Method for recovery of heavy metals from soil
JP2004261795A (en) * 2003-02-10 2004-09-24 Kankyo Eng Co Ltd Method of removing nonvolatile contaminant in soil

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JP2019181403A (en) * 2018-04-16 2019-10-24 清水建設株式会社 Cleaning system and cleaning method of agrochemical-contaminated soil
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JP2021109113A (en) * 2020-01-06 2021-08-02 鹿島建設株式会社 Dewatering method of muddy water
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