JP2016215112A - Contaminated soil cleaning equipment and cleaning method for contaminated soil - Google Patents

Contaminated soil cleaning equipment and cleaning method for contaminated soil Download PDF

Info

Publication number
JP2016215112A
JP2016215112A JP2015101875A JP2015101875A JP2016215112A JP 2016215112 A JP2016215112 A JP 2016215112A JP 2015101875 A JP2015101875 A JP 2015101875A JP 2015101875 A JP2015101875 A JP 2015101875A JP 2016215112 A JP2016215112 A JP 2016215112A
Authority
JP
Japan
Prior art keywords
heavy metal
iron powder
mud
contaminated
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2015101875A
Other languages
Japanese (ja)
Other versions
JP6458635B2 (en
Inventor
高田 尚哉
Naoya Takada
尚哉 高田
啓三 山崎
Keizo Yamazaki
啓三 山崎
三浦 俊彦
Toshihiko Miura
俊彦 三浦
洋一 守屋
Yoichi Moriya
洋一 守屋
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.)
Obayashi Corp
Original Assignee
Obayashi Corp
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 Obayashi Corp filed Critical Obayashi Corp
Priority to JP2015101875A priority Critical patent/JP6458635B2/en
Publication of JP2016215112A publication Critical patent/JP2016215112A/en
Application granted granted Critical
Publication of JP6458635B2 publication Critical patent/JP6458635B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly

Landscapes

  • Treatment Of Sludge (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide contaminated soil cleaning equipment capable of efficiently performing operation of cleaning heavy metal contaminated soil using an iron powder by simple equipment, and to provide a cleaning method for contaminated soil using the contaminated soil cleaning equipment.SOLUTION: A heavy metal removal apparatus comprises: a heavy metal adsorption tank in which contaminated muddy water and an iron powder are stirred and mixed to prepare iron powder added muddy water; and a centrifugal separator that is disposed downstream of the heavy metal adsorption tank to gravity separate the iron powder added muddy water into cleaned muddy water and an iron powder-containing separated material containing the iron powder adsorbing heavy metals. A circulation passage of the iron powder is formed by arranging three or more of the heavy metal removal apparatuses so that the iron powder-containing separated material gravity separated by the centrifugal separator of the heavy metal removal apparatus located upstream is directly charged down to the heavy metal adsorption tank of the heavy metal removal apparatus located downstream.SELECTED DRAWING: Figure 1

Description

本発明は、鉄粉を利用して重金属汚染土壌を洗浄する際に用いる汚染土壌洗浄設備、および汚染土壌洗浄設備を用いた汚染土壌の洗浄工法に関する。   The present invention relates to a contaminated soil cleaning facility used when cleaning heavy metal contaminated soil using iron powder, and a method for cleaning contaminated soil using the contaminated soil cleaning facility.

例えば、シールドやトンネル工事等で発生する自然由来の重金属汚染土壌は、細粒分を多く含む粘性土である場合が多い。そこで発明者らは、粘性土中に含まれるヒ素をはじめとする重金属を効率的に除去する方法として、鉄粉を用いた重金属汚染土壌の洗浄方法を開発した。   For example, naturally-derived heavy metal-contaminated soil generated by shields and tunnel construction is often viscous soil containing a large amount of fine particles. Therefore, the inventors have developed a method for cleaning heavy metal contaminated soil using iron powder as a method for efficiently removing heavy metals including arsenic contained in cohesive soil.

特許文献1に開示したように、鉄粉を用いた重金属汚染土壌の洗浄方法は、ヒ素吸着槽にてヒ素を含む泥水と鉄粉とを所定時間撹拌・混合し鉄粉添加泥水を作製した後、これを遠心分離機にて、ヒ素を吸着した鉄粉を含む泥水とヒ素を含まない泥水とに比重分離する。   As disclosed in Patent Document 1, the method for cleaning heavy metal-contaminated soil using iron powder is after stirring and mixing mud containing arsenic and iron powder for a predetermined time in an arsenic adsorption tank to produce iron powder-added mud water Then, this is subjected to specific gravity separation in a centrifuge into muddy water containing iron powder adsorbing arsenic and muddy water not containing arsenic.

ヒ素を含まない泥水はスラリー槽に供給されて、減容および脱水を経てケーキとなり、健全な産業廃棄物として搬出される。一方、ヒ素を吸着した鉄粉を含む泥水は、鉄粉を再利用するべく一旦、鉄粉前処理槽に貯留していた。   The arsenic-free muddy water is supplied to the slurry tank, volume-reduced and dehydrated to become a cake, which is carried out as healthy industrial waste. On the other hand, the muddy water containing the iron powder adsorbing arsenic was once stored in the iron powder pretreatment tank in order to reuse the iron powder.

特開2014−188408号公報JP 2014-188408 A

しかし、鉄粉前処理槽に貯留したヒ素を吸着した鉄粉を含む泥水は、再利用するべくそのままヒ素吸着槽に供給しようとすると、遠心分離機にて分離されたことに伴って比重及び粘性ともに大きい状態となっているため、ポンプ圧送することができない。   However, if mud containing iron powder adsorbed arsenic stored in the iron powder pretreatment tank is supplied to the arsenic adsorption tank as it is to be reused, it is separated by a centrifuge and has a specific gravity and viscosity. Since both are large, pumping cannot be performed.

このため、特許文献1では、鉄粉前処理槽の下流側にさらに鉄粉ストック槽を設置し、鉄粉前処理槽にて貯留したヒ素を吸着した鉄粉を含む泥水を、鉄粉ストック槽に移し替えて適宜な加水を行いポンプ圧送可能な鉄粉混合液を作製した上で、これをヒ素吸着槽に供給しており、多大なコストや手間を要していた。   For this reason, in patent document 1, an iron powder stock tank is installed in the downstream of an iron powder pretreatment tank, and the muddy water containing the iron powder which adsorb | sucked the arsenic stored in the iron powder pretreatment tank is made into an iron powder stock tank. The iron powder mixture that can be pumped by performing appropriate water addition is prepared and supplied to the arsenic adsorption tank, which requires a great deal of cost and labor.

また、特許文献1では、ヒ素吸着槽を複数設置していることから、各ヒ素吸着槽で使用する鉄粉どうしが混ざり合うことのないよう、ヒ素吸着槽の数と同数の鉄粉ストック槽を用意する必要があり、設備費が増大するだけでなく、広大な設備用の敷地を確保する必要があった。   Further, in Patent Document 1, since a plurality of arsenic adsorption tanks are installed, the same number of iron powder stock tanks as the number of arsenic adsorption tanks are used so that the iron powders used in each arsenic adsorption tank do not mix with each other. It was necessary not only to increase the equipment cost but also to secure a vast site for the equipment.

本発明は、かかる課題に鑑みなされたものであって、その主な目的は、鉄粉を用いて重金属汚染土壌を洗浄する作業を、簡略な設備にて効率よく実施することの可能な、汚染土壌洗浄設備、および汚染土壌洗浄設備を用いた汚染土壌の洗浄工法を提供することである。   The present invention has been made in view of such a problem, and its main purpose is contamination that can efficiently carry out an operation of washing heavy metal-contaminated soil using iron powder with simple equipment. It is to provide a soil cleaning facility and a method for cleaning contaminated soil using the contaminated soil cleaning facility.

かかる目的を達成するため、本発明の汚染土壌洗浄設備は、重金属に汚染された粘性土を含む汚染泥水を貯留し、該汚染泥水の比重を管理調整する泥水槽と、該泥水槽より供給される前記汚染泥水を鉄粉にて洗浄し、前記重金属が除去された洗浄泥水を作製する3つ以上の重金属除去装置と、該重金属除去装置各々より排出される前記洗浄泥水を貯留する洗浄泥水槽とを備える汚染土壌洗浄設備であって、前記重金属除去装置が、前記汚染泥水と前記鉄粉とを撹拌混合して該鉄粉に前記汚染泥水中の重金属を吸着させながら、鉄粉添加泥水を作製する重金属吸着槽と、該重金属吸着槽の下流側に配置されて、前記鉄粉添加泥水を前記洗浄泥水と前記重金属を吸着した鉄粉が含有された鉄粉含有分離物とに比重分離する遠心分離機と、を有し、3つ以上の該重金属除去装置を、上流側に位置する重金属除去装置の遠心分離機にて比重分離した前記鉄粉含有分離物が、下流側に位置する重金属除去装置の重金属吸着槽に直接投下されるよう配置して、前記鉄粉の循環路を形成することを特徴とする。   In order to achieve such an object, the contaminated soil cleaning facility of the present invention stores a contaminated mud containing viscous soil contaminated with heavy metals, and manages and adjusts the specific gravity of the contaminated mud, and is supplied from the mud tank. Three or more heavy metal removing devices for cleaning the contaminated mud water with iron powder and producing the washed mud water from which the heavy metals have been removed, and a washing mud tank for storing the washing mud water discharged from each of the heavy metal removing devices And the heavy metal removing device stirs and mixes the contaminated mud water and the iron powder and adsorbs the heavy metal in the contaminated mud water to the iron powder, Specific gravity separation of the heavy metal adsorption tank to be prepared and the iron powder-added muddy water separated into the washing muddy water and the iron powder-containing separation containing the iron powder adsorbed with the heavy metal, disposed on the downstream side of the heavy metal adsorption tank A centrifuge, The iron powder-containing separation obtained by separating the specific gravity of two or more heavy metal removal devices by the centrifugal separator of the heavy metal removal device located upstream is directly dropped into the heavy metal adsorption tank of the heavy metal removal device located downstream. It arrange | positions so that the circulation path of the said iron powder may be formed.

本発明の汚染土壌洗浄設備は、3つ以上の前記重金属除去装置のうち、少なくとも1つの重金属除去装置に備えた前記重金属吸着槽が、鉄粉含有分離物を廃棄するための廃棄汚泥水槽に連結されることを特徴とする。   In the contaminated soil cleaning equipment of the present invention, among the three or more heavy metal removal devices, the heavy metal adsorption tank provided in at least one heavy metal removal device is connected to a waste sludge water tank for discarding the iron powder-containing separation. It is characterized by being.

本発明の汚染土壌洗浄設備は、前記泥水槽から前記重金属吸着槽各々に汚染泥水を供給するための排泥管および前記重金属吸着槽から前記遠心分離機に前記鉄粉添加泥水を供給するための排泥管にそれぞれ自動バルブ及びポンプが、また、前記遠心分離機から前記洗浄泥水槽に前記洗浄泥水を供給するための排泥管に自動バルブが設けられるとともに、該自動バルブの開閉、およびこれに伴う前記ポンプの作動を制御する端末装置が備えられることを特徴とする。   The contaminated soil cleaning equipment of the present invention is for supplying the iron powder-added muddy water from the muddy water tank to the heavy metal adsorbing tank and supplying the contaminated mud water to the centrifuge from the heavy metal adsorbing tank. An automatic valve and a pump are respectively provided in the drainage pipe, and an automatic valve is provided in the drainage pipe for supplying the cleaning mud water from the centrifuge to the cleaning mud tank. The terminal device which controls the action | operation of the said pump accompanying is provided, It is characterized by the above-mentioned.

本発明の汚染土壌洗浄設備によれば、上流側に位置する重金属除去装置の遠心分離機にて比重分離した鉄粉含有分離物を、下流側に位置する重金属除去装置の重金属吸着槽に直接投下できる。これにより、遠心分離機にて分離した鉄粉を一時貯留する鉄粉前処理槽が不要になるとともに、前記鉄粉が比重及び粘性ともに大きい泥水に含まれた状態になっていても、ポンプ圧送可能な溶液状に作成し直す必要がないことから鉄粉ストック槽も不要とすることができ、設備コストを大幅に削減できるだけでなく、狭隘な敷地にも汚染土壌洗浄設備を設置することが可能となる。   According to the contaminated soil washing facility of the present invention, the iron powder-containing separation separated by specific gravity in the centrifuge of the heavy metal removal device located on the upstream side is directly dropped into the heavy metal adsorption tank of the heavy metal removal device located on the downstream side. it can. This eliminates the need for an iron powder pretreatment tank that temporarily stores the iron powder separated by the centrifuge, and even if the iron powder is contained in muddy water having a large specific gravity and viscosity, Since there is no need to recreate the solution as possible, an iron powder stock tank can be dispensed with. Not only can the equipment cost be greatly reduced, it is also possible to install contaminated soil cleaning equipment in a narrow site. It becomes.

また、鉄粉含有分離物をポンプ圧送可能な溶液状に作成し直すために要していた希釈水が不要となるため、材料コストを大幅に削減することが可能となる。   Moreover, since the diluting water required for recreating the iron powder-containing separated product into a solution that can be pumped is not necessary, the material cost can be greatly reduced.

加えて、鉄粉含有分離物をポンプ圧送可能な溶液状に作成し直す工程が不要となるため、作業時間が大幅に削減されるだけでなく、配管目詰まり等のポンプ圧送に関する不具合を考慮する必要がないため、作業全体の効率を大幅に向上することが可能となる。   In addition, there is no need to re-create the iron powder-containing separation into a solution that can be pumped, so not only the work time is greatly reduced, but also problems related to pumping such as clogging of piping are taken into account. Since it is not necessary, the efficiency of the entire work can be greatly improved.

本発明の汚染土壌の洗浄工法は、前記重金属除去装置各々において、前記重金属吸着槽にて、前記泥水と前記鉄粉もしくは前記鉄粉含有分離物を混在させる第1の工程、前記泥水と前記鉄粉もしくは前記鉄粉含有分離物を混合撹拌して、前記鉄粉もしくは前記鉄粉含有分離物に含まれる鉄粉に汚染泥水中の重金属を吸着させながら、前記鉄粉添加泥水を作製する第2の工程、および前記鉄粉添加泥水を前記重金属吸着槽から前記遠心分離機に供給し、前記洗浄泥水と前記鉄粉含有分離物とに比重分離する第3の工程を繰り返し実行させるとともに、少なくとも3つの重金属除去装置各々において同時に実施する作業工程を、上流側に位置する前記重金属除去装置に対して下流側に位置する重金属除去装置にて実施する工程が1工程先行した工程となるよう一つずつずらし、第1の工程を実施している下流に位置する重金属除去装置の重金属吸着槽に、第3の工程を実施している上流に位置する重金属除去装置から比重分離された鉄粉含有分離物を投下させることを特徴とする。   The contaminated soil cleaning method of the present invention is the first step of mixing the muddy water and the iron powder or the iron powder-containing separated material in the heavy metal adsorption tank in each of the heavy metal removing devices, the muddy water and the iron. Secondly, the iron powder-added muddy water is produced by mixing and stirring the powder or the iron powder-containing isolate to adsorb heavy metals in the contaminated muddy water to the iron powder contained in the iron powder or the iron powder-containing isolate. And the step of supplying the iron powder-added muddy water from the heavy metal adsorption tank to the centrifuge and repeatedly performing the specific gravity separation into the washing muddy water and the iron powder-containing separator, and at least 3 The work process performed simultaneously in each of the two heavy metal removal apparatuses is a process that precedes the process of performing the work process performed in the heavy metal removal apparatus located on the downstream side with respect to the heavy metal removal apparatus located on the upstream side. The specific gravity is separated from the heavy metal removal device located upstream in the third step in the heavy metal adsorption tank in the heavy metal removal device located downstream in the first step. It is characterized by dropping a separated product containing iron powder.

本発明の汚染土壌の洗浄工法は、前記第2の工程を複数回連続して行った後、第3の工程に移行することを特徴とする。   The contaminated soil cleaning method of the present invention is characterized in that the second step is continuously performed a plurality of times and then the third step is performed.

本発明の汚染土壌の洗浄工法によれば、鉄粉は重金属除去装置各々で洗浄泥水に含まれる重金属を吸着しながら、休眠することなく常に3つ以上の重金属除去装置を順に循環する。これにより、従来技術のような鉄粉前処理槽に一時貯留される時間や、ポンプ圧送可能な溶液状とするべく加水作業を行う時間が省略されるため、作業効率が向上し、作業時間を大幅に短縮することが可能となる。   According to the method for cleaning contaminated soil of the present invention, the iron powder circulates through three or more heavy metal removal devices in order, without sleeping, while adsorbing heavy metals contained in the washing mud water in each heavy metal removal device. This eliminates the time temporarily stored in the iron powder pretreatment tank as in the prior art and the time for performing the water addition work so as to obtain a solution that can be pumped, thereby improving work efficiency and reducing work time. It can be greatly shortened.

本発明によれば、鉄粉と汚染泥水を撹拌混合し作成した鉄粉添加泥水から遠心分離機にて重金属を吸着した鉄粉を分離するにあたり、上流に位置する重金属除去装置の遠心分離器にて分離された鉄粉を、一時貯留することなく下流に位置する重金属除去装置の重金属吸着槽に直接投下できるため、鉄粉が比重及び粘性ともに大きい鉄粉含有分離物に含まれた状態となっていても、過大な設備を必要とせず、また効率よく汚染土壌の浄化作業を複数の重金属除去装置にて繰り返し実施することが可能となる。   According to the present invention, when separating iron powder adsorbed heavy metal with a centrifuge from iron powder added mud prepared by stirring and mixing iron powder and contaminated mud, the centrifuge of the heavy metal removal device located upstream is used. The iron powder separated in this way can be dropped directly into the heavy metal adsorption tank of the heavy metal removal device located downstream without temporarily storing it, so that the iron powder is contained in the iron powder-containing isolate with both high specific gravity and viscosity. Even if it does, an excessive installation is not required and it becomes possible to repeatedly carry out the purification work of the contaminated soil efficiently with a plurality of heavy metal removing devices.

汚染土壌洗浄設備の概略を示す図である。It is a figure which shows the outline of a contaminated soil washing | cleaning equipment. 泥水処理施設の概略を示す図である。It is a figure which shows the outline of a muddy water treatment facility. 重金属汚染土壌の洗浄方法の流れを示すフロー図である。It is a flowchart which shows the flow of the washing | cleaning method of heavy metal contaminated soil. 重金属汚染土壌の洗浄方法を実施した際の鉄粉の流れを示す図である。It is a figure which shows the flow of the iron powder at the time of implementing the washing | cleaning method of heavy metal contaminated soil. 鉄粉の流れを2系統とした場合の重金属汚染土壌の洗浄方法の流れを示すフロー図である。It is a flowchart which shows the flow of the washing | cleaning method of heavy metal contaminated soil when the flow of iron powder is made into 2 systems. 汚染泥水の洗浄処理工程(s2)の作業状況を示す図である(その1)。It is a figure which shows the operation | work condition of the washing process process (s2) of contaminated mud water (the 1). 汚染泥水の洗浄処理工程(s2)の作業状況を示す図である(その2)。It is a figure which shows the operation | work condition of the washing process process (s2) of contaminated mud water (the 2). 汚染泥水の洗浄処理工程(s2)の作業状況を示す図である(その3)。It is a figure which shows the operation | work condition of the washing process process (s2) of contaminated mud water (the 3). 汚染土壌洗浄設備に備える重金属除去装置を4つにした場合の汚染泥水の洗浄処理工程(s2)における作業状況を示す図である。It is a figure which shows the operation | work condition in the washing process process (s2) of contaminated mud water at the time of using four heavy metal removal apparatuses with which a contaminated soil washing | cleaning equipment is equipped.

本発明は、ヒ素、フッ素、ホウ素、セレン、六価クロム、カドミウム、鉛、シアンなどの重金属を効率良く吸着し、固定化する性状を有する鉄粉を利用して、重金属汚染土壌を洗浄する方法であり、重金属汚染土壌を含む泥水に鉄粉を添加して撹拌・混合し、泥水中の土粒子に付着した重金属の微粒子を鉄粉表面に吸着させて固定化することにより、重金属汚染土壌を洗浄するものである。また、鉄粉が一定量あたりで吸着・固定化できる重金属量の限界を有し、吸着・固定化する能力がなくなるまで繰り返し利用可能であることに着目し、初期投下した鉄粉を、重金属汚染土壌の洗浄に繰り返し使用するものである。   The present invention is a method for cleaning heavy metal-contaminated soil using iron powder having the property of efficiently adsorbing and immobilizing heavy metals such as arsenic, fluorine, boron, selenium, hexavalent chromium, cadmium, lead, and cyanide By adding iron powder to the muddy water containing heavy metal contaminated soil, stirring and mixing, adsorbing the heavy metal fine particles adhering to the soil particles in the muddy water to the iron powder surface and immobilizing them, the heavy metal contaminated soil is It is to be washed. Also, paying attention to the fact that iron powder has a limit on the amount of heavy metals that can be adsorbed and immobilized per fixed amount, and can be used repeatedly until the ability to adsorb and immobilize is lost, the initially dropped iron powder is contaminated with heavy metals. It is used repeatedly for soil washing.

以下に、鉄粉を利用して重金属汚染土壌を洗浄する際に用いる汚染土壌洗浄設備、および汚染土壌洗浄設備を用いた汚染土壌の洗浄工法を、図1〜図9を用いて説明する。   Below, the contaminated soil washing | cleaning method used when wash | cleaning heavy metal-contaminated soil using iron powder and the cleaning method of contaminated soil using a contaminated soil washing | cleaning equipment are demonstrated using FIGS.

<汚染土壌洗浄設備>
まず、鉄粉を利用して重金属汚染土壌を洗浄する際に用いる汚染土壌洗浄設備1について、図1〜図2を参照して説明する。なお、汚染土壌洗浄設備1を説明するにあたり、鉄粉10の移動方向から上流側および下流側を定義している。
<Contaminated soil cleaning equipment>
First, the contaminated soil washing | cleaning equipment 1 used when wash | cleaning heavy metal contaminated soil using iron powder is demonstrated with reference to FIGS. In describing the contaminated soil cleaning facility 1, the upstream side and the downstream side are defined from the moving direction of the iron powder 10.

汚染土壌洗浄設備1は、図1に示すように、泥水槽2と、3つの重金属除去装置3を備えている。   As shown in FIG. 1, the contaminated soil cleaning facility 1 includes a mud tank 2 and three heavy metal removing devices 3.

泥水槽2は、重金属を含有する粘性土を含む汚染泥水100が貯留されるタンクであって、貯留されている汚染泥水100の比重を検出する比重検出器21と、後に述べる重金属除去装置3に汚染泥水100を供給するための、電磁バルブを設けた第1の排泥管22を備えている。貯留される汚染泥水100は、常に安定した比重にて重金属除去装置3に供給されるよう、比重検出器21にて比重の管理調整がなされている。   The muddy water tank 2 is a tank in which contaminated muddy water 100 containing viscous soil containing heavy metals is stored, and a specific gravity detector 21 that detects the specific gravity of the stored contaminated muddy water 100 and a heavy metal removing device 3 described later. A first mud discharge pipe 22 provided with an electromagnetic valve for supplying the contaminated mud water 100 is provided. Specific gravity management is adjusted by the specific gravity detector 21 so that the stored contaminated mud 100 is always supplied to the heavy metal removing device 3 with a stable specific gravity.

本実施の形態における泥水槽2は、泥水シールド工法で採用される泥水処理施設50に備えられた余剰泥水槽503である。泥水処理施設50は、図2に示すように、泥水式のシールド掘削機60から排出された排泥水より掘削土砂を分離し、掘削土砂を除去した泥水をシールド掘削機60の圧力室61に供給して、切羽面の安定及び掘削土砂の流体輸送に循環再利用するための装置である。   The muddy water tank 2 in the present embodiment is a surplus muddy water tank 503 provided in the muddy water treatment facility 50 employed in the muddy water shield method. As shown in FIG. 2, the muddy water treatment facility 50 separates the excavated sediment from the mud discharged from the muddy water type shield excavator 60 and supplies the mud water from which the excavated sediment has been removed to the pressure chamber 61 of the shield excavator 60. Thus, it is an apparatus for circulating and reusing for stabilizing the face and fluid transport of excavated soil.

具体的には、一次処理プラントである固液分離装置501と、二次処理プラントを構成する調整槽502および余剰泥水槽503を備えており、シールド掘削機60の圧力室61から排出された排泥水は、固液分離装置501にて一次処理として75μmm以上の土粒子が分離されて、分離された砂質分が一次処理土として搬出される。一方、75μmm以上の土粒子が除去された排泥水は、調整槽502に供給されて比重・粘性調整された後、再度シールド掘削機60の圧力室61に送泥される。   Specifically, it includes a solid-liquid separation device 501 that is a primary processing plant, an adjustment tank 502 and an excess mud tank 503 that constitute the secondary processing plant, and the exhaust discharged from the pressure chamber 61 of the shield excavator 60. As for the muddy water, soil particles of 75 μm or more are separated as a primary treatment by the solid-liquid separator 501, and the separated sandy matter is carried out as the primary treatment soil. On the other hand, the drained water from which the soil particles of 75 μm or more have been removed is supplied to the adjustment tank 502, adjusted for specific gravity and viscosity, and then sent to the pressure chamber 61 of the shield excavator 60 again.

そして、調整槽502の調整により生じた75μmm未満の土粒子を含む泥水のうち、地下水の流入による増加や泥水比重の上昇を抑制するために余剰となった余剰泥水は、余剰泥水槽503に供給される。本実施の形態では、余剰泥水槽503を泥水槽2としていることから、この75μmm未満の土粒子を含む余剰泥水を汚染泥水100として洗浄する。   Then, of the muddy water containing soil particles of less than 75 μm generated by the adjustment of the adjustment tank 502, surplus muddy water that has become surplus in order to suppress an increase due to the inflow of groundwater and an increase in the specific gravity of the muddy water is supplied to the excess muddy water tank 503. Is done. In the present embodiment, since the surplus muddy water tank 503 is the muddy water tank 2, the surplus muddy water containing soil particles of less than 75 μm is washed as the contaminated muddy water 100.

なお、泥水処理施設50は必ずしも泥水式シールド工法で採用されるものに限定するものではなく、例えば、連続地中壁工法等の泥水工法や、掘削した土に水を添加して泥水状態にして汚染土壌を浄化する分級洗浄施設に採用されるものでもよい。また、泥水槽2は、必ずしも泥水処理施設50に備えられた余剰泥水槽503を兼用するものでなくてもよく、独立して設置するものでもよい。   In addition, the muddy water treatment facility 50 is not necessarily limited to that employed in the muddy water type shield method, for example, a muddy water method such as a continuous underground wall method, or a muddy water state by adding water to the excavated soil. It may be employed in a classification and cleaning facility that purifies contaminated soil. Further, the muddy water tank 2 does not necessarily have to be used as the excess muddy water tank 503 provided in the muddy water treatment facility 50, and may be installed independently.

図1に示すように、重金属除去装置3はそれぞれ、重金属吸着水槽4とその下流側に配置される遠心分離機5を備えている。   As shown in FIG. 1, each heavy metal removing device 3 includes a heavy metal adsorbing water tank 4 and a centrifugal separator 5 disposed on the downstream side thereof.

重金属吸着水槽4は、泥水槽2より供給された汚染泥水100と鉄粉10を撹拌混合し、鉄粉10に汚染泥水100中の重金属を吸着させながら、鉄粉添加泥水101を作製するタンクであり、撹拌装置41を備えるとともに、遠心分離機5に鉄粉添加泥水101を供給するための、電磁バルブを設けた第2の排泥管42を備えている。なお、重金属吸着水槽4には、必要に応じて液面計や比重計、粘度計等を適宜備えてもよい。   The heavy metal adsorbing water tank 4 is a tank for producing the iron powder-added mud water 101 while stirring and mixing the contaminated mud water 100 and the iron powder 10 supplied from the mud water tank 2 and adsorbing the heavy metal in the contaminated mud water 100 to the iron powder 10. Yes, a stirring device 41 is provided, and a second mud discharge pipe 42 provided with an electromagnetic valve for supplying the iron powder-added mud water 101 to the centrifuge 5 is provided. In addition, the heavy metal adsorption water tank 4 may be appropriately provided with a liquid level meter, a specific gravity meter, a viscometer, or the like as necessary.

遠心分離機5は、重金属吸着水槽4より供給された鉄粉添加泥水101を比重分離する装置であり、本実施の形態ではサイクロンを採用している。サイクロンは、固体混じりの液体等を円筒容器に対して円周方向から渦を描く様に投入することで、比重の重い鉄粉10を遠心分離作用により円筒容器内壁に衝突させて下方向へ分離し、その他の泥水を円筒中心から上方向へ排出させる機能を有している。これにより、鉄粉添加泥水101は、鉄粉10及び分離しきれなかった土粒子を含む鉄粉含有分離物102と、重金属が除去された洗浄泥水103に分離される。   The centrifuge 5 is a device that separates the specific gravity of the iron powder-added mud water 101 supplied from the heavy metal adsorption water tank 4 and employs a cyclone in the present embodiment. The cyclone throws a solid mixed liquid or the like into the cylindrical container so as to draw a vortex from the circumferential direction, so that the iron powder 10 having a high specific gravity collides with the inner wall of the cylindrical container by the centrifugal separation and separates downward. In addition, it has a function of discharging other muddy water upward from the center of the cylinder. As a result, the iron powder-added muddy water 101 is separated into the iron powder 10 and the iron powder-containing separated product 102 containing soil particles that could not be separated, and the cleaning muddy water 103 from which heavy metals have been removed.

上述する構成の重金属除去装置3は、上流側に位置する重金属除去装置3の遠心分離機5が、下流側に位置する重金属除去装置3の重金属吸着水槽4の上方に位置するよう配置されている。これにより、例えば、最左に位置する重金属除去装置3の遠心分離機5にて分離された鉄粉含有分離物102は、ポンプ等の圧送装置を用いることなく、中央に位置する重金属除去装置3の重金属吸着水槽4に直接投下することができるものである。   The heavy metal removing device 3 configured as described above is arranged such that the centrifuge 5 of the heavy metal removing device 3 located on the upstream side is located above the heavy metal adsorbing water tank 4 of the heavy metal removing device 3 located on the downstream side. . Thereby, for example, the iron powder-containing separated product 102 separated by the centrifugal separator 5 of the heavy metal removing device 3 located on the leftmost side is not used by a pumping device such as a pump, and the heavy metal removing device 3 located in the center is used. The heavy metal adsorption water tank 4 can be directly dropped.

また、3つの重金属除去装置3は、後に述べる鉄粉タンク7から重金属吸着水槽4に投下された鉄粉10がすべての重金属除去装置3を経由して循環する循環路を形成するよう、連続的に配置されている。すなわち、最右に位置する重金属除去装置3の遠心分離機5にて分離された鉄粉含有分離物102は、ポンプ等の圧送装置を用いることなく、最左に位置する重金属除去装置3の重金属吸着水槽4に直接投下することができる。これにより、3つの重金属吸着水槽4はいずれも、第2の排泥管42の電磁バルブが閉の時に、鉄粉10に汚染泥水100中の重金属を吸着させながら鉄粉添加泥水101を作製する、鉄粉10を吸着させるためのタンクとして機能し、第2の排泥管42の電磁バルブが開の時に、下流側に位置する重金属除去装置3の重金属吸着水槽4に鉄粉10を含有した鉄粉含有分離物102を供給するための、鉄粉10をストックするタンクとして機能することとなる。   Further, the three heavy metal removing devices 3 are continuously formed so as to form a circulation path in which the iron powder 10 dropped from the iron powder tank 7 described later to the heavy metal adsorption water tank 4 circulates through all the heavy metal removing devices 3. Is arranged. In other words, the iron powder-containing separated product 102 separated by the centrifugal separator 5 of the heavy metal removal device 3 located on the rightmost side is used without using a pumping device such as a pump, and the heavy metal of the heavy metal removal device 3 located on the leftmost side. It can be dropped directly into the adsorption water tank 4. Thereby, all the three heavy metal adsorption water tanks 4 produce the iron powder-added mud water 101 while adsorbing the heavy metals in the contaminated mud water 100 to the iron powder 10 when the electromagnetic valve of the second mud pipe 42 is closed. The iron powder 10 is contained in the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located downstream when the electromagnetic valve of the second mud pipe 42 is open, functioning as a tank for adsorbing the iron powder 10. It functions as a tank for stocking the iron powder 10 for supplying the iron powder-containing separated product 102.

なお、重金属除去装置3は、図1で示す実施の形態では3つ、また図8で示す実施の形態では4つそれぞれ設置しているが、その数量は3つ以上であれば何ら限定されるものではない。   In the embodiment shown in FIG. 1, three heavy metal removing devices 3 and four in the embodiment shown in FIG. 8 are installed. However, the number of heavy metal removing devices 3 is not limited as long as the number is three or more. It is not a thing.

また、汚染土壌洗浄設備1は、図1に示すように、洗浄泥水槽6、鉄粉タンク7、廃棄汚泥水槽8、鉄粉分離装置9および廃棄鉄粉処理ピット91を備えている。   Moreover, the contaminated soil washing | cleaning equipment 1 is equipped with the washing | cleaning mud water tank 6, the iron powder tank 7, the waste sludge water tank 8, the iron powder separation apparatus 9, and the waste iron powder processing pit 91, as shown in FIG.

洗浄泥水槽6は、電磁バルブを設けた第3の排泥管51を介して遠心分離機5と連結されており、重金属が除去された洗浄泥水103が供給される。   The cleaning mud tank 6 is connected to the centrifuge 5 via a third drain pipe 51 provided with an electromagnetic valve, and is supplied with the cleaning mud 103 from which heavy metals have been removed.

鉄粉タンク7は、汚染泥水10に含まれる重金属を吸着するための鉄粉10が格納されており、重金属除去装置3の重金属吸着水槽4へ初期投下を行うものである。また、重金属除去装置3を循環することによって鉄粉10の量が規定量よりも減少した場合にも、この鉄粉タンク7より重金属吸着水槽4へ鉄粉10の追加投入を行う。   The iron powder tank 7 stores iron powder 10 for adsorbing heavy metals contained in the contaminated mud water 10, and performs an initial drop to the heavy metal adsorption water tank 4 of the heavy metal removal device 3. Further, even when the amount of the iron powder 10 is reduced from the specified amount by circulating the heavy metal removing device 3, the iron powder 10 is additionally charged from the iron powder tank 7 to the heavy metal adsorption water tank 4.

一方、廃棄汚泥水槽8は、電磁バルブを設けた第4の排泥管43を介して重金属吸着水槽4と連結されており、重金属吸着水槽4から鉄粉含有分離物102が供給されるものである。鉄粉分離装置9は、廃棄汚泥水槽8より供給される鉄粉含有分離物102を、鉄粉10及び分離しきれなかった土砂を含む最終鉄粉含有分離物104と洗浄泥水103とに分離するものである。そして、廃棄鉄粉処理ピット91は、鉄粉分離装置9より排出される最終鉄粉含有分離物104が投下されるピットである。   On the other hand, the waste sludge water tank 8 is connected to the heavy metal adsorbing water tank 4 through the fourth exhaust pipe 43 provided with an electromagnetic valve, and the iron powder-containing separated product 102 is supplied from the heavy metal adsorbing water tank 4. is there. The iron powder separator 9 separates the iron powder-containing separation 102 supplied from the waste sludge water tank 8 into the iron powder 10 and the final iron powder-containing separation 104 containing earth and sand that could not be separated, and the cleaning mud water 103. Is. The waste iron powder processing pit 91 is a pit into which the final iron powder-containing separation 104 discharged from the iron powder separation device 9 is dropped.

なお、本実施の形態では鉄粉分離装置9に、スクリューデカンタを採用しているが、これに限定されるものではなく、例えば水中比重選別機や磁力選別機等、鉄粉含有分離物102中から鉄粉10を分離できるものであれば、いずれを採用してもよい。また、鉄粉分離装置9は上記のいずれか1種類を採用してもよいが、複数を併用してより確実に、鉄粉含有分離物102から鉄粉10を分離するようにしてもよい。   In the present embodiment, a screw decanter is adopted as the iron powder separation device 9, but the present invention is not limited to this. For example, in the iron powder-containing separated material 102 such as an underwater specific gravity sorter or a magnetic sorter. As long as the iron powder 10 can be separated from the steel, any of them may be adopted. Further, any one of the above-described iron powder separation devices 9 may be adopted, but a plurality of them may be used together to more reliably separate the iron powder 10 from the iron powder-containing separated product 102.

このように、汚染土壌洗浄設備1は、上流側に位置する重金属除去装置3の遠心分離機5にて比重分離した鉄粉含有分離物102を下流側に位置する重金属除去装置3の重金属吸着槽4に直接投下させるものである。これにより、従来技術のような遠心分離機5にて分離した鉄粉10の一時貯留が不要になるとともに、鉄粉10が鉄粉含有分離物泥水102に含まれた状態になっていても、ポンプ圧送のために溶液状に作成し直す必要がない。このため、作業工程を減らすことができるだけでなく、設備を小規模化することができ、設備コストを大幅に削減できるとともに、狭隘な敷地にも汚染土壌洗浄設備1を設置することが可能となる。   As described above, the contaminated soil washing facility 1 has the heavy metal adsorption tank of the heavy metal removing device 3 located on the downstream side of the iron powder-containing separated material 102 separated by specific gravity in the centrifugal separator 5 of the heavy metal removing device 3 located on the upstream side. 4 to drop directly. This eliminates the need for temporary storage of the iron powder 10 separated by the centrifugal separator 5 as in the prior art, and even if the iron powder 10 is contained in the iron powder-containing separated mud water 102, There is no need to recreate the solution for pumping. For this reason, not only can the work process be reduced, but also the equipment can be reduced in scale, equipment costs can be greatly reduced, and the contaminated soil cleaning equipment 1 can be installed in a narrow site. .

<重金属汚染土壌の洗浄方法>
上述する汚染土壌洗浄設備1を用いて、汚染泥水100を鉄粉10にて洗浄する汚染土壌の洗浄工法を、図3〜図9を用いて以下に詳述する。
<How to clean heavy metal contaminated soil>
The contaminated soil cleaning method for cleaning the contaminated mud 100 with the iron powder 10 using the above-described contaminated soil cleaning facility 1 will be described in detail below with reference to FIGS.

図3のフロー図で示すように、汚染土壌100の洗浄工法は、前処理工程s1、汚染泥水100の洗浄処理工程s2、鉄粉含有物102の廃棄処理工程s3および洗浄泥水103の脱水処理工程s4、の4つの工程から構成されている。   As shown in the flowchart of FIG. 3, the cleaning method for the contaminated soil 100 includes a pretreatment step s1, a cleaning treatment step s2 for the contaminated mud water 100, a disposal processing step s3 for the iron powder-containing material 102, and a dehydration treatment step for the cleaning mud water 103. It consists of four steps s4.

<前処理工程:s1>
汚染泥水100を洗浄するに先立ち、泥水槽2に貯留された汚染泥水100に加水するなどして比重調整を行い、汚染泥水100が常に比重の上限値を超えないよう管理調整する工程である。比重の上限値は、汚染泥水100に鉄粉10を添加して作製した鉄粉添加泥水101を遠心分離機5に供給した際に、鉄粉含有分離物102に残留する土粒子が少なく、また洗浄泥水103に残留する鉄粉10が少なくなるよう、あらかじめ室内実験等により設定しておくとよい。
<Pretreatment process: s1>
Prior to washing the contaminated mud 100, the specific gravity is adjusted by adding water to the contaminated mud 100 stored in the mud tank 2, and the adjustment is performed so that the contaminated mud 100 does not always exceed the upper limit of the specific gravity. The upper limit of the specific gravity is such that when the iron powder-added mud water 101 prepared by adding the iron powder 10 to the contaminated mud water 100 is supplied to the centrifuge 5, there are few soil particles remaining in the iron powder-containing separated material 102, It may be set in advance by an indoor experiment or the like so that the iron powder 10 remaining in the cleaning mud 103 is reduced.

<汚染泥水の洗浄処理工程:s2>
前処理工程(s1)で比重管理された汚染泥水100を、鉄粉10と接触させて洗浄し、鉄粉含有分離物102と洗浄泥水103を得る工程であり、以下に示す第1〜第3の工程よりなる汚染泥水10の洗浄が3つの重金属除去装置3各々で実施される。このとき、3つの重金属除去装置3は同時に稼働するのではなく、1つずつ順番に稼働することとなる。図4(a)に示す鉄粉タンク7から初期投下される鉄粉10の動きを追いながら、処理の流れを説明する。
<Cleaning process of contaminated mud water: s2>
The contaminated mud water 100 whose specific gravity is controlled in the pretreatment step (s1) is washed by contacting with the iron powder 10 to obtain the iron powder-containing separated product 102 and the washed mud water 103. Cleaning of the contaminated mud water 10 consisting of the above steps is carried out by each of the three heavy metal removing devices 3. At this time, the three heavy metal removing devices 3 do not operate simultaneously, but operate one by one in order. The flow of processing will be described while following the movement of the iron powder 10 initially dropped from the iron powder tank 7 shown in FIG.

まず、最左に位置する重金属除去装置3にて、以下に示す第1〜第3の工程が実施される。
最左に位置する重金属除去装置3の重金属吸着水槽4に、鉄粉タンク7に収納されている鉄粉10を投下する。その後、泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉10を混在させる(第1の工程)。重金属吸着水槽4に貯留した汚染泥水100と鉄粉10とを撹拌装置41にて撹拌混合し、鉄粉10に汚染泥水100中の重金属を吸着させながら、鉄粉添加泥水101を作製する(第2の工程)。この後、鉄粉添加泥水101を遠心分離機5に供給し、鉄粉含有分離物102と洗浄泥水103とに分離する(第3の工程)。洗浄泥水103は洗浄泥水槽6に供給され、鉄粉含有分離物102は、中央に位置する重金属除去装置3の重金属吸着水槽4に投下される。こうして最左に位置する重金属除去装置3の重金属吸着水槽4は空の状態となる。
First, the following first to third steps are performed in the heavy metal removing device 3 located on the leftmost side.
The iron powder 10 stored in the iron powder tank 7 is dropped into the heavy metal adsorbing water tank 4 of the heavy metal removing device 3 located at the leftmost position. Then, the contaminated mud water 100 is supplied from the mud tank 2 and the contaminated mud water 100 and the iron powder 10 are mixed (first step). The contaminated mud water 100 and the iron powder 10 stored in the heavy metal adsorbing water tank 4 are stirred and mixed by the stirring device 41, and the iron powder-added mud water 101 is produced while adsorbing the heavy metal in the contaminated mud water 100 to the iron powder 10 (first). Step 2). Thereafter, the iron powder-added muddy water 101 is supplied to the centrifuge 5 and separated into the iron powder-containing separated product 102 and the washed muddy water 103 (third step). The cleaning muddy water 103 is supplied to the cleaning muddy water tank 6, and the iron powder-containing separated product 102 is dropped into the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located at the center. Thus, the heavy metal adsorbing water tank 4 of the heavy metal removing device 3 located on the leftmost side is in an empty state.

次に、中央に位置する重金属除去装置3にて、以下に示す第1〜第3の工程が実施される。
最左に位置する重金属除去装置3の第3の工程で分離された鉄粉含有分離物102が投下された、中央に位置する重金属除去装置3の重金属吸着水槽4に汚染泥水100を供給し、汚染泥水100と鉄粉含有分離物102を混在させる(第1の工程)。このように、以降の各重金属除去装置3における第1の工程では、最左に位置する重金属除去装置3の重金属吸着水槽4に、鉄粉タンク7から供給された鉄粉10が、鉄粉含有分離物102に含まれた状態となって循環供給されることとなる。
Next, in the heavy metal removing device 3 located in the center, the following first to third steps are performed.
Supplying the contaminated mud water 100 to the heavy metal adsorbing water tank 4 of the heavy metal removing device 3 located in the center where the iron powder-containing separated product 102 separated in the third step of the heavy metal removing device 3 located on the leftmost side is dropped, The contaminated mud water 100 and the iron powder-containing separated product 102 are mixed (first step). Thus, in the 1st process in each subsequent heavy metal removal apparatus 3, the iron powder 10 supplied from the iron powder tank 7 to the heavy metal adsorption | suction water tank 4 of the heavy metal removal apparatus 3 located in the leftmost is iron powder containing. It will be circulated and supplied in the state of being contained in the separated product 102.

そして、重金属吸着水槽4に貯留した汚染泥水100と鉄粉含有分離物102とを撹拌装置41にて撹拌混合し、鉄粉含有分離物102に含まれる鉄粉10に汚染泥水100中の重金属を吸着させながら、鉄粉添加泥水101を作製する(第2の工程)。この後、先に述べた第3の工程を実施すると、洗浄泥水103は洗浄泥水槽6に供給され、鉄粉含有分離物102は、最右に位置する重金属除去装置3の重金属吸着水槽4に投下される。こうして中央に位置する重金属除去装置3の重金属吸着水槽4は空の状態となる。   Then, the contaminated mud water 100 stored in the heavy metal adsorbing water tank 4 and the iron powder-containing isolate 102 are stirred and mixed by the stirring device 41, and the heavy metal in the contaminated mud water 100 is added to the iron powder 10 contained in the iron powder-containing isolate 102. While adsorbing, iron powder-added mud water 101 is produced (second step). Thereafter, when the third step described above is performed, the cleaning mud water 103 is supplied to the cleaning mud tank 6, and the iron powder-containing separated material 102 is placed in the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located at the rightmost position. Dropped. Thus, the heavy metal adsorbing water tank 4 of the heavy metal removing device 3 located in the center becomes empty.

この後、最右に位置する重金属除去装置3にて、以下に示す第1〜第3の工程が実施される。
中央に位置する重金属除去装置3の第3の工程で分離された鉄粉含有分離物102が投下された、最右に位置する重金属除去装置3の重金属吸着水槽4に、泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉含有分離物102を混在させる(第1の工程)。次に、第2の工程が実施され、この後、第3の工程が実施されて、洗浄泥水103は洗浄泥水槽6に供給され、鉄粉含有分離物102は、最左に位置する重金属除去装置3における空の状態の重金属吸着水槽4に投下される。こうして最右に位置する重金属除去装置3の重金属吸着水槽4は空の状態となる。
Then, the following 1st-3rd process is implemented in the heavy metal removal apparatus 3 located in the rightmost.
From the mud tank 2 to the heavy metal adsorbing water tank 4 of the heavy metal removing apparatus 3 located at the rightmost position where the iron powder-containing separated product 102 separated in the third step of the heavy metal removing apparatus 3 located in the center is dropped. 100 is supplied, and the contaminated mud water 100 and the iron powder-containing separator 102 are mixed (first step). Next, the second step is performed, and then the third step is performed. The cleaning mud water 103 is supplied to the cleaning mud tank 6 and the iron powder-containing separation 102 is removed from the leftmost heavy metal. It is dropped into an empty heavy metal adsorption water tank 4 in the apparatus 3. Thus, the heavy metal adsorbing water tank 4 of the heavy metal removing device 3 located on the rightmost side becomes empty.

このように、最左に位置する重金属除去装置3の重金属吸着水槽4に初期投下された鉄粉10は、3つの重金属除去装置3各々で繰り返し使用されることから、あらかじめ室内実験等にてその転用回数の上限値を算定しておくとともに、安全率を見込んで転用回数の上限値に至る手前の警告回数を設定しておくとよい。   In this way, the iron powder 10 initially dropped in the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located on the leftmost side is repeatedly used in each of the three heavy metal removing devices 3. The upper limit value of the number of diversions is calculated, and the number of warnings before reaching the upper limit value of the diversion number in consideration of the safety factor may be set.

そして、上述のとおり鉄粉10が、3つの重金属除去装置3各々にて汚染泥水100の洗浄を行いながら一巡した後、鉄粉含有分離物102に含まれる鉄粉100の転用回数が警告回数を超えておらず、かつ泥水槽2に貯留した汚染泥水100が残存している場合には、再度、最左に位置する重金属除去装置3に戻って、汚染泥水100の洗浄を繰り返す。   Then, as described above, after the iron powder 10 makes a round while cleaning the contaminated mud water 100 in each of the three heavy metal removing devices 3, the number of diversions of the iron powder 100 contained in the iron powder-containing separated product 102 indicates the number of warnings. If it does not exceed and the contaminated mud 100 stored in the mud tank 2 remains, the process returns to the heavy metal removing device 3 located at the leftmost and the washing of the contaminated mud 100 is repeated.

一方、汚染泥水の洗浄処理工程(s2)の過程で、鉄粉含有分離物102に含まれる鉄粉100の転用回数が警告回数を超えた場合、もしくは泥水槽2に貯留した汚染泥水100が尽きた場合に、鉄粉含有分離物102は廃棄汚泥水槽8に供給される。   On the other hand, in the course of the contaminated mud washing process (s2), when the number of diversions of the iron powder 100 contained in the iron powder-containing separated product 102 exceeds the number of warnings, or the contaminated mud 100 stored in the mud tank 2 is exhausted. In this case, the iron powder-containing separated product 102 is supplied to the waste sludge water tank 8.

<鉄粉含有分離物102の廃棄処理工程:s3>
上記の汚染泥水の洗浄処理工程(s2)を経て、廃棄汚泥水槽8に供給された鉄粉含有分離物102を廃棄処理するための工程である。
廃棄汚泥水槽8に貯留された鉄粉含有分離物102は、廃棄汚泥水槽8にて適宜加水されて鉄粉分離装置9にて分離処理するのに好適な比重となるように調整された上で、鉄粉分離装置9に供給され、鉄粉10及び分離しきれなかった土砂を含む最終鉄粉含有分離物104と洗浄泥水103とに分離される。そして、最終鉄粉含有分離物104は廃棄鉄粉処理ピット91に投下された後、減容および脱水を経てケーキとなり、重金属を含む産業廃棄物として搬出される。
<Disposal process of iron powder-containing separated product 102: s3>
This is a process for discarding the iron powder-containing separated product 102 supplied to the waste sludge water tank 8 through the above-described contaminated mud water cleaning process (s2).
The iron powder-containing separated substance 102 stored in the waste sludge water tank 8 is adjusted to have a specific gravity suitable for being separated by the iron powder separator 9 by being appropriately hydrated in the waste sludge water tank 8. Then, it is supplied to the iron powder separation device 9 and separated into a final iron powder-containing separation 104 containing the iron powder 10 and the earth and sand that could not be separated and the cleaning mud water 103. Then, the final iron powder-containing separated product 104 is dropped into the waste iron powder processing pit 91 and then reduced in volume and dehydrated to become a cake, which is carried out as industrial waste containing heavy metals.

<洗浄泥水103の脱水処理工程:s4>
上記の汚染泥水の洗浄処理工程(s2)もしくは鉄粉含有分離物102の廃棄処理工程(s3)を経て、洗浄泥水槽6に供給された洗浄泥水103を脱水する工程である。
洗浄泥水槽6に貯留された洗浄泥水103は、図示しないスラリー槽に供給されて減容および脱水を経てケーキとなり、健全な産業廃棄物もしくは浄化済土壌として搬出される。
<Dehydration process of cleaning mud 103: s4>
This is a step of dehydrating the cleaning mud 103 supplied to the cleaning mud tank 6 through the cleaning step (s2) of the contaminated mud or the disposal step (s3) of the iron powder-containing separated product 102.
The cleaning muddy water 103 stored in the cleaning muddy water tank 6 is supplied to a slurry tank (not shown), undergoes volume reduction and dehydration, becomes a cake, and is carried out as healthy industrial waste or purified soil.

なお、本実施の形態では、鉄粉10が3つの重金属除去装置3各々にて汚染泥水100の洗浄を行いながら一巡した後、鉄粉含有分離物102に含まれる鉄粉10の転用回数、および泥水槽2に貯留した汚染泥水100の貯留量を確認しているが、必ずしもこれに限定されるものではなく、重金属除去装置3各々で汚染泥水100の洗浄処理が終了するごとに、上記の確認を行うようにしてもよい。   In the present embodiment, after the iron powder 10 makes a round while washing the contaminated mud water 100 in each of the three heavy metal removing devices 3, the number of times of diversion of the iron powder 10 contained in the iron powder-containing separated product 102, and Although the amount of the contaminated mud water 100 stored in the mud tank 2 is confirmed, the present invention is not necessarily limited to this. Each time the cleaning process of the contaminated mud water 100 is completed in each heavy metal removal device 3, the above confirmation is performed. May be performed.

ところで、上記の汚染泥水の洗浄処理工程(s2)では、鉄粉タンク7に収納されている鉄粉10もしくは第3の工程で遠心分離機5にて比重分離される鉄粉含有分離物102を、空の状態の重金属吸着水槽4に投下した後、汚染泥水100を供給して、汚染泥水100と鉄粉10もしくは鉄粉含有分離物102を混在させ、これを第1の工程とした。しかし、第1の工程は、必ずしもこの方法に限定されるものではなく、重金属吸着水槽4に対して、鉄粉タンク7に収納されている鉄粉10もしくは遠心分離機5にて分離される鉄粉含有分離物102の投下と、汚染泥水100の供給を同時に行い、汚染泥水100と鉄粉10もしくは鉄粉含有分離物102を混在させて第1の工程としてもよい。   By the way, in the contaminated mud water washing step (s2), the iron powder 10 stored in the iron powder tank 7 or the iron powder-containing separated material 102 that is separated by the centrifugal separator 5 in the third step is used. Then, after dropping into the empty heavy metal adsorption water tank 4, the contaminated mud water 100 was supplied, and the contaminated mud water 100 and the iron powder 10 or the iron powder-containing separated substance 102 were mixed, which was defined as the first step. However, the first step is not necessarily limited to this method, and the iron separated in the iron powder tank 7 or the centrifuge 5 stored in the iron powder tank 7 with respect to the heavy metal adsorption water tank 4. The first step may be performed by simultaneously dropping the powder-containing separated material 102 and supplying the contaminated mud water 100 and mixing the contaminated mud water 100 and the iron powder 10 or the iron powder-containing separated material 102.

つまり、鉄粉含有分離物102の投下に着目すると、最左に位置する重金属除去装置3における第3の工程と、中央に位置する重金属除去装置3における第1の工程を同時に行う。同様に、中央に位置する重金属除去装置3における第3の工程と最右に位置する重金属除去装置3における第1の工程、及び最右に位置する重金属除去装置3における第3の工程と最左に位置する重金属除去装置3における第1の工程を、それぞれ同時に行う。こうすると、上流側に位置する重金属除去装置3の第3の工程と、下流側に位置する重金属除去装置3の第1の工程が同時に行われることとなり、汚染泥水の洗浄処理工程(s2)の作業時間を短縮することができ、作業の効率化を図ることが可能となる。   That is, paying attention to the dropping of the iron powder-containing separated product 102, the third step in the heavy metal removing device 3 located at the leftmost and the first step in the heavy metal removing device 3 located in the center are simultaneously performed. Similarly, the third step in the heavy metal removing device 3 located at the center and the first step in the heavy metal removing device 3 located at the rightmost, and the third step and the leftmost in the heavy metal removing device 3 located at the rightmost Each of the first steps in the heavy metal removing device 3 located at the same time is performed simultaneously. If it carries out like this, the 3rd process of the heavy metal removal apparatus 3 located in an upstream, and the 1st process of the heavy metal removal apparatus 3 located in a downstream will be performed simultaneously, and the cleaning process process (s2) of contaminated mud water The work time can be shortened, and the work efficiency can be improved.

そこで、重金属汚染土壌の洗浄方法における他の実施の形態として、上述する空の状態の下流側に位置する重金属除去装置3の重金属吸着槽4に対して、汚染泥水100の供給と、上流側に位置する重金属除去装置3の第3の工程で分離する鉄粉含有分離物102の投下を同時に行い、汚染泥水100と鉄粉含有分離物102を混在させ、これを第1の工程とする方法を示す。   Therefore, as another embodiment of the method for cleaning heavy metal contaminated soil, the supply of contaminated mud water 100 to the heavy metal adsorption tank 4 of the heavy metal removal device 3 located on the downstream side of the above-described empty state, and the upstream side A method of simultaneously dropping the iron powder-containing separated material 102 separated in the third step of the heavy metal removing device 3 that is located, mixing the contaminated mud water 100 and the iron powder-containing separated material 102, and setting this as the first step. Show.

また、この実施の形態では、図4(a)で示した鉄粉10の流れに図4(b)で示す鉄粉10の流れを追加して、図5で示すように鉄粉10の流れを2系統として、3つの重金属除去装置3をより効率よく稼働させる例を示す。   Moreover, in this embodiment, the flow of the iron powder 10 shown in FIG. 4 (b) is added to the flow of the iron powder 10 shown in FIG. 4 (a), and the flow of the iron powder 10 as shown in FIG. An example in which three heavy metal removing devices 3 are operated more efficiently is shown.

以下に、図5〜図8を参照しつつ、具体的に汚染土壌の洗浄工法における他の実施の形態を説明する。
なお、前処理工程s1、鉄粉含有物102の廃棄処理工程s3および洗浄泥水103の脱水処理工程s4は、先に示した実施の形態と同一であることから省略し、2系統の鉄粉10の流れを備えた汚染泥水100の洗浄処理工程s2に着目し、第1バッチ〜第9バッチの処理時間単位で詳述する。
Hereinafter, another embodiment of the contaminated soil cleaning method will be described with reference to FIGS.
Note that the pretreatment step s1, the waste treatment step s3 of the iron powder-containing material 102, and the dehydration treatment step s4 of the cleaning mud water 103 are omitted because they are the same as those in the above-described embodiment, and two types of iron powder 10 Focusing on the cleaning process step s2 of the contaminated mud 100 with the flow of the above, detailed description will be made in units of processing time of the first batch to the ninth batch.

第1バッチから第3バッチは3つの重金属除去装置3すべてを稼働させるための準備段階である。   The first to third batches are preparation steps for operating all three heavy metal removing devices 3.

<第1バッチ:図6(a)>
最左に位置する重金属除去装置3にて、鉄粉タンク7に収納されている鉄粉10(1系統目の鉄粉10)を添加すると同時に、重金属吸着水槽4に泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉10を混在させる(第1の工程)。
この時、中央に位置する重金属除去装置3及び最右に位置する重金属除去装置3は未稼働である。
<第2バッチ:図6(b)>
最左に位置する重金属除去装置3では、重金属吸着水槽4に貯留した汚染泥水100と鉄粉10とを撹拌装置41にて撹拌混合し、鉄粉10に汚染泥水100中の重金属を吸着させながら、鉄粉添加泥水101を作製する(第2の工程)。
中央に位置する重金属除去装置3は未稼働である。
最右に位置する重金属除去装置3では、鉄粉タンク7に収納されている鉄粉10(2系統目の鉄粉10)を添加すると同時に、重金属吸着水槽4に泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉10混在させる(第1の工程)。
<第3バッチ:図6(c)>
最左に位置する重金属除去装置3では、遠心分離機5にて鉄粉添加泥水101から鉄粉含有分離物102を分離し(第3の工程)、中央に位置する重金属除去装置3の重金属吸着水槽4に投下する。これにより、最左に位置する重金属除去装置3は空の状態となる。
中央に位置する重金属除去装置3では、重金属吸着水槽4に最左に位置する重金属除去装置3における第3の工程で分離された鉄粉含有分離物102が投下されると同時に、泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉含有分離物102を混在させる(第1の工程)。
最右に位置する重金属除去装置3では、重金属吸着水槽4に貯留した汚染泥水100と鉄粉10とを撹拌装置41にて撹拌混合し、鉄粉10に汚染泥水100中の重金属を吸着させながら、鉄粉添加泥水101を作製する(第2の工程)。
<First batch: Fig. 6 (a)>
At the leftmost heavy metal removing device 3, iron powder 10 (first iron powder 10) stored in the iron powder tank 7 is added, and at the same time, the contaminated muddy water 100 from the mud tank 2 to the heavy metal adsorption water tank 4. And contaminated mud water 100 and iron powder 10 are mixed (first step).
At this time, the heavy metal removing device 3 located at the center and the heavy metal removing device 3 located at the rightmost are not in operation.
<Second batch: FIG. 6B>
In the heavy metal removing device 3 located on the leftmost side, the contaminated mud water 100 and the iron powder 10 stored in the heavy metal adsorbing water tank 4 are stirred and mixed by the stirring device 41, and the heavy metal in the contaminated mud water 100 is adsorbed to the iron powder 10. The iron powder-added mud water 101 is prepared (second step).
The heavy metal removing device 3 located in the center is not in operation.
In the heavy metal removal device 3 located on the rightmost side, the iron powder 10 (second iron powder 10) stored in the iron powder tank 7 is added, and at the same time, the contaminated mud water 100 from the mud tank 2 is added to the heavy metal adsorption tank 4. Supply and mix the contaminated mud water 100 and the iron powder 10 (first step).
<Third batch: FIG. 6 (c)>
In the heavy metal removal device 3 located on the leftmost side, the iron powder-containing separation product 102 is separated from the iron powder-added mud water 101 by the centrifugal separator 5 (third step), and the heavy metal adsorption device 3 located in the center absorbs the heavy metal. Drop into the aquarium 4. As a result, the heavy metal removing device 3 located on the leftmost side is in an empty state.
In the heavy metal removing device 3 located in the center, the iron powder-containing separated product 102 separated in the third step in the heavy metal removing device 3 located on the leftmost side is dropped into the heavy metal adsorbing water tank 4 and at the same time from the muddy water tank 2. The contaminated mud water 100 is supplied, and the contaminated mud water 100 and the iron powder containing separated material 102 are mixed (first step).
In the heavy metal removing device 3 located on the rightmost side, the contaminated mud water 100 and the iron powder 10 stored in the heavy metal adsorbing water tank 4 are stirred and mixed by the stirring device 41, and the heavy metal in the contaminated mud water 100 is adsorbed to the iron powder 10. The iron powder-added mud water 101 is prepared (second step).

このように、第3バッチにて3つの重金属除去装置3すべてが稼働を開始することとなる。
次に示す第4バッチから第6バッチは、鉄粉含有分離物102に含まれる鉄粉100の転用回数が警告回数を超えておらず、かつ泥水槽2に貯留した汚染泥水100が残存している場合に、汚染泥水100の洗浄を繰り返す段階である。
Thus, all the three heavy metal removal apparatuses 3 will start operation in the third batch.
From the 4th batch to the 6th batch shown below, the number of diversions of the iron powder 100 contained in the iron powder-containing separated product 102 does not exceed the number of warnings, and the contaminated mud water 100 stored in the mud tank 2 remains. In this case, the cleaning of the contaminated mud 100 is repeated.

<第4バッチ:図7(a)>
最左に位置する重金属除去装置3では、空の状態の重金属吸着水槽4に最右に位置する重金属除去装置3における第3の工程で分離された鉄粉含有分離物102が投下されると同時に、泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉含有分離物102を混在させる(第1の工程)。
中央に位置する重金属除去装置3では、重金属吸着水槽4に貯留した汚染泥水100と鉄粉含有分離物102とを撹拌装置41にて撹拌混合し、鉄粉含有分離物102に含まれる鉄粉10に汚染泥水100中の重金属を吸着させながら、鉄粉添加泥水101を作製する(第2の工程)。
最右に位置する重金属除去装置3では、第3の工程を実施し、遠心分離機5にて分離した鉄粉含有分離物102を、最左に位置する重金属除去装置3の重金属吸着水槽4に投下する。これにより、最右に位置する重金属除去装置3は空の状態となる。
<Fourth batch: FIG. 7 (a)>
At the leftmost heavy metal removing device 3, the iron powder-containing separated material 102 separated in the third step in the rightmost heavy metal removing device 3 is dropped into the empty heavy metal adsorption water tank 4. Then, the contaminated mud water 100 is supplied from the mud tank 2, and the contaminated mud water 100 and the iron powder-containing separated substance 102 are mixed (first step).
In the heavy metal removal device 3 located in the center, the contaminated mud water 100 stored in the heavy metal adsorption water tank 4 and the iron powder-containing separated material 102 are stirred and mixed by the stirring device 41, and the iron powder 10 contained in the iron powder-containing separated material 102 is mixed. The iron powder-added mud water 101 is produced while adsorbing heavy metals in the contaminated mud water 100 (second step).
In the heavy metal removing device 3 located on the rightmost side, the third step is performed, and the iron powder-containing separation 102 separated by the centrifugal separator 5 is placed in the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located on the leftmost side. Drop it. As a result, the heavy metal removing device 3 located on the rightmost side is in an empty state.

<第5バッチ:図7(b)>
最左に位置する重金属除去装置3では、第2の工程を実施する。
中央に位置する重金属除去装置3では、第3の工程を実施し、遠心分離機5にて分離した鉄粉含有分離物102を、最右に位置する重金属除去装置3の重金属吸着水槽4に投下する。これにより、中央に位置する重金属除去装置3は空の状態となる。
最右に位置する重金属除去装置3では、空の状態の重金属吸着水槽4に中央に位置する重金属除去装置3における第3の工程で分離された鉄粉含有分離物102が投下されると同時に、泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉含有分離物102を混在させる(第1の工程)。
<Fifth batch: FIG. 7 (b)>
In the heavy metal removing device 3 located on the leftmost side, the second step is performed.
In the heavy metal removal device 3 located in the center, the third step is performed, and the iron powder-containing separation 102 separated by the centrifuge 5 is dropped into the heavy metal adsorption water tank 4 of the heavy metal removal device 3 located in the rightmost position. To do. Thereby, the heavy metal removal apparatus 3 located in the center will be in an empty state.
In the heavy metal removal device 3 located on the rightmost side, the iron powder-containing separation product 102 separated in the third step in the heavy metal removal device 3 located in the center is dropped into the empty heavy metal adsorption water tank 4, The contaminated mud water 100 is supplied from the mud tank 2 and the contaminated mud water 100 and the iron powder-containing separated material 102 are mixed (first step).

<第6バッチ:図7(c)>
最左に位置する重金属除去装置3では、第3の工程を実施し、遠心分離機5にて分離した鉄粉含有分離物102を、中央に位置する重金属除去装置3の重金属吸着水槽4に投下する。これにより、最左に位置する重金属除去装置3は空の状態となる。
中央に位置する重金属除去装置3では、空の状態の重金属吸着水槽4に最左に位置する重金属除去装置3における第3の工程で分離された鉄粉含有分離物102が投下されると同時に、泥水槽2から汚染泥水100を供給し、汚染泥水100と鉄粉含有分離物102を混在させる(第1の工程)。
最右に位置する重金属除去装置3では、第2の工程を実施する。
<6th batch: FIG. 7 (c)>
In the heavy metal removal device 3 located on the leftmost side, the third step is performed, and the iron powder-containing separation 102 separated by the centrifuge 5 is dropped into the heavy metal adsorption water tank 4 of the heavy metal removal device 3 located in the center. To do. As a result, the heavy metal removing device 3 located on the leftmost side is in an empty state.
In the heavy metal removal device 3 located in the center, the iron powder-containing separation 102 separated in the third step in the heavy metal removal device 3 located on the leftmost side is dropped into the empty heavy metal adsorption water tank 4, The contaminated mud water 100 is supplied from the mud tank 2 and the contaminated mud water 100 and the iron powder-containing separated material 102 are mixed (first step).
In the heavy metal removing device 3 located on the rightmost side, the second step is performed.

以下、第7バッチから第9バッチは、鉄粉含有分離物102に含まれる鉄粉10の転用回数が上限に達した場合、もしくは処理する汚染泥水100が尽きた場合に、鉄粉含有分離物102を、重金属除去装置3から廃棄汚泥水槽8に供給する廃棄準備段階である。   Hereinafter, in the seventh batch to the ninth batch, when the number of diversions of the iron powder 10 included in the iron powder-containing separated product 102 reaches the upper limit, or when the contaminated mud 100 to be processed is exhausted, the iron powder-containing separated product is used. This is a disposal preparation stage in which 102 is supplied from the heavy metal removing device 3 to the disposal sludge water tank 8.

<第7バッチ:図8(a)>
最左に位置する重金属除去装置3では、第3の工程が終了後、空の状態の重金属吸着水槽4に、最右に位置する重金属除去装置3における第3の工程で分離された鉄粉含有分離物102が投下される(第1の工程)。
中央に位置する重金属除去装置3では、第2の工程を実施する。
最右に位置する重金属除去装置3では、第3の工程を実施し、遠心分離機5にて分離した鉄粉含有分離物102を、最左に位置する重金属除去装置3の重金属吸着水槽4に投下する。これにより、最右に位置する重金属除去装置3は空の状態となる。
<Seventh batch: FIG. 8 (a)>
In the heavy metal removal device 3 located on the leftmost side, after the third step is finished, the empty heavy metal adsorption water tank 4 contains the iron powder separated in the third step in the heavy metal removal device 3 located on the rightmost side. The separated product 102 is dropped (first step).
In the heavy metal removing device 3 located in the center, the second step is performed.
In the heavy metal removing device 3 located on the rightmost side, the third step is performed, and the iron powder-containing separation 102 separated by the centrifugal separator 5 is placed in the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located on the leftmost side. Drop it. As a result, the heavy metal removing device 3 located on the rightmost side is in an empty state.

<第8バッチ:図8(b)>
最左に位置する重金属除去装置3では、重金属吸着水槽4に貯留した鉄粉含有分離物102(1系統目の鉄粉10を含む)を第4の排泥管43を介して廃棄汚泥水槽8に排出する。このとき、鉄粉含有分離物102がポンプ圧送できない場合には、適宜加水して溶液化し粘性を調整する。
中央に位置する重金属除去装置3では、第3の工程を実施し、遠心分離機5にて分離した鉄粉含有分離物102を、最右に位置する重金属除去装置3の重金属吸着水槽4に投下する。これにより、中央に位置する重金属除去装置3は空の状態となる。
最右に位置する重金属除去装置3では、空の状態の重金属吸着水槽4に中央に位置する重金属除去装置3における第3の工程で分離された鉄粉含有分離物102が投下される。投下された鉄粉含有分離物102がポンプ圧送できない程度の粘性を有している場合には、適宜加水して溶液化し粘性を調整しておく。
<Eighth batch: FIG. 8 (b)>
In the heavy metal removing device 3 located on the leftmost side, the waste sludge tank 8 containing the iron powder-containing separated material 102 (including the first iron powder 10) stored in the heavy metal adsorption tank 4 is passed through the fourth sludge pipe 43. To discharge. At this time, when the iron powder-containing separated product 102 cannot be pumped, it is appropriately added to make a solution to adjust the viscosity.
In the heavy metal removal device 3 located in the center, the third step is performed, and the iron powder-containing separation 102 separated by the centrifuge 5 is dropped into the heavy metal adsorption water tank 4 of the heavy metal removal device 3 located in the rightmost position. To do. Thereby, the heavy metal removal apparatus 3 located in the center will be in an empty state.
In the heavy metal removing device 3 located on the rightmost side, the iron powder-containing separated product 102 separated in the third step in the heavy metal removing device 3 located in the center is dropped into the empty heavy metal adsorption water tank 4. In the case where the dropped iron powder-containing separated product 102 has such a viscosity that it cannot be pumped, it is appropriately hydrated to form a solution to adjust the viscosity.

<第9バッチ:図8(c)>
最右に位置する重金属除去装置3では、遠心分離機5を介して鉄粉含有分離物102を最左に位置する重金属除去装置3の重金属吸着水槽4に供給する。これにより、最右に位置する重金属除去装置3は空の状態となる。
<9th batch: FIG. 8 (c)>
In the heavy metal removal device 3 located on the rightmost side, the iron powder-containing separated product 102 is supplied to the heavy metal adsorption water tank 4 of the heavy metal removal device 3 located on the leftmost side through the centrifugal separator 5. As a result, the heavy metal removing device 3 located on the rightmost side is in an empty state.

最後に、最左に位置する重金属除去装置3では、重金属吸着水槽4に貯留した鉄粉含有分離物102(2系統目の鉄粉10を含む)を廃棄汚泥水槽8に排出する。   Finally, in the heavy metal removing device 3 located on the leftmost side, the iron powder-containing separated material 102 (including the second iron powder 10) stored in the heavy metal adsorption water tank 4 is discharged to the waste sludge water tank 8.

なお、本実施の形態では最左に位置する重金属除去装置3の重金属吸着水槽4にのみ、第4の排泥管43を介して廃棄汚泥水槽8と連結したため、第9バッチの処理を必要としたが、すべての重金属除去装置3の重金属吸着水槽4を廃棄汚泥水槽8と連結してもよく、この場合には、第9バッチの処理は不要である。   In the present embodiment, since only the heavy metal adsorption water tank 4 of the heavy metal removing device 3 located on the leftmost side is connected to the waste sludge water tank 8 via the fourth sludge pipe 43, the processing of the ninth batch is required. However, the heavy metal adsorbing water tank 4 of all heavy metal removing devices 3 may be connected to the waste sludge water tank 8, and in this case, the processing of the ninth batch is unnecessary.

このように、上流側に位置する前記重金属除去装置3に対して下流側に位置する重金属除去装置3にて実施する工程が1工程先行した工程となるよう、3つ以上の重金属除去装置3にて実施する作業工程を一つずつずらす。こうすることで、同一バッチで第1の工程を実施している下流に位置する重金属除去装置3の重金属吸着槽4に、第3の工程を実施している上流に位置する重金属除去装置3から比重分離された鉄粉含有分離物102を投下させることができ、鉄粉10を繰り返し使用しつつ効率よく循環させて作業時間を短縮することが可能となる。   In this way, three or more heavy metal removing devices 3 are arranged so that the step performed by the heavy metal removing device 3 located on the downstream side with respect to the heavy metal removing device 3 located on the upstream side is a step preceding one step. Shift the work processes to be performed one by one. By carrying out like this, from the heavy metal removal apparatus 3 located in the upstream which is implementing the 3rd process to the heavy metal adsorption tank 4 of the heavy metal removal apparatus 3 located in the downstream which is implementing the 1st process in the same batch The iron powder-containing separated product 102 separated by specific gravity can be dropped, and the working time can be shortened by efficiently circulating the iron powder 10 while repeatedly using it.

そして、汚染土壌洗浄設備1内で鉄粉10の流れを2系統設け、各々の系統でこの作業を連続させると、3つの重金属除去装置3すべてを同時に稼働させることができ、より効率よく鉄粉10を使用した汚染泥水10の浄化を行うことが可能となる。また、汚染土壌洗浄設備1内で鉄粉10の流れを2系統設けても、図6〜図8をみてもわかるとおり、2系統の鉄粉10どうしが混ざり合うことはない。   When two flows of iron powder 10 are provided in the contaminated soil cleaning facility 1 and this operation is continued in each system, all three heavy metal removing devices 3 can be operated simultaneously, and iron powder is more efficiently processed. It becomes possible to purify the contaminated mud water 10 using 10. Moreover, even if two flows of the iron powder 10 are provided in the contaminated soil cleaning equipment 1, the two iron powders 10 are not mixed with each other as can be seen from FIGS.

なお、本実施の形態では、重金属除去装置3が3つの場合を事例としたが、4つの場合には、図9で示すように、汚染泥水100と鉄粉含有分離物102とを撹拌混合し、鉄粉含有分離物102に含まれる鉄粉10に汚染泥水100中の重金属を吸着させる時間を長く確保する方法が採用できる。   In the present embodiment, the case where there are three heavy metal removal devices 3 is taken as an example, but in the case of four, as shown in FIG. 9, the contaminated mud water 100 and the iron powder-containing separator 102 are stirred and mixed. A method of ensuring a long time for adsorbing heavy metal in the contaminated mud water 100 to the iron powder 10 contained in the iron powder-containing separated product 102 can be adopted.

つまり、図9において最左に位置する重金属除去装置3に着目すると、図9(a)では、重金属吸着水槽4に泥水槽2から汚染泥水100が供給されると同時に、最右に位置する重金属除去装置3の第3の工程で分離された鉄粉含有分離物102が投下される、第1の工程が実施されている。   That is, paying attention to the heavy metal removing device 3 located at the leftmost in FIG. 9, in FIG. 9A, the heavy metal located at the rightmost is simultaneously supplied to the heavy metal adsorption water tank 4 from the mud tank 2 at the same time. The 1st process in which the iron powder containing separated substance 102 isolate | separated at the 3rd process of the removal apparatus 3 is dropped is implemented.

次に、図9(b)では、重金属吸着水槽4に貯留した汚染泥水100と鉄粉含有分離物102とを撹拌装置41にて撹拌混合し、鉄粉含有分離物102に含まれる鉄粉10に汚染泥水100中の重金属を吸着させ、鉄粉添加泥水101を作製する、第2の工程が実施されている。また、図9(c)でも引き続き、第2の工程が実施されている。   Next, in FIG. 9B, the contaminated mud water 100 stored in the heavy metal adsorption water tank 4 and the iron powder-containing separator 102 are stirred and mixed by the stirring device 41, and the iron powder 10 contained in the iron powder-containing separator 102 is mixed. A second step is performed in which the heavy metal in the contaminated mud water 100 is adsorbed to produce the iron powder-added mud water 101. Further, in FIG. 9C, the second step is continued.

そして、図9(d)において、鉄粉添加泥水101を遠心分離機5に供給し、鉄粉含有分離物102と洗浄泥水103とに分離する、第3の工程が実施されている。なお、この場合には、図9を見るとわかるように、4つ存在する重金属吸着水槽4のうち3つに鉄粉10が添加されていることから、鉄粉10の流れは3系統存在している。   Then, in FIG. 9 (d), a third step is performed in which the iron powder-added mud water 101 is supplied to the centrifuge 5 and separated into the iron powder-containing separated product 102 and the cleaning mud water 103. In this case, as can be seen from FIG. 9, the iron powder 10 is added to three of the four heavy metal adsorption water tanks 4, and therefore there are three flows of the iron powder 10. ing.

このように、第2の工程を2バッチ連続で実施すると、全体の作業効率を低下させることなく、鉄粉10に汚染泥水100中の重金属を吸着させる時間を長く確保することができる。したがって、洗浄しようとする汚染泥水10に含まれる重金属の種類や汚染泥水10の性状に応じて、重金属除去装置3の数を増減し、第2の工程の連続回数を調整すれば、より確実に鉄粉10に重金属の微粒子を吸着・固定することが可能となる。   As described above, when the second step is performed continuously for two batches, it is possible to ensure a long time for the heavy metal in the contaminated mud water 100 to be adsorbed on the iron powder 10 without reducing the overall work efficiency. Therefore, if the number of heavy metal removal devices 3 is increased or decreased according to the type of heavy metal contained in the contaminated mud water 10 to be cleaned and the properties of the contaminated mud water 10 and the number of continuous times of the second process is adjusted, the second step is more reliably performed. It becomes possible to adsorb and fix fine particles of heavy metal on the iron powder 10.

ところで、汚染土壌洗浄設備1は、管理者が施工現場の管理事務所等に設置される端末装置90にて遠隔操作が可能な構成を有している。   By the way, the contaminated soil washing | cleaning equipment 1 has the structure in which an administrator can perform remote operation with the terminal device 90 installed in the management office etc. of a construction site.

図1に示すように、端末装置90は、情報処理装置91、入力装置92および出力装置93を少なくとも備えるいわゆるパソコンであり、情報処理装置91は演算処理装置及び記憶装置等のハードウェアと、該ハードウェア上で動作するソフトウェアとで構成されている。また、泥水槽2、3つの重金属除去装置3、洗浄泥水槽6、鉄粉タンク7、廃棄汚泥水槽8、鉄粉分離装置9各々と通信接続されている。   As shown in FIG. 1, the terminal device 90 is a so-called personal computer including at least an information processing device 91, an input device 92, and an output device 93. The information processing device 91 includes hardware such as an arithmetic processing device and a storage device, It consists of software that runs on hardware. The mud tank 2, the three heavy metal removing devices 3, the cleaning mud tank 6, the iron powder tank 7, the waste sludge water tank 8, and the iron powder separator 9 are connected in communication.

そして、端末装置90の情報処理装置91には、汚染土壌洗浄設備1にて上述した汚染土壌の洗浄工法を実施するための4つの工程(s1〜s4)を実行するための操作を支援するプログラムが格納されている。同時に、汚染土壌洗浄設備1を制御する自動制御部911、鉄粉タンク7より供給される鉄粉10を管理する鉄粉管理部912、汚染泥水の洗浄処理工程(s2)におけるバッチ処理時間を報知する時間報知部913、および泥水槽2内の汚染泥水100を監視する泥水監視部914を備えている。   And in the information processing apparatus 91 of the terminal device 90, the program which assists operation for performing four processes (s1-s4) for implementing the cleaning method of the contaminated soil mentioned above in the contaminated soil cleaning equipment 1 Is stored. At the same time, an automatic control unit 911 that controls the contaminated soil cleaning facility 1, an iron powder management unit 912 that manages the iron powder 10 supplied from the iron powder tank 7, and a batch processing time in the cleaning process step (s2) of contaminated mud water are notified. And a muddy water monitoring unit 914 for monitoring the contaminated muddy water 100 in the muddy water tank 2.

自動制御部911は、少なくとも、第1から第4の排泥管22、42、51、43各々に備えられている電磁バルブの開閉を制御するバルブ制御機能、電磁バルブの開閉に伴うポンプの作動を制御するポンプ制御機能、及び重金属吸着水槽4に備えられている撹拌装置42の作動を制御する撹拌制御機能を有している。そして、上述した4つの工程(s1〜s4)に応じて、電磁バルブの開閉、ポンプの作動、および撹拌装置42の作動を制御する。なお、本実施の形態では、第1から第4の排泥管22、42、51、43各々に電磁バルブを備えたが、必ずしもこれに限定されるものではなく、電動バルブやエアバルブなど、自動バルブであればいずれを採用してもよい。   The automatic control unit 911 includes at least a valve control function for controlling the opening and closing of the electromagnetic valves provided in each of the first to fourth drainage pipes 22, 42, 51 and 43, and the operation of the pump accompanying the opening and closing of the electromagnetic valves. And a stirring control function for controlling the operation of the stirring device 42 provided in the heavy metal adsorption water tank 4. And according to the four processes (s1 to s4) described above, the opening and closing of the electromagnetic valve, the operation of the pump, and the operation of the stirring device 42 are controlled. In the present embodiment, each of the first to fourth drainage pipes 22, 42, 51, 43 is provided with an electromagnetic valve. However, the present invention is not limited to this, and an automatic valve such as an electric valve or an air valve may be used. Any valve may be used.

鉄粉管理部912は、汚染泥水の洗浄処理工程(s2)において、例えば3つの重金属除去装置3各々にて第2の工程を実施する回数を鉄粉10の転用回数としてカウントする、転用回数カウント機能を備えている。また、あらかじめ設定した鉄粉10の転用に係る警告回数が格納されており、鉄粉10の転用回数が警告回数に達した時点で転用回数警告信号を出力装置93に出力する。   The iron powder management unit 912 counts, for example, the number of times of performing the second step in each of the three heavy metal removing devices 3 as the number of times of diversion of the iron powder 10 in the contaminated mud washing process (s2). It has a function. In addition, a preset number of warnings related to diversion of the iron powder 10 is stored, and a diversion number warning signal is output to the output device 93 when the number of diversions of the iron powder 10 reaches the number of warnings.

時間報知部913は、汚染泥水の洗浄処理工程(s2)における第1〜第9バッチの1バッチ分に必要な処理時間が格納されている。そして、第1バッチの処理開始から処理時間が経過するごとに、出力装置に処理時間が経過したことを知らせる時間報知信号を出力する。なお、1バッチ分の処理時間は、いずれの基準にて設定してもよいが、1バッチの間に3つの重金属除去装置3各々で実施される第1〜第3の工程のうち、第2の工程が最も時間を要することから、第2の工程を実施するのに必要な時間を、1バッチ分の処理時間として設定するとよい。   The time notification unit 913 stores a processing time necessary for one batch of the first to ninth batches in the contaminated mud water cleaning process (s2). Then, every time the processing time elapses from the start of processing of the first batch, a time notification signal is output to inform the output device that the processing time has elapsed. The processing time for one batch may be set according to any standard, but the second of the first to third steps performed by each of the three heavy metal removing devices 3 during one batch. Since this process takes the most time, the time required to implement the second process may be set as the processing time for one batch.

泥水監視部914は、汚染泥水100の比重を検知する比重検知機能と、泥水槽2内における汚染泥水100の液位を検知する液位検知機能を有している。そして、あらかじめ設定した汚染泥水100に係る比重の上限値を格納しておき、比重が上限値を超えた場合に出力装置93に比重警告信号を出力する。また、泥水槽2における汚染泥水100の下限液位を設定して格納しておき、泥水槽2における液位が下限液位に到達した場合に、出力装置93に液位警告信号を出力する。   The muddy water monitoring unit 914 has a specific gravity detection function for detecting the specific gravity of the contaminated mud water 100 and a liquid level detection function for detecting the liquid level of the contaminated mud water 100 in the muddy water tank 2. Then, an upper limit value of the specific gravity related to the contaminated mud 100 set in advance is stored, and a specific gravity warning signal is output to the output device 93 when the specific gravity exceeds the upper limit value. Further, the lower limit liquid level of the contaminated mud water 100 in the mud tank 2 is set and stored, and when the liquid level in the mud tank 2 reaches the lower limit liquid level, a liquid level warning signal is output to the output device 93.

これにより、自動制御部911は、入力装置92より汚染土壌洗浄設備1の運転開始信号を検知すると、前処理工程s1を実行して、泥水監視部914にて汚染泥水100の比重管理、および汚染泥水100の液位管理を開始し、比重警告信号および液位警告信号が出力されなければ、汚染泥水の洗浄処理工程s2に移行する。   As a result, when the automatic control unit 911 detects the operation start signal of the contaminated soil cleaning facility 1 from the input device 92, the automatic control unit 911 executes the pretreatment step s1, and the muddy water monitoring unit 914 manages the specific gravity of the contaminated mud water 100 and the contamination. The liquid level management of the muddy water 100 is started, and if the specific gravity warning signal and the liquid level warning signal are not output, the process proceeds to the contaminated mud water cleaning process step s2.

すると、自動制御部911は、汚染泥水の洗浄処理工程s2における第1バッチの処理(図6(a))を開始するとともに、鉄粉管理部912による鉄粉10の転用回数管理、および時間報知部913による処理時間管理を開始する。
具体的には、バルブ制御機能およびポンプ制御機能にて、泥水槽2と最左に位置する重金属吸着水槽4を連結する第1の排泥管22の、電磁バルブを開にするとともにポンプを作動する。また、鉄粉タンク7より鉄粉を最左に位置する重金属吸着水槽4に投下する。この後、時間報知部913より出力装置93に時間報知信号が出力されるとこれを検知し、バルブ制御機能およびポンプ制御機能にて、電磁バルブを閉にするとともにポンプの作動を停止し、第1バッチの処理を終了して第2バッチの処理を開始する。
Then, the automatic control unit 911 starts the first batch process (FIG. 6A) in the contaminated mud water cleaning process step s 2, manages the number of diversions of the iron powder 10 by the iron powder management unit 912, and reports the time. The processing time management by the unit 913 is started.
Specifically, with the valve control function and the pump control function, the electromagnetic valve of the first mud drain pipe 22 connecting the mud tank 2 and the heavy metal adsorption water tank 4 located at the leftmost is opened and the pump is operated. To do. Further, iron powder is dropped from the iron powder tank 7 into the heavy metal adsorbing water tank 4 located at the leftmost position. Thereafter, when the time notification signal is output from the time notification unit 913 to the output device 93, this is detected, and the valve control function and the pump control function are used to close the electromagnetic valve and stop the pump operation. The process for one batch is terminated and the process for the second batch is started.

第2バッチの処理(図6(b))では、自動制御部911は、バルブ制御機能およびポンプ制御機能にて、泥水槽2と最右に位置する重金属吸着水槽4を連結する第1の排泥管22の、電磁バルブを開にするとともにポンプを作動する。また、鉄粉タンク7より鉄粉10を最右に位置する重金属吸着水槽4に投下する。さらに、撹拌制御機能にて、最左に位置する重金属除去装置3における重金属吸着水槽4の撹拌装置41を作動させる。この後、時間報知部913より出力装置93に時間報知信号が出力されるとこれを検知し、バルブ制御機能およびポンプ制御機能にて、電磁バルブを閉にするとともにポンプの作動を停止し、また、撹拌制御機能にて、撹拌装置41の作動を停止する。そして、第2バッチの処理を終了して第3バッチの処理を開始する。   In the processing of the second batch (FIG. 6B), the automatic control unit 911 uses the valve control function and the pump control function to connect the muddy water tank 2 and the heavy metal adsorption water tank 4 positioned at the rightmost position. The electromagnetic valve of the mud pipe 22 is opened and the pump is operated. Moreover, the iron powder 10 is dropped from the iron powder tank 7 into the heavy metal adsorption water tank 4 positioned at the rightmost position. Furthermore, the stirring device 41 of the heavy metal adsorption water tank 4 in the heavy metal removing device 3 located at the leftmost is operated by the stirring control function. Thereafter, when the time notification signal is output from the time notification unit 913 to the output device 93, this is detected, and the valve control function and the pump control function are used to close the electromagnetic valve and stop the pump operation. The operation of the stirring device 41 is stopped by the stirring control function. Then, the process of the second batch is finished and the process of the third batch is started.

第3バッチの処理(図6(c))では、自動制御部911は、バルブ制御機能およびポンプ制御機能にて、泥水槽2と中央に位置する重金属吸着水槽4を連結する第1の排泥管22の、電磁バルブを開にするとともにポンプを作動する。また、最左に位置する重金属吸着水槽4と遠心分離機5を連結する第2の排泥管42の、電磁バルブを開にするとともにポンプを作動する。さらに、この遠心分離機5と洗浄泥水槽8を連結する第3の排泥管51の、電磁バルブを開にするとともにポンプを作動する。また、撹拌制御機能にて、最右に位置する重金属吸着水槽4の撹拌装置41を作動させる。   In the processing of the third batch (FIG. 6C), the automatic control unit 911 uses the valve control function and the pump control function to connect the mud tank 2 and the heavy metal adsorption water tank 4 located in the center to the first waste mud. The solenoid valve of the pipe 22 is opened and the pump is operated. Moreover, while opening the electromagnetic valve of the 2nd waste mud pipe 42 which connects the heavy metal adsorption water tank 4 and the centrifuge 5 located in the leftmost, a pump is operated. Further, the electromagnetic valve of the third mud drain pipe 51 connecting the centrifugal separator 5 and the washing mud tank 8 is opened and the pump is operated. Moreover, the stirring apparatus 41 of the heavy metal adsorption | suction water tank 4 located in the rightmost is operated with a stirring control function.

このように、時間報知部913より出力される時間管理信号を検知するごとに、第6バッチ(図8(c))まで処理を進め、それ以降は、第4バッチから第6バッチの処理(図8(a)〜図8(c))を繰り返す。   Thus, every time the time management signal output from the time notification unit 913 is detected, the process proceeds to the sixth batch (FIG. 8C), and thereafter, the process from the fourth batch to the sixth batch ( FIG. 8A to FIG. 8C are repeated.

そして、自動制御部911が、上記処理の途中で鉄粉10の転用回数警告信号もしくは泥水槽2の液位警告信号を検知すると、汚染泥水の洗浄処理工程s2の処理を終了させるべく、第4バッチから第6バッチの処理の繰り返しを終了し、第7バッチから第9バッチの処理に応じた処理を進める。この後、鉄粉10を最終鉄粉含有分離物104として廃棄するための鉄粉含有分離物の廃棄処理工程s3を開始する。   And when the automatic control part 911 detects the diversion frequency warning signal of the iron powder 10 or the liquid level warning signal of the muddy water tank 2 in the middle of the above process, the fourth process is performed to end the process of the contaminated muddy water cleaning process s2. The repetition of the processing from the batch to the sixth batch is finished, and the processing according to the processing from the seventh batch to the ninth batch is advanced. After this, the iron powder-containing separated disposal process s3 for discarding the iron powder 10 as the final iron powder-containing separated 104 is started.

このように、汚染土壌洗浄設備1は、端末装置90にて自動制御を行うことが可能となるが、少なくとも自動制御部911にて実施される制御は、入力装置92を介して、管理者が手動で実施することが可能であることは言うまでもない。   As described above, the contaminated soil cleaning facility 1 can be automatically controlled by the terminal device 90, but at least the control performed by the automatic control unit 911 is performed by the administrator via the input device 92. It goes without saying that it can be carried out manually.

本発明の汚染土壌の洗浄工法によれば、鉄粉10は重金属除去装置3各々で洗浄泥水100に含まれる重金属を吸着しながら、休眠することなく常に3つ以上の重金属除去装置3を順に循環する。これにより、作業効率が向上し、作業時間を大幅に短縮することが可能となる。   According to the method for cleaning contaminated soil of the present invention, the iron powder 10 circulates through the three or more heavy metal removing devices 3 in order, without sleeping, while adsorbing the heavy metals contained in the washing mud 100 in each heavy metal removing device 3. To do. As a result, work efficiency can be improved and work time can be greatly shortened.

本発明の汚染土壌洗浄設備1および汚染土壌洗浄設備1を用いた汚染土壌の浄化方法は、上記実施形態に限定されるものではなく、本発明の趣旨を逸脱しない範囲で種々の変更が可能であることはいうまでもない。   The contaminated soil cleaning facility 1 and the contaminated soil cleaning method 1 using the contaminated soil cleaning facility 1 are not limited to the above embodiment, and various modifications are possible without departing from the spirit of the present invention. Needless to say.

1 汚染土壌洗浄設備
2 泥水槽
21 比重検出器
22 第1の排泥管
3 重金属除去装置
4 重金属吸着槽
41 撹拌装置
42 第2の排泥管
43 第4の排泥管
5 遠心分離機
51 第3の排泥管
6 洗浄泥水槽
7 鉄粉タンク
8 廃棄汚泥水槽
9 鉄粉分離装置
10 鉄粉
100 汚染泥水
101 鉄粉添加泥水
102 鉄粉含有分離物
103 洗浄泥水
104 最終鉄粉含有分離物
50 泥水処理施設
501 固液分離装置
502 調整槽
503 余剰泥水槽
60 シールド掘削機
61 圧力室
90 端末装置
91 情報処理装置
92 入力装置
93 出力装置
911 自動制御部
912 鉄粉管理部
913 時間報知部
914 泥水監視部
DESCRIPTION OF SYMBOLS 1 Contaminated soil washing | cleaning equipment 2 Mud tank 21 Specific gravity detector 22 1st drainage pipe 3 Heavy metal removal apparatus 4 Heavy metal adsorption tank 41 Stirrer 42 2nd drainage pipe 43 4th drainage pipe 5 Centrifuge 51 1st 3 Mud pipe 6 Cleaning mud tank 7 Iron powder tank 8 Waste sludge tank 9 Iron powder separator 10 Iron powder 100 Contaminated mud water 101 Iron powder added mud water 102 Iron powder containing separator 103 Cleaning mud water 104 Final iron powder containing separator 50 Mud treatment facility 501 Solid-liquid separator 502 Adjustment tank 503 Surplus mud tank 60 Shield excavator 61 Pressure chamber 90 Terminal device 91 Information processing device 92 Input device 93 Output device 911 Automatic control unit 912 Iron powder management unit 913 Time notification unit 914 Mud water Monitoring unit

Claims (5)

重金属に汚染された粘性土を含む汚染泥水を貯留し、該汚染泥水の比重を管理調整する泥水槽と、該泥水槽より供給される前記汚染泥水を鉄粉にて洗浄し、前記重金属が除去された洗浄泥水を作製する3つ以上の重金属除去装置と、該重金属除去装置各々より排出される前記洗浄泥水を貯留する洗浄泥水槽とを備える汚染土壌洗浄設備であって、
前記重金属除去装置が、前記汚染泥水と前記鉄粉とを撹拌混合して該鉄粉に前記汚染泥水中の重金属を吸着させながら、鉄粉添加泥水を作製する重金属吸着槽と、該重金属吸着槽の下流側に配置されて、前記鉄粉添加泥水を前記洗浄泥水と前記重金属を吸着した鉄粉が含有された鉄粉含有分離物とに比重分離する遠心分離機と、を有し、
3つ以上の該重金属除去装置を、上流側に位置する重金属除去装置の遠心分離機にて比重分離した前記鉄粉含有分離物が、下流側に位置する重金属除去装置の重金属吸着槽に直接投下されるよう配置して、前記鉄粉の循環路を形成することを特徴とする汚染土壌洗浄設備。
The contaminated mud containing contaminated soil contaminated with heavy metals is stored, the mud tank that manages and adjusts the specific gravity of the contaminated mud, and the contaminated mud supplied from the mud tank is washed with iron powder to remove the heavy metals A contaminated soil cleaning facility comprising three or more heavy metal removing devices for producing the washed mud, and a washing mud tank for storing the washed mud discharged from each of the heavy metal removing devices,
A heavy metal adsorption tank in which the heavy metal removing device stirs and mixes the contaminated mud water and the iron powder to adsorb the heavy metal in the contaminated mud water to the iron powder, and the heavy metal adsorption tank A centrifuge that separates the iron powder-added muddy water into the washing muddy water and the iron powder-containing separated containing the iron powder that has adsorbed the heavy metal, and a centrifuge.
Three or more heavy metal removal devices having the specific gravity separated by the centrifugal separator of the heavy metal removal device located on the upstream side are directly dropped into the heavy metal adsorption tank of the heavy metal removal device located on the downstream side. The contaminated soil cleaning facility is characterized by being arranged to form a circulation path for the iron powder.
請求項1に記載の汚染土壌洗浄設備において、
3つ以上の前記重金属除去装置のうち、少なくとも1つの重金属除去装置に備えた前記重金属吸着槽が、鉄粉含有分離物を廃棄するための廃棄汚泥水槽に連結されることを特徴とする汚染土壌洗浄設備。
In the contaminated soil cleaning facility according to claim 1,
Of the three or more heavy metal removing devices, the heavy metal adsorption tank provided in at least one heavy metal removing device is connected to a waste sludge water tank for discarding the iron powder-containing separation. Cleaning equipment.
請求項1または2に記載の汚染土壌洗浄設備において、
前記泥水槽から前記重金属吸着槽各々に汚染泥水を供給するための排泥管および前記重金属吸着槽から前記遠心分離機に前記鉄粉添加泥水を供給するための排泥管にそれぞれ自動バルブ及びポンプが、また、前記遠心分離機から前記洗浄泥水槽に前記洗浄泥水を供給するための排泥管に自動バルブが設けられるとともに、
該自動バルブの開閉、およびこれに伴う前記ポンプの作動を制御する端末装置が備えられることを特徴とする汚染土壌洗浄設備。
The contaminated soil cleaning equipment according to claim 1 or 2,
An automatic valve and a pump for supplying a polluted mud from the mud tank to each of the heavy metal adsorbing tanks and a mud pipe for supplying the iron powder added mud from the heavy metal adsorbing tanks to the centrifuge, respectively. However, an automatic valve is provided in the mud pipe for supplying the washing mud from the centrifuge to the washing mud tank,
A contaminated soil washing facility, comprising a terminal device for controlling the opening and closing of the automatic valve and the operation of the pump associated therewith.
請求項1から3のいずれか1項に記載の汚染土壌洗浄設備を用いた汚染土壌の洗浄工法であって、
前記重金属除去装置各々において、前記重金属吸着槽にて、前記泥水と前記鉄粉もしくは前記鉄粉含有分離物を混在させる第1の工程、前記泥水と前記鉄粉もしくは前記鉄粉含有分離物を混合撹拌して、前記鉄粉もしくは前記鉄粉含有分離物に含まれる鉄粉に汚染泥水中の重金属を吸着させながら、前記鉄粉添加泥水を作製する第2の工程、および前記鉄粉添加泥水を前記重金属吸着槽から前記遠心分離機に供給し、前記洗浄泥水と前記鉄粉含有分離物とに比重分離する第3の工程を繰り返し実行させるとともに、
少なくとも3つの重金属除去装置各々において同時に実施する作業工程を、上流側に位置する前記重金属除去装置に対して下流側に位置する重金属除去装置にて実施する工程が1工程先行した工程となるよう一つずつずらし、
第1の工程を実施している下流に位置する重金属除去装置の重金属吸着槽に、第3の工程を実施している上流に位置する重金属除去装置から比重分離された鉄粉含有分離物を投下させることを特徴とする汚染土壌の洗浄工法。
A method for cleaning contaminated soil using the contaminated soil cleaning facility according to any one of claims 1 to 3,
In each of the heavy metal removing devices, in the heavy metal adsorption tank, the first step of mixing the muddy water and the iron powder or the iron powder-containing separated material, mixing the muddy water and the iron powder or the iron powder-containing separated material. The second step of producing the iron powder-added mud while stirring and adsorbing the heavy metal in the contaminated mud to the iron powder or the iron powder contained in the iron powder-containing isolate, and the iron powder-added mud While supplying to the centrifuge from the heavy metal adsorption tank, repeatedly performing a third step of specific gravity separation into the washing muddy water and the iron powder-containing separation,
The work process performed simultaneously in each of the at least three heavy metal removing apparatuses is performed so that the process performed in the heavy metal removing apparatus located on the downstream side with respect to the heavy metal removing apparatus located on the upstream side is a process preceding one process. Shift one by one,
The iron powder-containing separation separated by specific gravity from the heavy metal removal device located upstream in the third step is dropped into the heavy metal adsorption tank in the heavy metal removal device located downstream in the first step. A method for cleaning contaminated soil, characterized by
請求項4に記載の汚染土壌の洗浄工法において、
前記第2の工程を複数回連続して行った後、第3の工程に移行することを特徴とする汚染土壌の洗浄工法。
In the cleaning method for contaminated soil according to claim 4,
After performing the said 2nd process continuously several times, it transfers to a 3rd process, The cleaning construction method of the contaminated soil characterized by the above-mentioned.
JP2015101875A 2015-05-19 2015-05-19 Contaminated soil cleaning equipment and contaminated soil cleaning method Active JP6458635B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2015101875A JP6458635B2 (en) 2015-05-19 2015-05-19 Contaminated soil cleaning equipment and contaminated soil cleaning method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2015101875A JP6458635B2 (en) 2015-05-19 2015-05-19 Contaminated soil cleaning equipment and contaminated soil cleaning method

Publications (2)

Publication Number Publication Date
JP2016215112A true JP2016215112A (en) 2016-12-22
JP6458635B2 JP6458635B2 (en) 2019-01-30

Family

ID=57579036

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2015101875A Active JP6458635B2 (en) 2015-05-19 2015-05-19 Contaminated soil cleaning equipment and contaminated soil cleaning method

Country Status (1)

Country Link
JP (1) JP6458635B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021038540A (en) * 2019-09-02 2021-03-11 初雁興業株式会社 Dredging system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002339690A (en) * 2001-05-15 2002-11-27 Konoike Constr Ltd Slurry type pipe jacking method
JP2012187507A (en) * 2011-03-10 2012-10-04 Toshiba Corp Device and method for water treatment
JP2014188408A (en) * 2013-03-26 2014-10-06 Ohbayashi Corp Method for purifying contaminated soil and contaminated soil purification system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002339690A (en) * 2001-05-15 2002-11-27 Konoike Constr Ltd Slurry type pipe jacking method
JP2012187507A (en) * 2011-03-10 2012-10-04 Toshiba Corp Device and method for water treatment
JP2014188408A (en) * 2013-03-26 2014-10-06 Ohbayashi Corp Method for purifying contaminated soil and contaminated soil purification system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021038540A (en) * 2019-09-02 2021-03-11 初雁興業株式会社 Dredging system

Also Published As

Publication number Publication date
JP6458635B2 (en) 2019-01-30

Similar Documents

Publication Publication Date Title
CN105057340B (en) A kind of chromium-polluted soil dystopy elution renovation technique and its device
CN104874599A (en) Soil ex-situ leaching system and method thereof
JP6007144B2 (en) Contaminated soil purification method
CN101580322B (en) Sewage processing method and sewage processing device
KR100903593B1 (en) Ultrasonic soil washing method and apparatus for purifying polluted soil
CN105598147A (en) Soil washing device and washing method thereof
CN102225834A (en) Sludge treatment method and device for urban drainage pipe network
KR20150023716A (en) Apparatus and method for separating grinding oil from grinding sludges
KR101658523B1 (en) Remediation system of contaminated soil by soil separation and soil washing
KR20120125323A (en) Ballast flocculation and sedimentation water treatment system with simplified sludge recirculation, and process therefor
JP6411909B2 (en) Detoxification system for arsenic contaminated soil
CN104747107A (en) Integrated treatment method on waste drilling mud
CN201458889U (en) Sewage treatment device
JP6458635B2 (en) Contaminated soil cleaning equipment and contaminated soil cleaning method
CN102884009A (en) A method and plant for purifying raw water
CN106830594B (en) Sludge treatment system
CN202297311U (en) Automatic control device for sewage treatment
CN112317524A (en) Contaminated soil leaching treatment system and method
CN204620627U (en) A kind of soil heterotopic elution circuit
CN108409073A (en) Ditch mud processing method
JP5782816B2 (en) Radioactive substance removal method in radioactive liquid waste and radioactive substance removal system in radioactive liquid waste
JP6425170B2 (en) Muddy water treatment system and muddy water treatment method
CN108101274A (en) A kind of oils high-COD waste water pretreating process and equipment
JP2008080249A (en) Soil cleaning method and soil cleaning apparatus
JP5226730B2 (en) Cyan contaminated soil purification system

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20180420

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20180813

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20180918

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20181106

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

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20181127

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20181210

R150 Certificate of patent or registration of utility model

Ref document number: 6458635

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150