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JP5769082B2 - Cleaning treatment method for radioactive material contaminated soil - Google Patents

Cleaning treatment method for radioactive material contaminated soil Download PDF

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JP5769082B2
JP5769082B2 JP2011234001A JP2011234001A JP5769082B2 JP 5769082 B2 JP5769082 B2 JP 5769082B2 JP 2011234001 A JP2011234001 A JP 2011234001A JP 2011234001 A JP2011234001 A JP 2011234001A JP 5769082 B2 JP5769082 B2 JP 5769082B2
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sand
contaminated soil
radioactive
washing
radioactive material
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JP2013092428A (en
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祐一 谷本
祐一 谷本
哲一 木下
哲一 木下
充 土田
充 土田
光男 毛利
光男 毛利
千絵 山本
千絵 山本
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Shimizu Corp
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Description

本発明は、放射性物質汚染土壌の洗浄処理方法に関する。   The present invention relates to a method for cleaning radioactive material contaminated soil.

従来、有機化合物、油分などの有害物質で汚染された土壌からこれら有害物質を分離除去する方法として、汚染土壌に水を加えてスラリーとし、このスラリーを浮遊分離器に送り、これに界面活性剤、アルカリ剤を加えて、汚染土壌から有害物質を浮遊分離する方法が開示されている(例えば、特許文献1参照)。   Conventionally, as a method of separating and removing these harmful substances from soil contaminated with organic compounds, oils and other harmful substances, water is added to the contaminated soil to form a slurry, which is then sent to a floating separator, to which a surfactant is added. A method for floating and separating harmful substances from contaminated soil by adding an alkaline agent is disclosed (for example, see Patent Document 1).

ところで、土壌粒子表面に付着、吸着しているセシウム等の放射性物質を含む汚染土壌の浄化方法としては、フローテーション処理を用いたものが知られている。例えば、図2に示すように、湿式ふるい装置11とハイドロサイクロン12によって汚染土壌G0を粗粒子分G2と砂分S1と細粒子分S2とに分級処理を行う工程と、分級処理によって得られた砂分S1に対してスクラバー13及びフローテーション装置14によって発生させたフロスFとともに汚染物質を回収する工程と、前記洗浄した洗浄砂S3を脱水処理して回収する工程と、分級工程によって分級された細粒子分S2、フローテーション処理により得られたフロスF、及び脱水工程により生じた処理溶液Eを凝集沈殿装置16に投入して濃縮残渣Tと処理水Wとに分離処理による工程と、からなる洗浄処理工程が行われている。この場合、放射性物質を含む溶液の処理においては、RO膜(逆浸透膜)やゼオライトの吸着材を投入し、溶出した物質を前記吸着材で吸着させている。   By the way, the thing using the flotation process is known as a purification method of the contaminated soil containing radioactive substances, such as cesium adhering to and adsorbing on the soil particle surface. For example, as shown in FIG. 2, a process of classifying the contaminated soil G0 into a coarse particle part G2, a sand part S1, and a fine particle part S2 by the wet sieving device 11 and the hydrocyclone 12, and obtained by the classification process. Classification was performed by a step of collecting contaminants together with the floss F generated by the scrubber 13 and the flotation device 14 with respect to the sand S1, a step of dehydrating and collecting the washed washed sand S3, and a classification step. The fine particle S2, the froth F obtained by the flotation treatment, and the treatment solution E produced by the dehydration step are charged into the coagulating sedimentation apparatus 16 and separated into concentrated residue T and treated water W. A cleaning process is performed. In this case, in the treatment of a solution containing a radioactive substance, an RO membrane (reverse osmosis membrane) or zeolite adsorbent is introduced, and the eluted substance is adsorbed by the adsorbent.

特開昭63−72391号公報JP-A-63-72391

しかしながら、従来の放射性物質汚染土壌の洗浄処理方法では、以下のような問題があった。
すなわち、従来の工程では、フローテーション処理によって得られた洗浄土における汚染物質濃度の低減が不十分であり、さらなる汚染物質濃度の低減が求められていた。
また、分級工程の前の汚染土壌に対して直接、放射性物質抽出薬剤を添加しているため、持ち込まれた全ての汚染土壌の土量に対応する放射性物質抽出薬剤が必要となり、その投入量が増えることから、その点で改良の余地があった。
さらに、放射性物質を含む溶液の処理にはRO膜やゼオライトの使用が一般的であるが、これら吸着材が高価であり、抽出された濃縮残渣に加えてこれら吸着材も廃棄する必要があることから廃棄物量が増大するという問題があった。
However, conventional cleaning methods for radioactive material contaminated soil have the following problems.
That is, in the conventional process, the reduction of the pollutant concentration in the washing soil obtained by the flotation treatment is insufficient, and further reduction of the pollutant concentration has been demanded.
In addition, because the radioactive substance extraction agent is added directly to the contaminated soil before the classification process, a radioactive substance extraction agent corresponding to the amount of soil in all the contaminated soil that is brought in is required, and the amount of input is limited. There was room for improvement in that respect as it increased.
In addition, RO membranes and zeolites are generally used for the treatment of solutions containing radioactive materials, but these adsorbents are expensive and must be discarded in addition to the extracted concentrated residue. Therefore, there was a problem that the amount of waste increased.

本発明は、上述する問題点に鑑みてなされたもので、汚染物質濃度の低減を図ることができるうえ、処理費用と廃棄物量の低減を図ることができる放射性物質汚染土壌の洗浄処理方法を提供することを目的とする。   The present invention has been made in view of the above-mentioned problems, and provides a cleaning method for radioactive material-contaminated soil that can reduce the concentration of contaminants and can reduce the processing cost and the amount of waste. The purpose is to do.

上記目的を達成するため、本発明に係る放射性物質汚染土壌の洗浄処理方法では、放射性物質を含有する汚染土壌を洗浄するとともに、汚染土壌から放射性物質を分離、除去する放射性物質汚染土壌の洗浄処理方法であって、汚染土壌に水を添加し、湿式ふるい分級処理して粗粒子分を分離して、スラリー状の土砂とする第1分級工程と、この土砂を、ハイドロサイクロン処理して砂分と、汚染物質を含む細粒子分とに分級処理する第2分級工程と、砂分をフローテーション処理によって発生させたフロスにより回収する洗浄工程と、洗浄工程の洗浄砂に含まれる放射性物質を放射性物質抽出薬剤の溶液により抽出し、さらに濃度の低い低濃度洗浄砂を脱水処理により得る放射性物質抽出工程と、第2分級工程で得られた細粒子分を吸着材とし、細粒子分を用いて洗浄工程によるフロスと放射性物質抽出工程による処理溶液とから放射性物質を除去するとともに、凝集沈殿させて沈殿汚泥と水とに分離し、沈殿汚泥を脱水処理して濃縮残渣と処理水とに分離する吸着工程と、を有することを特徴としている。   In order to achieve the above object, in the cleaning method for radioactive material contaminated soil according to the present invention, the contaminated soil containing the radioactive material is cleaned, and the radioactive material contaminated soil is separated and removed from the contaminated soil. This is a method in which water is added to contaminated soil, wet sieving classification treatment is performed to separate coarse particles to form slurry-like sand, and the soil is hydrocyclone treated to obtain sand. And a second classifying process for classifying fine particles containing contaminants, a cleaning process for collecting sand using a floss generated by a flotation process, and radioactive substances contained in the cleaning sand in the cleaning process are radioactive Extraction with a solution of the substance extraction drug and further extraction of the radioactive substance obtained by dehydrating the low-concentration washed sand with low concentration, and the fine particles obtained in the second classification process as the adsorbent In addition to removing radioactive substances from the floss in the washing process and the processing solution in the radioactive substance extraction process using fine particles, coagulate sedimentation to separate into precipitated sludge and water, dehydrate the precipitated sludge, and concentrate residue And an adsorption step for separating into treated water.

また、本発明に係る放射性物質汚染土壌の洗浄処理方法では、第2分級工程で分級処理した砂分に付着している放射性物質を攪拌により離脱させる離脱工程が設けられていてもよい。   Moreover, in the washing | cleaning processing method of the radioactive substance contaminated soil which concerns on this invention, the detachment | leave process which leaves | separates the radioactive substance adhering to the sand content classified by the 2nd classification process by stirring may be provided.

本発明では、洗浄工程で得られた洗浄砂に対して放射性物質抽出薬剤を添加する放射性物質抽出工程を行うことで、洗浄砂の放射性物質濃度をさらに低減することが可能となる。つまり、通常の方法では放射性物質の抽出のために分級前の汚染土壌に対して直接薬剤を添加していた方法を、本発明では洗浄工程で洗浄した後の洗浄砂に対して薬剤を入れるので、薬剤の添加量を減らすことができる。   In the present invention, the radioactive substance concentration in the cleaning sand can be further reduced by performing the radioactive substance extraction process in which the radioactive substance extraction agent is added to the cleaning sand obtained in the cleaning process. That is, in the normal method, the chemical is directly added to the contaminated soil before classification for the extraction of radioactive substances. In the present invention, the chemical is put into the washed sand after washing in the washing step. The amount of drug added can be reduced.

また、ハイドロサイクロン処理によって得られた廃棄処分用の細粒子分を吸着材として用い、この細粒子分に対して洗浄工程で発生したフロスや放射性物質抽出工程で生じた処理溶液を吸着させる吸着工程を設けることにより、この細粒子分が従来使用していたRO膜やゼオライトの代替とすることが可能となり、吸着材にかかるコストの低減を図ることができる。そして、吸着材として使用する前記細粒子分は廃棄するものであり、従来のようにRO膜やゼオライト等の新たな吸着材を加える必要がないことから、廃棄物の減量化が可能である。   Also, an adsorption process that uses the fine particles for disposal obtained by hydrocyclone treatment as an adsorbent, and adsorbs the floss generated in the washing process and the treatment solution produced in the radioactive substance extraction process on the fine particles. By providing this, it becomes possible to replace the RO membrane and zeolite used in the past with the fine particles, and the cost for the adsorbent can be reduced. The fine particles used as the adsorbent are discarded, and it is not necessary to add a new adsorbent such as an RO membrane or zeolite as in the prior art, so that the amount of waste can be reduced.

本発明の放射性物質汚染土壌の洗浄処理方法によれば、洗浄工程で得られた洗浄砂に対して薬剤を添加する放射性物質抽出工程を行うことで、抽出効率を高めることができ、染物質濃度の低減を図ることができる。
また、投入された汚染土壌の土量に比べて洗浄工程で得られた洗浄砂が減量されているので、薬剤の添加量を減らすことができる。しかも、分級処理で得られた細粒子分を吸着材として再利用する方法であり、新たな吸着材を追加する必要がないことから、処理費用と廃棄物量の低減を図ることができる。
According to the method for cleaning radioactive material-contaminated soil of the present invention, the extraction efficiency can be increased by performing the radioactive material extraction step of adding a chemical to the cleaning sand obtained in the cleaning step, and the concentration of the dye material Can be reduced.
In addition, since the amount of washing sand obtained in the washing step is reduced compared to the amount of soil in the contaminated soil that has been input, the amount of chemical added can be reduced. And it is a method of reusing the fine particle part obtained by the classification process as an adsorbent, and since it is not necessary to add a new adsorbent, the processing cost and the amount of waste can be reduced.

本発明の実施の形態による放射性物質汚染土壌の洗浄処理工程を模式的に示すフロー図である。It is a flowchart which shows typically the washing process process of the radioactive material contamination soil by embodiment of this invention. 従来の汚染土壌の洗浄処理工程を模式的に示すフロー図である。It is a flowchart which shows the washing process process of the conventional contaminated soil typically.

以下、本発明の実施の形態による放射性物質汚染土壌の洗浄処理方法について、図面に基づいて説明する。   Hereinafter, a cleaning method for radioactive material contaminated soil according to an embodiment of the present invention will be described with reference to the drawings.

図1に示すように、本実施の形態による放射性物質汚染土壌の洗浄処理方法は、セシウムなどの放射性物質を含有する汚染土壌を洗浄するとともに、汚染土壌から放射性物質を分離、除去する方法に関するものである。   As shown in FIG. 1, the cleaning method for radioactive material-contaminated soil according to the present embodiment relates to a method for cleaning contaminated soil containing radioactive material such as cesium, and separating and removing the radioactive material from the contaminated soil. It is.

すなわち、放射性物質汚染土壌の洗浄処理方法は、汚染土壌G0に水を添加し、湿式ふるい分級処理して粗粒子分を分離して、スラリー状の土砂G1とする第1分級工程1と、このスラリー状の土砂G1を、ハイドロサイクロン処理して砂分S1と、汚染物質を含む細粒子分S2とに分級処理する第2分級工程2と、分級処理した砂分S1に付着している放射性物質を攪拌により離脱させる離脱工程3と、離脱工程3による離脱物をフローテーション処理によって発生させたフロスFにより回収する洗浄工程4と、洗浄工程4の洗浄砂S3に含まれる放射性物質を放射性物質抽出薬剤の溶液により抽出し、さらに濃度の低い低濃度洗浄砂S4を脱水処理により得る放射性物質抽出工程5と、第2分級工程2で得られた細粒子分S2を吸着材とし、その細粒子分S2を用いて洗浄工程4によるフロスFと放射性物質抽出工程5による処理溶液Eとから放射性物質を除去するとともに、凝集沈殿させて沈殿汚泥と水とに分離し、沈殿汚泥を脱水処理して濃縮残渣Tと処理水Wとに分離する吸着工程6と、を有している。   That is, the radioactive substance-contaminated soil washing treatment method includes the first classification step 1 in which water is added to the contaminated soil G0, the wet sieving classification treatment is performed to separate coarse particles, and the slurry-like earth and sand G1 is obtained. A second classification step 2 in which the slurry-like earth and sand G1 is subjected to a hydrocyclone treatment to classify it into a sand content S1 and a fine particle content S2 containing a contaminant, and a radioactive material adhering to the classified sand content S1 Detaching step 3 for detaching the material by agitation, cleaning step 4 for recovering the detachment in the detaching step 3 by floss F generated by the flotation process, and extraction of radioactive material contained in the cleaning sand S3 of the cleaning step 4 Extraction with a chemical solution and further extraction of a radioactive substance in the low-concentration washed sand S4 having a low concentration by dehydration, and the fine particle S2 obtained in the second classification step 2 as an adsorbent The fine particles S2 is used to remove radioactive substances from the froth F in the washing process 4 and the processing solution E in the radioactive substance extraction process 5, and to coagulate and precipitate to separate the precipitated sludge and water. And an adsorption step 6 that separates the concentrated residue T and the treated water W by dehydration.

(第1分級工程1)
先ず、第1分級工程1において、湿式ふるい装置11を用いて、セシウム等の土壌への吸着性の強い放射性物質汚染土壌(汚染土壌G0)から粗粒子分G2を分離し、スラリー状の土砂G1とする湿式ふるい分級処理が行われる。ここで、湿式ふるい装置11は、振動ふるいや超音波ふるい、比重選別等により、異物を選別して、礫・粗砂とそれ以下のスラリー状の土砂とに分級するものであり、網面を内部に備えている。この湿式ふるい装置11には、市販の公知の装置を使用することができる。なお、湿式ふるい装置11によって粗粒子分G2を分離しておくことにより、洗浄工程4における土砂G1の洗浄効率を向上させることができる。
(First classification step 1)
First, in the first classifying step 1, using a wet sieving device 11, coarse particles G2 are separated from radioactive material-contaminated soil (contaminated soil G0) having a strong adsorptivity to soil such as cesium and the like, and slurry-like earth and sand G1 is obtained. The wet sieving classification process is performed. Here, the wet sieving device 11 sorts foreign matter by vibration sieving, ultrasonic sieving, specific gravity sorting, etc., and classifies it into gravel / coarse sand and lower slurry-like earth and sand. Provided inside. As the wet sieving device 11, a commercially available known device can be used. In addition, the washing | cleaning efficiency of the earth and sand G1 in the washing | cleaning process 4 can be improved by isolate | separating the coarse particle content G2 with the wet sieve apparatus 11. FIG.

(第2分級工程2)
次に、第2分級工程2において、ハイドロサイクロン12を用いて、粗粒子分G2を除いた土壌土砂G1を砂分S1と汚染物質を含む細粒子分S2とに分級処理する。このハイドロサイクロン12は、例えば円筒底部が円錐型をした構造の容器からなり、土砂と水を混ぜたスラリーを導入する上部流入口と、アンダーフローを取り出す下部流出口と、オーバーフローを取り出す上部流出口とを備えている。上部流入口から入ったスラリー状の土砂は、円筒容器の円周方向に高速で供給されることにより、回転運動を起こし、回転流となって、円錐頂部に向かって進む。この時、スラリー中の比重の重い粒子は遠心力により周壁に集まり、次第にアンダーフロー出口(下部流出口)に向かい、濃縮して排出される。一方、液体と比重の軽い粒子は、円筒容器の中央部を渦流となって上昇し、オーバーフロー出口(上部流出口)から排出される。このハイドロサイクロン12には、市販の公知の装置を使用することができる。汚染物質は細粒子分S2に付着・吸着しているため、ハイドロサイクロン12で分級することにより、ほとんどの汚染物質を洗浄処理土から除去することができる。この分級の処理回数は、適宜設定されるが、1回以上行うのが好ましい。
(Second classification step 2)
Next, in the second classification step 2, the hydrocyclone 12 is used to classify the soil earth and sand G1 from which the coarse particle content G2 has been removed into a sand content S1 and a fine particle content S2 containing contaminants. The hydrocyclone 12 is composed of, for example, a container having a conical shape at the bottom of the cylinder, and includes an upper inlet for introducing slurry mixed with earth and sand, a lower outlet for taking out underflow, and an upper outlet for taking out overflow. And. The slurry-like earth and sand that has entered from the upper inflow port is rotated at a high speed in the circumferential direction of the cylindrical container, thereby causing a rotational motion, which becomes a rotational flow and proceeds toward the top of the cone. At this time, particles having a high specific gravity in the slurry gather on the peripheral wall due to centrifugal force, gradually move toward the underflow outlet (lower outlet), and are concentrated and discharged. On the other hand, particles having a low specific gravity with the liquid rise as a vortex in the center of the cylindrical container and are discharged from the overflow outlet (upper outlet). A commercially available known device can be used for the hydrocyclone 12. Since the contaminants adhere to and adsorb on the fine particle portion S2, most of the contaminants can be removed from the cleaning soil by classification with the hydrocyclone 12. The number of classification processes is appropriately set, but it is preferably performed once or more.

(離脱工程3)
続いて、離脱工程3において、スクラバー13を用いて、第2分級工程2で分級処理した砂分S1に付着している放射性物質を混合、攪拌によりもみ洗いにより離脱処理する。スクラバー13は、攪拌槽と攪拌羽根とが設けられている。このスクラバー13は、スラリー状の土砂に分散剤を添加した上で、攪拌羽根等を用いて機械的に混合・攪拌してスラリー状の土砂を相互に擦り合わせることにより、土砂表面に強固に付着した汚染物質を離脱し、分離するためのものである。このスクラバー13には、市販の公知の装置を使用することができる。なお、分散剤の添加量は、汚染物質の存在量によって任意に設定される。
(Leaving process 3)
Subsequently, in the separation step 3, the radioactive material adhering to the sand S1 classified in the second classification step 2 is mixed using the scrubber 13, and the separation processing is performed by mixing with agitation and washing. The scrubber 13 is provided with a stirring tank and a stirring blade. This scrubber 13 is firmly attached to the surface of the sand and sand by adding a dispersant to the sand and then mechanically mixing and stirring with a stirring blade and rubbing the slurry and sand together. For removing and separating the pollutants. As this scrubber 13, a commercially available known device can be used. In addition, the addition amount of a dispersing agent is arbitrarily set by the abundance of contaminants.

(洗浄工程4)
次に、洗浄工程4において、フローテーション装置14を用いて、スクラバー13からフローテーション装置14に投入された砂分S1のうち離脱工程3による離脱物(セシウム)をフローテーション処理によって発生させたフロスFにより回収するとともに、その洗浄砂S3を抽出する。つまり、フローテーション装置14では、気泡を発生させ、投入された砂分S1中の汚染物質を気泡と共に液面へと上昇させ、液面から泡と共にフロスFとして回収され、吸着工程6で用いられる凝集沈殿装置16に送られる。
なお、フローテーション処理によるフロスFによって回収されるセシウムは例えば最大で200μm程度のものであるため、それ以上の大きさのセシウムは洗浄砂S3に含有された状態となっている。
(Washing process 4)
Next, in the cleaning process 4, using the flotation device 14, the floss generated by the flotation process is the detachment substance (cesium) generated by the separation step 3 out of the sand S1 charged from the scrubber 13 into the flotation device 14. While collecting by F, the washing sand S3 is extracted. That is, in the flotation device 14, bubbles are generated, the pollutant in the charged sand S <b> 1 is raised to the liquid level together with the bubbles, and is recovered as floss F together with the bubbles from the liquid level and used in the adsorption step 6. It is sent to the coagulation sedimentation device 16.
In addition, since the cesium collect | recovered by the floss F by a flotation process is a thing about 200 micrometers at the maximum, for example, the cesium of the magnitude | size beyond it is in the state contained in the washing sand S3.

(放射性物質抽出工程5)
次に、放射性物質抽出工程5において、洗浄工程4の洗浄砂S3に含まれる放射性物質を、例えば抽出槽(図示省略)において、放射性物質抽出薬剤の溶液により抽出し、脱水処理装置15を用いてさらに濃度の低い2次洗浄砂(低濃度洗浄砂S4)を脱水処理する。ここで、放射性物質抽出薬剤として、例えば、カリウム化合物などのアルカリ金属類や、アンモニア、又は硝酸などの酸性物質を用いることができる。
脱水処理装置15は、公知の加圧式濾過装置(ベルトフィルタープレス)等であり、濾布等からなるフィルターとプレス機を備えている。なお、このときの処理溶液Eは、吸着工程6で用いられる凝集沈殿装置16に送られる。
(Radioactive substance extraction process 5)
Next, in the radioactive substance extraction step 5, the radioactive substance contained in the washing sand S3 in the washing step 4 is extracted with a solution of the radioactive substance extraction agent in, for example, an extraction tank (not shown), and the dehydration apparatus 15 is used. Further, the secondary washing sand having a low concentration (low concentration washing sand S4) is dehydrated. Here, as a radioactive substance extraction chemical | medical agent, acidic metals, such as alkali metals, such as a potassium compound, ammonia, or nitric acid, can be used, for example.
The dehydration processing device 15 is a known pressure filtration device (belt filter press) or the like, and includes a filter made of a filter cloth or the like and a press machine. In addition, the process solution E at this time is sent to the coagulation sedimentation apparatus 16 used by the adsorption process 6. FIG.

(吸着工程6)
次に、吸着工程6において、洗浄工程4によるフロスF、及び放射性物質抽出工程5による処理溶液Eが凝集沈殿装置16に送られるとともに、第2分級工程2によるハイドロサイクロン12で分離した細粒子分S2も凝集沈殿装置16に送られる。凝集沈殿装置16は、細粒子を含んだ懸濁水に凝集剤を添加・撹拌し、水中の微細な浮遊物を大きな沈殿汚泥として沈殿させ、清澄な処理水Wを分離するものである。なお、凝集沈殿装置16には、プレス脱水装置17を備えている。このプレス脱水装置17は、公知の加圧式濾過装置(ベルトフィルタープレス)等であり、濾布等からなるフィルターとプレス機を備えている。
そして、前記細粒子分S2を吸着材とし、この細粒子分S2に放射性物質(フロスF、処理溶液E)を吸着させて除去し、凝集沈殿させて沈殿汚泥と水とに分離し、プレス脱水装置17により沈殿汚泥を脱水処理し、濃縮残渣Tと処理水Wとに分離する。
この凝集沈殿装置16及びプレス脱水装置17には、市販の公知の装置を使用することができる。
(Adsorption process 6)
Next, in the adsorption process 6, the froth F from the washing process 4 and the treatment solution E from the radioactive substance extraction process 5 are sent to the coagulation sedimentation apparatus 16, and the fine particle fraction separated by the hydrocyclone 12 from the second classification process 2 is used. S2 is also sent to the coagulation sedimentation apparatus 16. The coagulating sedimentation apparatus 16 separates the clear treated water W by adding and stirring the coagulant to the suspension water containing fine particles to precipitate fine suspended matters in the water as large sedimentation sludge. The coagulation sedimentation device 16 is provided with a press dewatering device 17. The press dewatering device 17 is a known pressure-type filtration device (belt filter press) or the like, and includes a filter made of filter cloth or the like and a press machine.
Then, the fine particle portion S2 is used as an adsorbent, and a radioactive substance (floss F, treatment solution E) is adsorbed and removed on the fine particle portion S2, and coagulated and precipitated to separate into precipitated sludge and water, and press dewatering. The apparatus 17 dehydrates the precipitated sludge and separates it into a concentrated residue T and treated water W.
As the coagulation sedimentation apparatus 16 and the press dewatering apparatus 17, a commercially available known apparatus can be used.

次に、上述した放射性物質汚染土壌の洗浄処理方法の作用について、図面に基づいて説明する。
図1に示すように、洗浄工程4で得られた洗浄砂に対して放射性物質抽出薬剤を添加する放射性物質抽出工程5を行うことで、低濃度洗浄砂S4の放射性物質濃度をさらに低減することが可能となる。つまり、通常の方法では放射性物質の抽出のために分級前の汚染土壌に対して直接薬剤を添加していた方法を、洗浄工程4で洗浄した後の洗浄砂S3に対して薬剤を入れるので、薬剤の添加量を減らすことができる。
Next, the effect | action of the washing | cleaning processing method of the radioactive substance contaminated soil mentioned above is demonstrated based on drawing.
As shown in FIG. 1, the radioactive substance concentration of the low-concentration washing sand S4 is further reduced by performing the radioactive substance extraction process 5 in which the radioactive substance extraction agent is added to the washing sand obtained in the washing process 4. Is possible. That is, in the normal method, since the chemical is added directly to the contaminated soil before classification for extraction of radioactive substances, the chemical is put into the washing sand S3 after washing in the washing step 4, The amount of drug added can be reduced.

また、ハイドロサイクロン処理によって得られた廃棄処分用の細粒子分S2を吸着材として用い、この細粒子分S2に対して洗浄工程4で発生したフロスFや放射性物質抽出工程5で生じた処理溶液Eを吸着させる吸着工程6を設けることにより、この細粒子分S2が従来使用していたRO膜やゼオライトの代替とすることが可能となり、吸着材にかかるコストの低減を図ることができる。そして、吸着材として使用する前記細粒子分S2は廃棄するものであり、従来のようにRO膜やゼオライト等の新たな吸着材を加える必要がないことから、廃棄物の減量化が可能である。   In addition, the disposal fine particle S2 obtained by the hydrocyclone treatment is used as an adsorbent, and the treatment solution generated in the floss F generated in the cleaning step 4 and the radioactive substance extraction step 5 with respect to this fine particle S2. By providing the adsorption step 6 for adsorbing E, the fine particle portion S2 can be used as a substitute for the RO membrane and zeolite conventionally used, and the cost for the adsorbent can be reduced. And the said fine particle part S2 used as an adsorbent is discarded, and since it is not necessary to add new adsorbents, such as RO membrane and a zeolite conventionally, it can reduce the amount of waste. .

上述のように本実施の形態による放射性物質汚染土壌の洗浄処理方法では、洗浄工程4で得られた洗浄砂S3に対して放射性物質抽出薬剤を添加する放射性物質抽出工程5を行うことで、抽出効率を高めることができ、染物質濃度の低減を図ることができる。   As described above, in the cleaning method for radioactive material contaminated soil according to the present embodiment, extraction is performed by performing the radioactive substance extraction step 5 in which the radioactive substance extraction agent is added to the cleaning sand S3 obtained in the cleaning step 4. The efficiency can be increased, and the dye concentration can be reduced.

また、投入された汚染土壌G0の土量に比べて洗浄工程4で得られた洗浄砂S3が減量されているので、薬剤の添加量を減らすことができる。しかも、分級処理で得られた細粒子分S2を吸着材として再利用する方法であり、新たな吸着材を追加する必要がないことから、処理費用と廃棄物量の低減を図ることができる。   In addition, since the amount of the cleaning sand S3 obtained in the cleaning step 4 is reduced compared to the amount of soil in the contaminated soil G0 that has been input, the amount of chemical added can be reduced. In addition, the fine particle S2 obtained by the classification process is reused as an adsorbent, and it is not necessary to add a new adsorbent, so that the processing cost and the amount of waste can be reduced.

以上、本発明による放射性物質汚染土壌の洗浄処理方法の実施の形態について説明したが、本発明は上記の実施の形態に限定されるものではなく、その趣旨を逸脱しない範囲で適宜変更可能である。
例えば、本実施の形態では第2分級工程2の後にスクラバー13を用いた離脱工程3を有する処理方法としているが、この離脱工程3を省略し、第2分級工程2で分級された砂分S1をフローテーション装置14に投入して放射性物質抽出工程5を行うようにしてもかまわない。
その他、本発明の趣旨を逸脱しない範囲で、上記した実施の形態における構成要素を周知の構成要素に置き換えることは適宜可能である。
As mentioned above, although embodiment of the washing processing method of radioactive substance contamination soil by this invention was described, this invention is not limited to said embodiment, It can change suitably in the range which does not deviate from the meaning. .
For example, in the present embodiment, the second classification step 2 is followed by the treatment method having the separation step 3 using the scrubber 13, but the separation step 3 is omitted and the sand content S1 classified in the second classification step 2 is used. May be introduced into the flotation device 14 to perform the radioactive substance extraction step 5.
In addition, it is possible to appropriately replace the components in the above-described embodiments with known components without departing from the spirit of the present invention.

1 第1分級工程
2 第2分級工程
3 離脱工程
4 洗浄工程
5 放射性物質抽出工程
6 吸着工程
11 湿式ふるい装置
12 ハイドロサイクロン
13 スクラバー
14 フローテーション装置
15 脱水処理装置
16 凝集沈殿装置
17 プレス脱水装置
E 処理溶液
F フロス
G0 汚染土壌
G1 土砂
G2 粗粒子分
S1 砂分
S2 細粒子分
S3 洗浄砂
S4 低濃度洗浄砂
T 濃縮残渣
W 処理水
DESCRIPTION OF SYMBOLS 1 1st classification process 2 2nd classification process 3 Separation process 4 Washing process 5 Radioactive substance extraction process 6 Adsorption process 11 Wet sieving equipment 12 Hydrocyclone 13 Scrubber 14 Flotation equipment 15 Dehydration processing equipment 16 Coagulation sedimentation equipment 17 Press dehydration equipment E Treatment solution F Floss G0 Contaminated soil G1 Sediment G2 Coarse particles S1 Sand content S2 Fine particles S3 Washed sand S4 Low concentration washed sand T Concentrated residue W Treated water

Claims (2)

放射性物質を含有する汚染土壌を洗浄するとともに、該汚染土壌から放射性物質を分離、除去する放射性物質汚染土壌の洗浄処理方法であって、
前記汚染土壌に水を添加し、湿式ふるい分級処理して粗粒子分を分離して、スラリー状の土砂とする第1分級工程と、
この土砂を、ハイドロサイクロン処理して砂分と、汚染物質を含む細粒子分とに分級処理する第2分級工程と、
前記砂分をフローテーション処理によって発生させたフロスにより回収する洗浄工程と、
前記洗浄工程の洗浄砂に含まれる放射性物質を放射性物質抽出薬剤の溶液により抽出し、さらに濃度の低い低濃度洗浄砂を脱水処理により得る放射性物質抽出工程と、
前記第2分級工程で得られた細粒子分を吸着材とし、該細粒子分を用いて前記洗浄工程によるフロスと放射性物質抽出工程による処理溶液とから放射性物質を除去するとともに、凝集沈殿させて沈殿汚泥と水とに分離し、該沈殿汚泥を脱水処理して濃縮残渣と処理水とに分離する吸着工程と、
を有することを特徴とする放射性物質汚染土壌の洗浄処理方法。
A method for cleaning radioactive material-contaminated soil that cleans contaminated soil containing radioactive material, and separates and removes the radioactive material from the contaminated soil,
A first classification step of adding water to the contaminated soil, separating the coarse particles by wet sieving classification, and obtaining slurry-like soil;
A second classification step of classifying the earth and sand into a sand and a fine particle containing a pollutant by hydrocyclone treatment;
A washing step of collecting the sand by floss generated by a flotation treatment;
A radioactive substance extraction step in which radioactive substances contained in the washing sand of the washing step are extracted with a solution of a radioactive substance extraction drug, and a low concentration washing sand having a low concentration is obtained by dehydration;
The fine particles obtained in the second classification step are used as an adsorbent, and the fine particles are used to remove radioactive substances from the floss in the washing step and the treatment solution in the radioactive substance extraction step, and to coagulate and precipitate. An adsorption step of separating the precipitated sludge into water and separating the precipitated sludge into a concentrated residue and treated water;
A method for cleaning radioactive material-contaminated soil, comprising:
前記第2分級工程で分級処理した前記砂分に付着している放射性物質を攪拌により離脱させる離脱工程が設けられていることを特徴とする請求項1に記載の放射性物質汚染土壌の洗浄処理方法。
2. The method for cleaning radioactive material-contaminated soil according to claim 1, further comprising a separation step of separating the radioactive material adhering to the sand component classified in the second classification step by stirring. .
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