JP2019174393A - Contaminated soil decontamination method - Google Patents

Contaminated soil decontamination method Download PDF

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JP2019174393A
JP2019174393A JP2018065485A JP2018065485A JP2019174393A JP 2019174393 A JP2019174393 A JP 2019174393A JP 2018065485 A JP2018065485 A JP 2018065485A JP 2018065485 A JP2018065485 A JP 2018065485A JP 2019174393 A JP2019174393 A JP 2019174393A
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contaminated soil
soil
electrode
contaminated
moisture
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JP7002981B2 (en
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カビール・ムハムドゥル
Kabir Mahmudul
友祐 佐藤
Yusuke Sato
友祐 佐藤
春介 中島
Shunsuke Nakajima
春介 中島
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Akita University NUC
Sanwa Tekki Corp
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Sanwa Tekki Corp
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Abstract

To provide a contaminated soil decontamination method for preventing air pollution, carbon dioxide emission and secondary pollution due to transportation of contaminated soil, by quickly clarifying, dehydrating, and reducing the volume of contaminated soil with simple equipment at a collection site, a temporary storage yard, or intermediate storage facilities that do not involve the movement of the contaminated soil.SOLUTION: There is provided the contaminated soil decontamination method for collecting harmful contaminant from contaminated soil contaminated with radioactive material and heavy metal and the like. In the method, a water-permeable flexible container bag 2 is filled with contaminated soil D including moisture and suspended, and the positive and negative electrode rods 4 and 5 are inserted into the contaminated soil D with a space between them, and a voltage is applied between the electrode rods 4 and 5. The contaminant is ionized by electrolysis by the electric field between the electrode rods 4 and 5 and eluted on the particle surface of the contaminated soil D, and soil moisture D1 including the contaminant in the contaminated soil D is subjected to electrophoresis and electroosmosis, thereby concentrated to the periphery of electrode rod 5 (4), and is exuded under the flexible container bag 2 and dehydrated, and contaminant is removed from the contaminated soil D.SELECTED DRAWING: Figure 1

Description

本発明は、水分を多く含むと共に放射性物質や重金属などの有害物質で汚染された土壌並びに津波等により塩害を受けた土壌(以下、「汚染土」という)から汚染物質を分離しあるいは塩分を除去すると共に脱水を促進する汚染土の除染方法に関する。   The present invention separates or removes salt from soil that contains a lot of moisture and is contaminated with radioactive substances, heavy metals and other harmful substances, and soil that has been damaged by tsunami (hereinafter referred to as “contaminated soil”). The present invention also relates to a decontamination method for contaminated soil that promotes dehydration.

通常、重金属などの有害物質で汚染された土壌を除染するには、土壌から汚染土を掻き取り、生石灰などの乾燥促進剤や不溶化薬剤などの処理剤を添加して、最終処分場で処理される。また、放射性物質に汚染された土壌は表層土を剥ぎ取り、フレコンバッグに詰めて保管され、最終処分場で処理される。
従来、有害物質に汚染された土壌を除染する方法として、汚染領域に電極棒を挿入してこの電極棒を直流電源の陽極に接続し、汚染領域の外側位置に井戸を掘削し、この井戸に設置した導体を直流電源の陰極に接続し、井戸内に水中ポンプを設置する方法がある(特許文献1参照)。この方法では、直流電源を駆動すると、粘性地盤内に、陽極となる電極棒側から陰極となる導体が存在する井戸側へ電気浸透現象による強制排水を行い、汚染源及び汚染領域に存在する汚染物質を地下水と共に井戸に排出し、水中ポンプによって地上へ汲み上げ、浄化処理する。
また、フレコンバッグの側面にラミネートを施して透水性を失わせ、底面にメッシュ生地を用いて透水性を高めたフレコンバッグの内部に粒子状のゼオライト吸着剤を収容したものを、放射性セシウムを含有する排水と接触させて放射性セシウムを吸着させ水から分離し、これらを収容するフレコンを埋立て処分する方法がある(特許文献2参照)。
さらに、処理対象物を脱水する装置として、濾室の間隔を置いて相対向するスクリーンの相互間にアウタースペーサからインナースペーサに向かって電極部を突設し、電極部とスクリーンの間に直流電圧を印加することにより、電気浸透脱水を行う回転加圧脱水機がある(特許文献3参照)。
Usually, in order to decontaminate soil contaminated with toxic substances such as heavy metals, scrape the contaminated soil from the soil, add drying accelerators such as quick lime and treatment agents such as insolubilizing agents, and treat at the final disposal site. Is done. In addition, the soil contaminated with radioactive material is stripped of the surface soil, stored in a flexible container bag, and processed at the final disposal site.
Conventionally, as a method of decontaminating soil contaminated with harmful substances, an electrode rod is inserted into the contaminated area, this electrode rod is connected to the anode of a DC power source, a well is excavated outside the contaminated area, and this well There is a method of connecting a conductor installed in the cathode to the cathode of a DC power source and installing a submersible pump in the well (see Patent Document 1). In this method, when a DC power supply is driven, forced drainage by electroosmosis occurs from the electrode rod side serving as the anode to the well side where the conductor serving as the cathode exists in the viscous ground, and the pollutants present in the pollution source and the contaminated area. Is discharged into the well together with the groundwater, pumped up to the ground with a submersible pump, and purified.
In addition, it contains radioactive cesium that contains particulate zeolite adsorbent inside a flexible container bag that has been laminated on the side of the flexible container bag to lose water permeability and mesh fabric is used on the bottom to increase the water permeability. There is a method in which radioactive cesium is adsorbed and separated from water by contact with wastewater to be disposed of, and the flexible containers containing these are landfilled (see Patent Document 2).
Furthermore, as a device for dehydrating the object to be treated, an electrode part is projected from the outer spacer to the inner spacer between the screens facing each other with an interval between the filter chambers, and a DC voltage is applied between the electrode part and the screen. There is a rotary pressure dehydrator that performs electroosmotic dehydration by applying (see Patent Document 3).

特開平10-309562号公報Japanese Patent Laid-Open No. 10-309562 特開2013-186012号公報JP 2013-186012 JP 特開2017-023944号公報JP 2017-023944

汚染物質の除染に関する上記従来の方法における前者は、汚染土を現場で処理する方法であるが、井戸を掘削するスペースを必要とすると共に、井戸の掘削工事の費用が嵩む。
また後者は、廃棄物処分場や除染作業現場に埋立処理する方法であるが、東日本大震災での原子力発電所の事故に伴う放射性物質の飛散により膨大な汚染土が仮置場に長期間保管されている状況においては、これらの未処理の汚染土を中間貯蔵施設に移送し保管する必要があり、安全に埋立処分する前の安全な移送等を行う手段を確立する必要がある。また、膨大な未処理の汚染土を保管場所から最終処分場に運搬するとなると、相当量の大型運搬車の往来による大気汚染、二酸化炭素の放出、放射性物質の二次拡散が懸念される。
さらに、脱水処理に関する電気浸透を利用した上記回転加圧脱水機は、処理能力に応じた装置の大型化及び費用の増大をもたらすし、処理量に限界があり、上記のような膨大な量の汚染土への適用は現実的でない。
そこで、本発明は、汚染土の移動を伴わない収集現場、仮置き場又は中間貯蔵施設での簡易な設備により設置スペースや設置コストを抑えつつ、迅速に汚染土を浄化、脱水、減容化して、汚染土の運搬に伴う大気汚染、二酸化炭素の放出、二次汚染を防ぐ汚染土の除染方法を提供する。
The former method in the above-mentioned conventional method relating to the decontamination of pollutants is a method of treating contaminated soil on site. However, it requires a space for excavating a well, and the cost for excavating the well increases.
The latter is a landfill method at a waste disposal site or decontamination work site, but a huge amount of contaminated soil is stored in a temporary storage site for a long time due to the scattering of radioactive materials caused by the nuclear power plant accident in the Great East Japan Earthquake. In such a situation, it is necessary to transfer and store these untreated contaminated soils in an intermediate storage facility, and it is necessary to establish means for performing safe transfer before landfilling safely. In addition, if a large amount of untreated contaminated soil is transported from a storage location to a final disposal site, there are concerns about air pollution, carbon dioxide release, and secondary diffusion of radioactive materials due to the arrival of a considerable amount of large transport vehicles.
Furthermore, the rotary pressure dehydrator using electroosmosis related to the dehydration process increases the size and cost of the apparatus according to the processing capacity, has a limited processing amount, and has a huge amount as described above. Application to contaminated soil is not realistic.
Therefore, the present invention quickly purifies, dehydrates, and reduces the volume of contaminated soil while suppressing installation space and installation costs with simple equipment at a collection site, temporary storage, or intermediate storage facility that does not involve the movement of contaminated soil. Provide decontamination methods for contaminated soil to prevent air pollution, carbon dioxide emission and secondary pollution associated with transportation of contaminated soil.

本発明においては、汚染土Dから有害な汚染物質を分離しあるいは塩分を除去する汚染土の除染方法を採用する。水分を含む汚染土Dを収容したフレコンバッグ2のような透水性容器を宙づりにし、汚染土Dに相互に間隔を置いて差し込んだ正負両極の電極棒4,5に電圧を印加する。電極棒4,5間の電界による電気分解により汚染物質をイオン化して汚染土Dの粒子表面に溶出させ、汚染土D中の汚染物を含む土中水分D1を電気泳動及び電気浸透により電極棒5(4)の周辺に集中させて、汚染物質を除去すると共に、透水性容器の下方に土中水分を染み出させ脱水する。   In this invention, the decontamination method of the contaminated soil which isolate | separates a harmful pollutant from the contaminated soil D, or removes salt content is employ | adopted. A water-permeable container such as the flexible container bag 2 containing the contaminated soil D containing moisture is suspended, and a voltage is applied to the positive and negative electrode rods 4 and 5 inserted into the contaminated soil D at intervals. Contaminants are ionized by electrolysis by the electric field between the electrode rods 4 and 5 to be eluted on the particle surface of the contaminated soil D, and the soil moisture D1 containing the contaminants in the contaminated soil D is electrophoresed and electroosmotically electrophoresed. Concentrate around 5 (4) to remove contaminants and exude moisture in the soil below the permeable container.

本発明においては、汚染土を収集し又は保管した現場において簡易設備により設置スペースや設置コストを抑えつつ、汚染土を浄化、脱水、減容化することができるので、汚染土の運搬に伴う運搬等の労力を省き、運搬車の往来による大気汚染、二酸化炭素の放出、二次汚染の拡大を防ぐことができるという効果を有する。   In the present invention, the contaminated soil can be purified, dehydrated, and reduced in volume at a site where the contaminated soil is collected or stored, and the installation space and the installation cost can be reduced by simple equipment. This has the effect of preventing the air pollution, the release of carbon dioxide and the spread of secondary pollution caused by transportation vehicles.

本発明の第1実施例に係る除染方法に用いる除染設備の概略図である。It is the schematic of the decontamination equipment used for the decontamination method which concerns on 1st Example of this invention. 本発明の第2実施例に係る除染方法に用いる除染設備の概略図である。It is the schematic of the decontamination equipment used for the decontamination method concerning 2nd Example of this invention. 図2の除染設備の電極棒の断面図である。It is sectional drawing of the electrode rod of the decontamination equipment of FIG. 図2の除染設備の電極棒の一部を切り欠いた正面図である。It is the front view which notched some electrode bars of the decontamination equipment of FIG. 本発明の第3実施例に係る除染方法に用いる除染設備の概略図である。It is the schematic of the decontamination equipment used for the decontamination method concerning 3rd Example of this invention. 図5の除染設備の網状電極の展開図である。It is an expanded view of the mesh electrode of the decontamination equipment of FIG. 図5の除染設備の変形例の概略図である。It is the schematic of the modification of the decontamination equipment of FIG.

本発明の実施形態について図面を参照して説明する。
図1において、本発明の第1実施例に係る汚染土の除染方法に使用する除染設備は、架台1に吊り下げられた汚染土を収容するフレコンバッグ2と、直流式の電源3と、この電源3に接続される正負の電極棒4,5と、濾液受け槽6とを備えている。
フレコンバッグ2は、容易に破損しない程度の強度と柔軟性を有する透水性素材の容器であれば、他の周知のものを適用してよい。
電源3は、電極棒4,5に直流電圧を印加するためのもので、印加電圧を数V〜100V程度とする。電源3は、シリーズレギュレータ等の一次側を交流電源としてAC−DC変換するものの他、自動車バッテリー等の蓄電池を単独で又は複数を直列多段接続して昇圧するものでも良い。電圧の印加方向は、施工の開始から終了まで同一としても良いし、後述する極性によるイオンの移動域の拡散度合いの相違を考慮して、間歇的に切り替えるものとしてもよい。
電極棒4,5は、フレコン2内の汚染土に間隔を置いてほぼ平行に複数対並べて縦方向に差し込まれるものである。電極棒4,5は中空又は中実で長尺の棒状をなし、SUS、チタン、鉄等金属、カーボンなど各種の電極材を用いることができる。また、電極棒4,5は、側面部に汚染物質を固定するための活性炭、ゼオライト、層状粘土鉱物、くん炭、金属粉などの汚染物質を吸着する吸着材を貼着又は含滲させ、又はこれらと導電材とを混合して形成したものでもよい。電極棒4,5の先端部には、挿入時にバッグの突き抜けを防止するためのゴム等の柔軟素材からなる保護カバー7を被覆する。
濾液受け槽6は、フレコンバッグ2から滲み出した濾液を貯留回収するためのベッセル等の薄型の水槽である。濾液受け槽6内には、有害物質を吸着するために、ゼオライト、層状粘土鉱物、イオン交換樹脂、キレート樹脂、貝殻粉等の吸着剤8が投入してもよいし、他の凝集沈殿法などを用いる濁水処理装置を使用して浄化することとしてもよい。
Embodiments of the present invention will be described with reference to the drawings.
In FIG. 1, the decontamination equipment used for the decontamination method of the contaminated soil which concerns on 1st Example of this invention is the flexible container bag 2 which accommodates the contaminated soil suspended by the mount frame 1, the direct current | flow type power supply 3, and The positive and negative electrode rods 4 and 5 connected to the power source 3 and the filtrate receiving tank 6 are provided.
As the flexible container bag 2, as long as it is a container made of a water-permeable material having a strength and flexibility that does not easily break, another known bag may be applied.
The power source 3 is for applying a DC voltage to the electrode rods 4 and 5, and the applied voltage is about several V to 100 V. The power source 3 may be one that boosts the storage battery such as an automobile battery by a single or a plurality of stages connected in series, in addition to the AC-DC conversion using the primary side of the series regulator as an AC power source. The application direction of the voltage may be the same from the start to the end of the construction, or may be switched intermittently in consideration of the difference in the degree of diffusion of the ion movement region due to the polarity described later.
The electrode rods 4 and 5 are inserted in the longitudinal direction with a plurality of pairs arranged substantially parallel to each other at a distance from the contaminated soil in the flexible container 2. The electrode rods 4 and 5 are hollow or solid and have a long rod shape, and various electrode materials such as metals such as SUS, titanium and iron, and carbon can be used. The electrode rods 4 and 5 are attached or impregnated with adsorbents that adsorb pollutants such as activated carbon, zeolite, layered clay minerals, charcoal, and metal powder for fixing the pollutants on the side surfaces, or It may be formed by mixing these and a conductive material. The tip portions of the electrode rods 4 and 5 are covered with a protective cover 7 made of a flexible material such as rubber for preventing the bag from penetrating during insertion.
The filtrate receiving tank 6 is a thin water tank such as a vessel for storing and collecting the filtrate that has oozed out of the flexible container bag 2. In the filtrate receiving tank 6, an adsorbent 8 such as zeolite, layered clay mineral, ion exchange resin, chelate resin, shellfish powder, etc. may be introduced to adsorb harmful substances, or other coagulation precipitation methods, etc. It is good also as purifying using the muddy water processing apparatus using.

この実施例の除染装置を用いた除染方法を以下に説明する。
汚染土壌から掘削し、あるいは一時保管施設又は中間保管施設において保管してある汚染土Dを濾過用フレコンバッグ2に詰め込み、このフレコンバッグ2を架台1に吊り下げ、先端に保護カバー7を取り付けた電極棒4,5をフレコンバッグ2内の汚染土Dにフレコンバッグ2の底部近傍まで差し込み、電源3で電極棒4,5に電圧を印加する。正負の電極棒4,5間において電気分解、電気泳動、電気浸透の動電現象が生じる。このとき、電極棒4,5間の電界により汚染土Dの土中水分D1が電気分解されて生じる水素イオンが、汚染土D中を正極の電極棒4から負極の電極棒5へ移動することにより、水素よりイオン化傾向の大きな重金属等の汚染物質がイオン化して汚染土Dの粒子の表面に溶出する。この汚染物質が電極棒4,5間の電界により負極の電極棒5に引き付けられ移動する電気泳動が生じ電極棒5の周辺に集中する。一方、汚染土Dの土中水分D1の電気分解で生じた水酸化物イオンは、汚染土D中を負極の電極棒5から正極の電極棒4へ移動して、重金属等の汚染物質を不溶化し沈殿させる。水酸化物イオンは水素イオンよりはるかに重く、電気泳動等の動電現象に伴う水素イオンの移動速度がはるかに大きい。従って、水素イオンの移動域が拡散しやすく、負極の電極棒5の周辺はアルカリイオン化し易く、重金属等の汚染物質は不溶化しやすくなるため、収集しにくくなる。これを避けるために電極棒4,5の極性を定期的に変更することが効果的である。また、汚染土Dの粒子間の微細空間は通水間隙を形成し、この通水間隙の周囲の汚染土Dの粒子表面は負極性に帯電する。これにより、通水間隙の表面(間隙と汚染土Dの接触面)も負極性に帯電する。この通水間隙を移動する土中水分D1に含まれる陽イオンなどの正電荷粒子が通水間隙の表面に付着し、電極間に生じる電界により、これらが正極から負極へと移動する。陽イオンの移動に伴い通水間隙内の土中水分D1も流れることにより、電気浸透流が生じる。このようにして、電極棒4,5間の電界による電気分解の影響で汚染物質がイオン化して汚染土Dの粒子表面に溶出し、電気泳動と電気浸透により負極の電極棒5の周辺に集中すると共に、電気浸透流による水の流れが生じることにより水抜けが促進され、脱水効率が向上する。
なお、保護カバー7には、電極棒5に集中する水分の保護カバー7での貯留を防ぐため、水抜き穴を設けてもよい。
A decontamination method using the decontamination apparatus of this example will be described below.
The contaminated soil D excavated from the contaminated soil or stored in the temporary storage facility or intermediate storage facility is packed in the filtration flexible container bag 2, the flexible container bag 2 is suspended on the gantry 1, and a protective cover 7 is attached to the tip. The electrode bars 4 and 5 are inserted into the contaminated soil D in the flexible container bag 2 to the vicinity of the bottom of the flexible container bag 2, and a voltage is applied to the electrode bars 4 and 5 by the power source 3. Electrokinetic phenomena of electrolysis, electrophoresis and electroosmosis occur between the positive and negative electrode rods 4 and 5. At this time, hydrogen ions generated by electrolyzing soil moisture D1 of the contaminated soil D by the electric field between the electrode rods 4 and 5 move from the positive electrode rod 4 to the negative electrode rod 5 in the contaminated soil D. As a result, contaminants such as heavy metals having a higher ionization tendency than hydrogen are ionized and eluted on the surfaces of the particles of the contaminated soil D. The pollutant is attracted to the negative electrode rod 5 by the electric field between the electrode rods 4 and 5, causing migration, and concentrates around the electrode rod 5. On the other hand, the hydroxide ions generated by the electrolysis of the soil moisture D1 of the contaminated soil D move from the negative electrode rod 5 to the positive electrode rod 4 in the contaminated soil D to insolubilize contaminants such as heavy metals. And precipitate. Hydroxide ions are much heavier than hydrogen ions, and the migration speed of hydrogen ions associated with electrokinetic phenomena such as electrophoresis is much higher. Accordingly, the migration region of hydrogen ions is easily diffused, the periphery of the negative electrode rod 5 is easily alkalinized, and contaminants such as heavy metals are easily insolubilized, which makes collection difficult. In order to avoid this, it is effective to periodically change the polarities of the electrode rods 4 and 5. Moreover, the fine space between the particles of the contaminated soil D forms a water passage gap, and the particle surface of the contaminated soil D around the water passage gap is negatively charged. As a result, the surface of the water gap (the contact surface between the gap and the contaminated soil D) is also charged negatively. Positively charged particles such as cations contained in the moisture D1 in the soil moving through the water passage gap adhere to the surface of the water passage gap, and these move from the positive electrode to the negative electrode due to the electric field generated between the electrodes. As the cation moves, the soil moisture D1 in the water passage also flows, thereby generating an electroosmotic flow. In this way, contaminants are ionized by the influence of electrolysis due to the electric field between the electrode rods 4 and 5 and are eluted on the particle surface of the contaminated soil D, and are concentrated around the negative electrode rod 5 by electrophoresis and electroosmosis. At the same time, the flow of water due to the electroosmotic flow is generated, thereby facilitating drainage and improving the dewatering efficiency.
The protective cover 7 may be provided with a drain hole in order to prevent accumulation of moisture concentrated on the electrode rod 5 in the protective cover 7.

本発明に係る第2実施形態について図2を参照して説明する。なお以下において先の実施形態と同一の構成部分には同一符号を付して説明を省略する。
フレコンバッグ2に詰め込んだ汚染土Dには、ストレーナ電極14,15が差し込まれる。ストレーナ電極14,15の上端部には、図3に示すように、ホース10が接続され分岐用のマニホールド11を介してサクションポンプ9が接続され、サクションポンプ9の排出管が濾液受け槽6に臨む。図4に示すように、ストレーナ電極14,15は、土中水分D1を回収しやすくするために、側面にスリット14a(15a)や小孔を多数設けた管材でそれぞれ構成する。ストレーナ電極14,15の上端部には、サクション時の汚染水の有害物質を集積し減容化する吸着フィルター14b(15b)を挿入する。吸着フィルター14b(15b)は、ゼオライト、粘土鉱物等の吸着剤を混入した透水性の不織布等の繊維集合体で構成する。保護カバー7には、小孔7aを備える。
ストレーナ電極14,15間に電圧を印加すると、先と同様にして電気泳動及び電気浸透によりストレーナ電極15の周辺に汚染土Dの土中水分D1をスリット15aを通じて取り込み、サクションポンプ9により吸い取って、濾液受け槽6に排出する。土中水分D1は、吸着フィルター14b(15b)を通して汚染物質を吸着し、浄化と共に脱水を行うことにより減容化される。
なお、本実施形態においては、サクションポンプ9による吸引処理を行うためストレーナ電極14、15の極性の定期的な変更は行わない。
A second embodiment according to the present invention will be described with reference to FIG. In the following description, the same components as those of the previous embodiment are denoted by the same reference numerals and description thereof is omitted.
Strainer electrodes 14 and 15 are inserted into the contaminated soil D packed in the flexible container bag 2. As shown in FIG. 3, a hose 10 is connected to the upper ends of the strainer electrodes 14 and 15, and a suction pump 9 is connected via a branch manifold 11, and a discharge pipe of the suction pump 9 is connected to the filtrate receiving tank 6. Come on. As shown in FIG. 4, the strainer electrodes 14 and 15 are each formed of a pipe material provided with a large number of slits 14 a (15 a) and small holes on the side surface in order to easily collect the moisture D <b> 1 in the soil. An adsorption filter 14b (15b) that accumulates and reduces the harmful substances of contaminated water during suction is inserted into the upper ends of the strainer electrodes 14 and 15. The adsorption filter 14b (15b) is composed of a fiber assembly such as a water-permeable nonwoven fabric mixed with an adsorbent such as zeolite or clay mineral. The protective cover 7 includes a small hole 7a.
When a voltage is applied between the strainer electrodes 14 and 15, the soil moisture D1 of the contaminated soil D is taken into the periphery of the strainer electrode 15 through the slit 15a by electrophoresis and electroosmosis in the same manner as before, and sucked by the suction pump 9, The filtrate is discharged into the filtrate receiving tank 6. The soil moisture D1 is reduced in volume by adsorbing contaminants through the adsorption filter 14b (15b) and performing dehydration as well as purification.
In the present embodiment, since the suction process by the suction pump 9 is performed, the polarity of the strainer electrodes 14 and 15 is not periodically changed.

本発明に係る第3実施形態について図5を参照して説明する。
フレコンバッグ2には、外摺面を取り囲むように柔軟な網状電極12が固定される。網状電極12は、図6に示すように、SUS、チタン等の導電性金属板12aからなり、フレコンバッグ2から滲出する土中水分D1を通り抜け可能なメッシュ状又は多孔状に形成され、その周縁部がプラスチック、ゴム等による保護材12bで被覆され、長手方向両端部に互いに結合可能な連結部材12c,12dを備え、電源3の負極側及びアース線12eに接続される。
網状電極12は、電極棒4に対する電極棒5と同様に、電極棒4との間に電界を形成して、電気泳動と電気浸透により土中水分D1をフレコンバッグ2の側部にも集中させ、汚染物質の吸着、水抜きによる浄化を促進する。
また、網状電極12は、図7に示すように、狭小幅の網状電極12をフレコンバッグ2の外周に上下に複数並べて配置してもよい。
A third embodiment according to the present invention will be described with reference to FIG.
A flexible mesh electrode 12 is fixed to the flexible container bag 2 so as to surround the outer sliding surface. As shown in FIG. 6, the mesh electrode 12 is made of a conductive metal plate 12a such as SUS or titanium, and is formed in a mesh shape or a porous shape that can pass through the moisture D1 in the soil exuding from the flexible container bag 2. The portion is covered with a protective material 12b made of plastic, rubber or the like, and includes connecting members 12c and 12d that can be coupled to each other at both ends in the longitudinal direction, and is connected to the negative electrode side of the power source 3 and the ground wire 12e.
Similar to the electrode rod 5 for the electrode rod 4, the mesh electrode 12 forms an electric field between the electrode rod 4 and concentrates moisture D1 in the soil also on the side of the flexible container bag 2 by electrophoresis and electroosmosis. , Promote the adsorption of pollutants and purification by draining water.
Further, as shown in FIG. 7, the mesh electrode 12 may be a plurality of narrow mesh electrodes 12 arranged vertically on the outer periphery of the flexible container bag 2.

この実施形態において、網状電極12とフレコンバッグ2との間の電気的な接触抵抗が大きく、ここでの電圧降下が大きくなり、浄化対象の汚染土に十分な印加電圧を付与できない場合、網状電極12に対面するフレコンバッグ2を部分的に不織布などにカーボン粒子、金属粒子などを含ませる加工を施して、導電率を向上させてもよい。
網状電極12は市販のメッシュパレットを用いてもよい。
濾液受け槽6は、汚染土の汚染物質に応じて拡散を防止するためにベッセル等で覆う構成にしてもよい。この場合、メッシュパレットとベッセル等との接触を電気的に絶縁する。
濾過液に汚濁成分が多い場合は、凝集剤を投入して、簡易の凝集沈殿処理を行ってもよい。
なお、本実施形態における網状電極12は、前述のストレーナ電極14,15を設けた第2実施形態においても適用できることはいうまでもない。
In this embodiment, when the electrical contact resistance between the mesh electrode 12 and the flexible container bag 2 is large, the voltage drop here becomes large, and a sufficient applied voltage cannot be applied to the contaminated soil to be purified. The flexible container bag 2 facing 12 may be partially processed to include carbon particles, metal particles, etc. in a non-woven fabric to improve the conductivity.
The mesh electrode 12 may be a commercially available mesh pallet.
The filtrate receiving tank 6 may be configured to be covered with a vessel or the like in order to prevent diffusion according to the pollutant in the contaminated soil. In this case, the contact between the mesh pallet and the vessel is electrically insulated.
When there are many pollutant components in the filtrate, a flocculant may be added to perform a simple coagulation precipitation treatment.
In addition, it cannot be overemphasized that the mesh electrode 12 in this embodiment is applicable also in 2nd Embodiment which provided the strainer electrodes 14 and 15 mentioned above.

汚染土Dの動電現象を促進させるために、前処理として汚染土Dに導電助剤を添加してもよい。導電助剤は、電極との接触抵抗及び汚染土D中の電気抵抗を下げる食塩やカリウム塩からなる導電補助剤を添加してもよい。特に、汚染物質が放射性セシウムの場合、カリウムとセシウムとの置換作用によって、汚染土Dの粒子表面からのセシウムの溶出を促進する。汚染物質が重金属の場合、導電補助剤に酢酸、シュウ酸等の酸を用いると、重金属の汚染物質の溶出を促進する。汚染物質が鉛などの酸ともアルカリとも反応する両性元素や両性酸化物の場合、導電補助剤をアルカリ性薬剤の添加が効果的である。   In order to promote the electrokinetic phenomenon of the contaminated soil D, a conductive additive may be added to the contaminated soil D as a pretreatment. As the conductive auxiliary agent, a conductive auxiliary agent made of sodium chloride or potassium salt that lowers the contact resistance with the electrode and the electric resistance in the contaminated soil D may be added. In particular, when the pollutant is radioactive cesium, elution of cesium from the particle surface of the contaminated soil D is promoted by the substitution action of potassium and cesium. When the pollutant is a heavy metal, the use of an acid such as acetic acid or oxalic acid as the conductive auxiliary promotes the elution of the heavy metal pollutant. In the case where the pollutant is an amphoteric element or an amphoteric oxide that reacts with both an acid such as lead and an alkali, it is effective to add an alkaline agent as a conductive aid.

1 架台
2 フレコンバッグ
3 電源
4 電極棒
5 電極棒
6 濾液受け槽
7 保護カバー
8 吸着剤
9 サクションポンプ
10 ホース
11 マニホールド
12 網状電極
12a 導電性金属板
12b 保護材
12c 連結部材
12d 連結部材
12e アース線
14 ストレーナ電極
14a スリット
14b 吸着フィルター
15 ストレーナ電極
15a スリット
15b 吸着フィルター
17 保護カバー
17a 小孔
D 汚染土
D1 土中水分
L 濾液
DESCRIPTION OF SYMBOLS 1 Stand 2 Flexible container 3 Power supply 4 Electrode rod 5 Electrode rod 6 Filtrate receiving tank 7 Protective cover 8 Adsorbent 9 Suction pump 10 Hose 11 Manifold 12 Mesh electrode 12a Conductive metal plate 12b Protective material 12c Connection member 12d Connection member 12e Ground wire 14 Strainer electrode 14a Slit 14b Suction filter 15 Strainer electrode 15a Slit 15b Suction filter 17 Protective cover 17a Small hole D Contaminated soil D1 Soil moisture L Filtrate

Claims (5)

放射性物質や重金属などの汚染土並びに津波等による塩害を受けた土壌から有害な汚染物質や塩分を分離回収する汚染土の除染方法であって、
水分を含む汚染土を収容した透水性容器を宙づりにした状態で、この汚染土に相互に間隔を置いて差し込んだ正負両極の電極棒に電圧を印加し、電気分解により汚染物質をイオン化して汚染土粒子の表面に溶出させ、土壌中の汚染物を含有する土中水分を電気泳動及び電気浸透により電極棒周辺に集中させて汚染物質を除去すると共に、前記透水性容器の下方に土中水分を染み出させ脱水することを特徴とする汚染土の除染方法。
A decontamination method for contaminated soil that separates and collects harmful contaminants and salt from contaminated soil such as radioactive materials and heavy metals, and soil damaged by tsunami, etc.
In a state where a water-permeable container containing moisture is suspended, a voltage is applied to the positive and negative electrode rods inserted into the contaminated soil at intervals, and the contaminant is ionized by electrolysis. It elutes on the surface of the contaminated soil particles, removes the contaminants by concentrating the soil moisture containing the contaminants in the soil around the electrode rod by electrophoresis and electroosmosis, and in the soil below the permeable container A method for decontamination of contaminated soil, which exudes moisture and dehydrates it.
前記透水性容器はフレコンバッグであることを特徴とする請求項1に記載の汚染土の除染方法。   The method for decontamination of contaminated soil according to claim 1, wherein the water-permeable container is a flexible container bag. 前記電極棒は、側面に通水孔を備えたパイプ状のストレーナ電極であり、
前記ストレーナ電極に接続したホースを通じてストレーナ電極周辺に集中した土中水分をポンプにより吸い取って排出することを特徴とする請求項1又は2に記載の汚染土の除染方法。
The electrode rod is a pipe-shaped strainer electrode having a water passage hole on a side surface,
3. The method for decontamination of contaminated soil according to claim 1, wherein moisture in the soil concentrated around the strainer electrode is sucked and discharged by a pump through a hose connected to the strainer electrode.
前記ストレーナ電極に挿入されたフィルターにより土中水分から汚染物質を吸着することを特徴とする請求項3に記載の汚染土の除染方法。   The decontamination method for contaminated soil according to claim 3, wherein contaminants are adsorbed from moisture in the soil by a filter inserted in the strainer electrode. 前記透水性容器の側面に固定した網状電極と前記電極棒との間に電圧を印加して、透水性容器の側面周辺に土壌中の汚染物を含有する土中水分を集中させて、前記透水性容器の下方に染み出させ排出することを特徴とする請求項1ないし4のいずれかに記載の汚染土の除染方法。   Applying a voltage between the mesh electrode fixed to the side surface of the water permeable container and the electrode rod to concentrate water in the soil containing contaminants in the soil around the side surface of the water permeable container. 5. The method for decontaminating contaminated soil according to any one of claims 1 to 4, wherein the soil is squeezed out and discharged.
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