JP2006130395A - Treatment apparatus of contaminated soil and treatment method of contaminated soil - Google Patents

Treatment apparatus of contaminated soil and treatment method of contaminated soil Download PDF

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JP2006130395A
JP2006130395A JP2004321003A JP2004321003A JP2006130395A JP 2006130395 A JP2006130395 A JP 2006130395A JP 2004321003 A JP2004321003 A JP 2004321003A JP 2004321003 A JP2004321003 A JP 2004321003A JP 2006130395 A JP2006130395 A JP 2006130395A
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contaminated soil
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organic chlorine
chlorine compound
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JP4519605B2 (en
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Satoshi Imamura
聡 今村
Hideya Nakajima
秀也 中島
Masanori Negishi
昌範 根岸
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Taisei Corp
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<P>PROBLEM TO BE SOLVED: To provide a treatment apparatus of contaminated soil capable of efficiently and certainly separating an organochlorine compound from contaminated soil to detoxify the same, and a treatment method of contaminated soil. <P>SOLUTION: The treatment apparatus 1 of the contaminated soil is constituted of a separator 2 for separating the organochlorine compound from contaminated soil and a detoxifying device 3 for detoxifying the separated organochlorine compound. In the separator 2, a surfactant or a solvent is mixed with a solution W1 or ultrasonic waves are generated to accelerate the separation of soil particles and the organochlorine compound. On the other hand , In the detoxifying device 3, ultrasonic waves are generated in the solution to accelerate the electrolysis of the organochlorine compound. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理装置および汚染土壌の処理方法に係り、特に、有機塩素化合物を効率的かつ確実に無害化することのできる汚染土壌の処理装置および汚染土壌の処理方法に関するものである。   The present invention relates to a contaminated soil treatment apparatus and a contaminated soil treatment method for separating and detoxifying organochlorine compounds such as polychlorinated biphenyl (PCB) contained in contaminated soil, and in particular, efficiently treating organochlorine compounds. The present invention also relates to a contaminated soil treatment apparatus and a contaminated soil treatment method that can be reliably rendered harmless.

土壌汚染対策法の施行(2003年2月)による特定施設廃止時の汚染調査の義務付けや、不動産鑑定基準の改定(2003年1月)により、土壌汚染が不動産価格決定の要因として加えられるなど、わが国においても土壌汚染や地下水汚染の問題が顕在化する傾向にある。土壌汚染や地下水汚染の原因となる物質は多様であるが、中でも、ジクロロメタンやTCEなどの揮発性有機塩素化合物、およびPCBやダイオキシンなどの有機塩素化合物の占める割合が高い現状である。   Soil pollution is added as a factor in determining real estate prices due to the obligation to conduct pollution surveys when certain facilities are abolished by the enforcement of the Soil Contamination Countermeasures Law (February 2003) and the revision of real estate appraisal standards (January 2003). In Japan, the problem of soil contamination and groundwater contamination tends to become apparent. There are a variety of substances that cause soil contamination and groundwater contamination. Among them, the ratio of volatile organic chlorine compounds such as dichloromethane and TCE, and organic chlorine compounds such as PCB and dioxin is high.

有機塩素化合物の一つであるPCBは、その絶縁性・化学的安定性から絶縁油・熱媒体等として広く使用されてきた物質である。昭和40年代に発生した環境汚染問題を契機にその毒性が明らかになり、昭和47年通産省令によりその製造と使用が禁止された。しかしながら、有効な処理方法が確立されず、その廃棄物は30年以上に及び保管され現在に至っている。平成13年「残留性有機汚染物質に関するストックホルム条約(POPs条約)」が採択され、既に我が国もこれに批准しているが、50カ国を超える批准を得て平成16年5月に至って発効している。この条約において、PCBは製造・使用禁止9物質のひとつとして指定されるとともに平成28年までの適正処理目標が設定されている。国内でも「PCB廃棄物特別措置法」が制定され、これらのPCBを平成28年までに処理することが定められた。現在、国は環境再生保全機構を活用した拠点的な広域処理施設の立地を進め、PCB廃棄物処理の事業化を推進している。   PCB, which is one of the organic chlorine compounds, is a substance that has been widely used as an insulating oil, a heat medium, and the like because of its insulating properties and chemical stability. Its toxicity became apparent in the wake of the environmental pollution problem that occurred in the Showa 40s, and its manufacture and use were prohibited by the Ordinance of the Ministry of International Trade and Industry in 1972. However, an effective treatment method has not been established, and the waste has been stored for more than 30 years. The “Stockholm Convention on Persistent Organic Pollutants (POPs Convention)” was adopted in 2001, and Japan has already ratified it, but it came into effect in May 2004 with over 50 countries ratified. Yes. Under this treaty, PCB is designated as one of the nine substances whose production and use are prohibited, and appropriate disposal targets are set up until 2016. In Japan, the “PCB Waste Special Measures Law” was enacted, and it was determined that these PCBs would be processed by 2016. Currently, the country is promoting the establishment of a regional wide-area treatment facility utilizing the Environmental Rehabilitation and Conservation Organization, and promoting the commercialization of PCB waste disposal.

一方、既に環境中へ放出されたPCBについて目を転じると、大気・水質などは恒常的なモニタリングと排出抑制が主な対策となるが、土壌(あるいは底質)に関しては積極的な浄化対策が望まれる。しかしながら、対象となる濃度範囲がCo−PCBのTEQ値換算で数pg/g程度の低濃度域に及ぶため、PCB原液と同様の処理ではコスト・エネルギーの両面で非効率であること、高温高圧あるいは特殊薬品使用を伴うため環境アセスメントの面から「廃PCB等処理基準」で制定された6技術、すなわち、(1)高熱焼却、(2)脱塩素化分解、(3)水熱酸化分解、(4)還元熱化学分解、(5)光分解、(6)プラズマ分解については、オンサイトでの適用は難しいのが現状である。土壌汚染の場合には、原液と同じ処理ではエネルギー面において極めて非効率であり、コストが高騰するといった問題がある。さらには、高温高圧を伴う技術では、副生成物の懸念や排ガスの発生などが考えられ、環境アセスメントの面から地方自治体の許認可や周辺住民の理解が得られ難いといった問題もある。   On the other hand, looking at PCBs that have already been released into the environment, air and water quality are the main measures for constant monitoring and emission control. However, for soil (or sediment), there are active purification measures. desired. However, since the target concentration range reaches a low concentration range of about several pg / g in terms of CoQPC TEQ value, the processing similar to the PCB stock solution is inefficient in terms of both cost and energy, high temperature and high pressure Or, because it involves the use of special chemicals, 6 technologies established in the “Processing Standards for Waste PCB, etc.” from the aspect of environmental assessment: (1) High-temperature incineration, (2) Dechlorination decomposition, (3) Hydrothermal oxidation decomposition, As for (4) reducing thermochemical decomposition, (5) photolysis, and (6) plasma decomposition, it is difficult to apply on-site. In the case of soil contamination, the same treatment as the stock solution is extremely inefficient in terms of energy, and there is a problem that costs increase. In addition, technologies involving high temperature and pressure may cause by-products or exhaust gas generation, and there are problems such as it being difficult to obtain local government approval and understanding from the surrounding residents in terms of environmental assessment.

上記の問題に対して特許文献1においては、PCBを電気分解することで無害化することのできるPCB処理装置およびPCB処理方法に関する発明が開示されている。   With respect to the above problem, Patent Document 1 discloses an invention relating to a PCB processing apparatus and a PCB processing method that can be rendered harmless by electrolyzing a PCB.

特開2002−345991号公報Japanese Patent Laid-Open No. 2002-349591

特許文献1に開示のPCB処理装置およびPCB処理方法によれば、常温下で汚染物質の分解を促進することができ、排ガスなどの二次汚染の懸念も払拭することができる。しかし、汚染土壌の処理に対応したものではなく、したがって汚染土壌からPCBを洗浄分離する工程と、電気分解を並行処理することによる超音波の機能減衰が起こること、および土粒子の存在が電流を遮断することによる電気分解の阻害要因と考えられ、したがってPCB無害化処理のエネルギー効率が大幅に低下するものと考えられる。   According to the PCB processing apparatus and the PCB processing method disclosed in Patent Document 1, it is possible to promote the decomposition of pollutants at room temperature, and to eliminate the concern of secondary contamination such as exhaust gas. However, it does not correspond to the treatment of contaminated soil. Therefore, the process of washing and separating PCB from the contaminated soil, the functional attenuation of ultrasonic waves by parallel processing of electrolysis, and the presence of soil particles It is considered that this is an inhibiting factor of electrolysis due to blocking, and therefore, it is considered that the energy efficiency of the PCB detoxification treatment is greatly reduced.

本発明の汚染土壌の処理装置および汚染土壌の処理方法は、上記する問題に鑑みてなされたものであり、有機塩素化合物の無害化処理の前段階として汚染土壌から有機塩素化合物を分離することにより、効率的かつ確実に有機塩素化合物を無害化することのできる汚染土壌の処理装置および汚染土壌の処理方法を提供することを目的としている。   The contaminated soil treatment apparatus and the contaminated soil treatment method of the present invention have been made in view of the above-described problems, and by separating the organic chlorine compound from the contaminated soil as a pre-stage of the detoxification treatment of the organic chlorine compound. An object of the present invention is to provide a contaminated soil treatment apparatus and a contaminated soil treatment method capable of detoxifying organochlorine compounds efficiently and reliably.

前記目的を達成すべく、本発明による汚染土壌の処理装置は、汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理装置であって、汚染土壌から有機塩素化合物を分離する分離装置と、分離された有機塩素化合物を無害化する無害化装置と、からなることを特徴とする。   In order to achieve the above object, a contaminated soil treatment apparatus according to the present invention is a contaminated soil treatment apparatus for separating and detoxifying organochlorine compounds such as polychlorinated biphenyl (PCB) contained in contaminated soil, It is characterized by comprising a separation device for separating an organic chlorine compound from contaminated soil and a detoxification device for detoxifying the separated organic chlorine compound.

本発明の無害化装置は、汚染された土壌に付着したPCBなどの有機塩素化合物を分離装置にて土粒子から分離させ、分離後のPCBを脱塩素化させることで無害化(PCBの場合は無害なビフェニルにする)を図るものである。   The detoxification device of the present invention is detoxified by separating organochlorine compounds such as PCB attached to contaminated soil from soil particles with a separation device and dechlorinating the separated PCB (in the case of PCB) To harmless biphenyl).

また、本発明による汚染土壌の処理装置の他の実施形態において、前記分離装置は、汚染土壌を含有する溶液を収容する容器と、撹拌部材と、溶液内に超音波を発生させる発振部材とを少なくとも備えており、溶液内で超音波を発生させながら撹拌部材で溶液を撹拌させ、該溶液のうち、有機塩素化合物を含有した上澄み液を前記無害化装置へ送り出すことを特徴とする。   In another embodiment of the contaminated soil treatment apparatus according to the present invention, the separation device includes a container that contains a solution containing the contaminated soil, a stirring member, and an oscillation member that generates ultrasonic waves in the solution. At least, the solution is stirred by a stirring member while generating ultrasonic waves in the solution, and a supernatant liquid containing an organic chlorine compound is sent out to the detoxifying device.

溶液内に超音波を発生させることにより、土粒子に付着した有機塩素化合物を土粒子から分離しやすくできる。超音波によって有機塩素化合物を土粒子から分離しやすい状態とした上で、溶液を撹拌させることで、土粒子と有機塩素化合物を完全(または、ほぼ完全)に分離することができる。撹拌後は所定時間残置させることで、有機塩素化合物が分離された土粒子は容器内に沈積し、難溶性の有機塩素化合物は上澄み液内を浮遊した状態となる。   By generating ultrasonic waves in the solution, the organic chlorine compound attached to the soil particles can be easily separated from the soil particles. By making the organic chlorine compound easy to separate from the soil particles by ultrasonic waves and stirring the solution, the soil particles and the organic chlorine compound can be completely (or almost completely) separated. By leaving the mixture for a predetermined time after stirring, the soil particles from which the organic chlorine compound has been separated are deposited in the container, and the sparingly soluble organic chlorine compound is suspended in the supernatant.

分離装置の実施形態として、例えば、容器内に鉛直方向の隔壁を設けておき、隔壁の一側側には先端にプロペラを備えた撹拌部材と発振部材を設置しておき、隔壁の他側側には水中ポンプを設置しておく。隔壁の一側側には予め水が入っており、土砂投入ホッパから汚染土壌を投入する。汚染土壌から有機塩素化合物を分離し、該有機塩素化合物が浮遊する上澄み液ができた段階で隔壁の上部から他側側へ上澄み液を流入させる。この上澄み液を水中ポンプでポンプアップしながら無害化装置へ送ることができる。   As an embodiment of the separation device, for example, a vertical partition is provided in the container, a stirring member and an oscillation member provided with a propeller at the tip are installed on one side of the partition, and the other side of the partition Has a submersible pump installed. Water is already contained on one side of the partition wall, and contaminated soil is introduced from the earth and sand introduction hopper. The organic chlorine compound is separated from the contaminated soil, and the supernatant liquid is allowed to flow from the upper part of the partition wall to the other side when the supernatant liquid in which the organic chlorine compound floats is formed. This supernatant liquid can be sent to the detoxifying device while being pumped up by a submersible pump.

なお、土砂投入ホッパから汚染土壌を投入するに際して、予め汚染土壌を振動ふるいなどでふるい分けしておき、最大粒径を極力小さくしておくことが望ましい。有機塩素化合物の無害化の方法として後述する電気分解をおこなう場合などにおいては、粒径が小さなほどその分解効率が高いからである。   In addition, when introducing contaminated soil from the earth and sand charging hopper, it is desirable to screen the contaminated soil with a vibration sieve or the like in advance and make the maximum particle size as small as possible. This is because, in the case of performing electrolysis, which will be described later, as a method for detoxifying an organic chlorine compound, the smaller the particle size, the higher the decomposition efficiency.

また、本発明による汚染土壌の処理装置の他の実施形態において、前記分離装置は、汚染土壌を含有する溶液を収容する容器と、撹拌部材と、界面活性剤または溶剤が混入された溶液とを少なくとも備えており、撹拌部材で溶液を撹拌させ、該溶液のうち、有機塩素化合物を含有した上澄み液を前記無害化装置へ送り出すことを特徴とする。   In another embodiment of the contaminated soil treatment apparatus according to the present invention, the separation apparatus includes a container that contains a solution containing the contaminated soil, a stirring member, and a solution mixed with a surfactant or a solvent. At least, the solution is stirred by a stirring member, and a supernatant liquid containing an organic chlorine compound is sent out to the detoxifying device.

界面活性剤を溶液に加えて撹拌することにより、有機塩素化合物を水中へ分散させやすくすることができる。また、溶剤を使用する場合には、例えば、n−ヘキサン、イソプロピルアルコール、メタノールなどの溶剤を使用できる。   By adding a surfactant to the solution and stirring, the organic chlorine compound can be easily dispersed in water. Moreover, when using a solvent, solvents, such as n-hexane, isopropyl alcohol, and methanol, can be used, for example.

また、本発明による汚染土壌の処理装置の他の実施形態において、前記無害化装置は、有機塩素化合物を含有する溶液を収容する容器と、有機塩素化合物を電気分解するための陽極および陰極を形成する電極部材とから少なくとも構成されることを特徴とする。   Further, in another embodiment of the contaminated soil treatment apparatus according to the present invention, the detoxification apparatus forms a container containing a solution containing an organic chlorine compound, and an anode and a cathode for electrolyzing the organic chlorine compound. And at least an electrode member.

分離装置にて土粒子と分離された有機塩素化合物を含有する溶液であるため、溶液に通電することで効率的に有機塩素化合物の電気分解が促進される。電気分解することにより、陰極には脱塩素化された無害のビフェニルが付着し、陽極には塩素イオンと水中のカルシウムやカリウムなどからなる塩化化合物が付着することとなる。   Since it is a solution containing the organic chlorine compound separated from the soil particles by the separator, electrolysis of the organic chlorine compound is efficiently promoted by energizing the solution. By electrolysis, the harmless biphenyl dechlorinated adheres to the cathode, and a chloride compound composed of chlorine ions and calcium or potassium in water adheres to the anode.

また、本発明による汚染土壌の処理装置の好ましい実施形態として、前記無害化装置は、さらに溶液内に超音波を発生させる発振部材を備えていることを特徴とする。   Moreover, as a preferred embodiment of the contaminated soil treatment apparatus according to the present invention, the detoxification apparatus further includes an oscillating member that generates ultrasonic waves in the solution.

溶液内に超音波を発生させることにより、例えばPCBを水中に乳化させて該PCBの電気分解を促進させることができる。また、超音波によって発生する気泡の崩壊時にキャビテーションが起こり、脱塩素化を補助するといった効果もある。   By generating ultrasonic waves in the solution, for example, PCB can be emulsified in water to promote electrolysis of the PCB. In addition, cavitation occurs when bubbles generated by ultrasonic waves collapse, and there is an effect of assisting dechlorination.

また、本発明による汚染土壌の処理装置の他の実施態様は、前記無害化装置内の無害化処理後の溶液を前記分離装置内の溶液として再利用可能としたことを特徴とする。   In another embodiment of the contaminated soil treatment apparatus according to the present invention, the solution after the detoxification treatment in the detoxification device can be reused as the solution in the separation device.

例えば、無害化装置を構成する容器内に、鉛直方向の半透膜からなる隔壁を設けておく。隔壁の一側側には陰極を形成する電極部材と発振部材を設置しておき、有機塩素化合物を含有する上澄み液を流入させる。一方、隔壁の他側側には陽極を形成する電極部材と水中ポンプを設置しておく。隔壁の他側側の水溶液は、有機塩素化合物を含有しておらず、したがって、この水溶液を水中ポンプにてポンプアップして分離装置を構成する容器内へ戻すことにより、水溶液を形成する水の再利用を図ることが可能となる。   For example, the partition which consists of a semipermeable membrane of a perpendicular direction is provided in the container which comprises a detoxification apparatus. An electrode member for forming a cathode and an oscillation member are installed on one side of the partition wall, and a supernatant liquid containing an organic chlorine compound is allowed to flow in. On the other hand, an electrode member for forming an anode and a submersible pump are installed on the other side of the partition wall. The aqueous solution on the other side of the partition wall does not contain an organic chlorine compound. Therefore, the aqueous solution is formed by pumping up this aqueous solution with a submersible pump and returning it to the container constituting the separation device. It can be reused.

また、本発明による汚染土壌の処理装置の他の実施形態は、有機塩素化合物が分離された分離装置内の土壌を、回収可能としたことを特徴とする。   Further, another embodiment of the contaminated soil treatment apparatus according to the present invention is characterized in that the soil in the separation apparatus from which the organochlorine compound has been separated can be recovered.

分離装置を構成する容器内に沈積する有機塩素化合物が分離された土砂を、例えば容器内に設置したサンドポンプにてポンプアップするなどして回収することにより、回収された土砂を別途工事の埋め戻し土などに有効利用することが可能となる。   The collected earth and sand is recovered by pumping up the earth and sand separated from the organic chlorine compounds deposited in the container that constitutes the separation device, for example, with a sand pump installed in the container. It can be effectively used for returning soil.

また、本発明による汚染土壌の処理方法は、汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理方法であって、容器内で汚染土壌と水を混合して溶液を形成し、該溶液内で超音波を発生させながら溶液を撹拌させる第一工程と、撹拌された溶液のうち、有機塩素化合物を含有した上澄み液を別途の容器に移し、該容器内に通電させることにより、有機塩素化合物の電気分解をおこなうことで脱塩素化を図る第二工程と、からなることを特徴とする。   In addition, the method for treating contaminated soil according to the present invention is a method for treating contaminated soil that separates and detoxifies organic chlorine compounds such as polychlorinated biphenyl (PCB) contained in the contaminated soil. And water are mixed to form a solution, and the solution is stirred while generating ultrasonic waves in the solution, and the supernatant solution containing the organochlorine compound in the stirred solution is put in a separate container. And a second step of dechlorination by electrolyzing the organic chlorine compound by energizing the container.

第一工程においては、溶液内に超音波を発生させることにより、土粒子に付着した有機塩素化合物を土粒子から分離しやすくできる。また、土粒子から分離された有機塩素化合物を電気分解することにより、電気分解に要する時間を短縮することが可能となる。   In the first step, it is possible to easily separate the organochlorine compound adhering to the soil particles from the soil particles by generating ultrasonic waves in the solution. In addition, by electrolyzing the organochlorine compound separated from the soil particles, it is possible to shorten the time required for electrolysis.

また、本発明による汚染土壌の処理方法の他の実施形態は、汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理方法であって、容器内で汚染土壌と水を混合して溶液を形成し、該溶液内に界面活性剤または溶剤を混入させ、該溶液を撹拌させる第一工程と、撹拌された溶液のうち、有機塩素化合物を含有した上澄み液を別途の容器に移し、該容器内に通電させることにより、有機塩素化合物の電気分解をおこなうことで脱塩素化を図る第二工程と、からなることを特徴とする。   Another embodiment of the method for treating contaminated soil according to the present invention is a method for treating contaminated soil that separates and detoxifies organic chlorine compounds such as polychlorinated biphenyl (PCB) contained in the contaminated soil, A contaminated soil and water are mixed in a container to form a solution, a surfactant or solvent is mixed in the solution, and the solution is stirred, and among the stirred solutions, an organochlorine compound is added. It is characterized by comprising a second step of dechlorination by transferring the contained supernatant to a separate container and energizing the container to electrolyze the organic chlorine compound.

既述するように、界面活性剤を溶液に加えて撹拌することにより、有機塩素化合物を水中へ分散させやすくすることができる。なお、上記する界面活性剤または溶剤を溶液中に混入させるとともに、該溶液に超音波を発生させながら撹拌することにより、土粒子からの有機塩素化合物の分離をより一層促進させることが可能となる。   As described above, the organic chlorine compound can be easily dispersed in water by adding the surfactant to the solution and stirring. In addition, it becomes possible to further promote the separation of the organic chlorine compound from the soil particles by mixing the above-described surfactant or solvent into the solution and stirring the solution while generating ultrasonic waves. .

さらに、本発明による汚染土壌の処理方法の他の実施形態は、前記第二工程において、前記容器内で超音波を発生させながら有機塩素化合物の電気分解をおこなうことを特徴とする。   Furthermore, another embodiment of the method for treating contaminated soil according to the present invention is characterized in that in the second step, the organic chlorine compound is electrolyzed while generating ultrasonic waves in the container.

第二工程において、超音波を発生させながら有機塩素化合物の電気分解をおこなうことにより、電気分解を促進させることが可能となる。   In the second step, electrolysis can be promoted by electrolyzing the organic chlorine compound while generating ultrasonic waves.

以上の説明から理解できるように、本発明の汚染土壌の処理装置および汚染土壌の処理方法によれば、常温下で汚染物質の分解を促進することができ、排ガスなどの二次汚染の懸念もないことから、施工中および施工後の安全性を確保することができる。したがって、工事に対する住民の理解も得られやすくなる。また、本発明の汚染土壌の処理装置および汚染土壌の処理方法によれば、有機塩素化合物を効率的かつ確実に汚染土壌から分離するとともに無害化することができる。   As can be understood from the above description, according to the contaminated soil treatment apparatus and the contaminated soil treatment method of the present invention, it is possible to promote the decomposition of pollutants at room temperature, and there is a concern about secondary pollution such as exhaust gas. Therefore, safety during and after construction can be ensured. Therefore, it becomes easier for residents to understand the construction. Moreover, according to the contaminated soil processing apparatus and the contaminated soil processing method of the present invention, the organochlorine compound can be separated from the contaminated soil efficiently and reliably and detoxified.

以下、図面を参照して本発明の実施の形態を説明する。図1は、本発明の汚染土壌の処理装置を示した模式図であり、図2は、実験結果を示したグラフである。なお、図示する実施形態では、無害化装置が有機塩素化合物を電気分解するものを示しているが、無害化装置はかかる実施形態に限定されるものではない。また、図中には分離装置に発振部材が設けてあるが、分離装置内の溶液に界面活性剤や溶剤が混入されている場合には発振部材が設けられていない実施形態であってもよい。   Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic view showing a contaminated soil treatment apparatus of the present invention, and FIG. 2 is a graph showing experimental results. In the illustrated embodiment, the detoxification device shows that the organic chlorine compound is electrolyzed, but the detoxification device is not limited to such an embodiment. Further, in the figure, the separating device is provided with the oscillating member, but in the case where a surfactant or solvent is mixed in the solution in the separating device, an embodiment in which the oscillating member is not provided may be used. .

図1は、汚染土壌の処理装置1を示している。汚染土壌の処理装置1は、分離装置2と無害化装置3とから主に構成されている。   FIG. 1 shows a treatment apparatus 1 for contaminated soil. The contaminated soil treatment device 1 is mainly composed of a separation device 2 and a detoxification device 3.

分離装置2は、容器21の内部に隔壁22が設けられている。隔壁22の一側側には、複数の発振部材4,4と撹拌部材5が設置されており、さらに界面活性剤または溶剤が水中に混入されてできた溶液W1が収容されている。溶液W1の中へ土砂投入ホッパ6を介して振動ふるいにかけられた後の汚染土壌を投入する(矢印X方向)。汚染土壌は水中で土粒子S,S,…に分散される。ここで、発振部材4,4の先端から超音波を発生させながら撹拌部材5を回転させ、その先端に装着された撹拌翼51で溶液W1を掻き混ぜる。   In the separation device 2, a partition wall 22 is provided inside the container 21. A plurality of oscillating members 4 and 4 and a stirring member 5 are installed on one side of the partition wall 22 and a solution W1 formed by mixing a surfactant or a solvent in water is accommodated. The contaminated soil that has been passed through the vibrating screen through the earth and sand injection hopper 6 is introduced into the solution W1 (arrow X direction). The contaminated soil is dispersed in the soil particles S, S,. Here, the stirring member 5 is rotated while generating ultrasonic waves from the tips of the oscillation members 4, 4, and the solution W <b> 1 is stirred with the stirring blade 51 attached to the tip.

水中に混入された界面活性剤(または溶剤)と超音波によって、土粒子Sに付着した有機塩素化合物Cを土粒子Sから分離しやすくできる。   The organic chlorine compound C adhering to the soil particles S can be easily separated from the soil particles S by the surfactant (or solvent) mixed in water and the ultrasonic waves.

溶液W1を撹拌翼51によって掻き混ぜた後、所定時間残置させておくことにより、溶液W1の上層に有機塩素化合物Cが浮遊する上澄み液W2が形成され、有機塩素化合物Cが分離された土粒子Sが容器21の底に沈積する。   After stirring the solution W1 with the stirring blade 51 and leaving it for a predetermined time, a supernatant liquid W2 in which the organic chlorine compound C floats is formed in the upper layer of the solution W1, and the soil particles from which the organic chlorine compound C has been separated are formed. S deposits on the bottom of the container 21.

隔壁22の上部に設けられた開口22aを開くことにより、上澄み液W2を隔壁22の他側側へ流入させる。隔壁22の他側側には水中ポンプ81が設置されており、水中ポンプ81に連通された配水管83が無害化装置3を構成する容器31内に通じている。隔壁22の他側側に貯められた上澄み液W2を水中ポンプ81でポンプアップすることにより、上澄み液W2を容器31に送り込む(矢印Y方向)。   By opening the opening 22 a provided in the upper part of the partition wall 22, the supernatant liquid W <b> 2 flows into the other side of the partition wall 22. A submersible pump 81 is installed on the other side of the partition wall 22, and a water distribution pipe 83 communicated with the submersible pump 81 leads into the container 31 constituting the detoxifying device 3. The supernatant liquid W2 stored on the other side of the partition wall 22 is pumped up by the submersible pump 81, whereby the supernatant liquid W2 is fed into the container 31 (in the arrow Y direction).

無害化装置3の容器31の内部には半透膜の隔壁32が設けられている。隔壁32の一側側には陰極を形成する電極部材71と撹拌部材5、発振部材4が設けられている。一方、隔壁32の他側側には陽極を形成する電極部材72が設けられており、電極部材71,72は電源に繋げられている。   A semipermeable membrane partition wall 32 is provided inside the container 31 of the detoxifying device 3. On one side of the partition wall 32, an electrode member 71 forming a cathode, a stirring member 5, and an oscillation member 4 are provided. On the other hand, an electrode member 72 for forming an anode is provided on the other side of the partition wall 32, and the electrode members 71 and 72 are connected to a power source.

容器31内に上澄み液W2が所定量貯まった段階で、溶液中に電流を流す。なお、通電の際には、溶液中に超音波を発生させるとともに撹拌部材5による撹拌をおこなう。通電によって溶液中に浮遊する有機塩素化合物Cは電気分解する。有機塩素化合物Cが例えばPCBの場合は、陰極において塩素イオンが離脱して水の電気分解により発生する水素イオンと置換して無害のビフェニルhとなる。一方、塩素イオンは半透膜の隔壁32を通過して陽極側に移動し、塩素化合物fとして沈殿または溶解する。この時、ビフェニルhは半透膜の隔壁32を通過できないため、PCBの再合成はおこなわれない。   When a predetermined amount of the supernatant liquid W2 is stored in the container 31, an electric current is passed through the solution. During energization, ultrasonic waves are generated in the solution and stirring by the stirring member 5 is performed. The organochlorine compound C floating in the solution by electrolysis is electrolyzed. When the organic chlorine compound C is, for example, PCB, chlorine ions are separated from the cathode and replaced with hydrogen ions generated by electrolysis of water to form harmless biphenyl h. On the other hand, the chlorine ions pass through the partition wall 32 of the semipermeable membrane, move to the anode side, and precipitate or dissolve as the chlorine compound f. At this time, since biphenyl h cannot pass through the partition wall 32 of the semipermeable membrane, resynthesis of PCB is not performed.

陽極まわりの溶液には有機塩素化合物Cおよび脱塩素処理された有機化合物は含まれておらず、この溶液(水)を次の汚染土壌の処理に再利用する場合には、設置された水中ポンプ81に連通する配水管84を介して容器21へ送り込むことができる(矢印Z方向)。   The solution around the anode does not contain organochlorine compound C and dechlorinated organic compound. When this solution (water) is reused for the next treatment of contaminated soil, the submersible pump installed It can be fed into the container 21 through a water distribution pipe 84 communicating with 81 (in the direction of arrow Z).

また、有機塩素化合物Cが分離されて容器21内に沈積した土粒子S,S,…からなる土砂は容器底に設置されたサンドポンプ82にてポンプアップし、排出管85を介して外部へ排出する(矢印T方向)。外部へ排出された土砂は有機塩素化合物が脱離されたものであり、したがって別途工事の埋め戻し土などとして再利用することもできる。   Further, the earth and sand composed of the soil particles S, S,... Separated from the organic chlorine compound C and deposited in the container 21 is pumped up by the sand pump 82 installed at the bottom of the container, and is discharged to the outside through the discharge pipe 85. Discharge (arrow T direction). The earth and sand discharged to the outside are the ones from which the organic chlorine compounds have been removed, and therefore can be reused as backfill soil for construction work.

以下に発明者等による実験概要と実験結果を示す。この実験は、泥水中のPCB濃度を、「排水基準を定める環境省令」に基づく排水基準(0.003mg/L)以下とするのに必要な処理時間を求めたものである。   The outline of the experiment by the inventors and the result of the experiment are shown below. In this experiment, the processing time required to set the PCB concentration in the muddy water to be equal to or lower than the wastewater standard (0.003 mg / L) based on the “Ministry of the Environment Ordinance for Establishing Wastewater Standard” was obtained.

使用した実験装置は、分離装置(前処理装置)と、無害化装置(超音波電気分解槽)から構成されており、大略構成は図1に示されている。分離装置は、50Lの水槽と、撹拌部材(撹拌機)および発振部材(超音波発生器)から構成されている。この超音波発生器は、超音波周波数を20000Hz、超音波出力を2000Wに調整されている。この分離装置により、汚染土壌からPCBを洗浄抽出することになる。   The experimental apparatus used is composed of a separation device (pretreatment device) and a detoxification device (ultrasonic electrolysis tank), and the general configuration is shown in FIG. The separation device includes a 50 L water tank, a stirring member (stirrer), and an oscillation member (ultrasonic generator). This ultrasonic generator is adjusted to an ultrasonic frequency of 20000 Hz and an ultrasonic output of 2000 W. With this separation device, PCB is washed and extracted from the contaminated soil.

一方、無害化装置は、50Lの水槽と、撹拌機と超音波発生器、電極と半透膜から構成されている。この超音波発生器は、超音波周波数を20000Hz、超音波出力を2000W、電気分解電圧を20V、電流を50Aに調整されている。この無害化装置により、分離装置によってPCBが抽出された後の上澄み液を脱塩素処理することになる。   On the other hand, the detoxification device is composed of a 50 L water tank, a stirrer, an ultrasonic generator, an electrode, and a semipermeable membrane. This ultrasonic generator is adjusted to an ultrasonic frequency of 20000 Hz, an ultrasonic output of 2000 W, an electrolysis voltage of 20 V, and a current of 50 A. By this detoxification device, the supernatant liquid after the PCB is extracted by the separation device is dechlorinated.

また、分離装置内にある水中ポンプは送水速度を9L/分に、無害化装置内にある水中ポンプは送水速度を10L/分にそれぞれ調整されており、一定水位を超えた無害化処理後の水が送水されることになっている。   The submersible pump in the separation device is adjusted to a water supply rate of 9 L / min, and the submersible pump in the detoxification device is adjusted to a water supply rate of 10 L / min. Water is to be sent.

処理対象の汚染土壌はPCB汚染土壌とし、PCB初期濃度が2000mg/kgで乾燥状態の土壌を使用する。また、この汚染土壌は分離装置に投入するに際して予めふるい分けされており、投入される土壌粒子の粒径は2mm以下に調整されている。   The contaminated soil to be treated is PCB-contaminated soil, and dry soil with an initial PCB concentration of 2000 mg / kg is used. In addition, this contaminated soil is screened in advance when it is introduced into the separation device, and the particle size of the introduced soil particles is adjusted to 2 mm or less.

水槽内の溶液は水道水を使用し、さらに電解質として苛性ソーダを添加している。本実験では、分離装置の水槽と無害化装置の水槽の双方にそれぞれ40Lの水道水を満たしておき、さらに、双方の水槽に160gの苛性ソーダを添加している。   The solution in the water tank uses tap water, and caustic soda is added as an electrolyte. In this experiment, 40 L of tap water is filled in both the water tank of the separation device and the water tank of the detoxification device, and 160 g of caustic soda is added to both water tanks.

実験方法は、まず、分離装置にPCB汚染土壌を600g投入し、分離装置および無害化装置の撹拌機や超音波発生器を作動させ、無害化装置においては、さらに電極間の通電をおこなう。分離装置および無害化装置のそれぞれの水中ポンプも同時に作動させ、汚染土壌の処理装置内において洗浄水(処理後の水)の循環を図る。実験は30分ごとに分離装置内の泥水をサンプリングし、泥水中のPCB濃度の測定をおこなった。   In the experiment method, first, 600 g of PCB-contaminated soil is put into the separation device, the stirrer and the ultrasonic generator of the separation device and the detoxification device are operated, and the detoxification device further energizes between the electrodes. The submersible pumps of the separation device and the detoxification device are simultaneously operated to circulate cleaning water (treated water) in the contaminated soil treatment device. In the experiment, the muddy water in the separation apparatus was sampled every 30 minutes, and the PCB concentration in the muddy water was measured.

ここで、PCB濃度の分析方法は、まず、泥水100gをサンプリングし、サンプリング試料にn−ヘキサン200ccを添加し、10分の振とう処理を3セット実施した。この振とう処理後の試料を、ガスクロマトグラフ質量分析器(GC/MS)で測定し、試料中のPCB濃度を測定した。   Here, as a method for analyzing PCB concentration, first, 100 g of muddy water was sampled, 200 cc of n-hexane was added to the sampling sample, and three sets of shaking treatment for 10 minutes were performed. The sample after the shaking treatment was measured with a gas chromatograph mass spectrometer (GC / MS), and the PCB concentration in the sample was measured.

実験結果を、表1および図2に示している。   The experimental results are shown in Table 1 and FIG.

Figure 2006130395
Figure 2006130395

表1および図2からも分かるように、本発明の分離装置(前処理装置)と無害化装置から構成される処理装置によれば、排水基準(0.003mg/L)をはるかに上回るPCB汚染土壌であっても、わずか4時間程度で排水基準以下とすることが可能となる。   As can be seen from Table 1 and FIG. 2, according to the treatment apparatus composed of the separation apparatus (pretreatment apparatus) and the detoxification apparatus of the present invention, the PCB contamination far exceeds the drainage standard (0.003 mg / L). Even in soil, it can be reduced to below the drainage standard in about 4 hours.

以上、本発明の実施の形態を図面を用いて詳述してきたが、具体的な構成はこの実施形態に限定されるものではなく、本発明の要旨を逸脱しない範囲における設計変更等があっても、それらは本発明に含まれるものである。   The embodiment of the present invention has been described in detail with reference to the drawings. However, the specific configuration is not limited to this embodiment, and there are design changes and the like without departing from the gist of the present invention. They are also included in the present invention.

本発明の汚染土壌の処理装置を示した模式図。The schematic diagram which showed the processing apparatus of the contaminated soil of this invention. 実験結果を示すグラフ。The graph which shows an experimental result.

符号の説明Explanation of symbols

1…汚染土壌の処理装置、2…分離装置、3…無害化装置、4…発振部材、5…撹拌部材、6…土砂投入ホッパ、21,31…容器、22,32…隔壁、71,72…電極部材、W1…溶液、W2…上澄み液 DESCRIPTION OF SYMBOLS 1 ... Contaminated soil processing apparatus, 2 ... Separation apparatus, 3 ... Detoxification apparatus, 4 ... Oscillation member, 5 ... Stirring member, 6 ... Sediment injection hopper, 21, 31 ... Container, 22, 32 ... Septum, 71, 72 ... Electrode member, W1 ... Solution, W2 ... Supernatant

Claims (10)

汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理装置であって、
前記汚染土壌の処理装置は、汚染土壌から有機塩素化合物を分離する分離装置と、分離された有機塩素化合物を無害化する無害化装置と、からなることを特徴とする汚染土壌の処理装置。
An apparatus for treating contaminated soil for separating and detoxifying organochlorine compounds such as polychlorinated biphenyl (PCB) contained in contaminated soil,
The contaminated soil treatment apparatus comprises a separation apparatus for separating an organic chlorine compound from the contaminated soil and a detoxification apparatus for detoxifying the separated organic chlorine compound.
前記分離装置は、汚染土壌を含有する溶液を収容する容器と、撹拌部材と、溶液内に超音波を発生させる発振部材とを少なくとも備えており、溶液内で超音波を発生させながら撹拌部材で溶液を撹拌させ、該溶液のうち、有機塩素化合物を含有した上澄み液を前記無害化装置へ送り出すことを特徴とする請求項1に記載の汚染土壌の処理装置。   The separation device includes at least a container that contains a solution containing contaminated soil, a stirring member, and an oscillation member that generates ultrasonic waves in the solution, and the stirring member generates ultrasonic waves in the solution. The contaminated soil treatment apparatus according to claim 1, wherein the solution is stirred, and a supernatant liquid containing an organic chlorine compound is sent out to the detoxification device. 前記分離装置は、汚染土壌を含有する溶液を収容する容器と、撹拌部材と、界面活性剤または溶剤が混入された溶液とを少なくとも備えており、撹拌部材で溶液を撹拌させ、該溶液のうち、有機塩素化合物を含有した上澄み液を前記無害化装置へ送り出すことを特徴とする請求項1に記載の汚染土壌の処理装置。   The separation device includes at least a container for storing a solution containing contaminated soil, a stirring member, and a solution mixed with a surfactant or a solvent. The stirring member is used to stir the solution, and the The processing apparatus of contaminated soil of Claim 1 which sends out the supernatant liquid containing an organic chlorine compound to the said detoxification apparatus. 前記無害化装置は、有機塩素化合物を含有する溶液を収容する容器と、有機塩素化合物を電気分解するための陽極および陰極を形成する電極部材とから少なくとも構成されることを特徴とする請求項1〜3のいずれかに記載の汚染土壌の処理装置。   2. The detoxification device comprises at least a container for storing a solution containing an organic chlorine compound and an electrode member for forming an anode and a cathode for electrolyzing the organic chlorine compound. The processing apparatus of the contaminated soil in any one of -3. 前記無害化装置は、さらに溶液内に超音波を発生させる発振部材を備えていることを特徴とする請求項4に記載の汚染土壌の処理装置。   The contaminated soil treatment apparatus according to claim 4, wherein the detoxification device further includes an oscillation member that generates ultrasonic waves in the solution. 前記無害化装置内の無害化処理後の溶液を前記分離装置内の溶液として再利用可能としたことを特徴とする請求項1〜5のいずれかに記載の汚染土壌の処理装置。   The contaminated soil treatment device according to any one of claims 1 to 5, wherein the solution after the detoxification treatment in the detoxification device can be reused as a solution in the separation device. 有機塩素化合物が分離された分離装置内の土壌を、回収可能としたことを特徴とする請求項1〜6のいずれかに記載の汚染土壌の処理装置。   The contaminated soil treatment apparatus according to any one of claims 1 to 6, wherein the soil in the separation apparatus from which the organic chlorine compound has been separated can be collected. 汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理方法であって、
容器内で汚染土壌と水を混合して溶液を形成し、該溶液内で超音波を発生させながら溶液を撹拌させる第一工程と、撹拌された溶液のうち、有機塩素化合物を含有した上澄み液を別途の容器に移し、該容器内に通電させることにより、有機塩素化合物の電気分解をおこなうことで脱塩素化を図る第二工程と、からなることを特徴とする汚染土壌の処理方法。
A method for treating contaminated soil that separates and detoxifies organochlorine compounds such as polychlorinated biphenyl (PCB) contained in contaminated soil,
A first step of mixing a contaminated soil and water in a container to form a solution, stirring the solution while generating ultrasonic waves in the solution, and a supernatant liquid containing an organochlorine compound among the stirred solutions And a second step of dechlorination by electrolyzing the organic chlorine compound by transferring the water to a separate container and energizing the container.
汚染土壌に含まれるポリ塩化ビフェニル(PCB)などの有機塩素化合物を分離し、かつ無害化する汚染土壌の処理方法であって、
容器内で汚染土壌と水を混合して溶液を形成し、該溶液内に界面活性剤または溶剤を混入させ、該溶液を撹拌させる第一工程と、撹拌された溶液のうち、有機塩素化合物を含有した上澄み液を別途の容器に移し、該容器内に通電させることにより、有機塩素化合物の電気分解をおこなうことで脱塩素化を図る第二工程と、からなることを特徴とする汚染土壌の処理方法。
A method for treating contaminated soil that separates and detoxifies organochlorine compounds such as polychlorinated biphenyl (PCB) contained in contaminated soil,
In the container, contaminated soil and water are mixed to form a solution, a surfactant or solvent is mixed in the solution, and the solution is stirred, and among the stirred solutions, an organochlorine compound is added. Transferring the contained supernatant to a separate container and energizing the container to conduct dechlorination by electrolyzing the organochlorine compound, and a contaminated soil comprising Processing method.
前記第二工程において、前記容器内で超音波を発生させながら有機塩素化合物の電気分解をおこなうことを特徴とする請求項8または9に記載の汚染土壌の処理方法。   The method for treating contaminated soil according to claim 8 or 9, wherein in the second step, the organic chlorine compound is electrolyzed while generating ultrasonic waves in the container.
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