JP4024658B2 - Purification method and system for contamination by chemical substances - Google Patents

Purification method and system for contamination by chemical substances Download PDF

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JP4024658B2
JP4024658B2 JP2002338268A JP2002338268A JP4024658B2 JP 4024658 B2 JP4024658 B2 JP 4024658B2 JP 2002338268 A JP2002338268 A JP 2002338268A JP 2002338268 A JP2002338268 A JP 2002338268A JP 4024658 B2 JP4024658 B2 JP 4024658B2
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oxidant
groundwater
well
pumping
contaminated
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JP2004167426A (en
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正浩 江口
吉昭 長谷部
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Organo Corp
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Organo Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、化学物質、特に有機塩素化合物に汚染された土壌や底質、汚泥および地下水を含む汚染領域を、酸化剤を用いて浄化する方法およびシステムに関する。
【0002】
【従来の技術】
トリクロロエチレン(以下、TCEと略称することもある。)やテトラクロロエチレン(以下、PCEと略称することもある。)などの有機塩素化合物は、脱脂などの洗浄剤として、各種工場やクリーニング店等で広く使用されている。近年、これら有機塩素化合物による土壌や地下水の汚染が問題視されており、浄化対策が検討されつつある。これまで、一般的な浄化対策として、主に、封じ込め処理、汚染土壌の掘削・封じ込め処理、および揚水曝気や真空抽気、活性炭吸着処理などの組み合わせによる処理、等が行われてきた。
【0003】
しかし、このような浄化対策は、本質的に汚染物質を分解、無害化する処理ではないこと、これらの処理のみによる対策では莫大なエネルギーや手間を要すること、および、浄化期間が10〜20年と長いことから、より効率のよい安価な対策技術が要望されていた。また、上記のような浄化対策では、とくに揚水した汚染地下水を浄化することは可能であるものの、地下にあるいは地下水中に残っている汚染源に対しては積極的に除去処理を行わないので、この面からも浄化期間が著しく長引くという問題がある。
【0004】
このような問題点に対し、最近、酸化剤を直接井戸に注入し、汚染領域で酸化剤を直接反応させて積極的な浄化を行うようにした、原位置化学酸化手法の開発が進められつつある。たとえば、特許文献1には、重金属で汚染された土壌に、注入井から酸化剤溶液を注入して汚染土壌に接触させ、別に設けた揚水井から土壌と接触後の酸化剤溶液を揚水して回収する浄化方法が記載されている。また、特許文献2には、有害有機化合物で汚染された土壌または地下水を含む区域を区画し、その区画内に直接過硫酸塩を添加する浄化方法が記載されている。
【0005】
【特許文献1】
特開2002−96057号公報
【特許文献2】
特開2002−136961号公報
【0006】
【発明が解決しようとする課題】
ところが、上記特許文献2に記載の方法は、基本的に浄化用の過硫酸塩を所定の区画内に添加するだけであるから、回収処理は難しい。また、浄化すべき区域を矢板などで区画するようにしているので、そのための作業が必要になる。これに対し上記特許文献1に記載の方法では、注入井から注入した酸化剤溶液を揚水井から揚水するようにしているので、汚染物質の回収処理が可能になるという利点を有している。また、広い汚染領域に対しては、たとえば注入井の周囲に複数の揚水井を設けることにより、浄化範囲の拡大や浄化期間の短縮が可能になる。しかしながら、この方法においては、注入井と揚水井が必要であり、場合によっては複数の揚水井が必要となるので、掘削すべき井戸の数が多くなる。一つの井戸を掘削するにも相当の費用がかかることから、この方法の実施には大きな投資が要求される。したがって、少ない投資額で効率よく浄化したい場合や、浄化対象となる汚染領域が比較的狭い場合等に対しては、この方法は必ずしも適した方法とは言いがたい。
【0007】
そこで本発明の課題は、比較的小規模の汚染領域に対して、安価に、かつ簡単な方法にて、効率よく浄化することが可能な、化学物質による汚染の浄化方法および浄化システムを提供することにある。
【0008】
【課題を解決するための手段】
上記課題を解決するために、本発明に係る化学物質による汚染の浄化方法は、化学物質により汚染された地下水含有領域を酸化剤を用いて浄化する方法であって、汚染領域に設けられた井戸に酸化剤を注入し、該井戸から汚染領域に酸化剤を拡散させて汚染物質と反応させ、予め定められた一定期間経過後に、汚染領域に拡散され汚染物質と反応された酸化剤を地下水とともに同一の井戸へと引き込んで該同一の井戸からの揚水により回収することを特徴とする方法からなる。
【0009】
また、本発明に係る化学物質による汚染の浄化方法は、化学物質により汚染された地下水含有領域を酸化剤を用いて浄化する方法であって、汚染領域に設けられた井戸から揚水した地下水に酸化剤を添加し、酸化剤添加地下水を同一の井戸に注入し、該井戸から汚染領域に酸化剤を拡散させて汚染物質と反応させ、予め定められた一定期間経過後に、汚染領域に拡散され汚染物質と反応された酸化剤を地下水とともに同一の井戸へと引き込んで該同一の井戸からの揚水により回収することを特徴とする方法からなる。
【0010】
これら本発明に係る化学物質による汚染の浄化方法においては、酸化剤の注入または添加から、汚染領域に拡散され汚染物質と反応された酸化剤を地下水とともに同一の井戸へと引き込んで該同一の井戸から揚水するまでのステップを複数回繰り返すことも可能である。同じ汚染領域に対して浄化処理を複数回繰り返すことにより、汚染物質の濃度が段階的に順次低下され、最終的に問題のないレベルとすることができる。
【0011】
また、酸化剤としては、過マンガン酸カリウム、過酸化水素、過硫酸塩、次亜塩素酸、過塩素酸、塩素、オゾンなどの使用が可能であり、中でも、水への溶解性、操作性などの点から、過マンガン酸カリウム、過酸化水素、過硫酸塩の少なくとも一つを含んでいることが好ましい。とくに、汚染物質に対する安定した反応性や、周辺の水生生物等に対する影響度の低さなどの点から、過硫酸ナトリウム等の過硫酸塩の使用が好ましい。
【0012】
上記方法においては、揚水した酸化剤含有地下水に対し、還元処理、曝気処理、吸着処理の少なくとも一つの処理を施すことができる。このような処理を施すことにより、放流可能な水質にまで処理することが可能になる。
【0013】
本発明に係る化学物質による汚染の浄化システムは、上記のような化学物質による汚染の浄化方法を用いるシステムであって、汚染領域に設けられ、酸化剤または酸化剤添加地下水の注入用および酸化剤含有地下水の揚水用の両方に用いられる注入兼揚水井戸と、該井戸に酸化剤または酸化剤添加地下水を注入する手段および該井戸から酸化剤含有地下水を揚水する手段とを有することを特徴とするものからなる。
【0014】
このシステムにおいては、上記酸化剤注入手段は、注入兼揚水井戸に実質的に直接酸化剤を注入する手段から構成することもできるし、注入兼揚水井戸から揚水した地下水に酸化剤を添加し、酸化剤添加地下水を該井戸に注入する手段から構成することもできる。
【0015】
また、このシステムにおいても、酸化剤としては、過マンガン酸カリウム、過酸化水素、過硫酸塩の少なくとも一つを含んでいることが好ましく、中でも、過硫酸塩の使用が好ましい。
【0016】
さらに、上記酸化剤含有地下水揚水手段には、還元処理手段、曝気処理手段、吸着処理手段の少なくとも一つの処理手段を接続することができ、これら処理手段により、放流可能な水質にまで処理することが可能になる。
【0017】
このような本発明に係る化学物質による汚染の浄化方法および浄化システムにおいては、一つの同一の井戸から、酸化剤の注入と、所定期間経過後の酸化剤含有地下水の揚水との両方を行うので、前述の特許文献1に記載の技術のように、別途揚水井を設ける必要がない。すなわち、注入された酸化剤は井戸から汚染領域に拡散され、所定期間汚染領域の汚染物質と反応された後、地下水とともに同一の井戸へと引き込まれて揚水により回収される。したがって、この井戸周辺の汚染領域に対して、一つの井戸のみで原位置化学酸化処理を行うことが可能になり、極めて簡単に効率のよい浄化処理を行うことが可能になる。また、井戸設置費用は、深さにもよるが、1本約200万円程度かかるので、本発明では、従来の注入井と揚水井との複数の井戸を掘削する場合に比べ、大幅なコスト低減が可能となる。しかも、比較的小規模の汚染領域に対して、井戸を中心に拡散させた酸化剤を同一の井戸を中心に揚水回収するので、回収率も非常に高く保つことができ、かつ、酸化剤が不要に拡がってしまわないので(他の敷地に移行しないので)、安全性も極めて高い。その結果、汚染領域だけを、効率よく安価にしかも安全に浄化することが可能になる。
【0018】
【発明の実施の形態】
以下に、本発明の望ましい実施の形態について、図面を参照して説明する。
まず、汚染の原因となる化学物質に対する所定の酸化剤による浄化作用について確認した。トリクロロエチレン(TCE)やテトラクロロエチレン(PCE)などの有機塩素化合物に対し、過硫酸ナトリウムや過硫酸カリウム(ペルオキソ2硫酸カリウム)等の過硫酸塩により、常温で分解処理できることを確認した。これら酸化剤は、酸化剤による分解が比較的緩やかであり到達距離が長いので浄化範囲を広くとれる特徴があり、本発明における使用に非常に有効な酸化剤である。
【0019】
浄化作用の確認試験は、500mLのバイアルビンに、実汚染土壌20g、純水180mLを入れ、下記の条件になるように過硫酸ナトリウムを添加後(ブランクは、酸化剤の添加無し)、バイアルビンを密閉して処理を開始した。そして、経時的に各バイアルビンのヘッドスペースをガスクロマトグラフィーで測定することにより、浄化処理効果を評価した。
・ブランク(BL):酸化剤無添加
・テスト:過硫酸ナトリウムを500mg/Lの濃度になるように添加
【0020】
試験結果を図1に示す。過硫酸ナトリウムを添加したテストにおいては、TCEの分解が速やかに生じ、約1週間でごく低濃度にまで低減したのに対し、ブランクではTCEの分解が認められなかった。反応終了後の過硫酸濃度を測定した結果、100mg/L程度残留していることを確認した。
【0021】
このように、過硫酸塩により、常温で、有機塩素化合物を所定時間経過により浄化処理できることを確認できた。
【0022】
次に、実際の汚染領域に対し本発明を実施した場合の形態について説明する。
本発明においては、化学物質で汚染された土壌、底質、汚泥、地下水などを酸化剤を用いて浄化するに際し、浄化に必要な酸化剤濃度(たとえば、200〜5000mg/L)になるように調整した水(揚水処理済みの地下水、工業用水、水道水など)を井戸から浄化対象となる汚染領域に拡散するように一定時間注入し(たとえば、1日〜7日程度)、その後に分解に必要な反応時間(たとえば、1時間〜1ヵ月程度、好ましくは1日〜7日程度)をとった後に、注入したのと同一の井戸から注入したのと同じ量程度揚水する。好ましくは、このようなサイクルを複数回繰り返し行うことで、対象領域の汚染物質を浄化する。揚水した水がまだ有機塩素化合物を含んでいる場合には、曝気処理等を施し、酸化剤を補充し再注入する。浄化処理後、揚水した水に残留する酸化剤は、たとえば還元処理を施した後放流する。
【0023】
図2は、上記のような浄化処理を行うためのシステムの一実施態様を示している。化学物質により汚染された汚染領域1に、酸化剤の注入用および酸化剤含有地下水の揚水用の両方に用いられる注入兼揚水井戸2を設け、本実施態様では、注入兼揚水井戸2から適当に離れた位置に、浄化の効果を確認するためのモニタリング井3を設けた。ただし、このモニタリング井3は無くてもよい。この注入兼揚水井戸2に対し、該井戸2に酸化剤を注入する手段として、酸化剤調整槽4、該酸化剤調整槽4に酸化剤としての過硫酸ナトリウムを計量、投入する酸化剤添加装置5、酸化剤調整槽4内で所定の濃度に調整された酸化剤含有水を注入兼揚水井戸2に注入する注入ポンプ6とが設けられている。また、注入兼揚水井戸2から酸化剤含有地下水を揚水する手段として、井戸2内に配された揚水ポンプ7が設けられている。本実施態様ではさらに、揚水ラインには揚水ポンプ7により揚水された酸化剤含有地下水を曝気する曝気槽8が設けられており、エア供給装置9からエアが曝気槽8の底部に供給され、上部から排出される。曝気された水は、本実施態様では、酸化剤調整槽4に戻され、処理を繰り返す場合には、酸化剤が補充されて再び所定の濃度に調整された後注入兼揚水井戸2に注入される。浄化処理が終了すると、この酸化剤調整槽4に、還元剤添加装置10から還元剤が添加され、還元された後放流される。上記曝気槽8は、還元処理後の位置に配置してもよい。
【0024】
このようなシステムを用いて、汚染地下水を注入兼揚水井戸2から揚水し、曝気槽8で曝気処理後、その処理水に酸化剤調整槽4にて過硫酸ナトリウムを5000mg/Lになるように添加し、その酸化剤含有水を注入兼揚水井戸2に注入し汚染領域1に拡散させた。3日間反応後、同井戸2から再び揚水し、曝気処理を施すとともに、残留している酸化剤をチオ硫酸ナトリウムで還元後、放流した。また、上記浄化処理サイクルを2回繰り返し、同様に還元、曝気処理を施して放流した。モニタリング井3での確認の結果、図3に示すように、浄化処理前のモニタリング井3での地下水のTCE濃度が1.1mg/Lであったのに対し、上記本発明に係る浄化サイクルを1回施した場合には、TCE濃度が約0.5mg/Lまで低下し、2回目には、約0.1mg/Lまで低下した。したがって、本発明に係る浄化処理による顕著な効果を確認するとともに、繰り返し処理により、一層効果が上がることを確認できた。
【0025】
図4は、本発明の別の実施態様に係る、化学物質による汚染の浄化システムを示している。本実施態様では、化学物質により汚染された汚染領域11に、酸化剤の注入用および酸化剤含有地下水の揚水用の両方に用いられる注入兼揚水井戸12を設け、注入兼揚水井戸12から適当に離れた位置に、浄化の効果を確認するためのモニタリング井13を設けた。このモニタリング井13は無くてもよい。この注入兼揚水井戸12に対し、該井戸12に酸化剤を注入する手段として、市水18が導入される酸化剤調整槽14、該酸化剤調整槽14に酸化剤としての過硫酸ナトリウムを計量、投入する酸化剤添加装置15、酸化剤調整槽14内で所定の濃度に調整された酸化剤含有水を注入兼揚水井戸12に注入する注入ポンプ16とが設けられている。また、注入兼揚水井戸12から酸化剤含有地下水を揚水する手段として、井戸12内に配された揚水ポンプ17が設けられている。本実施態様ではさらに、揚水ポンプ17により酸化剤調整槽14に揚水された酸化剤含有地下水に、還元剤添加装置19から還元剤が添加され、活性炭吸着処理装置20で、残留している有機塩素化合物が吸着処理された後放流されるようになっている。このように構成されたシステムにおいても、実質的に図3に示したのと同等の効果が得られた。
【0026】
なお、本発明は、有機塩素化合物による汚染の浄化だけでなく、他の化学物質、たとえば、油、ベンゼン、トルエン、キシレンなどによる汚染の浄化にも適用可能である。
【0027】
【発明の効果】
以上説明したように、本発明に係る化学物質による汚染の浄化方法および浄化システムによれば、従来揚水曝気などを行っていた有機塩素化合物等の汚染物質の処理を、短期間のうちに簡単にかつ安全に浄化処理できるようになる。本発明は、とくに小規模の汚染領域を低コストで処理する場合に極めて有効である。また本発明は、従来曝気処理を行っていても浄化を終了できない汚染領域などの浄化促進に対しても極めて有効である。
【図面の簡単な説明】
【図1】酸化物による汚染の浄化効果を確認するために行った試験の結果を示すTCE濃度と時間との関係図である。
【図2】本発明の一実施態様に係る浄化システムの概略構成図である。
【図3】図2のシステムを用いて行った浄化処理結果を示すTCE濃度と処理回数との関係図である。
【図4】本発明の別の実施態様に係る浄化システムの概略構成図である。
【符号の説明】
1、11 汚染領域
2、12 注入兼揚水井戸
3、13 モニタリング井
4、14 酸化剤調整槽
5、15 酸化剤添加装置
6、16 注入ポンプ
7、17 揚水ポンプ
8 曝気槽
9 エア供給装置
10、19 還元剤添加装置
18 市水
20 活性炭吸着処理装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method and a system for purifying a contaminated area containing soil, sediment, sludge and groundwater contaminated with chemical substances, particularly organochlorine compounds, using an oxidizing agent.
[0002]
[Prior art]
Organochlorine compounds such as trichlorethylene (hereinafter sometimes abbreviated as TCE) and tetrachlorethylene (hereinafter also abbreviated as PCE) are widely used in various factories and cleaning stores as cleaning agents for degreasing. Has been. In recent years, contamination of soil and groundwater by these organochlorine compounds is regarded as a problem, and purification measures are being studied. Conventionally, as a general purification measure, mainly containment treatment, excavation / containment treatment of contaminated soil, treatment by a combination of pumping water aeration, vacuum extraction, activated carbon adsorption treatment, and the like have been performed.
[0003]
However, such purification measures are not essentially treatments for decomposing and detoxifying pollutants, the measures using only these treatments require enormous energy and labor, and the purification period is 10 to 20 years. Therefore, there has been a demand for more efficient and inexpensive countermeasure technology. In addition, although the above-mentioned purification measures can purify the contaminated groundwater that has been pumped in particular, it does not actively remove the contamination sources that remain underground or in the groundwater. There is also a problem that the purification period is significantly prolonged from the aspect.
[0004]
In response to these problems, in-situ chemical oxidation methods have recently been developed in which oxidants are directly injected into wells and oxidants are reacted directly in the contaminated area for active purification. is there. For example, in Patent Document 1, an oxidant solution is injected from an injection well into soil contaminated with heavy metals and brought into contact with the contaminated soil, and the oxidant solution after contact with the soil is pumped from a separate pumping well. The purification method to be recovered is described. Patent Document 2 describes a purification method in which an area containing soil or groundwater contaminated with a toxic organic compound is sectioned and persulfate is directly added to the section.
[0005]
[Patent Document 1]
JP 2002-96057 A [Patent Document 2]
JP-A-2002-136916 [0006]
[Problems to be solved by the invention]
However, since the method described in Patent Document 2 basically only adds a persulfate for purification into a predetermined compartment, the recovery process is difficult. Moreover, since the area to be purified is partitioned with a sheet pile or the like, work for that is required. On the other hand, the method described in Patent Document 1 has an advantage that the oxidant solution injected from the injection well is pumped from the pumping well, so that the contaminant can be recovered. Further, for a large contaminated area, for example, by providing a plurality of pumping wells around the injection well, the purification range can be expanded and the purification period can be shortened. However, in this method, an injection well and a pumping well are required, and in some cases, a plurality of pumping wells are required, so that the number of wells to be drilled is increased. Drilling a single well also costs a lot, so this method requires a large investment. Therefore, this method is not necessarily suitable for the case where it is desired to efficiently purify with a small investment amount or the case where the contaminated area to be purified is relatively narrow.
[0007]
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a chemical contamination purification method and a purification system capable of efficiently purifying a relatively small contaminated area at a low cost and with a simple method. There is.
[0008]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, a method for purifying contamination by a chemical substance according to the present invention is a method for purifying a groundwater-containing region contaminated by a chemical substance using an oxidizing agent, and a well provided in the contaminated region An oxidant is injected into the well and diffused from the well to the contaminated area to react with the pollutant. After a predetermined period of time, the oxidant diffused into the contaminated area and reacted with the pollutant together with the groundwater It consists of a method characterized in that it is drawn into the same well and recovered by pumping water from the same well .
[0009]
Further, the method for purifying contamination by a chemical substance according to the present invention is a method for purifying a groundwater-containing region contaminated by a chemical substance by using an oxidizing agent, and oxidizes the groundwater pumped from a well provided in the contaminated region. Add oxidant, inject oxidant-added groundwater into the same well, diffuse the oxidant from the well to the contaminated area and react with the pollutant. After a predetermined period of time, it diffuses into the contaminated area and becomes contaminated It comprises a method characterized in that the oxidant reacted with the substance is drawn together with groundwater into the same well and recovered by pumping from the same well .
[0010]
In the purification method for contamination by chemical substances according to the present invention, the oxidant diffused into the contaminated area and reacted with the pollutant is drawn into the same well together with the ground water from the injection or addition of the oxidant to the same well. It is also possible to repeat the steps from pumping up to pumping multiple times. By repeating the purification process for the same contaminated area a plurality of times, the concentration of the contaminant is lowered step by step, and finally it can be brought to a level with no problem.
[0011]
As oxidants, potassium permanganate, hydrogen peroxide, persulfate, hypochlorous acid, perchloric acid, chlorine, ozone, etc. can be used. In view of the above, it preferably contains at least one of potassium permanganate, hydrogen peroxide, and persulfate. In particular, it is preferable to use a persulfate such as sodium persulfate from the viewpoint of stable reactivity to pollutants and low influence on surrounding aquatic organisms.
[0012]
In the above method, at least one treatment of reduction treatment, aeration treatment, and adsorption treatment can be performed on the pumped ground water containing oxidant. By performing such a treatment, it is possible to treat the water quality so that it can be discharged.
[0013]
The system for purifying contamination by chemical substances according to the present invention is a system that uses the above-described method for purifying pollution by chemical substances , and is provided in a contaminated area for injecting oxidant or oxidant-added groundwater and oxidant. An injection / pumping well used for pumping both of the contained groundwater, means for injecting oxidant or oxidant-added groundwater into the well, and means for pumping oxidant-containing groundwater from the well Consists of things.
[0014]
In this system, the oxidant injecting means can be constituted by means for injecting an oxidant substantially directly into the injection / pumping well, or an oxidant is added to the groundwater pumped from the injection / pumping well, It can also comprise a means for injecting oxidant added groundwater into the well.
[0015]
Also in this system, it is preferable that the oxidizing agent contains at least one of potassium permanganate, hydrogen peroxide, and persulfate, and among these, the use of persulfate is preferable.
[0016]
Further, the oxidant-containing groundwater pumping means can be connected to at least one of a reduction processing means, an aeration processing means, and an adsorption processing means, and the processing means can treat the water quality to a dischargeable level. Is possible.
[0017]
In such a purification method and system for contamination by chemical substances according to the present invention, both injection of oxidant and pumping of oxidant-containing groundwater after a predetermined period of time are performed from one same well. There is no need to provide a separate pumping well as in the technique described in Patent Document 1 described above. That is, the injected oxidant is diffused from the well to the contaminated area, reacted with the pollutant in the contaminated area for a predetermined period, and then drawn into the same well together with the groundwater and recovered by pumping water. Therefore, it is possible to perform the in-situ chemical oxidation treatment with only one well on the contaminated area around the well, and it is possible to perform an efficient purification process very easily. In addition, although the well installation cost depends on the depth, it costs about 2 million yen, so in the present invention, the cost is much higher than the case of drilling a plurality of wells with conventional injection wells and pumping wells. Reduction is possible. Moreover, since the oxidant diffused around the well is pumped and recovered around the same well for a relatively small contaminated area, the recovery rate can be kept very high, and the oxidant is Since it does not spread unnecessarily (because it does not move to another site), it is extremely safe. As a result, only the contaminated area can be efficiently and inexpensively purified.
[0018]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
First, a purification action by a predetermined oxidant on a chemical substance that causes contamination was confirmed. It was confirmed that organic chlorine compounds such as trichlorethylene (TCE) and tetrachlorethylene (PCE) can be decomposed at room temperature with persulfates such as sodium persulfate and potassium persulfate (potassium peroxodisulfate). These oxidizing agents are characterized by a wide range of purification because they are relatively slowly decomposed and have a long reach, and are very effective oxidizing agents for use in the present invention.
[0019]
In the confirmation test of the purification action, 20 g of actual contaminated soil and 180 mL of pure water are placed in a 500 mL vial, and after adding sodium persulfate so that the following conditions are satisfied (blank is no oxidizer added), the vial Was sealed and the treatment was started. And the purification process effect was evaluated by measuring the head space of each vial bottle with time by gas chromatography.
・ Blank (BL): No oxidizer added ・ Test: Sodium persulfate added to a concentration of 500 mg / L [0020]
The test results are shown in FIG. In the test with sodium persulfate added, TCE degradation occurred rapidly and was reduced to a very low concentration in about 1 week, whereas no TCE degradation was observed in the blank. As a result of measuring the persulfuric acid concentration after completion of the reaction, it was confirmed that about 100 mg / L remained.
[0021]
Thus, it has been confirmed that perchlorate can purify an organic chlorine compound over a predetermined time at room temperature.
[0022]
Next, the form at the time of implementing this invention with respect to an actual contamination area | region is demonstrated.
In the present invention, when purifying soil, sediment, sludge, groundwater and the like contaminated with chemical substances using an oxidizing agent, the oxidizing agent concentration (for example, 200 to 5000 mg / L) necessary for the purification is obtained. Injected adjusted water (ground water that has been pumped, industrial water, tap water, etc.) for a certain period of time so that it diffuses from the well into the contaminated area to be purified (for example, about 1 to 7 days), and then decomposes After taking a necessary reaction time (for example, about 1 hour to 1 month, preferably about 1 day to 7 days), the water is pumped by the same amount as that injected from the same well. Preferably, the pollutant in the target region is purified by repeating such a cycle a plurality of times. If the pumped water still contains organochlorine compounds, perform aeration treatment, replenish the oxidant, and reinject. After the purification treatment, the oxidant remaining in the pumped water is discharged after, for example, a reduction treatment.
[0023]
FIG. 2 shows an embodiment of a system for performing the purification process as described above. An injection / pumping well 2 used for both injection of oxidant and pumping of oxidant-containing groundwater is provided in the contaminated area 1 contaminated with a chemical substance. In this embodiment, the injection / pumping well 2 is appropriately used. A monitoring well 3 was provided at a remote location to confirm the effect of purification. However, this monitoring well 3 may be omitted. As means for injecting an oxidant into the injection / pumping well 2, an oxidant adjusting tank 4, and an oxidant adding device for measuring and charging sodium persulfate as an oxidant into the oxidant adjusting tank 4 5. An injection pump 6 for injecting oxidant-containing water adjusted to a predetermined concentration in the oxidant adjusting tank 4 into the injection / pumping well 2 is provided. Further, as a means for pumping the oxidant-containing groundwater from the injection / pumping well 2, a pump 7 disposed in the well 2 is provided. In this embodiment, the pumping line is further provided with an aeration tank 8 for aeration of the oxidant-containing groundwater pumped by the pumping pump 7, and air is supplied from the air supply device 9 to the bottom of the aeration tank 8, Discharged from. In the present embodiment, the aerated water is returned to the oxidant adjustment tank 4, and when the process is repeated, the oxidant is replenished and adjusted again to a predetermined concentration and then injected into the injection / pumping well 2. The When the purification process is completed, a reducing agent is added to the oxidant adjusting tank 4 from the reducing agent addition device 10 and is reduced and discharged. The aeration tank 8 may be disposed at a position after the reduction process.
[0024]
Using such a system, the contaminated groundwater is pumped from the injection and pumping well 2, and after aeration treatment in the aeration tank 8, sodium persulfate is set to 5000 mg / L in the oxidant adjustment tank 4 in the treated water. The oxidant-containing water was added to the injection / pumping well 2 and diffused into the contaminated area 1. After reacting for 3 days, water was pumped up again from the well 2 and subjected to aeration treatment, and the remaining oxidizing agent was reduced with sodium thiosulfate and discharged. Moreover, the said purification process cycle was repeated twice and similarly reduced and aerated, and discharged. As a result of the confirmation in the monitoring well 3, as shown in FIG. 3, the TCE concentration of the groundwater in the monitoring well 3 before the purification treatment was 1.1 mg / L, whereas the purification cycle according to the present invention was performed. When applied once, the TCE concentration decreased to about 0.5 mg / L, and the second time decreased to about 0.1 mg / L. Therefore, while confirming the remarkable effect by the purification process which concerns on this invention, it has confirmed that the effect improved further by repeated process.
[0025]
FIG. 4 illustrates a chemical contamination purification system according to another embodiment of the present invention. In this embodiment, an injection / pumping well 12 used for both the injection of the oxidant and the pumping of the oxidant-containing groundwater is provided in the contaminated area 11 contaminated with the chemical substance. A monitoring well 13 for confirming the effect of purification was provided at a remote position. This monitoring well 13 may be omitted. As means for injecting an oxidant into the injection / pumping well 12, an oxidant adjustment tank 14 into which city water 18 is introduced, and sodium persulfate as an oxidant is measured in the oxidant adjustment tank 14. An oxidizer addition device 15 to be introduced, and an injection pump 16 for injecting the oxidant-containing water adjusted to a predetermined concentration in the oxidant adjustment tank 14 into the injection / pumping well 12 are provided. In addition, as a means for pumping the oxidant-containing groundwater from the injection / pumping well 12, a pumping pump 17 disposed in the well 12 is provided. In the present embodiment, the reducing agent is added from the reducing agent adding device 19 to the oxidizing agent-containing groundwater pumped to the oxidizing agent adjusting tank 14 by the pumping pump 17, and the remaining organic chlorine remains in the activated carbon adsorption treatment device 20. The compound is released after being adsorbed. Even in the system configured as described above, an effect substantially equivalent to that shown in FIG. 3 was obtained.
[0026]
The present invention can be applied not only to purification of contamination by organic chlorine compounds, but also to purification of contamination by other chemical substances such as oil, benzene, toluene, xylene and the like.
[0027]
【The invention's effect】
As described above, according to the purification method and system for contamination by chemical substances according to the present invention, it is possible to easily treat contaminants such as organic chlorine compounds that have been conventionally used for pumping aeration in a short period of time. And it becomes possible to clean up safely. The present invention is extremely effective particularly when a small contaminated area is treated at a low cost. In addition, the present invention is extremely effective in promoting purification of a contaminated area where purification cannot be completed even if conventional aeration processing is performed.
[Brief description of the drawings]
FIG. 1 is a graph showing the relationship between TCE concentration and time, showing the results of a test conducted to confirm the purification effect of oxide contamination.
FIG. 2 is a schematic configuration diagram of a purification system according to an embodiment of the present invention.
FIG. 3 is a relationship diagram between the TCE concentration and the number of treatments, showing the result of the purification treatment performed using the system of FIG.
FIG. 4 is a schematic configuration diagram of a purification system according to another embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1,11 Contamination area | region 2,12 Injection and pumping well 3,13 Monitoring well 4,14 Oxidant adjustment tank 5,15 Oxidant addition apparatus 6,16 Injection pump 7,17 Pumping pump 8 Aeration tank 9 Air supply apparatus 10, 19 Reducing agent addition device 18 City water 20 Activated carbon adsorption treatment device

Claims (7)

化学物質により汚染された地下水含有領域を酸化剤を用いて浄化する方法であって、汚染領域に設けられた井戸に酸化剤を注入し、該井戸から汚染領域に酸化剤を拡散させて汚染物質と反応させ、予め定められた一定期間経過後に、汚染領域に拡散され汚染物質と反応された酸化剤を地下水とともに同一の井戸へと引き込んで該同一の井戸からの揚水により回収することを特徴とする、化学物質による汚染の浄化方法。A method for purifying a groundwater-containing region contaminated with a chemical substance by using an oxidant, injecting an oxidant into a well provided in the contaminated region, and diffusing the oxidant from the well into the contaminated region. The oxidant diffused into the contaminated area and reacted with the pollutant after a predetermined period of time is drawn into the same well together with the groundwater and recovered by pumping from the same well. To clean up pollution caused by chemical substances. 化学物質により汚染された地下水含有領域を酸化剤を用いて浄化する方法であって、汚染領域に設けられた井戸から揚水した地下水に酸化剤を添加し、酸化剤添加地下水を同一の井戸に注入し、該井戸から汚染領域に酸化剤を拡散させて汚染物質と反応させ、予め定められた一定期間経過後に、汚染領域に拡散され汚染物質と反応された酸化剤を地下水とともに同一の井戸へと引き込んで該同一の井戸からの揚水により回収することを特徴とする、化学物質による汚染の浄化方法。A method for purifying groundwater-containing areas contaminated with chemical substances using an oxidizer, adding oxidizer to groundwater pumped from a well provided in the contaminated area, and injecting oxidizer-added groundwater into the same well The oxidant is diffused from the well into the contaminated area to react with the pollutant, and after a predetermined period of time, the oxidant diffused into the polluted area and reacted with the pollutant is returned to the same well together with the groundwater. A method for purifying contamination caused by chemical substances, wherein the method is drawn and collected by pumping water from the same well . 酸化剤の注入または添加から、汚染領域に拡散され汚染物質と反応された酸化剤を地下水とともに同一の井戸へと引き込んで該同一の井戸から揚水するまでのステップを複数回繰り返す、請求項1または2の化学物質による汚染の浄化方法。The process from injection or addition of an oxidant to drawing of the oxidant diffused into the contaminated area and reacted with the pollutant into the same well together with groundwater and pumped from the same well is repeated a plurality of times. 2. A method for purifying contamination caused by chemical substances. 酸化剤が、過マンガン酸カリウム、過酸化水素、過硫酸塩の少なくとも一つを含んでいる、請求項1〜3のいずれかに記載の化学物質による汚染の浄化方法。  The method for purifying contamination by chemical substances according to any one of claims 1 to 3, wherein the oxidizing agent contains at least one of potassium permanganate, hydrogen peroxide, and persulfate. 揚水した酸化剤含有地下水に対し、還元処理、曝気処理、吸着処理の少なくとも一つの処理を施す、請求項1〜4のいずれかに記載の化学物質による汚染の浄化方法。  The purification method of the contamination by the chemical substance in any one of Claims 1-4 which performs at least 1 process of a reduction process, an aeration process, and an adsorption process with respect to the oxidant containing groundwater pumped up. 請求項1〜5のいずれかに記載の化学物質による汚染の浄化方法を用いるシステムであって、汚染領域に設けられ、酸化剤または酸化剤添加地下水の注入用および酸化剤含有地下水の揚水用の両方に用いられる注入兼揚水井戸と、該井戸に酸化剤または酸化剤添加地下水を注入する手段および該井戸から酸化剤含有地下水を揚水する手段とを有することを特徴とする、化学物質による汚染の浄化システム。 A system using the method for purifying contamination by chemical substances according to any one of claims 1 to 5, wherein the system is provided in a contaminated area, for injecting oxidant or oxidant-added groundwater and for pumping oxidant-containing groundwater. It has an injection and pumping well used for both, means for injecting oxidant or oxidant-added groundwater into the well, and means for pumping oxidant-containing groundwater from the well, Purification system. 前記酸化剤含有地下水揚水手段に、還元処理手段、曝気処理手段、吸着処理手段の少なくとも一つの処理手段が接続されている、請求項に記載の化学物質による汚染の浄化システム。The system for purifying contamination by chemical substances according to claim 6 , wherein at least one of a reduction processing means, an aeration processing means, and an adsorption processing means is connected to the oxidant-containing groundwater pumping means.
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