JP2000210683A - Soil and / or groundwater purification method - Google Patents

Soil and / or groundwater purification method

Info

Publication number
JP2000210683A
JP2000210683A JP11014552A JP1455299A JP2000210683A JP 2000210683 A JP2000210683 A JP 2000210683A JP 11014552 A JP11014552 A JP 11014552A JP 1455299 A JP1455299 A JP 1455299A JP 2000210683 A JP2000210683 A JP 2000210683A
Authority
JP
Japan
Prior art keywords
soil
hydrogen peroxide
groundwater
added
permanganate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11014552A
Other languages
Japanese (ja)
Inventor
Hiroshi Matsutani
浩 松谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP11014552A priority Critical patent/JP2000210683A/en
Publication of JP2000210683A publication Critical patent/JP2000210683A/en
Pending legal-status Critical Current

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Removal Of Specific Substances (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

(57)【要約】 【課題】 有機塩素化合物で汚染された土壌及び/又は
地下水中の有機塩素化合物を効率的に分解処理する。 【解決手段】 有機塩素化合物で汚染された土壌及び/
又は地下水に、二価の鉄イオンの存在下に過酸化水素を
添加し、次いで過マンガン酸塩を添加する。
(57) [PROBLEMS] To efficiently decompose organic chlorine compounds in soil and / or groundwater contaminated with organic chlorine compounds. SOLUTION: The soil contaminated with an organochlorine compound and / or
Alternatively, hydrogen peroxide is added to groundwater in the presence of divalent iron ions, and then permanganate is added.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、有機塩素化合物で
汚染された土壌及び/又は地下水中の有機塩素化合物を
効率的に分解処理する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for efficiently decomposing organochlorine compounds in soil and / or groundwater contaminated with organochlorine compounds.

【0002】[0002]

【従来の技術】有機塩素化合物は、優れた溶解力を有す
る溶剤として使用されてきたが、近年その発癌性が指摘
され、環境への放出が制限されている。しかし、有機塩
素化合物による汚染は依然として解決されておらず、ト
リクロロエチレンやテトラクロロエチレン等の有機塩素
化合物による土壌や地下水の汚染が大きな社会問題とな
っている。
2. Description of the Related Art Organochlorine compounds have been used as solvents having excellent dissolving power, but their carcinogenicity has recently been pointed out, and their release into the environment has been restricted. However, contamination by organic chlorine compounds has not been solved yet, and soil and groundwater contamination by organic chlorine compounds such as trichloroethylene and tetrachloroethylene has become a major social problem.

【0003】有機塩素化合物は比較的揮発しやすく、水
に溶解し難い性質を有する。そこで、この性質を利用し
て、有機塩素化合物で汚染された土壌及び/又は地下水
の処理法として、土壌からブロア等により吸引する真空
抽出或いは地下水を一旦揚水してからエアーストリッピ
ング(曝気処理)し、活性炭等の吸着剤で回収して廃棄
物として処理する方法が行われている。
[0003] Organochlorine compounds are relatively volatile and hardly soluble in water. Therefore, utilizing this property, as a method for treating soil and / or groundwater contaminated with organochlorine compounds, vacuum extraction by suction from the soil with a blower or the like, or once groundwater is pumped and then air stripping (aeration treatment). Then, a method of collecting the waste with an adsorbent such as activated carbon and treating it as waste has been performed.

【0004】しかし、活性炭吸着による方法は、汚染物
質を回収、再利用しない限り、単に汚染物質を移行させ
るのみで、根本的な解決にはなっていない。また、これ
を焼却処分する場合、十分な温度管理を行わないと有毒
なダイオキシンを生成する可能性がある。このために、
有機塩素化合物を焼却以外の方法で分解して無害化する
方法に関する研究が、これまで積極的に行われ、例え
ば、紫外線のエネルギーを利用して分解する方法とし
て、有機ハロゲン化合物を含む排ガスを紫外線照射処理
して酸性の分解ガスとした後、アルカリで洗浄して無害
化処理する方法などが提案されている。
[0004] However, the method based on activated carbon adsorption merely transfers the contaminants unless the contaminants are recovered and reused, and has not been a fundamental solution. In addition, when this is incinerated, toxic dioxins may be produced unless sufficient temperature control is performed. For this,
Research on methods of decomposing organic chlorine compounds by methods other than incineration to make them harmless has been actively conducted.For example, as a method of decomposing using the energy of ultraviolet rays, an exhaust gas containing an organic halogen compound is irradiated with ultraviolet rays. A method has been proposed in which irradiation treatment is performed to form an acidic decomposed gas, followed by washing with alkali and detoxification treatment.

【0005】しかし、これらの方法はいずれも土壌中の
汚染物質を一旦真空抽出法や揚水・曝気法により土壌や
地下水中から除去してから処理を行うものであるため、
この真空抽出や揚水・曝気のために多大な処理コストが
かかる上に、これらの方法では浄化後期になると十分に
汚染物質を除去しきれなくなり、浄化効率は低下する。
従って、このような方法を取り続ける限り、汚染土壌或
いはその付近の地下水には低濃度の有機塩素化合物によ
る汚染が継続することになる。このような低濃度の有機
塩素化合物による汚染、例えば、トリクロロエチレンで
あれば汚染濃度が環境基準値である30μg/Lから1
000μg/L程度の汚染に対しては、実用的な見地か
ら有効な浄化手法は提案されていない。
[0005] However, in these methods, the treatment is performed after the pollutants in the soil are once removed from the soil or groundwater by a vacuum extraction method or a pumping / aeration method.
A great deal of processing cost is required for the vacuum extraction, water pumping and aeration, and in these methods, pollutants cannot be sufficiently removed in the later stage of purification, and purification efficiency is reduced.
Therefore, as long as such a method is continued, the contamination of the contaminated soil or the groundwater in the vicinity thereof with the low concentration of the organic chlorine compound will be continued. Contamination by such a low concentration of an organic chlorine compound, for example, in the case of trichlorethylene, the concentration of the contamination is reduced from the environmental standard value of 30 μg / L to 1
For a contamination of about 000 μg / L, no effective purification method has been proposed from a practical viewpoint.

【0006】また、一般に汚染土壌は、各種工場の敷地
内における稼動中の設備周辺や建築物の直下である場合
が多く、従って、このような汚染土壌を処理する場合に
は、汚染土壌を現場にて、即ち原位置で浄化処理するこ
とができ、処理後、残留する薬剤による弊害のない処理
方法が強く望まれている。
[0006] In general, the contaminated soil is often in the vicinity of operating facilities or immediately below buildings in the premises of various factories. Therefore, when such contaminated soil is treated, the contaminated soil is often removed from the site. In other words, there is a strong demand for a treatment method that can perform a purification treatment in situ and has no harmful effects due to residual chemicals after treatment.

【0007】[0007]

【発明が解決しようとする課題】そこで、上記方法とは
別に、汚染土壌に過酸化水素を直接注入してトリクロロ
エチレン等の汚染物質を分解する方法も提案されてい
る。また、有機塩素化合物が過マンガン酸塩により分解
除去できることも知られている。
Therefore, in addition to the above method, a method has been proposed in which hydrogen peroxide is directly injected into contaminated soil to decompose pollutants such as trichloroethylene. It is also known that organochlorine compounds can be decomposed and removed by permanganate.

【0008】こうした処理方法であれば、原位置での浄
化処理が可能で、処理後の残留薬剤による弊害の問題も
ない。
[0008] According to such a processing method, the in-situ purification processing can be performed, and there is no problem of adverse effects due to residual chemicals after the processing.

【0009】過酸化水素は二価の鉄イオンの存在下でラ
ジカルを発生して有機塩素化合物を急速に分解するが、
土壌や地下水中の物質との反応や土壌表面で分解されや
すく、本来の目的である有機塩素化合物の分解以外に無
駄に消費される割合が高い。
[0009] Hydrogen peroxide generates radicals in the presence of divalent iron ions and rapidly decomposes organic chlorine compounds.
It easily reacts with substances in soil and groundwater and is easily decomposed on the surface of the soil.

【0010】また、過マンガン酸塩は過酸化水素に比べ
て土壌による分解速度が小さいので、土壌表面で分解さ
れて無駄に消費される割合が比較的小さく、処理の影響
範囲を広く取ることができる点で優れているが、二価の
鉄イオンのような還元性物質との反応により無駄に消費
される。即ち、過酸化水素、過マンガン酸塩をそれぞれ
単独で用いた場合、これらは土壌表面で分解されたり還
元性物質と反応するなどして多くが無駄に消費され、処
理効率が悪くなるという問題があった。
[0010] Further, since permanganate is decomposed by soil at a lower rate than hydrogen peroxide, the rate of decomposition on the soil surface and wastefully consumed is relatively small, so that the range of influence of the treatment can be widened. It is excellent in that it can be used, but is wasted by the reaction with a reducing substance such as divalent iron ions. That is, when hydrogen peroxide and permanganate are used alone, a large amount of these are decomposed on the soil surface or reacted with a reducing substance, so that many of them are wasted and the processing efficiency is deteriorated. there were.

【0011】本発明は上記従来の問題点を解決し、有機
塩素化合物で汚染された土壌及び/又は地下水中の有機
塩素化合物を効率的に処理することができる土壌及び/
又は地下水の浄化方法を提供することを目的とする。
The present invention solves the above-mentioned conventional problems, and provides a soil and / or soil which can efficiently treat an organic chlorine compound in soil contaminated with the organic chlorine compound and / or groundwater.
Alternatively, an object of the present invention is to provide a method for purifying groundwater.

【0012】[0012]

【課題を解決するための手段】そこで、本発明者らは、
土壌や地下水中の代表的な還元性物質である二価の鉄イ
オンに着目し、これを過酸化水素の作用により三価に酸
化すると同時に汚染物質を分解し、その後、更に過マン
ガン酸塩を加えることで、これらを無駄に消費すること
なく、残存する汚染物質を完全に分解できることを見出
し、本発明を完成させた。
Means for Solving the Problems Accordingly, the present inventors have:
Focusing on divalent iron ion, a typical reducing substance in soil and groundwater, oxidizes this to trivalent by the action of hydrogen peroxide and simultaneously decomposes contaminants. By adding these, it was found that the remaining contaminants could be completely decomposed without wasting them, and the present invention was completed.

【0013】即ち、本発明は、有機塩素化合物で汚染さ
れた土壌及び/又は地下水に、二価の鉄イオンの存在下
に過酸化水素を添加し、次いで過マンガン酸塩を添加す
ることを特徴とする。
That is, the present invention is characterized in that hydrogen peroxide is added to soil and / or groundwater contaminated with an organochlorine compound in the presence of divalent iron ions, and then permanganate is added. And

【0014】本発明における有機塩素化合物の分解機構
は次の通りである。
The decomposition mechanism of the organic chlorine compound in the present invention is as follows.

【0015】先に添加された過酸化水素は、二価の鉄イ
オンが存在する条件では、次のように還元されてヒドロ
キシラジカルを生成する。
The previously added hydrogen peroxide is reduced as follows under the condition that divalent iron ions are present to generate a hydroxyl radical.

【0016】H22+Fe2+→OH・+OH-+Fe3+ このラジカル種は非常に反応性に富み、殆どすべての有
機物を酸化分解できる(フェントン反応)。このとき、
二価の鉄イオンは三価イオンに酸化される。従って、二
価の鉄イオンが存在する条件で過酸化水素を添加すると
二価の鉄イオンが三価まで酸化されると共に、同時に有
機塩素化合物が分解される。例えば、トリクロロエチレ
ン(TCE)であれば、次のように分解される。
H 2 O 2 + Fe 2+ → OH. + OH + Fe 3+ These radical species are very reactive and can oxidatively decompose almost all organic substances (Fenton reaction). At this time,
Divalent iron ions are oxidized to trivalent ions. Therefore, when hydrogen peroxide is added under the condition that divalent iron ions are present, the divalent iron ions are oxidized to trivalent and, at the same time, the organic chlorine compound is decomposed. For example, in the case of trichloroethylene (TCE), it is decomposed as follows.

【0017】 C2HCl3+6OH・→2CO2+3HCl+2H2O 次に、過マンガン酸塩を添加すると、二価の鉄イオンは
先に注入された過酸化水素の作用で既に大部分が三価ま
で酸化されているので、二価の鉄イオンによる過マンガ
ン酸塩の無駄な消費は抑制され、過マンガン酸塩は効率
良く有機塩素化合物と反応してこれを分解することがで
きる。
C 2 HCl 3 + 6OH.fwdarw.2CO 2 + 3HCl + 2H 2 O Next, when a permanganate is added, the divalent iron ions are already mostly converted to trivalent by the action of hydrogen peroxide previously injected. Since it is oxidized, wasteful consumption of permanganate by divalent iron ions is suppressed, and the permanganate can efficiently react with the organic chlorine compound to decompose it.

【0018】なお、添加した過酸化水素と過マンガン酸
塩が万が一処理対象区域外に流出しても、土壌や地下水
中の還元性物質との反応並びに土壌表面の触媒作用によ
り徐々に分解する。従って、比較的ゆっくりではあるが
濃度は低下するので、これらが長期に亘って土壌や地下
水中に残留し、二次汚染を引き起こす可能性は極めて小
さい。
Even if the added hydrogen peroxide and permanganate flow out of the area to be treated, the hydrogen peroxide and permanganate are gradually decomposed by the reaction with the reducing substances in the soil or groundwater and the catalytic action on the soil surface. Therefore, since the concentration decreases relatively slowly, it is very unlikely that these will remain in soil or groundwater for a long period of time and cause secondary pollution.

【0019】[0019]

【発明の実施の形態】以下に本発明の実施の形態を詳細
に説明する。
Embodiments of the present invention will be described below in detail.

【0020】本発明においては、二価の鉄イオンの存在
下に、有機塩素化合物で汚染された土壌及び/又は地下
水にまず過酸化水素を添加し、次いで過マンガン酸塩を
添加する。
In the present invention, hydrogen peroxide is first added to soil and / or groundwater contaminated with an organochlorine compound in the presence of divalent iron ions, and then permanganate is added.

【0021】ここで、二価の鉄イオンは有機塩素化合物
で汚染された土壌及び/又は地下水中に1mg/L以上
の濃度で存在する必要があり、これよりも二価の鉄イオ
ン濃度が低いと反応が円滑に進行しない場合がある。通
常の場合、二価の鉄イオンは天然に数ppm〜20又は
30ppm程度の濃度で存在しているため、二価の鉄イ
オンを特に添加する必要はない。ただし、土壌及び/又
は地下水中に二価の鉄イオンが不足する場合には、硫化
第一鉄や塩化第一鉄等の二価の鉄イオンを添加する。こ
の場合、二価の鉄イオンの添加濃度は1ppm以上で高
い方が好ましいが、高過ぎると酸化により生成した三価
の鉄イオンがオキシ水酸化鉄などの形態で析出すること
により注入孔が閉塞するなどの問題が生じる恐れがある
ため、10ppm程度の濃度となるように添加するのが
好ましい。
Here, the divalent iron ion must be present at a concentration of 1 mg / L or more in soil and / or groundwater contaminated with the organochlorine compound, and the concentration of the divalent iron ion is lower than this. And the reaction may not proceed smoothly. In a normal case, since divalent iron ions are naturally present at a concentration of about several ppm to 20 or 30 ppm, it is not necessary to particularly add divalent iron ions. However, when divalent iron ions are insufficient in soil and / or groundwater, divalent iron ions such as ferrous sulfide and ferrous chloride are added. In this case, the addition concentration of divalent iron ions is preferably as high as 1 ppm or more, but if it is too high, trivalent iron ions generated by oxidation precipitate in the form of iron oxyhydroxide or the like, so that the injection hole is closed. Therefore, it is preferable to add so that the concentration becomes about 10 ppm.

【0022】過酸化水素は、土壌又は地下水中の二価の
鉄イオン濃度と化学的にほぼ当量或いはわずかに過剰量
(例えば2倍当量程度)添加するのが好ましい。
Hydrogen peroxide is preferably added in a chemical equivalent or slightly excess (for example, about twice equivalent) to the concentration of divalent iron ions in soil or groundwater.

【0023】一般に、有機塩素化合物のような汚染物質
は水に溶解し難く、比重も大きいため、土壌中の滞水層
の下部にとどまる場合が多く、また、この領域に存在す
る鉄分も大部分が二価の鉄イオンとして地下水中に溶解
しているため、実用的には地下水中の二価の鉄イオンの
濃度を測定することにより過酸化水素の添加量を決定す
ることができる。
In general, pollutants such as organochlorine compounds are hardly soluble in water and have a large specific gravity, so that they often remain in the lower part of the aquifer in the soil. Is dissolved in groundwater as divalent iron ions, so that the amount of hydrogen peroxide to be added can be determined practically by measuring the concentration of divalent iron ions in the groundwater.

【0024】過酸化水素を多量に添加し過ぎると、その
後に添加した過マンガン酸塩と過酸化水素とが反応し、
過マンガン酸塩が無駄に消費されることとなることか
ら、過酸化水素の添加量が過剰とならないようにするこ
とが重要である。通常の場合、過酸化水素は、土壌や地
下水の汚染の程度によっても異なるが、前述の如く、地
下水中の二価の鉄イオンとほぼ当量或いは若干過剰量で
あって、有機塩素化合物で汚染された土壌及び/又は地
下水に対して1〜100ppm程度となるように添加す
るのが好ましい。
If a large amount of hydrogen peroxide is added, the permanganate added later reacts with hydrogen peroxide,
Since permanganate is wasted, it is important that the amount of added hydrogen peroxide is not excessive. In normal cases, hydrogen peroxide varies depending on the degree of contamination of soil and groundwater, but as described above, it is almost equivalent to or slightly in excess of divalent iron ions in groundwater, and is contaminated with organic chlorine compounds. It is preferable to add it so that it may be about 1 to 100 ppm with respect to soil and / or groundwater.

【0025】このような濃度で過酸化水素を二価の鉄イ
オンの存在下に添加することによって、過酸化水素と二
価の鉄イオンとの反応で二価の鉄イオンが三価の鉄イオ
ンに酸化されると共に活性なヒドロキシラジカルが生成
し、このヒドロキシラジカルにより土壌又は地下水中の
有機塩素化合物が効率的に分解される。
By adding hydrogen peroxide at such a concentration in the presence of divalent iron ions, the reaction between hydrogen peroxide and divalent iron ions causes the divalent iron ions to become trivalent iron ions. At the same time, active hydroxyl radicals are generated, and these hydroxyl radicals efficiently decompose organochlorine compounds in soil or groundwater.

【0026】なお、この過酸化水素の添加に当り、硫酸
等の酸を添加して、土壌又は地下水のpHを2〜6に低
下させることにより、有機塩素化合物の分解効率を向上
させることができる。これは、過酸化水素により二価か
ら三価に酸化された鉄イオンの一部が、酸性条件下では
過酸化水素により再び二価に還元される機構が作用し、
過酸化水素から効率良くヒドロキシラジカルのような活
性種が生成するため、過酸化水素が有機塩素化合物の分
解に有効に利用されるようになることによる。
In addition, when adding hydrogen peroxide, an acid such as sulfuric acid is added to lower the pH of soil or groundwater to 2 to 6, thereby improving the decomposition efficiency of the organic chlorine compound. . This is due to the mechanism by which some of the iron ions oxidized from divalent to trivalent by hydrogen peroxide are reduced to divalent again by hydrogen peroxide under acidic conditions.
This is because active species such as hydroxyl radicals are efficiently generated from hydrogen peroxide, so that hydrogen peroxide is effectively used for decomposing organic chlorine compounds.

【0027】過酸化水素の添加後は過マンガン酸塩を添
加する。過酸化水素は二価の鉄イオンと急激に反応する
ため、過マンガン酸塩は、過酸化水素添加後数時間経過
すれば添加してよく、過酸化水素添加後1〜10時間経
過後に添加するのが好ましい。
After the addition of the hydrogen peroxide, the permanganate is added. Since hydrogen peroxide rapidly reacts with divalent iron ions, permanganate may be added several hours after the addition of hydrogen peroxide, and may be added 1 to 10 hours after the addition of hydrogen peroxide. Is preferred.

【0028】過マンガン酸塩の添加量については特に制
限はなく、土壌又は地下水中に残留する有機塩素化合物
をほぼ完全に分解するに必要な最少添加量以上添加すれ
ば良い。この添加量は、過酸化水素による分解処理後に
土壌又は地下水中に残留する有機塩素化合物の濃度を基
準として、その全量を分解するに必要な理論量の1〜1
000倍とされる。
The amount of permanganate to be added is not particularly limited, and may be at least the minimum amount necessary to almost completely decompose the organochlorine compound remaining in soil or groundwater. This addition amount is, based on the concentration of the organochlorine compound remaining in the soil or groundwater after the decomposition treatment with hydrogen peroxide as a reference, from 1 to 1 of the theoretical amount required to decompose the entire amount.
000 times.

【0029】なお、過酸化水素は通常0.01〜5重量
%濃度の過酸化水素水として、過マンガン酸塩は0.0
1〜1重量%濃度の水溶液として土壌又は地下水に添加
される。過マンガン酸塩としては、過マンガン酸カリウ
ム、過マンガン酸ナトリウム等が用いられる。
The hydrogen peroxide is usually a hydrogen peroxide solution having a concentration of 0.01 to 5% by weight,
It is added to soil or groundwater as an aqueous solution having a concentration of 1 to 1% by weight. As the permanganate, potassium permanganate, sodium permanganate or the like is used.

【0030】過酸化水素及び過マンガン酸塩の添加量
は、処理対象とする有機塩素化合物で汚染された土壌及
び/又は地下水の汚染の程度によっても異なるが、通常
の場合、100〜1000μg/L程度の有機塩素化合
物で汚染された土壌又は地下水であれば、過酸化水素を
1〜25ppm添加した後、過マンガン酸塩を5〜10
0ppm程度添加することで処理が行われる。
The amount of hydrogen peroxide and permanganate to be added varies depending on the degree of contamination of the soil and / or groundwater contaminated with the organochlorine compound to be treated, but usually 100 to 1000 μg / L. In the case of soil or groundwater contaminated with a certain amount of organic chlorine compounds, hydrogen peroxide is added in an amount of 1 to 25 ppm, and then permanganate is added in an amount of 5 to 10 ppm.
The treatment is performed by adding about 0 ppm.

【0031】本発明で処理対象となるものは有機塩素化
合物で汚染された土壌及び/又は地下水であるが、本発
明の方法は、有機塩素化合物のうち、特にジクロロエチ
レン(DCE)、トリクロロエチレン(TCE)、テト
ラクロロエチレン(PCE)等の脂肪族塩素化合物の分
解に適している。
The object to be treated in the present invention is soil and / or groundwater contaminated with an organochlorine compound. Among the organochlorine compounds, the method of the present invention is particularly applicable to dichloroethylene (DCE) and trichloroethylene (TCE). And tetrachlorethylene (PCE).

【0032】本発明の方法は、現在実用化されている前
述の真空抽出法や揚水・曝気法を採用した浄化法による
浄化処理後期において、処理効率が低下し、除去しきれ
ない低濃度有機塩素化合物が残留する土壌及び/又は地
下水の処理に有効である。
In the method of the present invention, the treatment efficiency is reduced in the latter stage of the purification treatment by the purification method employing the above-mentioned vacuum extraction method or the pumping / aeration method which is currently put into practical use, and the low-concentration organic chlorine which cannot be completely removed is used. It is effective in treating soil and / or groundwater in which the compound remains.

【0033】このような本発明の方法は、特に、原位置
での浄化処理に有効であるが、原位置処理に限らず、土
壌を掘り起こして本発明に従って浄化処理した後埋め戻
すことにより実施することもできる。
Such a method of the present invention is particularly effective for in-situ treatment, but is not limited to in-situ treatment, and is carried out by excavating soil, purifying according to the present invention, and then backfilling. You can also.

【0034】原位置での浄化処理を行う場合、具体的に
は、汚染物質が存在する深さまで井戸を設置し、この井
戸を利用して過酸化水素の水溶液を注入し、次に過マン
ガン酸塩の水溶液を注入する方法が採用されるが、更に
注入井戸以外に揚水井戸を設けて、土壌中で地下水に流
れを与えて処理効率を向上させることも可能である。
In the case of performing in-situ purification treatment, specifically, a well is set up to a depth where contaminants exist, and an aqueous solution of hydrogen peroxide is injected using the well, and then permanganate is used. Although a method of injecting an aqueous solution of salt is adopted, it is also possible to improve the treatment efficiency by providing a pumping well other than an injection well to give a flow to groundwater in the soil.

【0035】このような浄化処理において、浄化対象と
なる区域が限定されている場合は、過酸化水素と過マン
ガン酸塩を1度づつ添加すれば十分な浄化効果を得るこ
とができるが、他の区域から浄化対象としている区域ま
で汚染物質が拡散してくるような場合は、更に過酸化水
素と過マンガン酸塩の添加を繰り返すことが必要にな
る。このような場合は浄化対象区域中の有機塩素化合物
濃度をモニタリングすることにより、その濃度が環境基
準値以下に低下するまで過酸化水素と過マンガン酸塩の
添加を繰り返せば良い。このように過酸化水素の添加と
過マンガン酸塩の添加を複数回交互に繰り返して行う場
合、過マンガン酸塩の添加から、次の過酸化水素の添加
までの時間は12時間〜数日程度の間隔とするのが好ま
しい。即ち、この間隔は、処理対象区域の地下水がおお
よそ入れ換わる時間に相当し、処理対象区域の地下水の
流速や、地下水の強制循環のための揚水井の設置の有無
によっても異なるが、一般的には上記範囲内で設定する
ことができる。
In such a purification treatment, if the area to be purified is limited, a sufficient purification effect can be obtained by adding hydrogen peroxide and permanganate once each, If contaminants diffuse from the area to the area to be purified, it is necessary to repeat the addition of hydrogen peroxide and permanganate. In such a case, by monitoring the concentration of the organic chlorine compound in the purification target area, the addition of hydrogen peroxide and permanganate may be repeated until the concentration falls below the environmental standard value. When the addition of the hydrogen peroxide and the addition of the permanganate are repeated alternately a plurality of times, the time from the addition of the permanganate to the addition of the next hydrogen peroxide is about 12 hours to several days. It is preferable to set the interval. That is, this interval is equivalent to the time when the groundwater in the treatment area is approximately replaced, and varies depending on the flow rate of the groundwater in the treatment area and the presence or absence of a pumping well for forced circulation of the groundwater. Can be set within the above range.

【0036】[0036]

【実施例】以下に実施例及び比較例を挙げて本発明をよ
り具体的に説明する。
The present invention will be described more specifically below with reference to examples and comparative examples.

【0037】実施例1,2、比較例1〜4 活性炭カラムに通して残留塩素を除去し、更に脱気及び
窒素パージした水道水に10mg/L(0.18mM)
の二価の鉄イオン(硫酸第一鉄)と1mg/LのTCE
を加えて試験液(模擬汚染地下水)とした。これをバイ
アル瓶に入れてアルミシールセプタムで密封し、表1に
示す量の過酸化水素を添加し、更に4時間後に表1に示
す量の過マンガン酸カリウムを加え(ただし、比較例
1,2では過酸化水素添加せず。比較例3,4では過マ
ンガン酸カリウム添加せず。)、20℃の条件で放置し
た。そして過酸化水素添加から24時間後に残留するT
CE濃度をガスクロマトグラフにより測定し、結果を表
1に示した。
Examples 1 and 2 and Comparative Examples 1 to 4 Residual chlorine was removed through an activated carbon column, and 10 mg / L (0.18 mM) was added to deaerated and nitrogen-purged tap water.
Iron (ferrous sulfate) and 1mg / L TCE
Was added to obtain a test solution (simulated contaminated groundwater). This was put in a vial bottle, sealed with an aluminum seal septum, hydrogen peroxide in the amount shown in Table 1 was added, and after 4 hours, potassium permanganate in the amount shown in Table 1 was added (however, Comparative Examples 1 and 2). In No. 2, no hydrogen peroxide was added. In Comparative Examples 3 and 4, potassium permanganate was not added.), And left at 20 ° C. And T remaining 24 hours after the addition of hydrogen peroxide
The CE concentration was measured by gas chromatography, and the results are shown in Table 1.

【0038】[0038]

【表1】 [Table 1]

【0039】比較例5 実施例1の条件で、過酸化水素と過マンガン酸カリウム
の添加順序を逆にして処理を行った。その結果、過マン
ガン酸カリウムは二価の鉄イオンと反応して消費され、
また二価の鉄イオンも三価に酸化されたので、次に過酸
化水素を添加しても24時間後の残留TCE濃度は0.
85mg/Lと初期濃度から殆ど変化しなかった。
Comparative Example 5 The treatment was performed under the same conditions as in Example 1 except that the order of adding hydrogen peroxide and potassium permanganate was reversed. As a result, potassium permanganate is consumed by reacting with divalent iron ions,
In addition, since divalent iron ions were also oxidized to trivalent, the residual TCE concentration after 24 hours even after adding hydrogen peroxide was 0.1%.
At 85 mg / L, there was almost no change from the initial concentration.

【0040】比較例6,7 実施例1,2において、活性炭カラムに通して残留塩素
を除去し、更に脱気及び窒素パージした水道水に二価の
鉄イオン(硫酸第一鉄)を加えず、1mg/LのTCE
のみを加えて試験液(模擬汚染地下水)としたこと以外
は同様に処理を行い、残留TCE濃度を測定し、結果を
表2に示した。
Comparative Examples 6 and 7 In Examples 1 and 2, residual chlorine was removed by passing through an activated carbon column, and divalent iron ions (ferrous sulfate) were not added to deaerated and nitrogen-purged tap water. 1 mg / L TCE
The same treatment was carried out except that only the test solution (simulated contaminated groundwater) was added thereto, and the residual TCE concentration was measured. The results are shown in Table 2.

【0041】[0041]

【表2】 [Table 2]

【0042】実施例3 活性炭カラムに通して残留塩素を除去し、更に脱気及び
窒素パージした水道水に10mg/L(0.18mM)
の二価の鉄イオン(硫酸第一鉄)と1mg/LのTCE
と1mg/Lのcis−DCEとを加えて試験液(模擬
汚染地下水)とした。この試験液を、粒子径約0.45
mmの砂80mLを入れた容量160mLのバイアル瓶
に40mL加え、直ちにアルミシールセプタムで密閉し
た。この中に濃度1000mg/Lの過酸化水素水2m
Lをシリンジで注入し、20℃、60rpmの条件で振
盪した。更に、4時間後に濃度1000mg/Lの過マ
ンガン酸カリウム水溶液2mLをシリンジで注入し同じ
条件で振盪を継続した。
Example 3 10 mg / L (0.18 mM) was added to dewatered and nitrogen-purged tap water to remove residual chlorine by passing through an activated carbon column.
Iron (ferrous sulfate) and 1mg / L TCE
And 1 mg / L of cis-DCE were added to make a test solution (simulated contaminated groundwater). This test liquid was used for a particle size of about 0.45.
40 mL was added to a vial having a capacity of 160 mL containing 80 mL of sand of mm, and immediately sealed with an aluminum seal septum. 2m of hydrogen peroxide solution with 1000mg / L concentration
L was injected with a syringe and shaken under the conditions of 20 ° C. and 60 rpm. Further, after 4 hours, 2 mL of a 1000 mg / L aqueous solution of potassium permanganate was injected with a syringe, and shaking was continued under the same conditions.

【0043】このように調製した試料とは別に過酸化水
素も過マンガン酸カリウムも添加せず、それ以外は同様
の手順で調製した試料をTCEとcis−DCEの標準
濃度試料とした。
Separately from the sample thus prepared, neither hydrogen peroxide nor potassium permanganate was added, and a sample prepared by the same procedure except for the above was used as a standard concentration sample of TCE and cis-DCE.

【0044】過酸化水素添加から2日後に各試料のヘッ
ドスペースをガスクロマトグラフにかけ、標準濃度試料
と比較することにより残留するTCEとcis−DCE
の濃度を求めた。その結果、TCE濃度は0.015m
g/L、cis−DCE濃度は0.008mg/Lであ
った。
Two days after the addition of hydrogen peroxide, the headspace of each sample was chromatographed and the residual TCE and cis-DCE were determined by comparison with a standard concentration sample.
Was determined. As a result, the TCE concentration was 0.015 m
g / L, cis-DCE concentration was 0.008 mg / L.

【0045】比較例8 過マンガン酸カリウムの添加を行わなかったこと以外は
実施例3と同様の操作を行った。その結果、過酸化水素
添加から2日後に残留するTCE及びcis−DCEの
濃度はそれぞれ0.43mg/L、0.24mg/Lで
あった。
Comparative Example 8 The same operation as in Example 3 was performed, except that potassium permanganate was not added. As a result, the concentrations of TCE and cis-DCE remaining two days after the addition of hydrogen peroxide were 0.43 mg / L and 0.24 mg / L, respectively.

【0046】比較例9 過酸化水素の添加を行わなかったこと以外は実施例3と
同様の操作を行った。その結果、過マンガン酸カリウム
添加から2日後に残留するTCE及びcis−DCEの
濃度はそれぞれ0.53mg/L、0.30mg/Lで
あった。
Comparative Example 9 The same operation as in Example 3 was carried out except that no hydrogen peroxide was added. As a result, the concentrations of TCE and cis-DCE remaining two days after the addition of potassium permanganate were 0.53 mg / L and 0.30 mg / L, respectively.

【0047】比較例10 過酸化水素と過マンガン酸カリウムの添加順序を逆にし
て実施例3と同様の操作を行った。その結果、過マンガ
ン酸カリウム添加から2日後に残留するTCE及びci
s−DCEの濃度はそれぞれ0.65mg/L、0.5
7mg/Lであった。
Comparative Example 10 The same operation as in Example 3 was performed except that the order of adding hydrogen peroxide and potassium permanganate was reversed. As a result, TCE and ci remaining two days after the addition of potassium permanganate were added.
The concentrations of s-DCE were 0.65 mg / L and 0.5, respectively.
It was 7 mg / L.

【0048】[0048]

【発明の効果】以上詳述した通り、本発明の土壌及び/
又は地下水の浄化方法によれば、有機塩素化合物で汚染
された土壌及び/又は地下水中の有機塩素化合物を効率
的に分解処理することができる。本発明の方法は、原位
置での処理も可能であり、また、残留薬剤による二次汚
染の問題もなく、その工業的有用性は極めて大きい。
As described in detail above, the soil and / or
Alternatively, according to the groundwater purification method, it is possible to efficiently decompose the organic chlorine compound in soil and / or groundwater contaminated with the organic chlorine compound. The method of the present invention can be processed in situ, has no problem of cross-contamination due to residual chemicals, and has extremely large industrial utility.

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成11年1月27日(1999.1.2
7)
[Submission date] January 27, 1999 (1999.1.2
7)

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0021[Correction target item name] 0021

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0021】ここで、二価の鉄イオンは有機塩素化合物
で汚染された土壌及び/又は地下水中に1mg/L以上
の濃度で存在する必要があり、これよりも二価の鉄イオ
ン濃度が低いと反応が円滑に進行しない場合がある。通
常の場合、二価の鉄イオンは天然に数ppm〜20又は
30ppm程度の濃度で存在しているため、二価の鉄イ
オンを特に添加する必要はない。ただし、土壌及び/又
は地下水中に二価の鉄イオンが不足する場合には、硫
第一鉄や塩化第一鉄等の二価の鉄イオンを添加する。こ
の場合、二価の鉄イオンの添加濃度は1ppm以上で高
い方が好ましいが、高過ぎると酸化により生成した三価
の鉄イオンがオキシ水酸化鉄などの形態で析出すること
により注入孔が閉塞するなどの問題が生じる恐れがある
ため、10ppm程度の濃度となるように添加するのが
好ましい。
Here, the divalent iron ion must be present at a concentration of 1 mg / L or more in soil and / or groundwater contaminated with the organochlorine compound, and the concentration of the divalent iron ion is lower than this. And the reaction may not proceed smoothly. In a normal case, since divalent iron ions are naturally present at a concentration of about several ppm to 20 or 30 ppm, it is not necessary to particularly add divalent iron ions. However, in the case of insufficient divalent iron ions in the soil and / or groundwater, adding a divalent iron ion such as sulfate <br/> ferrous and ferrous chloride. In this case, the addition concentration of divalent iron ions is preferably as high as 1 ppm or more, but if it is too high, trivalent iron ions generated by oxidation precipitate in the form of iron oxyhydroxide or the like, so that the injection hole is closed. Therefore, it is preferable to add so that the concentration becomes about 10 ppm.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 有機塩素化合物で汚染された土壌及び/
又は地下水に、二価の鉄イオンの存在下に過酸化水素を
添加し、次いで過マンガン酸塩を添加することを特徴と
する土壌及び/又は地下水の浄化方法。
A soil contaminated with an organochlorine compound and / or
Alternatively, a method for purifying soil and / or groundwater, comprising adding hydrogen peroxide to groundwater in the presence of divalent iron ions, and then adding permanganate.
JP11014552A 1999-01-22 1999-01-22 Soil and / or groundwater purification method Pending JP2000210683A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11014552A JP2000210683A (en) 1999-01-22 1999-01-22 Soil and / or groundwater purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11014552A JP2000210683A (en) 1999-01-22 1999-01-22 Soil and / or groundwater purification method

Publications (1)

Publication Number Publication Date
JP2000210683A true JP2000210683A (en) 2000-08-02

Family

ID=11864324

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11014552A Pending JP2000210683A (en) 1999-01-22 1999-01-22 Soil and / or groundwater purification method

Country Status (1)

Country Link
JP (1) JP2000210683A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6315494B1 (en) * 2000-10-24 2001-11-13 Daniel W. Oberle Soil remediation by permanganate oxidation
JP2002119977A (en) * 2000-10-13 2002-04-23 Japan Organo Co Ltd Method and apparatus for cleaning polluted ground water
WO2003063774A3 (en) * 2002-01-30 2004-05-06 Richard Greenberg Method of treating contaminants in an in situ environment
RU2288183C1 (en) * 2006-02-02 2006-11-27 Закрытое акционерное общество "ДАР/ВОДГЕО" Method of cleaning underground water to remove iron and manganese under low temperature, water alkalinity and hardness conditions
JP2006341195A (en) * 2005-06-09 2006-12-21 Japan Organo Co Ltd Purification method for organic pollutants
JP2007105555A (en) * 2005-09-09 2007-04-26 Toagosei Co Ltd Method for decomposing organic compounds
JP2007521940A (en) * 2003-07-29 2007-08-09 エフ エム シー コーポレーション Treatment of environmental pollutants
CN103521509A (en) * 2013-10-12 2014-01-22 江苏上田环境修复有限公司 Electric intensive oxidation process for restoration of organic contaminated soil
CN104307869A (en) * 2014-10-29 2015-01-28 环境保护部南京环境科学研究所 Method for intensively removing hexachloro-cyclohexane soprocide and dichlorodiphenyl trichloroethane in soil by zero-valent iron
CN114888064A (en) * 2022-05-19 2022-08-12 北京化工大学 Method for repairing polycyclic aromatic hydrocarbon contaminated soil by organic solvent pretreatment and hydrogen peroxide
CN120155193A (en) * 2025-05-16 2025-06-17 中国科学技术大学 A kind of iron sulfide oxide catalyst and its preparation method and application

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002119977A (en) * 2000-10-13 2002-04-23 Japan Organo Co Ltd Method and apparatus for cleaning polluted ground water
US6315494B1 (en) * 2000-10-24 2001-11-13 Daniel W. Oberle Soil remediation by permanganate oxidation
WO2003063774A3 (en) * 2002-01-30 2004-05-06 Richard Greenberg Method of treating contaminants in an in situ environment
JP2007521940A (en) * 2003-07-29 2007-08-09 エフ エム シー コーポレーション Treatment of environmental pollutants
JP2006341195A (en) * 2005-06-09 2006-12-21 Japan Organo Co Ltd Purification method for organic pollutants
JP2007105555A (en) * 2005-09-09 2007-04-26 Toagosei Co Ltd Method for decomposing organic compounds
RU2288183C1 (en) * 2006-02-02 2006-11-27 Закрытое акционерное общество "ДАР/ВОДГЕО" Method of cleaning underground water to remove iron and manganese under low temperature, water alkalinity and hardness conditions
CN103521509A (en) * 2013-10-12 2014-01-22 江苏上田环境修复有限公司 Electric intensive oxidation process for restoration of organic contaminated soil
CN103521509B (en) * 2013-10-12 2015-11-18 上田环境修复股份有限公司 A kind of electronic oxidation strengthening technique for renovation of organic pollution soil
CN104307869A (en) * 2014-10-29 2015-01-28 环境保护部南京环境科学研究所 Method for intensively removing hexachloro-cyclohexane soprocide and dichlorodiphenyl trichloroethane in soil by zero-valent iron
CN114888064A (en) * 2022-05-19 2022-08-12 北京化工大学 Method for repairing polycyclic aromatic hydrocarbon contaminated soil by organic solvent pretreatment and hydrogen peroxide
CN114888064B (en) * 2022-05-19 2023-08-29 北京化工大学 A method for the remediation of PAH-contaminated soil by organic solvent pretreatment and hydrogen peroxide
CN120155193A (en) * 2025-05-16 2025-06-17 中国科学技术大学 A kind of iron sulfide oxide catalyst and its preparation method and application

Similar Documents

Publication Publication Date Title
CN109304363B (en) Chemical remediation agent suitable for petroleum-polluted soil and use method thereof
JP2000210683A (en) Soil and / or groundwater purification method
JP4167052B2 (en) Purification method for organic compound contamination
US20220176426A1 (en) Compositions and methods for oxidizing and sequestering carbon and stabilizing metals
JP4405692B2 (en) Purification method for underground pollution area
JP2002159959A (en) Purification method and purification device for underground pollution area
JP4095490B2 (en) Purification method for contamination by chemical substances
RU2379136C2 (en) Method of detoxication from organic pollutants of soil and aquatic media
JP2000301172A (en) Soil and / or groundwater purification method
CN110372048B (en) Method for removing organic matters in water
KR20100069729A (en) Soil and groundwater treatment method and reagent using fenton oxidation reaction with stabilized hydrogen peroxide
JP2002136961A (en) Soil or groundwater purification treatment method
JP4639309B2 (en) Treatment method of wastewater containing cyanide
JP3766298B2 (en) Wastewater treatment method and apparatus
JP3784654B2 (en) Purification method for chemical contaminants
Herraiz-Carboné et al. Sustainable management of SEAR waste emulsions from lindane production by electrochemical oxidation: performance and environmental implications
KR102435104B1 (en) Composition for accelerating the natural reduction of arsenic in groundwater and method of accelerating natural reduction of arsenic in groundwater
JP2004167426A (en) Method and system for purifying contamination by chemical substances
JP4027209B2 (en) Purification method for contamination by chemical substances
JP2003290770A (en) Method and device for decomposing harmful substance existing in air
JP2007038113A (en) Organic arsenic compound-containing water treatment method
US10947137B2 (en) Process for treatment of mine impacted water
KR20090021749A (en) Soil and groundwater treatment method and reagent
JP3501719B2 (en) Pollutant decomposition apparatus and method
JP3095336U (en) Equipment for treating polluted air containing organochlorine compounds

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060119

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20071220

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090310

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090424

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090526

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20091006