JP3784654B2 - Purification method for chemical contaminants - Google Patents

Purification method for chemical contaminants Download PDF

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Publication number
JP3784654B2
JP3784654B2 JP2001055242A JP2001055242A JP3784654B2 JP 3784654 B2 JP3784654 B2 JP 3784654B2 JP 2001055242 A JP2001055242 A JP 2001055242A JP 2001055242 A JP2001055242 A JP 2001055242A JP 3784654 B2 JP3784654 B2 JP 3784654B2
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soil
hydrogen peroxide
added
contaminated
pollutant
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Japanese (ja)
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JP2002254060A (en
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正浩 江口
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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、化学物質により汚染された汚染物(化学物質汚染物)を物理化学的に浄化する方法に関する。本発明に係る化学物質汚染物の浄化方法は、例えば有機塩素化合物に汚染された土壌、底質、汚泥等の浄化に好適に使用される。
【0002】
【従来の技術】
トリクロロエチレン、テトラクロロエチレン等の有機塩素化合物は、洗浄剤として各種工場やクリーニング店で広く使用されているが、これら有機塩素化合物は発癌性物質である疑いがあるため、近年、上記有機塩素化合物による土壌、地下水等の汚染が大きな社会問題となっている。
【0003】
従来、有機塩素化合物で汚染された土壌の処理方法としては、汚染土壌の封じ込め処理、汚染土壌の掘削・封じ込め処理、揚水ばっ気や真空抽気と活性炭吸着処理等とを組み合わせたポンプ・アンド・トリート法などが主に採られている。
【0004】
また、近年では、鉄粉を用いた汚染化学物質の還元的分解処理法、鉄粉及び嫌気性微生物を用いた汚染化学物質の還元的分解処理法、過酸化水素を用いた汚染化学物質の酸化分解処理法が研究されている。
【0005】
【発明が解決しようとする課題】
しかし、前述した汚染土壌の封じ込め処理、掘削・封じ込め処理、ポンプ・アンド・トリート法は、汚染化学物質を積極的に分解して無害化する技術ではないこと、莫大なコスト、エネルギー、手間を要すること、浄化期間が10〜20年と長いことなどが問題となっていた。
【0006】
また、鉄粉あるいは鉄粉と嫌気性微生物を用いた還元的分解処理法は、有機塩素化合物を嫌気的に脱塩素して還元分解するものであるが、浄化期間が半年から1年と長く、また脱塩素が不完全であると有害な副生成物であるジクロロエチレン、ビニルクロライドが発生するという問題があった。
【0007】
さらに、過酸化水素を用いた酸化分解処理法は、汚染土壌中には酸化の対象となる有機物が非常に多く含まれるため、汚染化学物質を選択的に酸化することができず、その結果、処理後の汚染化学物質濃度を十分に低減できないという問題があった。また、酸化剤(過酸化水素)を汚染土壌の数重量%程度使用する必要があり、汚染土壌に添加する酸化剤量が非常に多いため、作業上危険であるという問題があった。
【0008】
本発明は、前述した事情に鑑みてなされたもので、化学物質により汚染された汚染物、特に有機塩素化合物で汚染された土壌、底質、汚泥等を、短期間で、かつ低コスト、低エネルギーで浄化することができる方法を提供することを目的とする。
【0009】
【課題を解決するための手段】
本発明者は、前記目的を達成するために、トリクロロエチレン(TCE)、シス−1,2−ジクロロエチレン(c−DCE)などの有機塩素化合物に汚染された土壌を浄化する酸化処理法について鋭意検討を行った。その結果、上記汚染土壌に金属系触媒として鉄粉を添加して均一に攪拌混合した後、金属系触媒を添加した汚染土壌に過酸化水素水を添加して酸性条件下で均一に攪拌混合した場合、金属系触媒と過酸化水素との接触により発生するヒドロキシルラジカルによって、例えば1日程度という短期間で高濃度の有機塩素化合物を分解できることを見出した。
【0010】
本発明は、上述した知見に基づいてなされたもので、化学物質により汚染された汚染物を浄化するに当たり、汚染物に鉄粉を添加して攪拌した後、汚染物の含水率が5〜40重量%になるように、該汚染物に過酸化水素水と硫酸の混合液を添加して酸性条件下で攪拌することを特徴とする化学物質汚染物の浄化方法を提供する。
【0011】
従来、汚染土壌に過酸化水素のみを添加したり、過酸化水素と鉄化合物や鉄イオンとを同時に添加する酸化処理法は知られていた。しかし、これらの従来法では、汚染化学物質をある程度までは酸化分解できても、汚染化学物質を環境基準値以下にまで低減することは難しかった。
【0012】
これに対し、本発明では、汚染物に過酸化水素を添加する前に汚染物に金属系触媒を添加して攪拌してあるので、過酸化水素が金属系触媒と接触して汚染化学物質の酸化分解反応が開始される時点で、既に金属系触媒が汚染物中に均一に存在している。そのため、本発明では、過酸化水素が酸素と水に分解して無駄に消費されることが抑制され、ヒドロキシルラジカルが有効に生成し、汚染化学物質の分解効率が向上したものと推測される。また、過酸化水素を添加した後にさらに汚染物を攪拌することで、汚染化学物質の分解効率がより向上したものと推測される。
【0013】
以下、本発明につきさらに詳しく説明する。本発明では、まず、化学物質汚染物に金属系触媒を添加して均一に攪拌する。金属系触媒としては、過酸化水素と接触してヒドロキシルラジカルを発生させるものを用いる。金属系触媒として、具体的には、鉄粉を用いる
【0014】
金属系触媒として鉄粉を使用する場合、鉄粉の性状に特に限定はないが、粒径が小さく均一な鉄粉であることが好ましい。また、鉄粉の添加量は化学物質汚染物の0.01〜1重量%、特に0.05〜0.5重量%とすることが適当である。
【0016】
本発明では、次に、金属系触媒を添加した汚染物に過酸化水素水と硫酸の混合液を添加して均一に攪拌する。過酸化水素水の添加量は100%過酸化水素として、化学物質汚染物の1.0重量%以下、特に0.1〜0.5重量%とすることが適当である。過酸化水素水の添加量が100%過酸化水素として化学物質汚染物の1.0重量%を超えても、汚染化学物質の分解効果はそれ以上は改善されず、浄化費用が高くなることがある。
【0017】
また、本発明では、過酸化水素水と硫酸の混合液を添加した汚染物を酸性条件下、好ましくはpH3〜5の条件下で攪拌する。これにより、汚染化学物質をさらに効率的に酸化分解することが可能となる。pHを3〜5とするために酸を添加するが、本発明においては硫酸を用いる。塩酸は揮発性が高く、安全性、作業性の面で好ましくない。硝酸の使用は窒素成分が増加するため好ましくない。有機酸の使用は酸化の対象となる有機物を不要に多くし、コスト的にも高くなるため好ましくない。
【0018】
本発明では、汚染物の含水率が5〜40重量%になるように汚染物に過酸化水素水と硫酸の混合液を添加する。これは、汚染物の含水率が5重量%未満であると、汚染物に過酸化水素が均一に混合されず、汚染化学物質の酸化分解効率が悪くなるからである。汚染物の含水率のより好ましい値は10〜40重量%である。汚染物の含水率が40重量%を超えると、汚染物を地中に埋め戻す際などに支障が生じることがある。上記汚染物の含水率は、汚染物に添加する過酸化水素水中の水の割合によって調整することができる。
【0019】
本発明では、得られた浄化物をさらに中和処理することが好ましい。これにより、得られた浄化物を再利用することが容易になる。中和処理の方法としては、例えば、浄化物に水酸化カルシウム等のアルカリ剤を添加する手段を挙げることができる。
【0020】
また、本発明においては、得られた浄化物に改質剤を添加することができる。改質剤としては、例えばセメント系土質改良剤(固化剤)が挙げられる。浄化した土にセメント系改質剤を1〜5重量%程度添加することにより、含水率が増えて軟弱になった土を浄化前の状態(例えば地耐力50kg/m2)に戻してから地中に埋め戻すことができる。
【0021】
本発明に係る化学物質汚染物の浄化方法は、有機塩素化合物に汚染された土壌、底質、汚泥等の浄化に好適に使用されるが、これに限定されるものではない。すなわち、本発明の浄化方法は、金属系触媒と過酸化水素との接触により発生する酸化力の強いヒドロキシルラジカルによって有機物を酸化分解するため、様々な有機物を効率的に分解することができる。したがって、本発明の浄化方法は、有機塩素化合物(TCE、PCE、ダイオキシン類、PCB類など)による汚染物の浄化のみならず、他の有機物、例えば油、ベンゼン、トルエン、キシレン等による汚染物の浄化にも適用可能である。
【0022】
【発明の実施の形態】
次に、添付図面を参照して本発明の実施の形態を説明する。図1は本発明の実施形態を示す図である。本実施形態では、まず、(a)図に示すように汚染土壌2を掘削し、これを混練機4に移す。次に、(b)図に示すように混練機4内の汚染土壌2に鉄粉6を添加し、混練機4により汚染土壌2と鉄粉6とを均一に攪拌混合する。さらに、(c)図に示すように鉄粉6を添加した汚染土壌2に過酸化水素水と硫酸の混合液8を添加し、混練機4により上記汚染土壌2と混合液8とを均一に攪拌混合する。一定時間(通常2〜60分程度)攪拌を行うと汚染土壌2が浄化される。ただし、攪拌終了後も汚染化学物質の酸化分解反応は進行する。その後、(d)図に示すように混練機4から浄化土壌10を排出する。さらに、(e)図に示すように浄化土壌10にセメント系土質改良剤12を添加して混合し、(f)図に示すように浄化土壌10を元の場所に埋め戻す。埋め戻し後、雨水などが混入しないように浄化土壌10をビニールシートなどで覆い、経時的に土をサンプリングして汚染化学物質の浄化状況をモニタリングする。
【0024】
【実施例】
100mLのバイアルビンに土150gを入れ、この土に下記(1)(6)に示す条件で鉄粉、過酸化水素などを添加するとともに、トリクロロエチレン(TCE)を溶出TCE(バイアルビンのヘッドスペース中に含まれるトリクロロエチレン)濃度が1mg/Lとなるように注入した後、バイアルビンを密閉して処理実験を開始した。そして、経時的に各バイアルの溶出TCE濃度をガスクロマトグラフィーで測定することにより、処理効果について評価した。下記条件(1)(6)の内、(3)及び(4)は本発明例、他は比較例である。また、条件(5)は鉄粉と過酸化水素の添加順を本発明の逆にした例、条件(6)は土壌の含水率が低い例である。
【0025】
(実験条件)
(1)ブランク試験
土に水45mLを添加して攪拌した。
(2)鉄粉還元法
土に水45mL及び還元鉄5gを添加して攪拌した。
(3)鉄粉+過酸化水素(pH4)
土に水45mL及び鉄粉5gを添加して攪拌した後、過酸化水素1000mg/kg土及び硫酸を添加して攪拌した。
(4)鉄粉+過酸化水素(pH7)
土に水45mL及び鉄粉5gを添加して攪拌した後、過酸化水素1000mg/kg土を添加して攪拌した。
(5)過酸化水素+鉄粉(pH4)
土に水45mL及び過酸化水素1000mg/kg土を添加して攪拌した後、鉄粉5g及び硫酸を添加して攪拌した。
(6)鉄粉+過酸化水素(pH4)
土に水4.5mL及び鉄粉5gを添加して攪拌した後、過酸化水素1000mg/kg土及び硫酸を添加して攪拌した。
【0026】
(処理結果)
に処理結果を示す。(2)の鉄粉還元法では、TCEは徐々に還元分解されるが、浄化に数ヶ月の時間がかかること、中間生成物としてジクロロエチレン、ビニルクロライドが蓄積することが確認された。(3)(4)の本発明では、各々2時間、1日という短時間でTCEを環境基準値以下に浄化できることが明らかとなった。以上の処理結果から、本発明が汚染土壌の短期の浄化に極めて有効であることが明らかとなった。また、酸性条件下では汚染化学物質の分解速度がより高いことも明らかとなった。これに対し、添加薬剤量は同じで過酸化水素を鉄粉より先に添加する(5)では、TCEを環境基準値まで浄化するに至らなかった。また、土壌の含水率が3.3%と低い(6)では、過酸化水素が土壌全体に行き渡らず、土壌全体を浄化することはできなかった。
【0027】
【発明の効果】
以上のように、本発明によれば、化学物質により汚染された汚染物、特に有機塩素化合物で汚染された土壌、底質、汚泥等を、数時間から数ヶ月程度という短期間で、かつ低コスト、低エネルギーで浄化することができる。また、本発明は、各種の難分解性化学物質を効率的に分解できるラジカル反応を利用しているため、高濃度の複合汚染物の浄化にも有効であり、その有用性は極めて大きい。
【図面の簡単な説明】
【図1】 本発明の実施形態を示す図である。
【図2】 実施例の浄化処理における処理経過日数と溶出TCE濃度との関係を示すグラフである。
【符号の説明】
2 汚染土壌
4 混練機
6 鉄粉
8 過酸化水素水と硫酸の混合液
10 浄化土壌
12 セメント系土質改良剤
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for physicochemically purifying contaminants (chemical contaminants) contaminated by chemical substances. The method for purifying chemical contaminants according to the present invention is suitably used for purification of soil, sediment, sludge and the like contaminated with organic chlorine compounds, for example.
[0002]
[Prior art]
Organochlorine compounds such as trichlorethylene and tetrachlorethylene are widely used as cleaning agents in various factories and cleaning shops, but these organochlorine compounds are suspected to be carcinogenic substances. Contamination of groundwater is a major social problem.
[0003]
Conventional methods for treating soil contaminated with organochlorine compounds include pumping and treating by combining contaminated soil containment, excavation and containment of contaminated soil, pumping aeration and vacuum extraction, and activated carbon adsorption treatment. Laws are mainly adopted.
[0004]
Also, in recent years, reductive decomposition of pollutant chemicals using iron powder, reductive decomposition of pollutant chemicals using iron powder and anaerobic microorganisms, oxidation of pollutant chemicals using hydrogen peroxide Decomposition methods have been studied.
[0005]
[Problems to be solved by the invention]
However, the contaminated soil containment process, excavation / containment process, and pump-and-treat method are not technologies that aggressively decompose and detoxify polluted chemicals, requiring enormous costs, energy, and labor. The problem is that the purification period is as long as 10 to 20 years.
[0006]
In addition, the reductive decomposition method using iron powder or iron powder and anaerobic microorganisms is an anaerobic dechlorination method for reductive decomposition, but the purification period is as long as six months to one year. In addition, when dechlorination is incomplete, dichloroethylene and vinyl chloride, which are harmful byproducts, are generated.
[0007]
Furthermore, the oxidative decomposition treatment method using hydrogen peroxide cannot selectively oxidize pollutant chemicals because the contaminated soil contains a large amount of organic matter to be oxidized, and as a result, There was a problem that the concentration of contaminated chemicals after treatment could not be reduced sufficiently. In addition, it is necessary to use an oxidizing agent (hydrogen peroxide) of about several percent by weight of the contaminated soil, and the amount of the oxidizing agent added to the contaminated soil is very large.
[0008]
The present invention has been made in view of the above-described circumstances, and it is possible to remove pollutants contaminated with chemical substances, particularly soil, sediment, sludge, etc. contaminated with organochlorine compounds in a short period of time at low cost and low cost. The object is to provide a method that can be purified with energy.
[0009]
[Means for Solving the Problems]
In order to achieve the above object, the present inventor has intensively studied an oxidation treatment method for purifying soil contaminated with an organic chlorine compound such as trichlorethylene (TCE) or cis-1,2-dichloroethylene (c-DCE). went. As a result, were uniformly stirred and mixed by adding iron powder as metallic catalysts in the contaminated soil, uniformly stirred and mixed under acidic conditions by adding hydrogen peroxide to the contaminated soil by adding a metal-based catalyst In such a case, it has been found that a high concentration of an organic chlorine compound can be decomposed in a short period of time, for example, about one day by hydroxyl radicals generated by contact between the metal catalyst and hydrogen peroxide.
[0010]
The present invention has been made on the basis of the above-described knowledge. In purifying contaminants contaminated with chemical substances, after adding iron powder to the contaminants and stirring , the moisture content of the contaminants is 5 to 40. Provided is a method for purifying chemical contaminants, characterized in that a mixed solution of hydrogen peroxide and sulfuric acid is added to the contaminants so as to be in weight% and stirred under acidic conditions.
[0011]
Conventionally, an oxidation treatment method in which only hydrogen peroxide is added to contaminated soil, or hydrogen peroxide and an iron compound or iron ion are simultaneously added has been known. However, in these conventional methods, it is difficult to reduce the pollutant chemicals to the environmental standard value or less even if the pollutant chemicals can be oxidatively decomposed to some extent.
[0012]
On the other hand, in the present invention, since the metal catalyst is added to the contaminant before the hydrogen peroxide is added to the contaminant, the hydrogen peroxide is brought into contact with the metal catalyst and the pollutant When the oxidative decomposition reaction is started, the metal catalyst is already present uniformly in the contaminant. Therefore, in this invention, it is estimated that hydrogen peroxide is decomposed | disassembled into oxygen and water, and is consumed wastefully, a hydroxyl radical is produced | generated effectively and the decomposition | disassembly efficiency of a pollutant chemical substance improved. Further, it is presumed that the decomposition efficiency of the contaminating chemical substance is further improved by further stirring the contaminant after adding hydrogen peroxide.
[0013]
Hereinafter, the present invention will be described in more detail. In the present invention, first, a metal-based catalyst is added to a chemical contaminant and stirred uniformly. As the metal catalyst, a catalyst that generates hydroxyl radicals by contact with hydrogen peroxide is used. Specifically, iron powder is used as the metal catalyst.
[0014]
When iron powder is used as the metal-based catalyst, there is no particular limitation on the properties of the iron powder, but it is preferably a uniform iron powder having a small particle size. The amount of iron powder added is suitably 0.01 to 1% by weight, especially 0.05 to 0.5% by weight of the chemical contaminant.
[0016]
In the present invention, next, a mixed solution of hydrogen peroxide and sulfuric acid is added to the contaminated material to which the metal catalyst has been added, and stirred uniformly. The amount of hydrogen peroxide water added is 100% hydrogen peroxide, and it is appropriate that it is 1.0% by weight or less, particularly 0.1 to 0.5% by weight of the chemical contaminant. Even if the amount of hydrogen peroxide added exceeds 100% by weight as 100% hydrogen peroxide, the decomposition effect of the pollutant chemicals will not be improved any further, and the purification cost will increase. is there.
[0017]
Moreover, in this invention, the contaminant which added the liquid mixture of hydrogen peroxide solution and a sulfuric acid is stirred on acidic conditions, Preferably the conditions of pH 3-5 are stirred. This makes it possible to oxidize and decompose pollutant chemical substances more efficiently. An acid is added to adjust the pH to 3 to 5. In the present invention, sulfuric acid is used. Hydrochloric acid is highly volatile and is not preferable in terms of safety and workability. The use of nitric acid is not preferred because the nitrogen component increases. The use of an organic acid is not preferable because an organic matter to be oxidized is unnecessarily increased and the cost is increased.
[0018]
In the present invention, you of hydrogen peroxide and a mixture of sulfuric acid to contaminants as the water content I became 5 to 40 wt% of contaminants. This is because if the water content of the contaminant is less than 5% by weight, hydrogen peroxide is not uniformly mixed with the contaminant, and the oxidative decomposition efficiency of the contaminant chemical is deteriorated. A more preferable value of the moisture content of the contaminant is 10 to 40% by weight. If the moisture content of the pollutant exceeds 40% by weight, trouble may occur when the pollutant is backfilled in the ground . The water content of the upper Symbol contaminants can be adjusted by the proportion of water in the hydrogen peroxide solution to be added to the contaminant.
[0019]
In the present invention, it is preferable to further neutralize the obtained purified product. Thereby, it becomes easy to reuse the obtained purified material. Examples of the neutralization treatment method include means for adding an alkaline agent such as calcium hydroxide to the purified product.
[0020]
Further, in the present invention, a modifier can be added to the obtained purified product. Examples of the modifier include a cement-based soil improver (solidifying agent). By adding about 1 to 5% by weight of cement-based modifier to the purified soil, the soil that has become weak due to an increase in water content is returned to the state before purification (for example, with a soil strength of 50 kg / m 2 ). Can be backfilled inside.
[0021]
The method for purifying chemical contaminants according to the present invention is preferably used for purification of soil, sediment, sludge and the like contaminated with organic chlorine compounds, but is not limited thereto. That is, in the purification method of the present invention, organic substances are oxidatively decomposed by hydroxyl radicals having strong oxidizing power generated by contact between the metal catalyst and hydrogen peroxide, so that various organic substances can be efficiently decomposed. Therefore, the purification method of the present invention is not limited to the purification of pollutants by organochlorine compounds (TCE, PCE, dioxins, PCBs, etc.), but also the contamination of other organic substances such as oil, benzene, toluene, xylene, etc. It can also be applied to purification.
[0022]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described with reference to the accompanying drawings. FIG. 1 is a diagram showing an embodiment of the present invention. In the present embodiment, first, the contaminated soil 2 is excavated as shown in FIG. Next, as shown in (b), iron powder 6 is added to the contaminated soil 2 in the kneader 4, and the contaminated soil 2 and the iron powder 6 are uniformly stirred and mixed by the kneader 4. Further, as shown in FIG. 5 (c), a mixed solution 8 of hydrogen peroxide and sulfuric acid is added to the contaminated soil 2 to which the iron powder 6 is added, and the contaminated soil 2 and the mixed solution 8 are uniformly made by the kneader 4. Stir and mix. When the stirring is performed for a certain time (usually about 2 to 60 minutes), the contaminated soil 2 is purified. However, the oxidative decomposition reaction of the contaminated chemical substance proceeds even after the stirring is completed. Thereafter, the purified soil 10 is discharged from the kneader 4 as shown in FIG. Further, as shown in (e), the cementitious soil conditioner 12 is added to the purified soil 10 and mixed, and (f) the purified soil 10 is refilled in the original location as shown in the figure. After the backfilling, the purified soil 10 is covered with a vinyl sheet or the like so that rainwater or the like is not mixed, and the soil is sampled over time to monitor the purification status of polluted chemical substances.
[0024]
【Example】
150 g of soil is put into a 100 mL vial, and iron powder, hydrogen peroxide, etc. are added to the soil under the conditions shown in (1) to (6) below, and trichlorethylene (TCE) is eluted with TCE (headspace of the vial) After injecting so that the concentration of trichlorethylene contained therein was 1 mg / L, the vial was sealed and a treatment experiment was started. Then, the treatment effect was evaluated by measuring the elution TCE concentration of each vial over time by gas chromatography. Of the following conditions (1) to (6) , (3) and (4) are examples of the present invention, and others are comparative examples. Condition (5) is an example in which the order of addition of iron powder and hydrogen peroxide is reversed in the present invention, and condition (6) is an example in which the moisture content of the soil is low.
[0025]
(Experimental conditions)
(1) Blank test 45 mL of water was added to the soil and stirred.
(2) Iron powder reduction method 45 mL of water and 5 g of reduced iron were added to the soil and stirred.
(3) Iron powder + hydrogen peroxide (pH 4)
After adding 45 mL of water and 5 g of iron powder to the soil and stirring, hydrogen peroxide 1000 mg / kg soil and sulfuric acid were added and stirred.
(4) Iron powder + hydrogen peroxide (pH 7)
After 45 mL of water and 5 g of iron powder were added to the soil and stirred, 1000 mg / kg soil of hydrogen peroxide was added and stirred.
(5) Hydrogen peroxide + iron powder (pH 4)
After 45 mL of water and 1000 mg / kg of hydrogen peroxide were added to the soil and stirred, 5 g of iron powder and sulfuric acid were added and stirred.
(6) Iron powder + hydrogen peroxide (pH 4)
To the soil, 4.5 mL of water and 5 g of iron powder were added and stirred, and then 1000 mg / kg of hydrogen peroxide and sulfuric acid and sulfuric acid were added and stirred.
[0026]
(Processing result)
FIG. 2 shows the processing result. In the iron powder reduction method (2) , TCE was gradually reduced and decomposed, but it took several months to purify, and it was confirmed that dichloroethylene and vinyl chloride accumulate as intermediate products. In the present inventions of (3) and (4) , it has become clear that TCE can be purified below the environmental standard value in a short time of 2 hours and 1 day, respectively. From the above treatment results, it became clear that the present invention is extremely effective for short-term purification of contaminated soil. It was also found that the degradation rate of pollutant chemicals is higher under acidic conditions. On the other hand, when the amount of the added drug was the same and hydrogen peroxide was added before the iron powder (5) , TCE was not purified to the environmental standard value. Moreover, when the moisture content of the soil was as low as 3.3% (6) , hydrogen peroxide did not reach the entire soil, and the entire soil could not be purified.
[0027]
【The invention's effect】
As described above, according to the present invention, contaminants contaminated with chemical substances, particularly soil, sediment, sludge, etc. contaminated with organochlorine compounds can be reduced in a short period of several hours to several months. It can be purified at low cost and low energy. In addition, since the present invention utilizes a radical reaction that can efficiently decompose various hardly decomposable chemical substances, it is also effective for purification of high-concentration complex contaminants, and its usefulness is extremely large.
[Brief description of the drawings]
FIG. 1 is a diagram showing an embodiment of the present invention.
FIG. 2 is a graph showing the relationship between the elapsed processing days and the eluted TCE concentration in the purification process of the example.
[Explanation of symbols]
2 Contaminated soil 4 Kneading machine 6 Iron powder 8 Liquid mixture of hydrogen peroxide and sulfuric acid 10 Purified soil 12 Cement-based soil conditioner

Claims (5)

化学物質により汚染された汚染物を浄化するに当たり、汚染物に鉄粉を添加して攪拌した後、汚染物の含水率が5〜40重量%になるように、該汚染物に過酸化水素水と硫酸の混合液を添加して酸性条件下で攪拌することを特徴とする化学物質汚染物の浄化方法。In purifying the pollutant contaminated with the chemical substance, after adding iron powder to the pollutant and stirring, the pollutant is charged with hydrogen peroxide so that the water content of the pollutant becomes 5 to 40% by weight. A method for purifying chemical contaminants, comprising adding a liquid mixture of sulfuric acid and sulfuric acid and stirring under acidic conditions. 汚染物の含水率が10〜40重量%になるように、該汚染物に過酸化水素水と硫酸の混合液を添加して酸性条件下で攪拌することを特徴とする請求項1に記載の化学物質汚染物の浄化方法。 The mixed solution of hydrogen peroxide and sulfuric acid is added to the contaminant so that the moisture content of the contaminant is 10 to 40% by weight, and the mixture is stirred under acidic conditions . Purification method for chemical contaminants. 得られた浄化物をさらに中和処理することを特徴とする請求項1又は2に記載の化学物質汚染物の浄化方法。The method for purifying chemical contaminants according to claim 1 or 2 , wherein the obtained purified product is further neutralized. 得られた浄化物に改質剤を添加することを特徴とする請求項1〜のいずれか1項に記載の化学物質汚染物の浄化方法。The method for purifying chemical contaminants according to any one of claims 1 to 3 , wherein a modifier is added to the obtained purified product. 化学物質により汚染された汚染物が、化学物質により汚染された土壌、底質および汚泥から選ばれることを特徴とする請求項1〜4のいずれか1項に記載の化学物質汚染物の浄化方法。The pollutant contaminated with a chemical substance is selected from soil, sediment and sludge contaminated with a chemical substance, The chemical substance contaminant purification method according to any one of claims 1 to 4, .
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