JP2004154778A - Soil detoxification treatment method - Google Patents
Soil detoxification treatment method Download PDFInfo
- Publication number
- JP2004154778A JP2004154778A JP2003433379A JP2003433379A JP2004154778A JP 2004154778 A JP2004154778 A JP 2004154778A JP 2003433379 A JP2003433379 A JP 2003433379A JP 2003433379 A JP2003433379 A JP 2003433379A JP 2004154778 A JP2004154778 A JP 2004154778A
- Authority
- JP
- Japan
- Prior art keywords
- soil
- iron powder
- weight
- iron
- contaminated
- 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
Links
- 239000002689 soil Substances 0.000 title claims abstract description 85
- 238000000034 method Methods 0.000 title claims abstract description 51
- 238000001784 detoxification Methods 0.000 title claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 84
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000003673 groundwater Substances 0.000 claims abstract description 25
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 14
- 239000002245 particle Substances 0.000 claims abstract description 14
- 150000004045 organic chlorine compounds Chemical class 0.000 claims abstract description 13
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 229910052742 iron Inorganic materials 0.000 abstract description 14
- 239000003638 chemical reducing agent Substances 0.000 abstract description 9
- 229920006395 saturated elastomer Polymers 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 14
- 238000000354 decomposition reaction Methods 0.000 description 13
- 239000003344 environmental pollutant Substances 0.000 description 12
- 231100000719 pollutant Toxicity 0.000 description 12
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 238000000746 purification Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 238000011065 in-situ storage Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000005086 pumping Methods 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 238000009412 basement excavation Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000002680 soil gas Substances 0.000 description 2
- 239000004334 sorbic acid Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- -1 trichloroethylene Chemical class 0.000 description 2
- UOORRWUZONOOLO-OWOJBTEDSA-N (E)-1,3-dichloropropene Chemical compound ClC\C=C\Cl UOORRWUZONOOLO-OWOJBTEDSA-N 0.000 description 1
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- LGXVIGDEPROXKC-UHFFFAOYSA-N 1,1-dichloroethene Chemical group ClC(Cl)=C LGXVIGDEPROXKC-UHFFFAOYSA-N 0.000 description 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- KFUSEUYYWQURPO-UPHRSURJSA-N cis-1,2-dichloroethene Chemical group Cl\C=C/Cl KFUSEUYYWQURPO-UPHRSURJSA-N 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- RAQDACVRFCEPDA-UHFFFAOYSA-L ferrous carbonate Chemical compound [Fe+2].[O-]C([O-])=O RAQDACVRFCEPDA-UHFFFAOYSA-L 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002896 organic halogen compounds Chemical class 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910001562 pearlite Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- UOORRWUZONOOLO-UHFFFAOYSA-N telone II Natural products ClCC=CCl UOORRWUZONOOLO-UHFFFAOYSA-N 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Landscapes
- Fire-Extinguishing Compositions (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
【課題】有機塩素系化合物で汚染された土壌について、地下水水位以下の飽和帯のみならず掘削土壌をも対象として、比較的安価で、かつ従来と比較して少量の鉄材単味で、短期間において常温で無害化処理できる方法を提供する。
【解決手段】鉄粉を還元剤として土壌に高圧媒体と共に地中散布するまたは土木機械等を利用して機械的に混合する等の手段で添加・混合する方法とする。好ましくは、鉄粉は、0.1重量%以上の炭素を含有し、50重量%以上が150μmのふるいを通過する粒度をもち、また、500cm2/g以上の比表面積を有しており、土壌に対して0.1〜10重量%の範囲で添加される方法とする。前記鉄粉として海綿状鉄粉を用いることにより効率的に目的を達成できる。
【選択図】 なし[PROBLEMS] For a soil contaminated with an organochlorine compound, relatively inexpensive and a small amount of iron material in comparison with the conventional one in a short period of time, not only for a saturated zone below the groundwater level but also for excavated soil, And a method capable of detoxifying at room temperature.
A method of adding and mixing iron powder as a reducing agent by means of spraying underground together with a high-pressure medium on soil or mechanically mixing using a civil engineering machine or the like. Preferably, the iron powder contains 0.1% by weight or more of carbon, 50% by weight or more has a particle size passing through a 150 μm sieve, and has a specific surface area of 500 cm 2 / g or more, It is a method of being added in the range of 0.1 to 10% by weight based on the soil. The purpose can be efficiently achieved by using spongy iron powder as the iron powder.
[Selection diagram] None
Description
本発明は、有機塩素系化合物で汚染された土壌の浄化技術に関する。 The present invention relates to a technique for purifying soil contaminated with an organochlorine compound.
半導体工場や金属加工工場等において脱脂溶剤として過去より多量に使用され、使用後排出されあるいは投棄されてきたトリクロロエチレン等有機塩素系化合物が、土壌または地下水を汚染した状態で蓄積され、工場跡地の再利用や周辺地域の土地開発に障害をもたらし、また、その蓄積有機塩素系化合物による地下水の汚染がこの地下水利用上の障害になる等大きな社会問題となっている。 Organochlorine compounds such as trichloroethylene, which have been used in larger quantities as degreasing solvents in semiconductor factories and metal processing factories than ever before and have been discharged or discarded after use, accumulate in soil or groundwater contaminated areas and rebuild the factory site. The use and land development in the surrounding area are hindered, and the contamination of groundwater by the accumulated organochlorine compounds is a major social problem such as an obstacle to the use of the groundwater.
このような有機塩素系化合物による汚染水を鉄系金属還元剤で処理し、汚染物質を分解させ無害化する方法については、例えば、特公平2−49158号公報、特公平2−49798号公報、特許第2636171号公報、特表平5−501520号公報および特表平6−506631号公報に開示されている。 For the method of treating contaminated water with such an organic chlorine-based compound with an iron-based metal reducing agent to decompose and detoxify contaminants, for example, Japanese Patent Publication No. 2-49158 and Japanese Patent Publication No. 2-49798, It is disclosed in Japanese Patent Publication No. 2636171, Japanese Patent Publication No. 5-501520 and Japanese Patent Publication No. 6-506661.
特公平2−49158号公報の方法は、被処理水即ち難分解性ハロゲン化炭化水素含有水をpH6.5〜9.5に調整したのち鉄等卑金属系還元剤により還元処理する方法であり、特公平2−49798号公報の方法は、有機化合物を有する被処理水を金属系還元剤により無害化処理するにあたり、予め被処理水をpH6.5以上とし、還元性物質により酸化還元電位を下げて酸化性物質を除去しておく方法であり、特許第2636171号公報の方法は、有機ハロゲン化合物を含有する汚染水に水素を供給して溶存酸素を除いた後、鉄等金属を担持した活性炭等担体物質に接触させて還元処理を行う方法である。 The method disclosed in Japanese Patent Publication No. 49158/1990 is a method in which water to be treated, that is, water containing hardly decomposable halogenated hydrocarbons is adjusted to pH 6.5 to 9.5 and then reduced with a base metal-based reducing agent such as iron. In the method disclosed in Japanese Patent Publication No. 49798/1990, when water to be treated having an organic compound is rendered harmless by a metal-based reducing agent, the water to be treated is adjusted to pH 6.5 or higher in advance, and the oxidation-reduction potential is reduced by a reducing substance. In the method disclosed in Japanese Patent No. 2636171, hydrogen is supplied to contaminated water containing an organic halogen compound to remove dissolved oxygen, and then activated carbon carrying a metal such as iron. This is a method in which a reduction treatment is carried out by contacting a carrier substance.
また、特表平5−501520号公報の方法は、ハロゲン有機汚染物質による汚染地下水の浄化方法として、酸素が遮断された環境の下で、汚染地下水を鉄粒子等金属体からなる透過性の地中層に通して汚染物質の分解を行わせる方法であり、さらに、特表平6−506631号公報の方法は、同様の汚染地下水の浄化方法として、汚染地下水を地中に形成した活性炭等吸着物質と鉄ヤスリ屑等金属粒子からなる混合物による透過性の層を通過させることで、汚染物質の吸着・分解を行わせる方法である。 The method disclosed in Japanese Patent Application Laid-Open No. 5-501520 discloses a method for purifying contaminated groundwater with halogen organic pollutants in an environment in which oxygen is cut off. This is a method of decomposing pollutants through a middle layer, and the method of Japanese Patent Publication No. Hei 6-506631 discloses a method for purifying contaminated groundwater, which is a method for adsorbing activated carbon such as activated carbon formed in the ground. This is a method in which a contaminant is adsorbed and decomposed by passing through a permeable layer made of a mixture of metal particles such as iron filings and dust.
その他、汚染地下水については、この汚染地下水を土壌外に抽出して無害化処理する真空抽出法や揚水曝気法等があり、また、土壌については、土壌を掘削して加熱処理によって無害化する熱脱着法および熱分解法が知られ、さらにまた、土壌または地下水中の汚染物質を分解して無害化する方法として、微生物を利用したバイオレメディエーション法による浄化法が知られている。
しかしながら、特公平2−49158号公報、特公平2−49798号公報および特許第2636171号公報の発明方法は、いずれも用水あるいは工場排水を処理対象としているもので、汚染地下水の処理には面倒な汚染水の排水作業が前提となり、また、汚染水についてpH調整および他の還元物質や水素ガスの供給等による溶存酸素の除去操作を必要としているので、汚染された土壌または地下水の原位置処理には適用し難く、さらに、鉄還元剤を活性炭等に担持させて用いる等コストの点からも不利な面が多い。 However, the invention methods disclosed in Japanese Patent Publication No. 2-49158, Japanese Patent Publication No. 2-49798 and Japanese Patent No. 2636171 target water or industrial wastewater, and are troublesome for treating contaminated groundwater. It is premised on the drainage of contaminated water, and it is necessary to adjust the pH of contaminated water and remove dissolved oxygen by supplying other reducing substances and hydrogen gas, etc., so that in-situ treatment of contaminated soil or groundwater is required. Is difficult to apply, and there are many disadvantages in terms of cost such as using an iron reducing agent carried on activated carbon or the like.
また特表平5−501520号と特表平6−506631号の発明方法は、地下水を対象とした原位置処理法でもあるが、汚染地域を流れる地下水流による下流域への汚染拡散防止を主な目的としており、汚染地域自体の無害化を目的としたものではない。さらに、金属還元剤を活性炭による吸着剤と併用する、また鉄の層が地下水中の炭酸塩イオンと反応して生成した炭酸鉄(FeCO3 )により閉塞し、そのため定期的に交換を必要とする等コストの点から不利な面が多い。 即ち、有機塩素系化合物で汚染された土壌および土壌中の汚染水の無害化処理に関して、従来の技術の場合、次のような問題があった。 The methods of the inventions of Japanese Patent Application Laid-Open Nos. 5-501520 and 6-506661 are also in-situ treatment methods for groundwater, but mainly for preventing the diffusion of pollution to downstream areas by groundwater flow flowing through the contaminated area. It is not intended to detoxify the contaminated area itself. Furthermore, a metal reducing agent is used in combination with an adsorbent made of activated carbon, and an iron layer is clogged with iron carbonate (FeCO 3 ) generated by reacting with carbonate ions in groundwater, and therefore requires periodic replacement. There are many disadvantages in terms of equal cost. That is, regarding the detoxification treatment of soil contaminated with the organochlorine compound and contaminated water in the soil, the conventional technique has the following problems.
(1) 真空抽出・揚水ばっき等で汚染物質を含む土壌ガス・地下水を地中より抽出、揚水する方法では、土壌ガス、抽出水について汚染物質除去および分解のため活性炭や分解剤を使用するにあたり地上に設備を設け、抽出、揚水して発生した汚染物質を無害化処理を行う等、高コストな別途処理を必要としている。また、土壌そのものを浄化するものでないので、前記したような土地開発上の障害を除く等の目的は達成できず、十分な無害化処理方法とはいえない。 (1) In the method of extracting and pumping soil gas and groundwater containing pollutants from the ground by vacuum extraction and pumping, etc., use activated carbon or a decomposer to remove and decompose pollutants in soil gas and extracted water. Therefore, high-cost separate treatment is required, such as installing facilities on the ground and detoxifying pollutants generated by extraction and pumping. In addition, since the method does not purify the soil itself, it is not possible to achieve the object of eliminating the above-mentioned obstacles in land development and the like, and it cannot be said that this is a sufficient detoxification method.
(2) 鉄等金属系還元剤による地下水浄化法は、飽くまでも地下水を対象とするものであり、汚染地下水の拡散は防げても、土壌自体の汚染を浄化するものではなく、したがって、地下水の水位以上の不飽和帯あるいは掘削後の土壌の浄化に適用できないので、上記方法と同様に十分な無害化処理方法とはいえない。
また、本法は地下水の通過性を良くし、かつ上述したような閉塞の問題を避けるために、粒度の大きい鉄を使用する。そのため反応性が悪く使用量も多くなるためコスト面でも不利がある。
(2) The groundwater purification method using a metal-based reducing agent such as iron is intended for groundwater to the utmost and does not purify the soil itself even if it can prevent the diffusion of contaminated groundwater. Since it cannot be applied to the purification of the unsaturated zone or soil after excavation, it cannot be said to be a sufficient detoxification method as in the above method.
The method also uses large-grain iron to improve groundwater permeability and to avoid the blockage problem described above. For this reason, the reactivity is poor and the amount of use is large, which is disadvantageous in terms of cost.
(3) 掘削土壌を高温で熱分解する方法では、土壌を加熱処理する大がかりな設備が必要であり、かつ土壌粒子自体が熱により変質し、例えば、構造物を支持する、生物を生息させるといった土壌の機能が著しく損なわれるため、処理後の土壌の再利用が難しくなる。 (3) The method of pyrolyzing excavated soil at a high temperature requires large-scale equipment for heat-treating the soil, and the soil particles themselves are altered by heat, such as supporting structures and inhabiting living organisms. Significant loss of soil function makes it difficult to reuse the soil after treatment.
(4) バイオレメディエーション法では、各々の土壌のもつ特性により全ての土壌に適応可能なわけではなく、又、可能であったとしても微生物作用によるため反応が遅く、長期の処理期間を必要としている。 (4) The bioremediation method cannot be applied to all soils due to the characteristics of each soil, and even if possible, the reaction is slow due to the action of microorganisms and requires a long treatment period. .
従って、本発明は、地下水水位以下の飽和帯の土壌のみならず、掘削後の土壌を含む土壌などを処理対象とすることができ、有機塩素系化合物で汚染された土壌について比較的安価な鉄材のみの還元剤により、短期間で、且つ、常温で汚染物質を分解できる土壌の無害化処理方法の提供を目的とする。 Therefore, the present invention can treat not only soil in the saturated zone below the groundwater level but also soil including excavated soil and the like, and relatively inexpensive iron material for soil contaminated with organochlorine compounds. An object of the present invention is to provide a method for detoxifying soil, which can decompose pollutants in a short period of time and at room temperature using only a reducing agent.
この目的を達成するため、本発明は、地下水水位より深部に位置する土壌又は掘削された土壌であり且つ有機塩素系化合物で汚染された土壌に、鉄粉を添加・混合することにより、前記有機塩素化合物を分解して土壌を浄化する土壌の無害化処理方法を、また、前記鉄粉は、0.1重量%以上望ましくは0.2重量%以上の炭素を含むところの土壌の無害化処理方法を、もしくは、前記鉄粉は、0.1重量%以上望ましくは0.2重量%以上の炭素を含み且つ500cm2 /g以上望ましくは2,000cm2 /g以上の比表面積を有すると共に50重量%以上が150μmのふるいを通過する粒度を有し、前記土壌に対して0.1〜10重量%の範囲内で添加されるところの土壌の無害化処理方法を、そしてまた、前記鉄粉が海綿状鉄粉であるところの土壌の無害化処理方法を提供する。 In order to achieve this object, the present invention provides a method for adding and mixing iron powder to soil located deeper than the groundwater level or excavated soil and contaminated with an organochlorine compound. A method for detoxifying a soil, wherein the soil is purified by decomposing a chlorine compound, and wherein the iron powder contains 0.1% by weight or more, preferably 0.2% by weight or more of carbon. the method, or the iron powder, is desirable and 500 cm 2 / g or more include preferably at least 0.2 wt% carbon 0.1% by weight or more and has a higher specific surface area 2,000 cm 2 / g 50 A method for detoxifying a soil, wherein at least about 10% by weight of the iron powder has a particle size passing through a sieve of 150 μm and added in a range of 0.1 to 10% by weight to the soil; Is spongy iron powder To provide a detoxification method of soil of a certain place.
本発明によれば従来方法では処理対象外となっていた有機塩素系化合物で汚染された土壌について、地下水水位以下の飽和帯の土壌のみならず掘削土壌をも対象とし、鉄粉の炭素成分、形状、寸法を規制し、また、土壌への添加量を規制するのみで、比較的安価で、かつ従来と比較して少量の鉄粉単味の添加混合という簡便な常温処理方法により、短期間で環境への影響のない状況にまで汚染物質を分解し無害化できるという効果が得られる。さらに、鉄粉として海綿状鉄粉を利用することで、前記効果を容易に得ることができる。 According to the present invention, in the conventional method, the soil contaminated with the organochlorine compound which has been excluded from the treatment, not only the soil in the saturated zone below the groundwater level but also the excavated soil, the carbon component of the iron powder, It is relatively inexpensive only by controlling the shape and dimensions and the amount added to the soil. Thus, the effect that the pollutant can be decomposed and made harmless to a state where there is no influence on the environment can be obtained. Further, by using spongy iron powder as the iron powder, the above effect can be easily obtained.
本発明は、ジクロロメタン、四塩化炭素、1,2−ジクロロエタン、1,1−ジクロロエチレン、シス−1,2−ジクロロエチレン、1,1,1−トリクロロエタン、1,1,2−トリクロロエタン、トリクロロエチレン、テトラクロロエチレン、1,3−ジクロロプロペンなどの揮発性有機塩素系化合物や、PCB、ダイオキシン類などの有機塩素系化合物により汚染された土壌を浄化の対象とし、これらの有機塩素系化合物を、脱塩素あるいは脱塩化水素作用により分解させ無害化することを特徴としている。 The present invention relates to dichloromethane, carbon tetrachloride, 1,2-dichloroethane, 1,1-dichloroethylene, cis-1,2-dichloroethylene, 1,1,1-trichloroethane, 1,1,2-trichloroethane, trichloroethylene, tetrachloroethylene, Soil contaminated with volatile organic chlorinated compounds such as 1,3-dichloropropene and organic chlorinated compounds such as PCBs and dioxins is the object of purification, and these organic chlorinated compounds are dechlorinated or dechlorinated. It is characterized by being decomposed and rendered harmless by the action of hydrogen.
汚染土壌の浄化に用いる鉄粉は、炭素量が0.1重量%以上であり、殆どの普通鋼成分及び普通鋳鉄成分のものが含まれる。炭素量が0.1重量%より低いと汚染物質の分解速度が遅くなり実用的ではない。また、鉄粉の粒度は目開き150μmのふるいを全体の50重量%以上が通過するように調整されたものを用いる。これより粗い粒度の鉄粉を用いれば、汚染物質の分解速度が低下すると共に、鉄粉の利用効率が低下し、より多くの鉄粉添加量を強いられるため、経済的に不利となる。 The iron powder used for the purification of the contaminated soil has a carbon content of 0.1% by weight or more, and includes most ordinary steel components and ordinary cast iron components. If the amount of carbon is lower than 0.1% by weight, the decomposition rate of the pollutants becomes slow, which is not practical. The particle size of the iron powder is adjusted so that 50% by weight or more of the iron powder passes through a sieve having an opening of 150 μm. If iron powder having a coarser particle size is used, the decomposition rate of pollutants is reduced, the utilization efficiency of iron powder is reduced, and a larger amount of iron powder must be added, which is economically disadvantageous.
土壌に添加する鉄粉の形状としては、汚染物質との接触面積を大として反応効率を高める点から比表面積が500cm2 /g以上のものが用いられるが、このような比表面積の大きいものは海綿状鉄(スポンジ鉄)によって容易に得ることができる。また、同時に鉄粉としては、汚染物質との反応性を高める点で、結晶成長度が低く、結晶構造としてパーライト組織が存在するものが望ましい。
土壌への鉄粉の添加量は、土壌の湿重量に対して、0.1〜10重量%の範囲とする。0.1重量%よりも添加量が少ないときには分解速度が著しく低下し、10重量%以上の多量の添加量では、経済的に不利となる。
As the shape of the iron powder to be added to the soil, a powder having a specific surface area of 500 cm 2 / g or more is used from the viewpoint of increasing the contact area with the pollutant and increasing the reaction efficiency. It can be easily obtained by sponge iron (sponge iron). At the same time, the iron powder desirably has a low crystal growth degree and has a pearlite structure as a crystal structure in order to enhance the reactivity with contaminants.
The amount of iron powder added to the soil is in the range of 0.1 to 10% by weight based on the wet weight of the soil. When the amount added is less than 0.1% by weight, the decomposition rate is remarkably reduced, and when the amount added is 10% by weight or more, it is economically disadvantageous.
鉄粉を土壌に添加して混合するには、原位置処理の場合、空気または水等による高圧媒体を利用して地中に散布する方法または地盤改良工事で利用される土木機械を用いて機械的に掘削混合する方法がとられる。掘削処理の場合は、ニーダー、ミキサー、ブレンダー等の混合装置の利用も可能である。 To add iron powder to the soil and mix it, in the case of in-situ treatment, use a high-pressure medium such as air or water to spray it into the ground, or use a civil engineering machine used in ground improvement work The method of excavation and mixing is adopted. In the case of excavation processing, it is also possible to use a mixing device such as a kneader, a mixer or a blender.
なお、鉄粉は表面が酸化されることで徐々に不働態化して反応力が低下するので、鉄粉による汚染物質の分解作用を助けるために、鉄粉を混合した後の土壌に対して新たな酸素あるいは酸化性物質の供給が行われないように注意する必要がある。即ち、原位置処理または掘削後処理において、土壌表面が新たな外気と直接接触しないようにすることが望ましい。 Since the surface of the iron powder is gradually passivated as the surface is oxidized and its reaction force is reduced, in order to assist the decomposition of pollutants by the iron powder, the soil after the mixing of the iron powder is newly added to the soil. Care must be taken not to supply any oxygen or oxidizing substances. That is, it is desirable that the soil surface does not come into direct contact with fresh air in the in-situ processing or the post-digging processing.
以上のような土壌処理を行うことにより、2〜3か月で土壌の汚染に係る環境基準(平成3年8月23日環告、改正、平5環告19、平6環告5・環告25、平成7年環告19)以下まで土壌を無害化することができる。 By performing the above-mentioned soil treatment, the environmental standards for soil pollution can be achieved in two to three months (Announcement on August 23, 1991, amendment, Hei 5 Announcement 19, Hei 6 Announcement 5 Soil can be rendered harmless up to the following levels:
実施例1〜4のサンプルの調整は、内径100mm×高さ500mmの塩化ビニル製の光を透さない容器に、トリクロロエチレンで汚染された土壌と所定割合の鉄粉とを混合して作成した試料を封入した。さらに容器下部から150mmまでは蒸留水を添加して地下水水位以下の土壌に相当する飽和帯を再現した。 The samples prepared in Examples 1 to 4 were prepared by mixing soil contaminated with trichlorethylene and a predetermined ratio of iron powder in a light-impermeable container made of vinyl chloride having an inner diameter of 100 mm and a height of 500 mm. Was enclosed. Distilled water was further added from the bottom of the vessel to 150 mm to reproduce a saturated zone corresponding to soil below the groundwater level.
試料は、前もって予定されるサンプルの数だけ容器を用意して作成し、所定期間常温で放置した後、各容器ごとにサンプリングを行った。サンプルは筒型のサンプラーを用いて容器最上部から最下部まで棒状に採取したので、サンプル中には、飽和帯土壌と不飽和帯土壌の両方が含まれている。
鉄粉は同和鉄粉工業(株)製、海綿状鉱石還元鉄粉(E−200)を原料として還元精製、焼結、粉砕、ふるい分けの操作により所定の物性値に調整したものを用いた。
Samples were prepared by preparing containers in a number equal to the number of samples expected in advance, and after being left at room temperature for a predetermined period, sampling was performed for each container. Since the sample was collected in a rod shape from the top to the bottom of the container using a cylindrical sampler, the sample contained both saturated zone soil and unsaturated zone soil.
As the iron powder, a sponge ore-reduced iron powder (E-200) manufactured by Dowa Iron Powder Co., Ltd. was used as a raw material and adjusted to predetermined physical properties by reduction, sintering, pulverization, and sieving operations.
トリクロロエチレンの分析方法について、今回は当該鉄粉が有機塩素化合物を分解している状況をより完全に把握するため環境基準に準拠した方法ではなく、土壌中の水分含有量を測定し、土壌乾量に対するトリクロロエチレン濃度を求める方法によった(本方法は、社団法人日本環境測定分析協会発行「環境と測定技術」Vol.16,No.15,1989,31-34に記載の方法に準ずる)。 Regarding the analysis method of trichlorethylene, this time it is not a method that complies with environmental standards in order to more fully grasp the situation in which the iron powder is decomposing organic chlorine compounds, but the moisture content in soil is measured and the soil dryness is measured. (This method is based on the method described in "Environment and Measurement Technology" Vol. 16, No. 15, 1989, 31-34, published by the Japan Society for Environmental Measurement and Analysis).
尚、土壌環境基準は土壌重量の10倍量の水への溶出値(mg/l)で示される。よって、土壌環境基準値(mg/l)の10倍値以下の含有量値(mg/kg)であれば土壌環境基準を満たすと判断できる。 In addition, the soil environmental standard is indicated by an elution value (mg / l) of 10 times the soil weight in water. Therefore, if the content value (mg / kg) is 10 times or less the soil environment standard value (mg / l), it can be determined that the soil environment standard is satisfied.
[実施例1]鉄粉の粒度を変えて土壌中のトリクロロエチレンの分解状況を調べた。
鉄粉には、炭素含有量が0.2重量%、比表面積が2,000cm2 /gのものを用い、土壌に対する添加量を0.2重量%とし、土壌に鉄粉を加えなかった場合と、土壌に50重量%以上が300μmのふるいを通過する粒度の鉄粉を加えた場合と、土壌に50重量%以上が150μmのふるいを通過する粒度の鉄粉を加えた場合とについてトリクロロエチレンの分解状況を調べた。
結果を表1に示した。
Example 1 The state of decomposition of trichlorethylene in soil was examined by changing the particle size of iron powder.
Iron powder having a carbon content of 0.2% by weight and a specific surface area of 2,000 cm 2 / g was used, and the amount added to the soil was 0.2% by weight, and iron powder was not added to the soil. And the case where 50% by weight or more of iron powder having a particle size passing through a sieve of 300 μm is added to the soil, and the case where 50% by weight or more of iron powder having a particle size passing through a sieve of 150 μm is added to the soil. The decomposition situation was examined.
The results are shown in Table 1.
〔実施例2〕鉄粉の土壌への添加割合を変えてトリクロロエチレンの分解状況を調べた。
鉄粉は、炭素含有量が0.2重量%、比表面積は2,000cm2/gのものとし、粒度としては、50重量%以上が150μmのふるいを通過するものを用い、鉄粉を土壌に添加しない場合と、鉄粉を0.03重量%、0.1重量%及び1.0重量%の割合で添加した場合についてトリクロロエチレンの分解状況を調べた。
結果を表2に示した。
[Example 2] Decomposition of trichlorethylene was examined by changing the addition ratio of iron powder to soil.
The iron powder has a carbon content of 0.2% by weight, a specific surface area of 2,000 cm 2 / g, and a particle size of 50% by weight or more passes through a 150 μm sieve. The decomposition state of trichlorethylene was examined when no iron powder was added and when iron powder was added at a ratio of 0.03% by weight, 0.1% by weight and 1.0% by weight.
The results are shown in Table 2.
〔実施例3〕鉄粉の炭素含有量を変えてトリクロロエチレンの分解状況を調べた。
鉄粉には、比表面積が2,000cm2 /gのものを用い、土壌に対する添加割合を0.2重量%とし、粒度としては50重量%以上が150μmのふるいを通過するものを用い、炭素含有量が0.005重量%、0.05重量%、0.1重量%及び0.2重量%の鉄粉について、トリクロロエチレンの分解状況を調べた。
結果を表3に示した。
Example 3 The decomposition state of trichlorethylene was examined by changing the carbon content of iron powder.
Iron powder having a specific surface area of 2,000 cm 2 / g is used. The proportion of the iron powder added to the soil is 0.2% by weight. The particle size of 50% by weight or more passes through a 150 μm sieve. The decomposition state of trichlorethylene was examined for iron powders having contents of 0.005% by weight, 0.05% by weight, 0.1% by weight and 0.2% by weight.
The results are shown in Table 3.
〔実施例4〕単位重量当たりの表面積即ち比表面積の異なる鉄粉についてトリクロロエチレンの分解状況を調べた。
鉄粉には、炭素含有量が0.2重量%で、粒度としては50重量%以上が150μmのふるいを通過する粒度分布のものを用い、土壌への添加割合は0.2重量%とし、鉄粉の比表面積を300cm2/g、500cm2/gおよび2,000cm2/gとした場合のトリクロロエチレンの分解状況を調べた。
結果を表4に示した。
[Example 4] The decomposition state of trichlorethylene was examined for iron powders having different surface areas per unit weight, that is, different specific surface areas.
Iron powder having a carbon content of 0.2% by weight and a particle size distribution of 50% by weight or more passing through a 150 μm sieve with a particle size of 0.2% by weight is used as the iron powder. the specific surface area of 300 cm 2 / g of iron powder, was examined degradation status of trichlorethylene in the case of a 500 cm 2 / g and 2,000 cm 2 / g.
The results are shown in Table 4.
以上のように、有機塩素化合物分解に必要な鉄粉とは、鉄粉中の炭素含有量が0.1重量%以上で、150μmのふるいを50重量%以上が通過する粒度分布を有し、比表面積としては500cm2/g以上特には2,000cm2/g以上で、且つ、土壌に対して土壌の0.1重量%乃至10重量%の割合で添加することにより従来には見られない顕著な効果を得ることができたものである。 As described above, iron powder necessary for decomposing organochlorine compounds has a particle size distribution in which the carbon content of iron powder is 0.1% by weight or more and 50% by weight or more passes through a 150 μm sieve, in a specific surface area 500 cm 2 / g or more and particularly 2,000 cm 2 / g or more and not found in the prior art by the addition in a proportion of 0.1 wt% to 10 wt% of the soil with respect to the soil A remarkable effect was obtained.
〔参考例〕土壌の含水率(%)の違いによるトリクロロエチレンの分解状況
乾燥状態の異なる不飽和帯土壌を再現した試験を行った。
100mlガラスバイアルびんに、乾燥土壌:40g、トリクロロエチレン4g、鉄粉E−200:1gおよび添加量を変化させて水を加え混合した後放置し、ヘッドスペース中のTCE濃度変化を測定した。
[Reference Example] Decomposition state of trichlorethylene due to difference in moisture content (%) of soil A test was conducted in which unsaturated zone soils with different dry conditions were reproduced.
In a 100 ml glass vial, dry soil: 40 g, trichlorethylene 4 g, iron powder E-200: 1 g, water was added in varying amounts and mixed, and the mixture was allowed to stand. The change in TCE concentration in the headspace was measured.
従来方法では処理対象外となっていた有機塩素系化合物で汚染された土壌について、地下水水位以下の飽和帯の土壌のみならず掘削土壌をも対象とし、汚染物質を分解し無害化できる。 With regard to soil contaminated with organochlorine compounds, which has not been treated in the conventional method, not only soil in the saturated zone below the groundwater level but also excavated soil can be used to decompose pollutants and render them harmless.
Claims (4)
The method for detoxifying soil according to any one of claims 1 to 3, wherein the iron powder is spongy iron powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003433379A JP2004154778A (en) | 1997-12-19 | 2003-12-26 | Soil detoxification treatment method |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP36526097 | 1997-12-19 | ||
| JP2003433379A JP2004154778A (en) | 1997-12-19 | 2003-12-26 | Soil detoxification treatment method |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP36717797A Division JP3862394B2 (en) | 1997-12-19 | 1997-12-25 | Detoxification method of soil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2004154778A true JP2004154778A (en) | 2004-06-03 |
Family
ID=32827278
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2003433379A Pending JP2004154778A (en) | 1997-12-19 | 2003-12-26 | Soil detoxification treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2004154778A (en) |
-
2003
- 2003-12-26 JP JP2003433379A patent/JP2004154778A/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US10737959B2 (en) | Compositions for removing hydrocarbons and halogenated hydrocarbons from contaminated environments | |
| JP3862394B2 (en) | Detoxification method of soil | |
| JP4069174B2 (en) | Detoxification method of soil | |
| US20090090677A1 (en) | Method of treating organic compounds in groundwater | |
| JPWO2000029137A1 (en) | Soil detoxification method | |
| US20030083195A1 (en) | Iron powder for remediation and method for remediating soil, water, or gas | |
| CA2362002C (en) | Remediation method of media and iron powder for dehalogenation of hydrogenated hydrocarbons | |
| JP4377657B2 (en) | Organochlorine compound removing agent and organochlorine compound removing method | |
| US20070241063A1 (en) | Process for treating water using atomized ferrous powders containing 0.25 to 4 wt% carbon and 1 to 6 wt% oxygen | |
| JP4482678B2 (en) | Detoxification method of soil | |
| JP3516613B2 (en) | Contaminated groundwater purification method | |
| JP2004154778A (en) | Soil detoxification treatment method | |
| JP4127102B2 (en) | Detoxification method for workpieces contaminated with organic halogen compounds | |
| JP4660958B2 (en) | Purification of soil, water and gas contaminated with organochlorine compounds | |
| JP5109036B2 (en) | Detoxification method of soil | |
| JP2004305235A (en) | Detoxification treatment method for objects contaminated with organic halogen compounds | |
| KR100638765B1 (en) | Permeation reaction wall for removing chlorine-based organic contaminants using steelmaking slag / cement paste / 2 valent iron and its removal method | |
| JP2002159960A (en) | Soil detoxification method and iron powder material for decomposing organic halogen compounds | |
| JP4126347B2 (en) | Purification method of contaminated soil or contaminated water | |
| JP4786936B2 (en) | Organohalogen compound treatment material | |
| JP2002166171A (en) | Iron powder for decomposing organic halogen compounds and method for detoxifying contaminated soil, groundwater and gas | |
| JP2006075773A (en) | Purification method of contaminated soil groundwater with persistent organic compounds | |
| JP2004243226A (en) | How to prevent leaching of pollutants | |
| JP2011156453A (en) | In-situ cleaning method of contaminated soil and contaminated underground water | |
| JP2004283650A (en) | Soil or groundwater purification method and contaminated water treatment method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20040225 |
|
| RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20040206 |
|
| RD04 | Notification of resignation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7424 Effective date: 20040318 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20060420 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20060516 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20060718 |
|
| A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20061003 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20061204 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20061220 |
|
| A911 | Transfer to examiner for re-examination before appeal (zenchi) |
Free format text: JAPANESE INTERMEDIATE CODE: A911 Effective date: 20070110 |
|
| A912 | Re-examination (zenchi) completed and case transferred to appeal board |
Free format text: JAPANESE INTERMEDIATE CODE: A912 Effective date: 20070223 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20090702 |
|
| A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A712 Effective date: 20100810 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20100810 |