JP2005021873A - Cleaning method for contaminated soil - Google Patents

Cleaning method for contaminated soil Download PDF

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JP2005021873A
JP2005021873A JP2003289376A JP2003289376A JP2005021873A JP 2005021873 A JP2005021873 A JP 2005021873A JP 2003289376 A JP2003289376 A JP 2003289376A JP 2003289376 A JP2003289376 A JP 2003289376A JP 2005021873 A JP2005021873 A JP 2005021873A
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soil
contaminated soil
purification
cleaning liquid
zeolite powder
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Kazuhide Notake
和秀 野竹
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SHINANO KENSETSU KK
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SHINANO KENSETSU KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a cleaning method for contaminated soil where artificial zeolite powder maintaining required performance is dispersed and mixed into water so as to be a cleaning liquid, the liquid is penetrated and diffused into gaps between contaminated soil, and the contaminated soil can easily be purified at a low cost. <P>SOLUTION: This cleaning method for contaminated soil comprises: the survey of the soil of a land to be cleaned; an excavation stage of excavating cleaning liquid injection holes at uniform intervals and a required hole size and a depth on the whole face of the contaminated soil by a boring machine; and a cleaning liquid injection stage where a cleaning liquid is penetrated and diffused into the gaps between the contaminated soil through the insides of the cleaning liquid injection holes under a required injection pressure by using an injection tube. The cleaning method further comprises a backfilling stage where the soil is subjected to backfilling by using the cleaning liquid consisting of the artificial zeolite powder mixed in the weight ratio of 10 to 35% to water, and having a particle diameter of ≤30 μm and a specific surface area of ≥100 m<SP>2</SP>/g, and whose volume (meq/100g) expressed in terms of a base is ≥200 mg, and cleaning packed sand blended with 10 to 35 wt.% artificial zeolite powder based on the excavated and discharged sand through the cleaning liquid injection holes. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

発明の詳細な説明Detailed Description of the Invention

産業上の利用分野Industrial application fields

本発明は汚染されてなる土壌を、現位置において簡便且安価に浄化できる汚染土壌の浄化工法に関するものである。  The present invention relates to a contaminated soil purification method capable of purifying contaminated soil simply and inexpensively at the current position.

従来技術Conventional technology

我が国では産業規模の拡大と且化学工業の発達とが相俟って、著しい経済成長がなされてきたものの、産業規模の拡大に伴い多量の煤煙や廃水が排出されつづけられ且廃棄物の廃棄がなされてきており、とりわけ化学工業の発達に伴う多量の化学物質の排出や廃棄により大気や水はもとより土壌に至る環境全体が著しく汚染化されており、既に数多の健康被害が惹起されるに至っている。  In Japan, the expansion of the industrial scale and the development of the chemical industry have led to remarkable economic growth, but with the expansion of the industrial scale, a large amount of soot and wastewater continues to be discharged, and waste disposal In particular, the entire environment, including the atmosphere and water as well as the soil, has been significantly polluted due to the discharge and disposal of large amounts of chemical substances accompanying the development of the chemical industry, and many health hazards have already been caused. Has reached.

そして土壌においては一旦化学物質等で汚染された場合には大気や水とは異なり自然浄化作用が働かず蓄積が逐次増長されてきたため、既にその汚染度合は極限にまで至っており各地で地下水の著しい汚染も頻発している。
これがため近年に至っては汚染土壌の浄化が重要な課題として提起され、土地取引きにおける汚染土壌の浄化義務の指導や、更には汚染土地に対する評価見直しもなされるに至っている。
And once soil has been contaminated with chemical substances, the natural purification action does not work unlike air and water, and the accumulation has been gradually increased. Contamination is also frequent.
For this reason, in recent years, the purification of contaminated soil has been raised as an important issue, and guidance on the obligation to purify contaminated soil in land transactions and the evaluation of contaminated land have been reviewed.

而して汚染土壌の浄化手段としては、従来広大な汚染土壌においては現位置における浄化が、更に狭少な土壌で且汚染度合の激しい汚染土壌においては汚染土壌を掘削搬出のうえ高温度処理や化学処理による浄化をなしえるうえ再搬入し埋戻すことが好適とされていたものであるが、近年に至っては一段と都市化が進んでいるため、仮令汚染土壌を掘削搬出させる場合にも都市近郊には該汚染土壌を浄化するための立地条件やスペース等も殆んど無く、従って遠隔地への搬出と浄化処理及び再搬入をなさねばならず、莫大な労力並びに費用が強いられる結果となる。  Thus, as a means of remediating contaminated soil, the conventional method is to remediate the vastly contaminated soil, and in the case of a more narrow and highly contaminated contaminated soil, the contaminated soil is excavated and transported and treated with high temperature treatment or chemical treatment. In addition to being able to purify by treatment, it is considered suitable to be re-imported and backfilled.However, since urbanization has further progressed in recent years, even when excavating and transporting temporarily contaminated soil, There is almost no site conditions or space for purifying the contaminated soil, and therefore, it must be carried out to a remote place, cleaned and re-introduced, resulting in enormous labor and cost.

更に現位置浄化方法においても、ボーリングによる地下水面より上の不飽和帯に吸引井戸を設置し、真空ポンプやブロワーで減圧にして汚染物の蒸気を吸引し且該汚染物の蒸気を活性炭で吸着させ或いは紫外線で分解させる土壌ガス吸引法を初め、複数の円注状にボーリング掘削のうえ土壌中に特殊セメント等の不溶化・固化剤を注入する固化・不溶化方法や、A重油等の汚染土壌を珪酸ナトリウム水溶液中に流動させて洗浄する土壌洗浄方法、鉱物類により六価クロムの還元安定化処理及び還元剤として硫酸第一鉄(FeSO)を用いて六価クロムを還元不溶化処理後にベントナイトを用いて土壌改良する還元処理方法、或いは土壌中に電極を挿入しイオン性の汚染物質を移動後分解する電気的分離方法等々が知られている。Furthermore, in the in-situ purification method, a suction well is installed in the unsaturated zone above the groundwater surface by boring, and the vapor of the pollutant is sucked by reducing the pressure with a vacuum pump or blower, and the vapor of the pollutant is adsorbed by activated carbon. In addition to soil gas suction method, which is decomposed by ultraviolet rays, or by drilling in multiple circular shapes, solidification / insolubilization methods such as injecting special cement or other insolubilizing / solidifying agent into soil, and contaminated soil such as heavy oil A A soil washing method in which it is washed by flowing it in an aqueous solution of sodium silicate, a reduction stabilization treatment of hexavalent chromium with minerals, and a hexagonal chromium after reduction insolubilization treatment using ferrous sulfate (FeSO 4 ) as a reducing agent. There are known reduction treatment methods that improve the soil by using them, or electrical separation methods in which electrodes are inserted into the soil and ionic pollutants are transferred and then decomposed.

然るにこれら公知方法は、その実施に際して工事規模が大掛かりとなるばかりか、高度の専門技術や機械類も要請されるとともに浄化費用も莫大となるため、公共事業の如く特別な予算措置等を講ぜぬ限りは一般民間の汚染土壌の浄化には適用され難く、而も浄化の効果も十分に確認されるまでには至っていない。  However, these publicly known methods not only require a large scale of construction, but also require sophisticated technical skills and machinery and enormous purification costs. As long as it is difficult to apply to the purification of contaminated soil in the general private sector, the effect of the purification has not been fully confirmed.

本発明はかかる実情に鑑み研究を重ねた。近年に至り石炭灰等の産業廃棄物を用いて膨大数の微細孔隙を有し吸着性や吸湿吸水性に優れ、更には大きな塩基置換容量(meq/100g)を付与せしむる人工ゼオライト粉体が比較的安価に量産可能となったこと、及び該人工ゼオライト粉体の粒径を30μm以下の微粒状となし接触表面積率が極めて大きく且物理的吸着容量並びに吸湿、吸水容量の大きなものが好適であることから、その比表面積においては少なくとも100m/g以上で而も吸着される重金属類や有機化合物を吸着固定し若しくは吸着分解させる上からは、その本来的に保持する触媒作用に加えて強い塩基置換性が要請されるため塩基置換容量(meq/100g)において少なくとも200mg以上の人工ゼオライト粉体を用い、この人工ゼオライト粉体を蓄積されてなる土壌汚染物質たる重金属類や有機化合物と有効に接触させるため、水に対して10乃至35%重量割合で混合分散させて浄化液となしたるうえ、汚染土壌の間隙内に加圧注入させて浸透拡散させることにより、簡便且安価に汚染浄化がなしえることを究明し本発明に至った。The present invention has been studied in view of such circumstances. Artificial zeolite powder that has a large number of fine pores using industrial waste such as coal ash, has excellent adsorptivity and hygroscopic water absorption, and gives a large base substitution capacity (meq / 100 g). Is suitable for mass production at relatively low cost, and the artificial zeolite powder has a particle size of 30 μm or less, a very large contact surface area, and a large physical adsorption capacity, moisture absorption and water absorption capacity. Therefore, in terms of adsorbing, fixing or decomposing heavy metals and organic compounds which are adsorbed at a specific surface area of at least 100 m 2 / g or more, in addition to their inherently retained catalytic action, Since strong base substitution is required, at least 200 mg of artificial zeolite powder is used in the base substitution capacity (meq / 100 g), and this artificial zeolite powder is stored. In order to make effective contact with the heavy metals and organic compounds that are the soil pollutants that are accumulated, they are mixed and dispersed at a rate of 10 to 35% by weight with respect to water to form a cleaning solution, and added to the gaps in the contaminated soil. The inventors of the present invention have found that contamination can be purified easily and inexpensively by pressure injection and osmotic diffusion.

発明が解決しようとする課題Problems to be solved by the invention

本発明は所要の性能を保持する人工ゼオライト粉体を水に混合分散せしめて浄化液となしたるうえ、汚染土壌の間隙内に浸透拡散させ、以って簡便で安価に且優れた浄化を実現できる汚染土壌の浄化工法を提供することにある。  In the present invention, artificial zeolite powder having the required performance is mixed and dispersed in water to obtain a purification solution, and it is permeated and diffused into the gaps in the contaminated soil, thereby allowing simple, inexpensive and excellent purification. It is to provide a method for purifying contaminated soil that can be realized.

課題を解決するための手段Means for solving the problem

上述の課題を解決するために本発明が用いた技術的手段は、浄化すべき土地の適宜位置をボーリングし、土壌の汚染状態や汚染分布及び土壌の間隙率を調査し、この土壌調査に基づき汚染土壌全面に亘って均等な間隔で且所要の孔径と深さの浄化液注入孔をボーリングマシンで掘削する掘削工程と、それぞれの浄化液注入孔内にボーリングマシン掘削ロッド内に配備されてなる浄化液注入口より所要の注入圧力及び注入量を以って汚染土壌間隙内に浸透拡散させて浄化液を汚染物質と接触させる浄化液注入工程と、水に対して10乃至35%重量割合で混合分散され、且その粒径が30μm以下で比表面積が100m/g以上及び塩基置換容量(meq/100g)が200mg以上の人工ゼオライト粉体からなる浄化液と、この浄化液が浸透拡散された浄化液注入孔内に、該浄化液注入孔の掘削に際して排出された土壌に人工ゼオライト粉体を10乃至35%重量割合で配合させた浄化充填土により埋戻しをなす埋戻し工程とからなる構成に存する。The technical means used by the present invention in order to solve the above-mentioned problems are to drill the appropriate position of the land to be cleaned, investigate the soil contamination state, contamination distribution and soil porosity, and based on this soil survey. A drilling process in which a cleaning liquid injection hole having a required hole diameter and depth is excavated at a uniform interval over the entire contaminated soil with a boring machine, and each cleaning liquid injection hole is provided in a drilling rod for a drilling machine. A purification liquid injection step of infiltrating and diffusing into the contaminated soil gap with a required injection pressure and injection amount from the purification liquid injection port, and bringing the purification liquid into contact with the pollutant, and 10 to 35% by weight with respect to water A purification solution comprising an artificial zeolite powder mixed and dispersed and having a particle size of 30 μm or less, a specific surface area of 100 m 2 / g or more, and a base substitution capacity (meq / 100 g) of 200 mg or more; The backfilling step of backfilling with the purified filling soil in which the artificial zeolite powder is mixed in the soil discharged at the time of excavation of the purified solution injection hole in the permeated and diffused purified solution injection hole in a proportion of 10 to 35% by weight. It exists in the composition which consists of.

更に浄化液中の人工ゼオライト粉体の分散を一段と高めて汚染土壌間隙内への浸透拡散を促進させるうえから、浄化液中にカチオン界面活性剤が0.5乃至5.0%重量割合で混合させてなる構成、並びに腐触土や粘土等微粒土壌に強固に付着した汚染物質を凝集剥落させて吸着固定若しくは吸着分解させるうえから、浄化液中に硫酸カルシウムが0.5乃至5.0%重量割合で混合された構成、及び浄化液が汚染土壌間隙内に浸透拡散され埋立しされた汚染土壌表面全体に亘って所要量の浄化液を散水浸透せしめて、汚染土壌表面の確実な浄化と且浄化液注入孔埋戻しの締固めを図る構成に存する。  Furthermore, in order to further enhance the dispersion of artificial zeolite powder in the cleaning solution and promote the permeation and diffusion into the contaminated soil gap, a cationic surfactant is mixed in the cleaning solution in an amount of 0.5 to 5.0% by weight. In addition to coagulating and peeling off the contaminants firmly attached to fine soils such as rust and clay, and adsorbing and fixing or decomposing them, 0.5 to 5.0% of calcium sulfate is contained in the purification solution. The composition mixed by weight ratio, and the cleaning solution penetrates and diffuses into the contaminated soil gap, and the necessary amount of the cleaning solution is sprayed over the entire contaminated soil surface. And it exists in the structure which aims at compacting of a cleaning liquid injection hole backfill.

作用Action

本発明はかかる構成を用いてなるため以下のような作用を有する。即ち浄化に先立ってボーリングにより土壌調査がなされるため汚染物質と汚染状態や汚染分布及び汚染土壌の間隙率が確認されるため、使用する浄化液の人工ゼオライト粉体の混合割合並びに適正粘度が判別でき、且注入圧力及び注入量も判別できる。
そして汚染土壌全面に亘ってボーリングマシンにより均等な間隔で且所要の孔径と深さを以って浄化液注入孔が掘削され、且それぞれの浄化液注入孔内にはボーリングマシン掘削ロッド先端に配備された浄化液注入口より所要の注入圧力で掘削密閉状の浄化液注入孔内で浄化液を注入させることにより、該浄化液は浄化液注入孔を中心として所要の放射状範囲の土壌間隙内に浸透拡散され、蓄積されてなる重金属類や有機化合物と密に接触されることとなる。
Since the present invention uses such a configuration, it has the following effects. In other words, since the soil is surveyed by drilling prior to purification, the contamination, contamination status, contamination distribution, and porosity of the contaminated soil are confirmed, so the mixing ratio and appropriate viscosity of the artificial zeolite powder in the purification solution to be used are determined. The injection pressure and the injection amount can also be discriminated.
Then, a cleaning solution injection hole is drilled over the entire contaminated soil by a boring machine at equal intervals and with the required hole diameter and depth, and is placed at the tip of the boring machine drilling rod in each cleaning solution injection hole. The purifying liquid is injected into the excavated and sealed purifying liquid injection hole at the required injection pressure from the prepared purifying liquid injection port, so that the purifying liquid enters the soil gap in the required radial range around the purifying liquid injection hole. It is intimately contacted with heavy metals and organic compounds that have been permeated and diffused.

更にこの人工ゼオライト粉体が混合分散された浄化液と接触された重金属や有機化合物は、微粒状で接触表面積率が極めて大きく且吸着容量や吸湿、吸水容量も大きく、而もその絶対吸着容量や吸湿、吸水容量も膨大な人工ゼオライト粉体に積極的且効率的に吸着或いは吸湿、吸水されるとともに吸着された重金属類や有機化合物は本質的に保持する触媒作用と且強い塩基置換性とにより、重金属類は強固に吸着固定され而も有機化合物は容易に吸着分解されることとなる。  Furthermore, the heavy metals and organic compounds that are in contact with the purification liquid in which the artificial zeolite powder is mixed and dispersed are fine particles, have an extremely large contact surface area ratio, and have a large adsorption capacity, moisture absorption, and water absorption capacity. Actively and efficiently adsorbed or absorbed and absorbed by artificial zeolite powder with a large amount of moisture absorption and water absorption, and the adsorbed heavy metals and organic compounds are essentially retained in their catalytic action and strong base substitution. Heavy metals are strongly adsorbed and fixed, and organic compounds are easily adsorbed and decomposed.

而も浄化液が加圧注入された浄化液注入孔内には、掘削排出された汚染土壌に対して10乃至35%重量割合の人工ゼオライト粉体が配合された浄化充填土で埋戻しがなされるため、該浄化充填土内の重金属類や有機化合物も混合された人工ゼオライト粉体により強固に吸着固定され若しくは吸着分解される。
加えて浄化液中に0.5乃至5.0%重量割合でカチオン界面活性剤が混合された場合には浄化液中の人工ゼオライト粉体の分散性が高まることにより、汚染土壌間隙内への浸透拡散が著しく促進されて重金属類の吸着固定や有機化合物の吸着分解も著しく高められ、或いは浄化液中に硫酸カルシウムが0.5乃至5.0%重量割合で混合されることにより、腐触土や粘土或いは麈埃等微粒体に多量に付着蓄積する重金属や有機化合物に対して凝集性に伴う剥離力が働き、容易に吸着固定若しくは吸着分解がなされる。
Further, the purification solution injection hole into which the purification solution is injected under pressure is backfilled with a purification filling soil in which 10 to 35% by weight of artificial zeolite powder is mixed with the contaminated soil excavated and discharged. Therefore, it is firmly adsorbed and fixed or decomposed by adsorption with the artificial zeolite powder mixed with the heavy metals and organic compounds in the purification packed soil.
In addition, when a cationic surfactant is mixed in the purification solution at a weight ratio of 0.5 to 5.0%, the dispersibility of the artificial zeolite powder in the purification solution increases, so that Osmotic diffusion is significantly promoted, and adsorption and fixation of heavy metals and adsorption and decomposition of organic compounds are remarkably enhanced, or by mixing calcium sulfate in the purification solution in a proportion of 0.5 to 5.0% by weight, Peeling force accompanying cohesion acts on heavy metals and organic compounds that adhere and accumulate in large quantities on fine particles such as soil, clay, and dust, and they are easily adsorbed and fixed or decomposed.

更に浄化液注入孔内に所要の注入圧力と注入量を以って浄化液が注入され土壌間隙内に浸透拡散されたうえ埋戻しされた汚染土壌表面全体に亘って所要量の浄化液が散水浸透されるため、汚染土壌表面の汚染物質にも人工ゼオライト粉体が均等に浸透接触し吸着固定や吸着分解がなされるとともに埋戻し部分の土壌の締固めもなされることとなる。  Further, the purification liquid is injected into the purification liquid injection hole with the required injection pressure and injection volume, and the required amount of the purification liquid is sprayed over the entire contaminated soil surface that has been permeated and diffused into the soil gap and backfilled. Therefore, the artificial zeolite powder is infiltrated and contacted evenly with the pollutant on the contaminated soil surface to perform adsorption fixation and adsorption decomposition and to compact the soil in the backfill portion.

以下に本発明実施例を図とともに詳細に説明すれば、図1は本発明の浄化工法の実施に先立ってなされる土壌調査方法の説明図であって、該土壌調査1は浄化すべき汚染土壌1Aの適宜位置にアースオーガーやボーリングマシン等の適宜の掘削機1Bを用いて所要の口径及び深さの掘削孔1Cを掘削して表層1D、中層10D、或いは下層11Dに亘る土壌サンプルを採取し、それぞれの土壌サンプルに基づき汚染物質毎の汚染度合や汚染分布及び土壌間隙率を判断するものである。
かかる場合に汚染物質毎の汚染状態は本来的にはガスクロマトグラフ等の分析機器を用いて定性及び定量分析がなされるものであるが、現状においては汚染物質毎の試薬による簡易分析方法所謂パックテスト方法が普及しており、大まかな汚染度合の判断には該パックテスト方法の利用が至便である。
In the following, the embodiment of the present invention will be described in detail with reference to the drawings. FIG. 1 is an explanatory diagram of a soil survey method performed prior to the implementation of the purification method of the present invention. Using a suitable excavator 1B, such as an earth auger or a boring machine, at 1A, an excavation hole 1C having a required diameter and depth is excavated, and a soil sample covering the surface layer 1D, the middle layer 10D, or the lower layer 11D is collected. Based on each soil sample, the degree of pollution, pollution distribution and soil porosity are determined for each pollutant.
In such a case, the contamination state for each pollutant is essentially qualitative and quantitative analysis using an analytical instrument such as a gas chromatograph. Currently, a simple analysis method using a reagent for each pollutant, so-called pack test. The method is widespread, and it is convenient to use the pack test method to roughly determine the degree of contamination.

かかる土壌調査1において汚染物質毎の汚染状態や汚染分布及び土壌間隙率が把握されたうえ本発明浄化工法が施される。
即ち図2は本発明浄化工法の実施に際して使用されるボーリングマシン2の説明図であって、該ボーリングマシン2は基台2Aの上に駆動装置2Bが設けられてなるとともに、該基台2Aの一側端には所要の深さ方向に上下に可動でき、且所要の孔径で浄化液注入孔3が掘削できるよう回転可能に且その先端に掘削刀所謂ビット2Cが装着されたロッド2Dが配備されてなるもので、更に該ロッド2D内には所要の孔径と深さに掘削した浄化液注入孔3内に所要の注入圧力と注入量を以って浄化液4を注入させるため、その下端に浄化液注入口2Eを有する浄化液注入管2Fが装備されている。
In the soil survey 1, the contamination state, the contamination distribution, and the soil porosity for each pollutant are grasped, and the purification method of the present invention is applied.
That is, FIG. 2 is an explanatory view of a boring machine 2 used in carrying out the purification method of the present invention. The boring machine 2 is provided with a driving device 2B on a base 2A, and the base 2A. A rod 2D, which can move up and down in a required depth direction at one side end and is rotatable so that the purifying solution injection hole 3 can be excavated with a required hole diameter, and a so-called bit 2C attached to the tip of the drill 2C is provided. In addition, the lower end of the rod 2D has a lower end for injecting the cleaning liquid 4 with the required injection pressure and injection amount into the cleaning liquid injection hole 3 drilled to the required hole diameter and depth. Is equipped with a purification liquid injection pipe 2F having a purification liquid injection port 2E.

そして当然のことながら該ボーリングマシン2の浄化液注入孔3の浄化液注入管2Fの他端2Gには、浄化液槽40内に所要量で貯留された浄化液4を所要の注入圧力と注入量を以って移送させる加圧ポンプ41と連通されてなる耐圧移送ホース42が取付けられてなるものである。
更に該ボーリングマシン2を用いて掘削してなる浄化液注入孔3内への浄化液4の注入圧力はその土壌の間隙率や注入量によっても異なるが、一般的土壌においては略20乃至40kgf/cm程度の注入圧力を保持するものが好都合である。
As a matter of course, the cleaning liquid 4 stored in a required amount in the cleaning liquid tank 40 is injected into the other end 2G of the cleaning liquid injection pipe 2F of the cleaning liquid injection hole 3 of the boring machine 2 with a required injection pressure and injection. A pressure-resistant transfer hose 42 communicated with a pressurizing pump 41 to be transferred by an amount is attached.
Furthermore, the injection pressure of the purification liquid 4 into the purification liquid injection hole 3 excavated by using the boring machine 2 varies depending on the porosity and the injection amount of the soil, but in general soil, about 20 to 40 kgf / It is advantageous to maintain an injection pressure of about cm 2 .

かくしてなるボーリングマシン2による掘削される浄化液注入孔3は土壌調査に基づき均等な間隔と且所要の孔径及び深さに掘削がなされるものであって、図3は本発明による浄化液注入孔3の掘削状態を示す説明図が示されてなるもので、ボーリングマシン2のロッド2Dの先端にビット2Cが装着されたうえ、汚染土壌1Aの適宜位置より該ロッド2Dを回転させつつ下方に移動させることにより、所要の深さと孔径の浄化液注入孔3が掘削される。
かかる場合に該浄化液注入孔3の掘削深さは汚染分布に従って決定されるものであり且浄化注入孔3の孔径については特段の制約はないが、浄化液4の所要量を汚染土壌1Aの間隙内に放射状に浸透拡散させるうえから、通常においては略50乃至100mmφ程度が望ましい。
The purifying fluid injection hole 3 excavated by the boring machine 2 thus constructed is excavated at equal intervals and with a required hole diameter and depth based on the soil survey. FIG. 3 shows the purifying fluid injection hole according to the present invention. 3 is an explanatory diagram showing the excavation state 3 and a bit 2C is attached to the tip of the rod 2D of the boring machine 2 and moves downward while rotating the rod 2D from an appropriate position of the contaminated soil 1A. By doing so, the purification liquid injection hole 3 having a required depth and hole diameter is excavated.
In this case, the excavation depth of the purification liquid injection hole 3 is determined according to the contamination distribution, and the hole diameter of the purification injection hole 3 is not particularly limited, but the required amount of the purification liquid 4 is reduced to the contaminated soil 1A. Usually, about 50 to 100 mmφ is desirable in order to diffuse and diffuse radially into the gap.

かくして所要の深さ及び孔径にロッド2Dを回転させ掘削させたる後該ロッド2Dの回転を停止し、而して浄化液4の加圧ポンプ41を駆動させてロッド2D先端に装備されてなる浄化液注入口2Eより所要の注入圧力及び注入量を以って加圧注入させることにより、該浄化液注入口2Eより注入された浄化液4は、汚染土壌1Aの間隙内に放射状に浸透拡散される。
そして掘削された浄化液注入孔3内に加圧注入された浄化液4が汚染土壌1Aの間隙内に放射状に浸透拡散される範囲と、他の掘削された浄化液注入孔3内に加圧注入された浄化液4が汚染土壌1Aの間隙内を放射状に浸透拡散される範囲とにより、汚染土壌1Aの間隙内全体が実質的に浄化液4で浸透拡散されるよう均等な間隔を以ってそれぞれの浄化液注入孔3を掘削させれば良い。
Thus, after the rod 2D is rotated to the required depth and hole diameter and excavated, the rotation of the rod 2D is stopped, and the pressure pump 41 of the cleaning liquid 4 is driven to purify the rod 2D. By performing pressure injection from the liquid injection port 2E with a required injection pressure and injection amount, the purification solution 4 injected from the purification solution injection port 2E is permeated and diffused radially into the gap of the contaminated soil 1A. The
Then, the range in which the purifying fluid 4 pressurized and injected into the excavated purifying fluid injection hole 3 is permeated and diffused radially into the gap of the contaminated soil 1A and the other excavated purifying fluid injection hole 3 is pressurized. Due to the range in which the injected cleaning solution 4 is permeated and diffused radially in the gap of the contaminated soil 1A, the entire clearance gap of the contaminated soil 1A is substantially uniformly permeated and diffused by the cleaning solution 4. Then, the respective purifying liquid injection holes 3 may be excavated.

そして浄化液4の汚染土壌1Aの間隙内に浸透拡散させる範囲並びに注入量は、浄化液4の粘度や注入圧力及び汚染土壌1Aの間隙率によって大きく変動するものであって、一般的に浄化液4の浸透拡散量所謂注入量は式Q=V×n×α=V×λ(但しQ=注入量/kl、V=浄化対象土壌量、n=土壌の間隙率%、α=充填率、λ−注入率%)で示されるものであるから、注入率λ=土壌の間隙率n×充填率αとして表すことが出来る。  The range in which the clarified liquid 4 is permeated and diffused into the gap of the contaminated soil 1A and the injection amount vary greatly depending on the viscosity of the clarified liquid 4, the injection pressure, and the porosity of the contaminated soil 1A. The amount of osmotic diffusion of the so-called injection amount is the formula Q = V × n × α = V × λ (where Q = injection amount / kl, V = soil amount to be purified, n = soil porosity%, α = filling rate, (λ−injection rate%), it can be expressed as injection rate λ = soil porosity n × filling rate α.

而して汚染土壌1Aの土質と圧密程度により間隙率nも変動するものであって粘性土の場合には高圧密状態では略50、低圧密状態においては略70、更に砂質土の場合では高圧密状態で略30、低圧密状態では略50、更には砂礫土における高圧密状態では略25、低圧密状態では略50程度とされている。
他方汚染土壌1A内に蓄積されてなる重金属類や有機化合物に浄化液4を有効に接触させて該重金属類の吸着固定若しくは有機化合物の吸着分解を図るうえからは、間隙内への浄化液の充填率としては略50乃至70%以上に充填させることが望まれる。
Thus, the porosity n also varies depending on the soil quality and the degree of compaction of the contaminated soil 1A. In the case of viscous soil, it is approximately 50 in the high pressure dense state, approximately 70 in the low pressure dense state, and further in the case of sandy soil. It is about 30 in the high-pressure dense state, about 50 in the low-pressure dense state, further about 25 in the high-pressure dense state in gravel soil, and about 50 in the low-pressure dense state.
On the other hand, in order to effectively contact the heavy metal or organic compound accumulated in the contaminated soil 1A with the purification solution 4 to adsorb and fix the heavy metal or to adsorb and decompose the organic compound, the purification solution into the gap The filling rate is preferably about 50 to 70% or more.

他方浄化液4は、水に対して10乃至35%重量割合で人工ゼオライト粉体4Aが混合分散されてなるものであるが、汚染土壌1Aに蓄積されてなる重金属類や有機化合物との接触機会を高めて積極的に該重金属類や有機化合物を吸着させ若しくは吸湿、吸水させること及び微細な汚染土壌1Aの間隙内に容易に浸透拡散させるうえから、使用する人工ゼオライト粉体4Aはその粒径が30μm以下好ましくは1乃至10μm程度の微粒状で、且重金属類や有機化合物を効率良く吸着させ若しくは吸湿、吸水させるうえからは、吸着容量若しくは吸湿、吸水容量の大きなもの所謂比表面積が大きなものが好適であることから、その比表面積においては少なくとも100m/g以上望ましくは160乃至200m/gのものが使用される。On the other hand, the purification solution 4 is a mixture of the artificial zeolite powder 4A in a proportion of 10 to 35% by weight with respect to water, but the opportunity for contact with heavy metals and organic compounds accumulated in the contaminated soil 1A. The artificial zeolite powder 4A to be used has a particle size that allows the heavy metals and organic compounds to be adsorbed or absorbed, absorbed and absorbed, and easily penetrated and diffused into the gaps of the fine contaminated soil 1A. Is 30 μm or less, preferably about 1 to 10 μm, and has a large adsorption capacity, moisture absorption, water absorption capacity, so-called large specific surface area for efficiently adsorbing, absorbing, or absorbing heavy metals and organic compounds. at least 100 m 2 / g or more preferably those 160 to 200 meters 2 / g is used in a specific surface area because it is preferable

加えて重要なことは浄化液4を汚染土壌1Aの間隙内に浸透拡散せしめて浄化を図ることは、汚染物質たる重金属の吸着固定並びに有機化合物の吸着分解にある。これがためには人工ゼオライト粉体4Aが本質的に保持する触媒作用に強い塩基置換性を付与せしむることが不可欠であることから、その塩基置換容量(meq/100g)においては少なくとも200mg以上望ましくは240乃至280mgの人工ゼオライト粉体4Aが選択使用される。  In addition, what is important is that the purifying solution 4 is infiltrated and diffused into the gaps of the contaminated soil 1A to purify it by adsorbing and fixing heavy metals as contaminants and adsorbing and decomposing organic compounds. For this purpose, it is indispensable to impart strong base substitution to the catalytic action inherently retained by the artificial zeolite powder 4A. Therefore, the base substitution capacity (meq / 100 g) is preferably at least 200 mg or more. 240 to 280 mg of artificial zeolite powder 4A is selectively used.

而して浄化液4は汚染土壌1Aの間隙内に浸透拡散を図るうえから、水に対して該人工ゼオライト粉体4Aが10乃至35%重量割合で混合されてなるもので、かかる理由は汚染土壌1Aの間隙内に可能な限り多量の人工ゼオライト粉体4Aを浸透拡散させ、その絶対吸着容量を以って汚染物質たる重金属類の吸着固定並びに有機化合物の吸着分解を確実になさしむるものであって、人工ゼオライト粉体4Aが10%重量割合以下ではその粘度もせいぜい数拾pis(ポイズ)程度であるから浸透拡散には優れるものの、十分な吸着固定や吸着分解が実現されにくく、反面35%以上の混合割合ではその粘度も数百pis(ポイズ)以上の高粘度となり、間隙率の小さな汚染土壌1Aにおいては十分な浸透拡散がなされにくくなることによる。  Thus, the purification solution 4 is formed by mixing the artificial zeolite powder 4A with water at a ratio of 10 to 35% by weight in order to permeate and diffuse into the gaps in the contaminated soil 1A. Infiltrate and diffuse as much artificial zeolite powder 4A as possible into the gaps in the soil 1A, and with its absolute adsorption capacity, adsorbing and fixing heavy metals as contaminants and adsorbing and decomposing organic compounds reliably However, when the artificial zeolite powder 4A is less than 10% by weight, its viscosity is at most several psi (poise), so it is excellent in osmotic diffusion, but it is difficult to achieve sufficient adsorption fixation and adsorption decomposition. When the mixing ratio is 35% or more, the viscosity becomes high viscosity of several hundred psi (poise) or more, and it is difficult to sufficiently permeate and diffuse in the contaminated soil 1A having a small porosity.

加えて吸着固定や吸着分解にはその塩基置換容量(meq/100g)の大きなものが望まれるものの、その塩基置換容量(meq/100g)が200mgを超えると水に対する分散性が悪くなる傾向が生ずる。そこでかかる問題への対処としては浄化液4の全体量に対して0.5乃至5.0%のカチオン界面活性剤を混合させ分散性を高めてやることが好適である。かかる場合におけるカチオン界面活性剤については特段の制約はなく、具体的なものとしてはアルキルトリメチルアンモニウムクロライドやアルキルジメチルベンゾルアンモニウム等が挙げられる。  In addition, although a large base substitution capacity (meq / 100 g) is desired for adsorption fixation and adsorption decomposition, when the base substitution capacity (meq / 100 g) exceeds 200 mg, the dispersibility in water tends to deteriorate. . Therefore, as a countermeasure against such a problem, it is preferable to improve the dispersibility by mixing 0.5 to 5.0% of the cationic surfactant with respect to the total amount of the cleaning liquid 4. The cationic surfactant in such a case is not particularly limited, and specific examples thereof include alkyltrimethylammonium chloride and alkyldimethylbenzolammonium.

更に汚染土壌1Aの汚染物質は土壌中の塵埃や腐食土或いは粘土等の微粒状の物質に多量に付着蓄積されているケースが多く、従って該微粒状の物質に付着蓄積された汚染物質を効果的に吸着固定若しくは吸着分解させるためには、凝集作用を活用してこれら微粒物から汚染物質を剥離させることが有利であることから、浄化液合体に対して凝集剤としての硫酸カルシウムを0.5乃至5.0%重量割合で混合させることが提案される。  In addition, the contaminated soil 1A often has a large amount of contaminants deposited and accumulated on fine particulate matter such as dust, corrosive soil or clay in the soil. In order to achieve adsorption fixation or adsorption decomposition, it is advantageous to peel off contaminants from these fine particles by utilizing the agglomeration action. It is proposed to mix in a 5 to 5.0% weight ratio.

図4は本発明における浄化液の加圧注入施工の説明図であって、本発明においてはボーリングマシン2により掘削した浄化液注入孔3内において、その汚染分布に対応した深さ位置で所要の注入圧力と注入量を以って浄化液4を汚染土壌1Aの間隙内に加圧注入させ浸透拡散させるものであるが、発明者の数多の施工経緯からは人工ゼオライト粉体4Aが15%重量割合で混合分散された浄化液4を用いて、平均間隙率50%の汚染土壌1Aに注入圧が30kgf/cmで加圧注入した場合の平均的放射浸透拡散範囲4Bは、浄化液注入口2Eを中心として略2.1乃至2.8m程度の距離範囲たることが把握されている。従って汚染分布が高範囲に亘る場合においては、図示するようにボーリングマシン2のロッド2D先端をLのレベルに配位のうえ浄化液4を所要の注入圧力と注入量を汚染土壌1Aの間隙内に浸透拡散させ、而して該ロッド2Dの先端Lのレベルまで引上げ配位させ、再び浄化液4を所要の注入圧力および注入量を以って加圧注入させ、垂直方向における汚染土壌1A全体の間隙内に浸透拡散させる。FIG. 4 is an explanatory view of the pressure injection construction of the purification liquid in the present invention. In the present invention, the purification liquid injection hole 3 excavated by the boring machine 2 has a required depth position corresponding to the contamination distribution. The purification solution 4 is injected under pressure and injected into the gap between the contaminated soil 1A with the injection pressure and the injection amount, and the artificial zeolite powder 4A is 15% due to many inventors' background. The average radiation osmosis diffusion range 4B when the injection pressure is 30 kgf / cm 2 and injected into the contaminated soil 1A having an average porosity of 50% using the purification liquid 4 mixed and dispersed in the weight ratio is the purification liquid injection. It is understood that the distance is about 2.1 to 2.8 m around the entrance 2E. Thus when the pollution distribution over a high range, the gap of the contaminated soil 1A the required injection pressure and injection rate of the rod 2D tip of the boring machine 2 after purification liquid 4 coordination on the level of L 1 as shown infiltrated diffused within and Thus by pulling coordinated to the level of the distal end L 2 of the rod 2D, it is injected under pressure drives out the required injection pressure and injection volume cleaning solution 4 again, contamination in the vertical direction soil Permeate and diffuse into the entire 1A gap.

図5は浄化液の散水浸透の状態を示す説明図であって、汚染土壌1A全面に亘って均等な間隔で且所要の孔径及び深さで浄化液注入孔3が掘削され、且それぞれの浄化液注入孔3内に浄化液4を所要の注入圧力と注入量を以って汚染土壌1Aの間隙内に浸透拡散せしめたる後は、該浄化液注入孔3の掘削に伴う掘削排出土10Aに、人工ゼオライト粉体4Aが10乃至35%重量割合で配合させてなる浄化充填土5により浄化液注入孔3の埋戻しがなされる。  FIG. 5 is an explanatory diagram showing the state of water spray penetration of the cleaning liquid, and the cleaning liquid injection holes 3 are excavated at equal intervals and at the required hole diameter and depth over the entire contaminated soil 1A. After the purifying liquid 4 is infiltrated and diffused into the gap of the contaminated soil 1A with the required injection pressure and injection amount into the liquid injection hole 3, it is applied to the excavated discharge soil 10A accompanying the excavation of the purification liquid injection hole 3. Then, the purification liquid injection hole 3 is backfilled with the purification filling soil 5 in which the artificial zeolite powder 4A is mixed at a weight ratio of 10 to 35%.

而しながら浄化液注入孔3内での浄化液4の所要注入圧力及び注入量による加圧注入手段では、汚染土壌1Aの表面近傍においては高い注入圧力に伴い放出が随所で発生し、汚染土壌1A表面近傍の間隙内への浸透拡散が十分になしえぬばかりか、浄化充填土5による埋戻しも十分に充填固化された状態には至らない。
そこで埋戻しがなされた汚染土壌1A表面全体に亘って浄化液4を所要量散水浸透6させることにより、汚染土壌1A表面の浄化と且埋戻し部分の締固めが実現できる。
かかる場合において浄化液4の散水浸透6に際しては、適宜の散水具6Aと浄化液4の加圧注入のための加圧ポンプ41とを適宜のホース6Bで連結させるのみで容易になしえる。かかる場合の浄化液4の散水浸透量は、人工ゼオライト粉体4Aの混合割合によっても多少異なるが概ね1m当り20乃至40l程度で十分である。
However, in the pressure injection means based on the required injection pressure and the injection amount of the purification liquid 4 in the purification liquid injection hole 3, the discharge occurs everywhere in the vicinity of the surface of the contaminated soil 1A due to the high injection pressure, and the contaminated soil. Not only the penetration and diffusion into the gap near the surface of 1A cannot be sufficiently achieved, but also the backfilling with the clarified filling soil 5 does not lead to a sufficiently filled and solidified state.
Accordingly, by purifying the surface of the contaminated soil 1A and compacting the backfill portion by spraying the required amount of the cleaning solution 4 over the entire surface of the contaminated soil 1A that has been backfilled.
In such a case, the sprinkling permeation 6 of the purification liquid 4 can be easily achieved by simply connecting an appropriate watering tool 6A and a pressurization pump 41 for pressurizing the purification liquid 4 with an appropriate hose 6B. In this case, about 20 to 40 l per 1 m 2 is sufficient as the amount of water permeation of the purification liquid 4 slightly depending on the mixing ratio of the artificial zeolite powder 4A.

発明の効果The invention's effect

本発明は以上述べたように、予め浄化すべき土地の適宜位置をボーリングして土壌の汚染状態や汚染分布及び土壌の間隙率が把握されるため、浄化液を注入すべき浄化液注入孔の深さや掘削間隔及び浄化液の混合分散濃度並びに注入圧力や注入量と浸透拡散範囲も判断でき、正確な施工計画も容易に作成できる。
加えてロッド先端にビットが装着され且該ロッドの内部には浄化液注入管と且その先端に浄化液注入口を有するボーリングマシン及び該ボーリングマシンの浄化液注入管の他端に浄化液槽並びに加圧ポンプとを連結させておくことにより極めて孔径の小さな浄化液注入孔が簡便に掘削できるとともに、ロッドの先端を所要のレベル位置に配位させて浄化液を所要の注入圧力と注入量を以って注入させることの繰返しにより、汚染土壌の間隙内全体に亘って浸透拡散がなされるため、汚染土壌を原位置において極めて簡便且能率的に汚染土壌中の拡散蓄積されてなる汚染物質と浄化液とを接触させることが出来る。
As described above, the present invention bores the appropriate position of the land to be cleaned in advance and grasps the soil contamination state, the contamination distribution, and the soil porosity, so that the cleaning solution injection hole to which the cleaning solution should be injected The depth, excavation interval, mixed dispersion concentration of the cleaning liquid, injection pressure, injection amount, and permeation diffusion range can also be determined, and an accurate construction plan can be easily created.
In addition, a bit is attached to the tip of the rod, and a cleaning liquid injection pipe inside the rod, a boring machine having a cleaning liquid injection port at the tip, a purification liquid tank at the other end of the cleaning liquid injection pipe of the boring machine, and By connecting the pressurizing pump, the cleaning solution injection hole with a very small hole diameter can be easily excavated, and the tip of the rod is arranged at the required level position, and the cleaning solution is supplied with the required injection pressure and injection volume. By repeating the injection, the osmotic diffusion is carried out throughout the gap of the contaminated soil, so that the contaminated soil can be diffused and accumulated in the contaminated soil in an extremely simple and efficient manner. The cleaning liquid can be contacted.

そして汚染物質と接触する浄化液には、その粒径が30μm以下で比表面積が100m/g以上で而も本来的に保持する触媒作用に加えて塩基置換容量(meq/100g)が200mg以上の極めて強い塩基置換性を保持する人工ゼオライト粉体が水に対して10乃至35%重量割合で混合分散されてなるから間隙率の低い汚染土壌間隙内でも容易に浸透拡散できるばかりか、人工ゼオライト粉体の極めて大きな接触表面積率と且比表面積の大きさに加えて混合分散量とが相俟って絶対吸着容量若しくは吸湿、吸水容量が膨大量となるため重金属類や有機化合物等が積極的且効率的に吸着若しくは吸湿、吸水されるとともに、重金属類は強固に吸着固定され且有機化合物においては吸着分解され、而も人工ゼオライト粉体は土壌中に長期に残存するため浄化作用が将来に亘って発揮され続けられる等、極めて画期的な汚染土壌の浄化工法である。In addition, the purification solution that comes into contact with the pollutant has a base substitution capacity (meq / 100 g) of 200 mg or more in addition to the catalytic action that the particle size is 30 μm or less and the specific surface area is 100 m 2 / g or more and is inherently retained. Since the artificial zeolite powder having extremely strong base substitution property is mixed and dispersed at a ratio of 10 to 35% by weight with respect to water, not only can it easily permeate and diffuse even in contaminated soil gaps with low porosity, but also artificial zeolite powder. Combined with the extremely large surface area of the powder, the specific surface area, and the amount of mixing and dispersion, the absolute adsorption capacity, moisture absorption, and water absorption capacity are enormous, so heavy metals and organic compounds are aggressive. Adsorbed or absorbed and absorbed efficiently, heavy metals are strongly adsorbed and fixed, and organic compounds are adsorbed and decomposed. This is a groundbreaking method for the purification of contaminated soil.

土壌調査方法の説明図である。  It is explanatory drawing of a soil investigation method. ボーリングマシンの説明図である。  It is explanatory drawing of a boring machine. 浄化液注入孔の掘削状態説明図である。  It is explanatory drawing of the excavation state of a purification liquid injection hole. 浄化液加圧注入施工の説明図である。  It is explanatory drawing of purification liquid pressurization injection construction. 浄化液散水浸透の状態を示す説明図である。  It is explanatory drawing which shows the state of purification liquid sprinkling.

符号の説明Explanation of symbols

1 土壌調査
1A 汚染土壌
10A 掘削排出土
1B 掘削機
1C 掘削孔
2 ボーリングマシン
2A 基台
2B 駆動装置
2C ビット
2D ロッド
2E 浄化液注入口
2F 浄化液注入管
2G 浄化液注入管の他端
3 浄化液注入孔
4 浄化液
4A 人工ゼオライト粉体
4B 放射浸透拡散範囲
40 浄化液槽
41 加圧ポンプ
42 耐圧移送ホース
5 浄化充填土
6 散水浸透
6A 散水具
6B ホース
DESCRIPTION OF SYMBOLS 1 Soil investigation 1A Contaminated soil 10A Excavation discharge soil 1B Excavator 1C Excavation hole 2 Boring machine 2A Base 2B Drive device 2C Bit 2D Rod 2E Purification liquid inlet 2F Purification liquid injection pipe 2G The other end of the purification liquid injection pipe 3 Purification liquid Injection hole 4 Purification liquid 4A Artificial zeolite powder 4B Radiation penetration diffusion range 40 Purification liquid tank 41 Pressure pump 42 Pressure-resistant transfer hose 5 Purification filling soil 6 Sprinkling penetration 6A Sprinkling tool 6B hose

Claims (4)

浄化すべき土地の適宜位置をボーリングし、土壌の汚染状態や汚染分布及び土壌の間隙率を判断する土壌調査と、該土壌調査に基づき汚染土壌全面に亘って均等な間隔と所要の孔径及び深さの浄化液注入孔をボーリングマシンで掘削する掘削工程と、それぞれの浄化液注入孔内にボーリングマシン掘削ロッド内に配備された浄化液注入口より所要の注入圧力及び注入量を以って土壌間隙内に浸透拡散させる浄化液注入工程と、水に対して10乃至35%重量割合で混合分散され且その粒径が30μm以下で比表面積が100m/g以上及び塩基置換容量(meq/100g)が200mg以上の人工ゼオライト粉体からなる浄化液と、該浄化液が浸透拡散された浄化液注入孔内に掘削排出された土壌に対して、前記人工ゼオライト粉体が10乃至35%重量割合で配合された浄化充填土で埋戻しをする埋戻し工程とからなる汚染土壌の浄化方法。Boring the appropriate position of the land to be cleaned, soil survey to determine the soil contamination status, contamination distribution and soil porosity, and based on the soil survey, even intervals and required pore size and depth over the entire contaminated soil The excavation process of excavating the purification liquid injection hole with a boring machine, and the soil with the required injection pressure and injection amount from the purification liquid injection hole arranged in the boring machine excavation rod in each purification liquid injection hole A purification liquid injection step for permeating and diffusing into the gap, and a mixture of 10 to 35% by weight with respect to water, the particle size of which is 30 μm or less, the specific surface area is 100 m 2 / g or more, and the base substitution capacity (meq / 100 g ) Is 200 mg or more of the purified zeolite powder, and the artificial zeolite powder is 1 to the soil excavated and discharged into the purified solution injection hole into which the purified solution is permeated and diffused. A method for purifying contaminated soil, comprising a backfilling step of backfilling with a cleansing filled soil blended at a ratio of 0 to 35% by weight. 浄化液中にカチオン界面活性剤が0.5乃至5.0%重量割合で混合されてなる請求項1記載の汚染土壌の浄化工法。  2. The method for purifying contaminated soil according to claim 1, wherein a cationic surfactant is mixed in the purification solution in an amount of 0.5 to 5.0% by weight. 浄化液中に硫酸カルシウムが0.5乃至5.0%重量割合で混合されてなる、請求項1記載の汚染土壌の浄化工法。  The method for purifying contaminated soil according to claim 1, wherein calcium sulfate is mixed in the purification solution at a weight ratio of 0.5 to 5.0%. 浄化液が浸透拡散され埋戻しされた汚染土壌表面全体に亘って所要量の浄化液を散水浸透させ、土壌表面の浄化と締固めを図る請求項1乃至請求項3記載の汚染土壌の浄化工法。  4. The method for purifying contaminated soil according to claim 1, wherein a necessary amount of the purifying liquid is sprayed and permeated over the entire contaminated soil surface in which the purifying liquid has been permeated and diffused, and the soil surface is purified and compacted. .
JP2003289376A 2003-07-03 2003-07-03 Cleaning method for contaminated soil Pending JP2005021873A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006342961A (en) * 2005-05-09 2006-12-21 Nippon Shiigatekku Kk Piping connecting structure
JP4934832B2 (en) * 2005-12-10 2012-05-23 ザ ユニバーシティ コート オブ ザ ユニバーシティ オブ エジンバラ Method and apparatus for improving contaminated land
CN106050157A (en) * 2016-08-15 2016-10-26 南京市宜德思环境科技有限责任公司 Drill pipe device for mixed injection of various medicaments

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006342961A (en) * 2005-05-09 2006-12-21 Nippon Shiigatekku Kk Piping connecting structure
JP4934832B2 (en) * 2005-12-10 2012-05-23 ザ ユニバーシティ コート オブ ザ ユニバーシティ オブ エジンバラ Method and apparatus for improving contaminated land
CN106050157A (en) * 2016-08-15 2016-10-26 南京市宜德思环境科技有限责任公司 Drill pipe device for mixed injection of various medicaments

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