JP2014104425A - Soil purification method and soil purification apparatus - Google Patents

Soil purification method and soil purification apparatus Download PDF

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JP2014104425A
JP2014104425A JP2012259378A JP2012259378A JP2014104425A JP 2014104425 A JP2014104425 A JP 2014104425A JP 2012259378 A JP2012259378 A JP 2012259378A JP 2012259378 A JP2012259378 A JP 2012259378A JP 2014104425 A JP2014104425 A JP 2014104425A
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well
soil
suction
heating
injection
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Takuya Shimomura
卓矢 下村
Keiichi Yokoyama
圭一 横山
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Dowa Eco Systems Co Ltd
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Dowa Eco Systems Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a soil purification method which promotes vaporization of a contaminated material by sufficiently heating the contaminated material in soil, and also can efficiently remove the contaminated material.SOLUTION: In the soil purification method which purifies soil S by sucking a contaminated material that vaporizes in soil from a sucking well 2 provided in the soil, the soil S is heated by a heater 10 inserted into a heating well 3 provided in the soil, and air is injected into the soil through an injection well 4 provided in the soil.

Description

本発明は、汚染土壌を浄化する土壌浄化方法及び土壌浄化装置に関するものである。   The present invention relates to a soil purification method and a soil purification apparatus for purifying contaminated soil.

工場の廃棄物等から漏洩した汚染物質(VOC、油等)が地下水に流れ込むと、地下水が汚染される。この場合、地下水汚染と同時に地下水面より上方にある不飽和帯の土壌中にも汚染物質が存在していることが多い。土壌中に存在するVOC等の汚染物質は、人体に悪影響を及ぼすため、可能な限り汚染物質を除去して土壌を浄化しなければならない。   When pollutants (VOC, oil, etc.) leaked from factory wastes flow into the groundwater, the groundwater is contaminated. In this case, contaminants often exist in the unsaturated zone soil above the groundwater surface at the same time as the groundwater contamination. Contaminants such as VOC present in the soil adversely affect the human body, so the soil must be purified by removing the contaminant as much as possible.

従来の土壌浄化方法としては、土壌中の加熱井戸に設けられた熱源により土壌を加熱し、土壌中で気化した汚染物質を吸引除去する方法がある(特許文献1)。また、地上で加熱した圧縮空気を不飽和帯の土壌中に注入し、気化した汚染物質を吸引除去する方法もある(特許文献2)。   As a conventional soil purification method, there is a method in which the soil is heated by a heat source provided in a heating well in the soil, and contaminants vaporized in the soil are removed by suction (Patent Document 1). There is also a method of injecting compressed air heated on the ground into unsaturated zone soil and removing the evaporated pollutants by suction (Patent Document 2).

特開平11−57685号公報JP-A-11-57685 特開平9−174033号公報JP-A-9-174033

しかしながら、特許文献1に記載された土壌浄化方法では、土壌中に通気性の悪い部分が存在する場合、土壌中で気化した汚染物質をすべて吸引することができず、効率良く汚染物質を除去することができなかった。   However, in the soil purification method described in Patent Document 1, when there is a poorly breathable part in the soil, it is not possible to suck all the pollutants evaporated in the soil and efficiently remove the pollutants. I couldn't.

また、特許文献2に記載された土壌浄化方法は、地上で加熱した圧縮空気を用いて土壌を加熱することから、土壌中で通気性にバラつきがある場合に、通気性の良い部分と悪い部分で加熱された空気の通過量が異なり、土壌を均一に加熱することが困難であった。その結果、通気性の悪い部分では、土壌を十分に加熱することができず、汚染物質を十分に気化させることができなかった。   Moreover, since the soil purification method described in patent document 2 heats soil using the compressed air heated on the ground, when there is a variation in air permeability in the soil, a part with good air permeability and a bad part It was difficult to heat the soil uniformly due to the difference in the amount of air that was heated in. As a result, in the part with poor air permeability, the soil could not be heated sufficiently and the pollutants could not be sufficiently vaporized.

これに加えて、土壌中の汚染物質を十分に気化させることができる温度まで空気を加熱するためには、地上に設置される空気の加熱設備が大型になってしまうという問題点もあった。加熱設備の設置場所によっては、設備の大型化が困難な場合があり、そのよう場合には、土壌中に注入する空気を十分に加熱することができなかった。その結果、汚染物質を十分に気化させることができず、土壌の汚染物質を十分に除去することができなかった。   In addition to this, in order to heat the air to a temperature at which the pollutants in the soil can be sufficiently vaporized, there is a problem that the air heating equipment installed on the ground becomes large. Depending on the installation location of the heating equipment, it may be difficult to increase the size of the equipment. In such a case, the air injected into the soil could not be heated sufficiently. As a result, the contaminants could not be sufficiently vaporized, and the soil contaminants could not be removed sufficiently.

また、例えば、特許文献2に記載された土壌浄化方法において、土壌中に注入する媒体を空気ではなく、スチームとすることも考えられる。しかしながら、土壌中に高圧スチームを注入すると、スチームが地上に噴き出したり、土壌中に溜まったスチームの圧力が上昇し、爆発してしまうおそれもある。   For example, in the soil purification method described in Patent Document 2, it is also conceivable that the medium injected into the soil is steam instead of air. However, when high-pressure steam is injected into the soil, there is a risk that the steam will erupt to the ground, or the pressure of the steam accumulated in the soil will rise and explode.

本発明の目的は、上記問題点を解決するため、土壌中の汚染物質を十分に加熱して汚染物質の気化を促進させると共に、その汚染物質を効率良く除去することができる土壌浄化方法及び土壌浄化装置を提供することにある。   In order to solve the above problems, the object of the present invention is to sufficiently heat the pollutants in the soil to promote vaporization of the pollutants and to efficiently remove the pollutants and the soil. It is to provide a purification device.

上記課題を解決するため、本発明によれば、土壌中で気化した汚染物質を、土壌中に設けられた吸引井戸から吸引することにより土壌を浄化する土壌浄化方法であって、土壌中に設けられた加熱井戸に挿入されたヒーターにより土壌を加熱し、土壌中に設けられた注入井戸を介して、土壌中に空気を注入することを特徴とする土壌浄化方法が提供される。   In order to solve the above problems, according to the present invention, there is provided a soil purification method for purifying soil by sucking contaminants vaporized in the soil from a suction well provided in the soil, which is provided in the soil. There is provided a soil purification method characterized in that the soil is heated by a heater inserted into the heated well, and air is injected into the soil through an injection well provided in the soil.

また、前記加熱井戸の下端部を地下水中に浸漬させても良い。また、前記注入井戸の下端部を地下水中に浸漬させても良い。   Moreover, you may immerse the lower end part of the said heating well in groundwater. Moreover, you may immerse the lower end part of the said injection well in groundwater.

また、前記加熱井戸を複数設け、前記吸引井戸を囲むようにして各加熱井戸を配置しても良い。このとき、各加熱井戸の穴中心と前記吸引井戸の穴中心との距離をそれぞれ等しくしても良い。また、各加熱井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角をそれぞれ等しくしても良い。   Further, a plurality of the heating wells may be provided, and each heating well may be arranged so as to surround the suction well. At this time, the distance between the hole center of each heating well and the hole center of the suction well may be made equal. Further, the angles formed by the straight lines connecting the hole centers of the respective heating wells and the hole centers of the suction wells may be equalized.

また、前記注入井戸を複数設け、前記吸引井戸を囲むようにして各注入井戸を配置しても良い。このとき、各注入井戸の穴中心と前記吸引井戸の穴中心との距離をそれぞれ等しくしても良い。また、各注入井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角をそれぞれ等しくしても良い。   Further, a plurality of the injection wells may be provided, and each injection well may be arranged so as to surround the suction well. At this time, the distance between the hole center of each injection well and the hole center of the suction well may be made equal. Further, the angles formed by the straight lines connecting the hole centers of the respective injection wells and the hole centers of the suction wells may be equalized.

また、気化した汚染物質の流出を防ぐ遮蔽物を用いて地表面を覆っても良い。   In addition, the ground surface may be covered with a shield that prevents the vaporized contaminants from flowing out.

また、上記課題を解決するため、本発明によれば、土壌中で気化した汚染物質を吸引できる構成を有する吸引井戸を備えた土壌浄化装置であって、土壌中に設けられた加熱井戸と、土壌中に設けられ、土壌中に空気を注入できる構成を有する注入井戸と、前記吸引井戸に接続され、前記吸引井戸内の雰囲気を吸引する吸引管と、前記加熱井戸に挿入されるように設けられたヒーターと、前記注入井戸に空気を注入する注入管とを備えていることを特徴とする土壌浄化装置も提供される。   Moreover, in order to solve the said subject, according to this invention, it is a soil purification apparatus provided with the suction well which has the structure which can attract | suck the contaminant vaporized in soil, Comprising: The heating well provided in the soil, An injection well provided in the soil and configured to inject air into the soil, a suction pipe connected to the suction well for sucking the atmosphere in the suction well, and provided to be inserted into the heating well There is also provided a soil purification apparatus comprising a heater and an injection pipe for injecting air into the injection well.

また、前記土壌浄化装置において、前記加熱井戸の下端部が地下水中に浸漬するように設けられていても良い。また、前記注入井戸の下端部が地下水中に浸漬するように設けられていても良い。   Moreover, the said soil purification apparatus WHEREIN: The lower end part of the said heating well may be provided so that it may be immersed in groundwater. Moreover, the lower end part of the said injection well may be provided so that it may be immersed in groundwater.

また、前記加熱井戸が複数設けられ、各加熱井戸が前記吸引井戸を囲むように配置されていても良い。このとき、各加熱井戸の穴中心と前記吸引井戸の穴中心との距離がそれぞれ等しくなるように各加熱井戸が配置されていても良い。また、各加熱井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角がそれぞれ等しくなるように各加熱井戸が配置されていても良い。   Moreover, the said heating well may be provided with two or more, and each heating well may be arrange | positioned so that the said suction well may be enclosed. At this time, each heating well may be arranged so that the distance between the hole center of each heating well and the hole center of the suction well is equal. In addition, each heating well may be arranged so that the angles formed by the straight lines connecting the hole center of each heating well and the hole center of the suction well are equal.

また、前記注入井戸が複数設けられ、各注入井戸が前記吸引井戸を囲むように配置されていても良い。このとき、各注入井戸の穴中心と前記吸引井戸の穴中心との距離がそれぞれ等しくなるように各注入井戸が配置されていても良い。また、 各注入井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角がそれぞれ等しくなるように各注入井戸が配置されていても良い。   A plurality of the injection wells may be provided, and each injection well may be disposed so as to surround the suction well. At this time, each injection well may be arranged so that the distance between the hole center of each injection well and the hole center of the suction well is equal. Further, the respective injection wells may be arranged so that the angles formed by the straight lines connecting the hole centers of the respective injection wells and the hole centers of the suction wells are equal.

また、気化した汚染物質の流出を防ぐ遮蔽物を備え、前記遮蔽物は、地表面を覆うように配置され、前記吸引管及び前記注入管が前記遮蔽物を貫通するようにして設けられていても良い。   In addition, a shield that prevents the vaporized contaminants from flowing out is provided, the shield is disposed so as to cover the ground surface, and the suction pipe and the injection tube are provided so as to penetrate the shield. Also good.

本発明によれば、加熱井戸内にヒーターを設けることにより、土壌を十分に加熱して汚染物質の気化を促進させると共に、注入井戸内に空気を注入することにより、土壌中の雰囲気の移動を促進させることができる。これにより、気化した汚染物質を確実に吸引することができ、土壌の浄化効率を向上させることができる。   According to the present invention, by providing a heater in the heating well, the soil is sufficiently heated to promote the vaporization of the pollutant, and the atmosphere in the soil is moved by injecting air into the injection well. Can be promoted. Thereby, the vaporized contaminant can be attracted | sucked reliably and the purification | cleaning efficiency of soil can be improved.

本発明の実施の形態に係る土壌浄化装置における各井戸の配置を示す概略平面図である。It is a schematic plan view which shows arrangement | positioning of each well in the soil purification apparatus which concerns on embodiment of this invention. 図1中のA−A断面図である。It is AA sectional drawing in FIG. 本発明の変形例を示す図である。It is a figure which shows the modification of this invention. 加熱井戸の加熱範囲の調査方法を示す図である。It is a figure which shows the investigation method of the heating range of a heating well. 加熱井戸の加熱範囲を示す結果である。It is a result which shows the heating range of a heating well. 加熱井戸の下端部を地下水に浸漬させた場合の地下水温の変化を示す図である。It is a figure which shows the change of groundwater temperature at the time of making the lower end part of a heating well immersed in groundwater. 本発明の変形例に係る汚染物質の回収能力を示す図である。It is a figure which shows the collection | recovery capability of the contaminant which concerns on the modification of this invention. 通気量に対する模擬汚染土及び模擬汚染水のTCEの除去状態を示す図である。It is a figure which shows the removal state of the simulated contaminated soil and simulated contaminated water with respect to the air flow.

以下、本発明の実施の形態を、汚染物質に汚染された土壌Sを浄化する土壌浄化装置1に基づいて説明する。なお、本実施の形態における汚染物質とは、油(例えば灯油、軽油等)やVOC等である。また、本明細書および図面において、実質的に同一の機能構成を有する要素においては、同一の符号を付することにより重複説明を省略する。   Hereinafter, an embodiment of the present invention will be described based on a soil purification apparatus 1 that purifies soil S contaminated with a pollutant. Note that the contaminant in the present embodiment is oil (for example, kerosene or light oil), VOC, or the like. In the present specification and drawings, elements having substantially the same functional configuration are denoted by the same reference numerals, and redundant description is omitted.

図1,2に示すように、土壌浄化装置1は、土壌中の雰囲気を吸引する吸引井戸2と、土壌Sを加熱する加熱井戸3と、土壌中に圧縮空気を注入する注入井戸4から構成される。ここで、本発明における「井戸」とは、土壌中に形成された孔に、管状(例えば円管状や角管状)の金属部材が挿入されたものを指す。なお、本実施の形態における井戸の形状は、一例として円管形状のものを採用した。また、金属部材の材質としては、例えばステンレス等の耐食性のあるものを採用するのが好ましい。   As shown in FIGS. 1 and 2, the soil purification apparatus 1 includes a suction well 2 that sucks an atmosphere in the soil, a heating well 3 that heats the soil S, and an injection well 4 that injects compressed air into the soil. Is done. Here, the “well” in the present invention refers to a material in which a tubular (for example, circular or rectangular) metal member is inserted into a hole formed in soil. In addition, the shape of the well in this Embodiment employ | adopted the thing of the circular tube shape as an example. Further, as the material of the metal member, it is preferable to employ a corrosion-resistant material such as stainless steel.

図1に示すように、加熱井戸3及び注入井戸4は、吸引井戸2の周囲を囲むようにして、6本ずつ設けられている。各加熱井戸3及び各注入井戸4は、平面視において、吸引井戸2を中心とする正六角形の頂点上及び辺上に配置されており、正六角形の頂点には各加熱井戸3が配置され、正六角形の辺の中点には各注入井戸4が配置されている。   As shown in FIG. 1, six heating wells 3 and six injection wells 4 are provided so as to surround the periphery of the suction well 2. Each heating well 3 and each injection well 4 are arranged on the top and sides of a regular hexagon centering on the suction well 2 in plan view, and each heating well 3 is placed on the top of the regular hexagon, Each injection well 4 is arranged at the midpoint of the side of the regular hexagon.

すなわち、各加熱井戸3の穴中心と吸引井戸2の穴中心との距離は、それぞれ等しく、各加熱井戸3の穴中心と吸引井戸2の穴中心とを結ぶ直線同士のなす角は互いに等しくなるように配置されている。なお、各加熱井戸3の穴中心と吸引井戸2の穴中心との距離は、1.5m以内であることが好ましい。同様に、各注入井戸4の穴中心と吸引井戸2の穴中心との距離は、それぞれ等しく、各注入井戸4の穴中心と吸引井戸2の穴中心を結ぶ直線同士のなす角は、互いに等しくなるように配置されている。なお、穴中心とは、井戸の形状が円管形状であれば円管の中心軸、角管形状であれば対角線の交点を通る管軸のことを指す。   That is, the distance between the hole center of each heating well 3 and the hole center of the suction well 2 is equal, and the angles formed by the straight lines connecting the hole center of each heating well 3 and the hole center of the suction well 2 are equal to each other. Are arranged as follows. In addition, it is preferable that the distance of the hole center of each heating well 3 and the hole center of the suction well 2 is 1.5 m or less. Similarly, the distance between the hole center of each injection well 4 and the hole center of the suction well 2 is equal, and the angles formed by the straight lines connecting the hole center of each injection well 4 and the hole center of the suction well 2 are equal to each other. It is arranged to be. The center of the hole refers to the central axis of the circular tube if the well shape is a circular tube shape, and the tube axis passing through the intersection of diagonal lines if the shape of the well is a rectangular tube shape.

図2に示すように、吸引井戸2は、略鉛直方向に沿って土壌中に埋め込まれるようにして設けられ、吸引井戸2には、吸引井戸内の雰囲気を吸引する吸引管5が接続されている。この吸引管5は、真空ポンプ6を介して、汚染物質を浄化する汚染物質処理装置7に接続されている。また、吸引井戸2は、下端部8以外が気密構造となっている。吸引井戸2の下端部8には、土壌中の雰囲気が通過できる小径の穴(図示せず)が形成され、その穴の周囲はストレーナ9により覆われている。なお、真空ポンプ6の吸引圧は、適宜変更されるものであるが、例えば−0.1MPa〜−0.4MPaである。   As shown in FIG. 2, the suction well 2 is provided so as to be embedded in the soil along a substantially vertical direction, and a suction pipe 5 that sucks the atmosphere in the suction well is connected to the suction well 2. Yes. This suction pipe 5 is connected via a vacuum pump 6 to a contaminant treatment device 7 that purifies the contaminant. The suction well 2 has an airtight structure except for the lower end 8. A small-diameter hole (not shown) through which the atmosphere in the soil can pass is formed at the lower end 8 of the suction well 2, and the periphery of the hole is covered with a strainer 9. In addition, although the suction pressure of the vacuum pump 6 is changed as appropriate, it is, for example, −0.1 MPa to −0.4 MPa.

各加熱井戸3は、略鉛直方向に沿って土壌中に埋め込まれるようにして設けられ、各加熱井戸3には、土壌Sを加熱するためのヒーター10が各加熱井戸3に挿入されるようにして設けられている。ヒーター10の設置深度は任意に変更することができるように構成されており、ヒーター10に接続された電線11は温調器12に接続されている。また、ヒーター10の下端には、熱電対13が設けられており、ヒーター10の温度を測定している。また、各加熱井戸3は、土壌中において気密構造となっている。   Each heating well 3 is provided so as to be embedded in the soil along a substantially vertical direction, and a heater 10 for heating the soil S is inserted into each heating well 3 in each heating well 3. Is provided. The installation depth of the heater 10 is configured to be arbitrarily changed, and the electric wire 11 connected to the heater 10 is connected to the temperature controller 12. A thermocouple 13 is provided at the lower end of the heater 10 to measure the temperature of the heater 10. Each heating well 3 has an airtight structure in the soil.

なお、加熱井戸3内に挿入されるヒーター10及び電線11の長さは、加熱井戸3の深さに応じて適宜変更されるものである。また、ヒーター10の能力も土壌Sの浄化時間や各井戸の配置状態等に応じて適宜変更されるものであるが、例えば2.5kwh/mであり、ヒーター10が300℃〜600℃程度に発熱できるようにすることが好ましい。   In addition, the length of the heater 10 and the electric wire 11 inserted in the heating well 3 is appropriately changed according to the depth of the heating well 3. Moreover, although the capability of the heater 10 is also suitably changed according to the purification time of the soil S, the arrangement state of each well, etc., it is 2.5 kwh / m, for example, and the heater 10 is about 300 ° C. to 600 ° C. It is preferable that heat can be generated.

各注入井戸4は、略鉛直方向に沿って土壌中に埋め込まれるようにして設けられ、各注入井戸内における地表面GLの近傍には、各注入井戸4に圧縮空気を注入する注入管14が設けられている。この注入管14は、レギュレーター15、流量計16を介して、コンプレッサー17に接続されている。また、各注入井戸4は、土壌中において下端部18以外が気密構造となっている。各注入井戸4の下端部18には、圧縮空気が通過できる小径の穴(図示せず)が形成され、その穴の周囲はストレーナ9により覆われている。なお、空気の注入量は、浄化対象となる土壌Sの通気性や各井戸の配置状態等により適宜変更されるものであるが、例えば土壌1mに対して30L/min〜50L/minである。 Each injection well 4 is provided so as to be embedded in soil along a substantially vertical direction, and an injection tube 14 for injecting compressed air into each injection well 4 is provided in the vicinity of the ground surface GL in each injection well. Is provided. The injection pipe 14 is connected to a compressor 17 via a regulator 15 and a flow meter 16. Each injection well 4 has an airtight structure except for the lower end 18 in the soil. A small-diameter hole (not shown) through which compressed air can pass is formed in the lower end portion 18 of each injection well 4, and the periphery of the hole is covered with a strainer 9. The air injection amount is appropriately changed depending on the air permeability of the soil S to be purified, the arrangement state of each well, and the like, for example, 30 L / min to 50 L / min with respect to 1 m 3 of soil. .

以上のように構成された土壌浄化装置1を用いた土壌浄化方法について説明する。   A soil purification method using the soil purification apparatus 1 configured as described above will be described.

まず、図2に示す真空ポンプ6を作動させることにより、吸引井戸2に接続された吸引管5から吸引井戸2内の雰囲気を吸引する。これにより、吸引井戸内の圧力が吸引井戸2の周囲の土壌Sの雰囲気に対して負圧となることから、吸引井戸2の下端部8に形成された小径の穴(図示せず)を介して、吸引井戸内に土壌中の雰囲気が流入する。すなわち、吸引井戸2により土壌中の雰囲気が吸引される。このときの土壌中の雰囲気の吸引範囲は、吸引井戸2の下端部8の近傍の雰囲気に限られず、浄化対象とする土壌全体に及ぶ。   First, the atmosphere in the suction well 2 is sucked from the suction pipe 5 connected to the suction well 2 by operating the vacuum pump 6 shown in FIG. Thereby, since the pressure in the suction well becomes a negative pressure with respect to the atmosphere of the soil S around the suction well 2, the small diameter hole (not shown) formed in the lower end portion 8 of the suction well 2 is used. Thus, the atmosphere in the soil flows into the suction well. That is, the atmosphere in the soil is sucked by the suction well 2. The suction range of the atmosphere in the soil at this time is not limited to the atmosphere in the vicinity of the lower end portion 8 of the suction well 2, but extends to the entire soil to be purified.

次に、各加熱井戸3に挿入されたヒーター10を作動させる。ヒーター10の熱は、加熱井戸全体に伝わり、各加熱井戸3の周囲の土壌Sの温度を上昇させる。このとき、図1に示すように、各加熱井戸3は、平面視において、吸引井戸2を中心とする正六角形の頂点上に設けられているため、各加熱井戸3に囲まれた土壌Sは、均一に加熱される。このとき、浄化対象となる土壌の深度によっては、十分に加熱できていない部分が存在する場合がある。その場合は、ヒーター10の設置深度を変更すればよい。これにより、浄化対象となる土壌Sを十分に加熱することができる。   Next, the heater 10 inserted in each heating well 3 is operated. The heat of the heater 10 is transmitted to the whole heating well and raises the temperature of the soil S around each heating well 3. At this time, as shown in FIG. 1, each heating well 3 is provided on the top of a regular hexagon centering on the suction well 2 in a plan view, so that the soil S surrounded by each heating well 3 is , Uniformly heated. At this time, depending on the depth of the soil to be purified, there may be a portion that is not sufficiently heated. In that case, the installation depth of the heater 10 may be changed. Thereby, the soil S to be purified can be sufficiently heated.

また、各加熱井戸3から生じる熱の影響を及ぼす範囲(加熱範囲)は、各加熱井戸3を中心として円形に広がるため、吸引井戸2を囲むように配置された各加熱井戸3の加熱範囲は重複する。これにより、加熱範囲が重複する部分では加熱能力が高まり、各加熱井戸3に囲まれた土壌Sを効率良く加熱することができる。各加熱井戸3により土壌Sが加熱される結果、土壌Sに含まれる汚染物質が気化する。   Moreover, since the range (heating range) in which the heat generated from each heating well 3 affects is expanded in a circle around each heating well 3, the heating range of each heating well 3 arranged so as to surround the suction well 2 is Duplicate. Thereby, a heating capability increases in the part which a heating range overlaps, and the soil S enclosed by each heating well 3 can be heated efficiently. As a result of heating the soil S by each heating well 3, the contaminant contained in the soil S is vaporized.

次に、コンプレッサー17を作動させる。コンプレッサー17により圧縮された空気は、レギュレーター15で圧力が調整され、各注入管14から各注入井戸4に注入される。注入された圧縮空気は、土壌Sの通気性の良否に関わらず、土壌Sの間隙中を流れていく。これにより、土壌中の通気性の悪い部分の雰囲気の移動を促進させることができ、気化した汚染物質が土壌中の通気性の悪い部分に滞留しなくなる。その結果、土壌中において気化した汚染物質を全て吸引井戸2により吸引することができ、効率良く汚染物質を除去することができる。   Next, the compressor 17 is operated. The pressure of the air compressed by the compressor 17 is adjusted by the regulator 15 and is injected from the injection pipes 14 to the injection wells 4. The injected compressed air flows through the gaps in the soil S regardless of whether the air permeability of the soil S is good or bad. Thereby, the movement of the atmosphere of the poorly breathable portion in the soil can be promoted, and the vaporized contaminant does not stay in the poorly breathable portion of the soil. As a result, all the pollutants evaporated in the soil can be sucked by the suction well 2, and the pollutants can be efficiently removed.

また、図1に示すように、吸引井戸2を囲むようにして各注入井戸4が配置されているため、各注入井戸4に囲まれた土壌Sに対して圧縮空気を均一に注入することができる。これにより、土壌中の雰囲気を効率良く移動させることができる。   Moreover, as shown in FIG. 1, since each injection well 4 is arrange | positioned so that the suction well 2 may be enclosed, compressed air can be uniformly inject | poured with respect to the soil S enclosed by each injection well 4. As shown in FIG. Thereby, the atmosphere in soil can be moved efficiently.

そして、吸引井戸2に吸引された汚染物質は、吸引管5を通って汚染物質処理装置7に流入する。この汚染物質処理装置7において、汚染物質が無害化され大気に放出される。以上のようにして、汚染された土壌Sは浄化される。   The contaminant sucked into the suction well 2 flows into the contaminant treatment device 7 through the suction pipe 5. In this pollutant processing apparatus 7, the pollutant is rendered harmless and released to the atmosphere. As described above, the contaminated soil S is purified.

以上、本発明によれば、各加熱井戸内にヒーターを設けることにより、土壌を十分に加熱して汚染物質の気化を促進させると共に、各注入井戸内に圧縮空気を注入することにより、土壌中の雰囲気の移動を促進させることができる。これにより、気化した汚染物質を確実に吸引することができ、土壌の浄化効率を向上させることができる。   As described above, according to the present invention, by providing a heater in each heating well, the soil is sufficiently heated to promote the vaporization of pollutants, and by injecting compressed air into each injection well, The movement of the atmosphere can be promoted. Thereby, the vaporized contaminant can be attracted | sucked reliably and the purification | cleaning efficiency of soil can be improved.

また、従来の加熱空気を注入する浄化装置では、加熱空気の温度を本発明が例示するヒーターの発熱温度である300℃〜600℃まで加熱することは困難であった。これに加えて、加熱空気が加熱井戸内に注入されると、加熱空気の温度が加熱井戸内で低下してしまい、土壌を十分に加熱できないおそれもある。これに対して、本発明では、加熱空気では到達し得ない温度を有するヒーターを、加熱井戸内に設けたため、加熱後の土壌温度を従来よりも高くすることができると共に、加熱井戸内の温度低下も抑制することができる。この結果、土壌を十分に加熱することができ、汚染物質の気化を促進させることができる。   Moreover, in the conventional purification apparatus which inject | pours heated air, it was difficult to heat the temperature of heated air to 300 to 600 degreeC which is the heat_generation | fever temperature of the heater which this invention illustrates. In addition to this, when heated air is injected into the heated well, the temperature of the heated air decreases in the heated well, and the soil may not be heated sufficiently. On the other hand, in the present invention, the heater having a temperature that cannot be reached by heated air is provided in the heating well, so that the soil temperature after heating can be made higher than before, and the temperature in the heating well The decrease can also be suppressed. As a result, the soil can be sufficiently heated and the vaporization of the pollutant can be promoted.

また、本発明では、ヒーターを加熱井戸内に設けたことから、従来の加熱空気を注入するための大型の加熱設備が不要となる。さらにヒーターの使い回しも可能であることから、土壌浄化装置を容易に移動することができる。このため、従来の土壌浄化装置では達成し得ない、浄化完了後の土壌浄化装置の撤去、及び異なる土壌への再設置を容易に行うことができる。   Moreover, in this invention, since the heater was provided in the heating well, the conventional large-sized heating equipment for injecting heated air becomes unnecessary. Furthermore, since the heater can be reused, the soil purification apparatus can be easily moved. For this reason, the removal of the soil purification apparatus after completion of purification, and the re-installation to a different soil which cannot be achieved with the conventional soil purification apparatus can be easily performed.

以上、本発明の好適な実施形態について説明したが、本発明はかかる例に限定されない。当業者であれば、特許請求の範囲に記載された技術的思想の範疇内において、各種の変更例または修正例に想到しうることは明らかであり、それらについても当然に本発明の技術的範囲に属するものと了解される。   As mentioned above, although preferred embodiment of this invention was described, this invention is not limited to this example. It is obvious for those skilled in the art that various changes or modifications can be conceived within the scope of the technical idea described in the claims. It is understood that it belongs to.

例えば、本発明の実施の形態では、加熱井戸及び注入井戸を6本ずつ設けることとしたが、各井戸の数はこれに限定されるものではなく、浄化対象の土壌の広さ等に応じて適宜変更されるものである。また、本発明の実施の形態では、吸引井戸を中心とする正六角形の頂点上及び辺上に各加熱井戸及び各注入井戸を配置したが、各井戸の配置はこれに限定されるものではなく、吸引井戸を囲むように加熱井戸及び注入井戸を配置する構成であれば、本実施の形態で説明した作用効果を享受することができる。また、各井戸の形状は、円管形状に限られるものではなく、角管形状やその他の形状であっても良い。すなわち、土壌中に形成された孔に管状の金属部材を挿入するものは、本発明の技術的範囲に属する。   For example, in the embodiment of the present invention, six heating wells and six injection wells are provided, but the number of each well is not limited to this, depending on the size of the soil to be purified, etc. It is changed as appropriate. In the embodiment of the present invention, the heating wells and the injection wells are arranged on the apexes and sides of the regular hexagon centering on the suction well, but the arrangement of the wells is not limited to this. If it is the structure which arrange | positions a heating well and an injection well so that a suction well may be enclosed, the effect demonstrated in this Embodiment can be enjoyed. The shape of each well is not limited to a circular tube shape, and may be a square tube shape or other shapes. That is, what inserts a tubular metal member in the hole formed in soil belongs to the technical scope of the present invention.

また、例えば、本発明の実施の形態では、各加熱井戸3を土壌中に設けることとしたが、各加熱井戸3の設置深度をさらに下げて、図3に示すように、各加熱井戸3の下端部を地下水GWに浸漬させても良い。この場合、各加熱井戸3から生じる熱により地下水GWの温度も上昇させることができる。これにより、土壌中の汚染物質と共に地下水中の汚染物質も気化させることができる。すなわち、このような構成を有する本発明によれば、土壌のみならず地下水の汚染も浄化することができる。   In addition, for example, in the embodiment of the present invention, each heating well 3 is provided in the soil, but the installation depth of each heating well 3 is further reduced, and as shown in FIG. You may immerse a lower end part in groundwater GW. In this case, the temperature of the groundwater GW can also be raised by the heat generated from each heating well 3. Thereby, the contaminant in groundwater can be vaporized together with the contaminant in soil. That is, according to the present invention having such a configuration, not only soil but also groundwater contamination can be purified.

また、図3に示すように、各注入井戸4の下端部18を地下水GWに浸漬させても良い。この場合、圧縮空気の注入深度が低くなるため、注入された空気の拡散範囲が拡大し、より広範囲の土壌Sに圧縮空気を送り込むことができる。また、地下水中に圧縮空気を注入した場合、好機性微生物活性による汚染物質の浄化効果も期待できる。   Moreover, as shown in FIG. 3, you may immerse the lower end part 18 of each injection well 4 in the groundwater GW. In this case, since the injection depth of the compressed air is lowered, the diffusion range of the injected air is expanded, and the compressed air can be fed into a wider range of soil S. In addition, when compressed air is injected into the groundwater, the effect of purifying contaminants due to the microbial activity can be expected.

また、図3に示すように、気化した汚染物質の流出を防ぐ遮蔽物20を用いて、浄化対象となる土壌Sの地表面GLを覆うようにしても良い。この場合、吸引管5及び注入管14は、遮蔽物20を貫通するようにして吸引井戸2及び注入井戸4に接続される。このようにして地表面GLを遮蔽物20で覆った場合、土壌浄化中に地表面GLから流出してしまった気化汚染物質が大気へ流出してしまうことを防止することができる。なお、地表面GLと遮蔽物20との間に存在する気化汚染物質は、地表面GLあるいは注入井戸4を通って土壌中に戻り、吸引井戸2から吸引される。また、遮蔽物20とは、例えばコンクリートである。   Moreover, as shown in FIG. 3, you may make it cover the ground surface GL of the soil S used as the purification | cleaning object using the shielding 20 which prevents the outflow of the vaporized contaminant. In this case, the suction pipe 5 and the injection pipe 14 are connected to the suction well 2 and the injection well 4 so as to penetrate the shield 20. When the ground surface GL is covered with the shield 20 in this way, it is possible to prevent the vaporized pollutant that has flowed out of the ground surface GL during the soil purification from flowing out to the atmosphere. The vaporized contaminants existing between the ground surface GL and the shield 20 return to the soil through the ground surface GL or the injection well 4 and are sucked from the suction well 2. Moreover, the shielding object 20 is concrete, for example.

また、各井戸を構成する金属部材の外側面と、土壌中に形成された孔の内面は密接していることが好ましい。吸引井戸を構成する金属部材の外側面が孔の内面に密接している場合、吸引井戸の下端部から土壌中の雰囲気を吸引する際に、金属部材の外側面と孔の内面との間に形成された隙間に地表面からの大気雰囲気が入り込まなくなる。その結果、吸引井戸により土壌中の雰囲気のみを効率良く吸引することができる。また、加熱井戸を構成する金属部材の外側面が孔の内面に密接している場合、金属部材の外側面と孔の内面との間に形成された隙間に地表面からの大気雰囲気が入り込まなくなる。その結果、加熱井戸の熱を土壌に直接伝達させることができ、効率良く土壌を加熱することができる。また、注入井戸を構成する金属部材の外側面が孔の内面に密接している場合、注入井戸の下端部から土壌中に注入した空気が、金属部材の外側面と孔の内面との間に形成された隙間を通って地表面に漏れることがなくなる。その結果、注入井戸により土壌中に効率良く空気を注入することができる。   Moreover, it is preferable that the outer surface of the metal member which comprises each well and the inner surface of the hole formed in soil are closely_contact | adhered. When the outer surface of the metal member constituting the suction well is in close contact with the inner surface of the hole, when the atmosphere in the soil is sucked from the lower end of the suction well, the space between the outer surface of the metal member and the inner surface of the hole is The atmospheric atmosphere from the ground surface does not enter the formed gap. As a result, only the atmosphere in the soil can be efficiently sucked by the suction well. Further, when the outer surface of the metal member constituting the heating well is in close contact with the inner surface of the hole, the atmospheric atmosphere from the ground surface does not enter the gap formed between the outer surface of the metal member and the inner surface of the hole. . As a result, the heat of the heating well can be directly transmitted to the soil, and the soil can be efficiently heated. In addition, when the outer surface of the metal member constituting the injection well is in close contact with the inner surface of the hole, the air injected into the soil from the lower end of the injection well is between the outer surface of the metal member and the inner surface of the hole. It will not leak to the ground surface through the formed gap. As a result, air can be efficiently injected into the soil by the injection well.

(実施例1)
本発明に係る加熱井戸が発する熱の伝達範囲(加熱範囲)について調査した。調査は、図4に示すように、加熱井戸の穴中心から0.5m、1.0m、2.0m、3.0mの位置に測定井戸を設けて実地で行った。各測定井戸の中には、地表面から0.2m(GL.−0.2m)、1.0m(GL.−1.0m)、2.0m(GL.−2.0m)、3.0m(GL.−3.0m)の位置に熱電対が取り付けられている。このような構成で加熱井戸内のヒーターを作動させて、経過時間と土壌温度の関係について測定を行った。結果を図5に示す。なお、実地調査に用いたヒーターは、能力が2.5kwh/m、長さが1.0mのものを用いた。
Example 1
The heat transfer range (heating range) generated by the heating well according to the present invention was investigated. As shown in FIG. 4, the investigation was conducted in the field by providing measurement wells at positions 0.5 m, 1.0 m, 2.0 m, and 3.0 m from the hole center of the heating well. In each measurement well, 0.2 m (GL.-0.2 m), 1.0 m (GL.-1.0 m), 2.0 m (GL.-2.0 m), 3.0 m from the ground surface. A thermocouple is attached at the position (GL.-3.0 m). The heater in the heating well was operated with such a configuration, and the relationship between elapsed time and soil temperature was measured. The results are shown in FIG. In addition, the heater used for the field survey used the capacity | capacitance of 2.5 kwh / m and a length of 1.0 m.

図5によれば、加熱井戸から離れるに従い、加熱井戸の熱の影響が低下していくことがわかる。加熱井戸からの距離が2.0mと3.0mのときでは、測定結果にほぼ違いはないため、加熱井戸からの距離が2.0mの時点では、既に加熱井戸の熱の影響を受けていないものと考えられる。このため、加熱井戸からの距離が0.5m、1.0m、2.0mの測定結果を比較した場合の土壌に対する熱の影響の減衰を考慮すると、加熱井戸の加熱範囲の上限は、加熱井戸からの距離が1.5mであるといえる。   According to FIG. 5, it can be seen that as the distance from the heating well increases, the influence of the heating well heat decreases. When the distance from the heating well is 2.0 m and 3.0 m, there is almost no difference in the measurement results. Therefore, when the distance from the heating well is 2.0 m, it is not already affected by the heat of the heating well. It is considered a thing. For this reason, the upper limit of the heating range of the heating well is determined by considering the attenuation of the effect of heat on the soil when the measurement results of the distance from the heating well are 0.5 m, 1.0 m, and 2.0 m are compared. It can be said that the distance from is 1.5 m.

(実施例2)
次に、加熱井戸を地下水に浸漬させた場合の地下水の温度変化について調査した。調査は実地で行い、図6に示すように、吸引井戸2を囲むようにして正三角形の頂点上に加熱井戸3を配置した。加熱井戸を加熱した結果、3つの加熱井戸に囲まれた地下水をほぼ均一に加熱することができた。
(Example 2)
Next, the temperature change of the groundwater when the heated well was immersed in the groundwater was investigated. The investigation was conducted in the field, and as shown in FIG. 6, the heating well 3 was arranged on the apex of the equilateral triangle so as to surround the suction well 2. As a result of heating the heating well, the groundwater surrounded by the three heating wells could be heated almost uniformly.

(実施例3)
次に、地下水に灯油が漏洩した現場において灯油の回収を行った。回収の初期段階では揚水のみで回収を行い、その後、本発明によって回収を行った。結果を図7に示す。なお、各井戸の配置は、実施例2と同様であり、吸引井戸2の吸引圧は、−0.2MPaとした。図7に示すように、揚水のみによる回収では、経過日数と共に灯油の回収量が低下していき、100日後には灯油の回収量がほぼ横ばいとなった。その後、加熱井戸3を加熱して地下水温を上昇させた後に、吸引井戸2により吸引したところ、灯油回収量が増加し、200日後には全ての灯油を回収することができた。すなわち、本発明によれば、従来の浄化装置では除去できない汚染物質も除去することができる。
(Example 3)
Next, kerosene was collected at the site where kerosene leaked into the groundwater. In the initial stage of recovery, recovery was performed only with pumped water, and then recovery was performed according to the present invention. The results are shown in FIG. In addition, arrangement | positioning of each well was the same as that of Example 2, and the suction pressure of the suction well 2 was made into -0.2MPa. As shown in FIG. 7, in the recovery using only pumped water, the recovery amount of kerosene decreased with the elapsed days, and after 100 days, the recovery amount of kerosene was almost flat. Thereafter, the heating well 3 was heated to raise the groundwater temperature, and then suctioned by the suction well 2, the amount of kerosene recovered increased, and after 200 days, all kerosene could be recovered. That is, according to the present invention, it is possible to remove contaminants that cannot be removed by the conventional purification apparatus.

(実施例4)
次に、TCE(トリクロロエチレン)を含有させた模擬試験土壌及び模擬試験地下水を用いて、模擬試験土壌に注入する空気の通気量とTCE濃度の関係を調査した。模擬試験土壌及び模擬試験地下水は、TCEを含有させた土壌及び水を1ヶ月間養生したものである。また、通気時間は3時間とし、試験中の模擬試験土壌の温度及び模擬試験地下水の温度は一定とした。このような試験を温度条件を変えて3回行った。
Example 4
Next, the relationship between the air flow rate of the air injected into the simulated test soil and the TCE concentration was investigated using simulated test soil and simulated test groundwater containing TCE (trichlorethylene). The simulated test soil and the simulated test groundwater are obtained by curing soil and water containing TCE for one month. The aeration time was 3 hours, and the temperature of the simulated test soil during the test and the temperature of the simulated test groundwater were constant. Such a test was performed three times while changing the temperature conditions.

土壌中のTCE濃度の変化を図8(a)に、模擬試験地下水中のTCE濃度の変化を図8(b)に示す。なお、図8に示す縦軸は、模擬試験土壌又は模擬試験地下水中に残存するTCEの濃度Cと、TCEの初期濃度Cとの比である。また、図8に示す横軸は、注入する空気の体積と模擬試験土壌の体積との比であり、例えば横軸の5は、模擬試験土壌体積に対して5倍の体積の空気を注入することを意味する。 The change in the TCE concentration in the soil is shown in FIG. 8A, and the change in the TCE concentration in the simulated test groundwater is shown in FIG. 8B. The vertical axis shown in FIG. 8 is the ratio between the concentration C of TCE remaining in the simulated test soil or the simulated test ground water and the initial concentration C 0 of TCE. The horizontal axis shown in FIG. 8 is the ratio of the volume of air to be injected and the volume of the simulated test soil. Means that.

図8(a)及び図8(b)によれば、通気量を増大させることにより、TCE濃度が急激に低下することがわかる。また、その傾向は、温度が高ければ高いほど顕著になる。すなわち、本発明のように土壌を十分に加熱し、圧縮空気を土壌中に注入すれば、効率良く汚染物質を除去できることがわかる。   According to FIG. 8A and FIG. 8B, it can be seen that the TCE concentration rapidly decreases by increasing the air flow rate. The tendency becomes more prominent as the temperature is higher. That is, it can be seen that if the soil is sufficiently heated as in the present invention and compressed air is injected into the soil, the pollutants can be efficiently removed.

本発明は、汚染物質に汚染された土壌を浄化する土壌浄化方法及び土壌浄化装置に適用できる。   The present invention can be applied to a soil purification method and a soil purification apparatus for purifying soil contaminated with pollutants.

1 土壌浄化装置
2 吸引井戸
3 加熱井戸
4 注入井戸
5 吸引管
6 真空ポンプ
7 汚染物質処理装置
8 吸引井戸下端部
9 ストレーナ
10 ヒーター
11 電線
12 温調器
13 熱電対
14 注入管
15 レギュレーター
16 流量計
17 コンプレッサー
18 注入井戸下端部
19 加熱井戸下端部
20 遮蔽物
S 土壌
GL 地表面
GW 地下水
DESCRIPTION OF SYMBOLS 1 Soil purification apparatus 2 Suction well 3 Heating well 4 Injection well 5 Suction pipe 6 Vacuum pump 7 Contaminant processing apparatus 8 Suction well lower end part 9 Strainer 10 Heater 11 Electric wire 12 Temperature controller 13 Thermocouple 14 Injection pipe 15 Regulator 16 Flow meter 17 Compressor 18 Lower end of injection well 19 Lower end of heating well 20 Shield S Soil GL Ground surface GW Groundwater

Claims (20)

土壌中で気化した汚染物質を、土壌中に設けられた吸引井戸から吸引することにより土壌を浄化する土壌浄化方法であって、
土壌中に設けられた加熱井戸に挿入されたヒーターにより土壌を加熱し、
土壌中に設けられた注入井戸を介して、土壌中に空気を注入することを特徴とする土壌浄化方法。
A soil purification method for purifying soil by sucking contaminants vaporized in the soil from a suction well provided in the soil,
The soil is heated by a heater inserted in a heating well provided in the soil,
A soil purification method comprising injecting air into soil through an injection well provided in the soil.
前記加熱井戸の下端部を地下水中に浸漬させることを特徴とする請求項1に記載の土壌浄化方法。   The soil purification method according to claim 1, wherein a lower end portion of the heating well is immersed in groundwater. 前記注入井戸の下端部を地下水中に浸漬させることを特徴とする請求項1又は請求項2に記載の土壌浄化方法。   The soil purification method according to claim 1 or 2, wherein a lower end portion of the injection well is immersed in groundwater. 前記加熱井戸を複数設け、前記吸引井戸を囲むようにして各加熱井戸を配置することを特徴とする請求項1〜3のいずれかに記載の土壌浄化方法。   The soil purification method according to any one of claims 1 to 3, wherein a plurality of the heating wells are provided, and each heating well is disposed so as to surround the suction well. 各加熱井戸の穴中心と前記吸引井戸の穴中心との距離をそれぞれ等しくすることを特徴とする請求項4に記載の土壌浄化方法。   The soil purification method according to claim 4, wherein the distance between the hole center of each heating well and the hole center of the suction well is made equal. 各加熱井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角をそれぞれ等しくすることを特徴とする請求項4又は請求項5に記載の土壌浄化方法。   The soil purification method according to claim 4 or 5, wherein angles formed by straight lines connecting the hole center of each heating well and the hole center of the suction well are made equal to each other. 前記注入井戸を複数設け、前記吸引井戸を囲むようにして各注入井戸を配置することを特徴とする請求項1〜6のいずれかに記載の土壌浄化方法。   The soil purification method according to any one of claims 1 to 6, wherein a plurality of the injection wells are provided and the injection wells are arranged so as to surround the suction well. 各注入井戸の穴中心と前記吸引井戸の穴中心との距離をそれぞれ等しくすることを特徴とする請求項7に記載の土壌浄化方法。   The soil purification method according to claim 7, wherein the distance between the center of each injection well and the center of the suction well is made equal. 各注入井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角をそれぞれ等しくすることを特徴とする請求項7又は請求項8に記載の土壌浄化方法。   The soil purification method according to claim 7 or 8, wherein angles formed by straight lines connecting the hole centers of the injection wells and the hole centers of the suction wells are made equal to each other. 気化した汚染物質の流出を防ぐ遮蔽物を用いて地表面を覆うことを特徴とする請求項1〜9のいずれかに記載の土壌浄化方法。   The soil purification method according to any one of claims 1 to 9, wherein the ground surface is covered with a shield that prevents the vaporized pollutant from flowing out. 土壌中で気化した汚染物質を吸引できる構成を有する吸引井戸を備えた土壌浄化装置であって、
土壌中に設けられた加熱井戸と、
土壌中に設けられ、土壌中に空気を注入できる構成を有する注入井戸と、
前記吸引井戸に接続され、前記吸引井戸内の雰囲気を吸引する吸引管と、
前記加熱井戸に挿入されるように設けられたヒーターと、
前記注入井戸に空気を注入する注入管とを備えていることを特徴とする土壌浄化装置。
A soil purification apparatus comprising a suction well having a configuration capable of sucking contaminants vaporized in soil,
A heating well provided in the soil;
An injection well provided in the soil and having a configuration capable of injecting air into the soil;
A suction pipe connected to the suction well for sucking the atmosphere in the suction well;
A heater provided to be inserted into the heating well;
A soil purification apparatus comprising an injection pipe for injecting air into the injection well.
前記加熱井戸の下端部が地下水中に浸漬するように設けられていることを特徴とする請求項11に記載の土壌浄化装置。   The soil purification apparatus according to claim 11, wherein a lower end portion of the heating well is provided so as to be immersed in groundwater. 前記注入井戸の下端部が地下水中に浸漬するように設けられていることを特徴とする請求項11又は請求項12に記載の土壌浄化装置。   The soil purification apparatus according to claim 11 or 12, wherein a lower end portion of the injection well is provided so as to be immersed in groundwater. 前記加熱井戸が複数設けられ、各加熱井戸が前記吸引井戸を囲むように配置されていることを特徴とする請求項11〜13のいずれかに記載の土壌浄化装置。   The soil purification apparatus according to any one of claims 11 to 13, wherein a plurality of the heating wells are provided, and each heating well is disposed so as to surround the suction well. 各加熱井戸の穴中心と前記吸引井戸の穴中心との距離がそれぞれ等しくなるように各加熱井戸が配置されていることを特徴とする請求項14に記載の土壌浄化装置。   The soil purification apparatus according to claim 14, wherein each heating well is disposed so that a distance between a hole center of each heating well and a hole center of the suction well is equal. 各加熱井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角がそれぞれ等しくなるように各加熱井戸が配置されていることを特徴とする請求項14又は請求項15に記載の土壌浄化装置。   16. Each heating well is arrange | positioned so that the angle | corner which the straight line which ties the hole center of each heating well and the hole center of the said suction well makes becomes equal, respectively. Soil purification device. 前記注入井戸が複数設けられ、各注入井戸が前記吸引井戸を囲むように配置されていることを特徴とする請求項11〜16のいずれかに記載の土壌浄化装置。   The soil purification apparatus according to any one of claims 11 to 16, wherein a plurality of the injection wells are provided, and each injection well is disposed so as to surround the suction well. 各注入井戸の穴中心と前記吸引井戸の穴中心との距離がそれぞれ等しくなるように各注入井戸が配置されていることを特徴とする請求項17に記載の土壌浄化装置。   18. The soil purification apparatus according to claim 17, wherein each of the injection wells is disposed so that a distance between a hole center of each injection well and a hole center of the suction well is equal. 各注入井戸の穴中心と前記吸引井戸の穴中心とを結ぶ直線同士のなす角がそれぞれ等しくなるように各注入井戸が配置されていることを特徴とする請求項17又は請求項18に記載の土壌浄化装置。   19. The injection wells according to claim 17, wherein the injection wells are arranged so that angles formed by straight lines connecting the hole centers of the injection wells and the hole centers of the suction wells are equal to each other. Soil purification device. 気化した汚染物質の流出を防ぐ遮蔽物を備え、前記遮蔽物は、地表面を覆うように配置され、前記吸引管及び前記注入管が前記遮蔽物を貫通するようにして設けられていることを特徴とする請求項11〜19のいずれかに記載の土壌浄化装置。

It is provided with a shield that prevents the vaporized pollutant from flowing out, the shield is disposed so as to cover the ground surface, and the suction pipe and the injection tube are provided so as to penetrate the shield. The soil purification apparatus according to any one of claims 11 to 19, characterized in that

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