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JP7639381B2 - Soil or groundwater purification method - Google Patents
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JP7639381B2 - Soil or groundwater purification method - Google Patents

Soil or groundwater purification method Download PDF

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JP7639381B2
JP7639381B2 JP2021019964A JP2021019964A JP7639381B2 JP 7639381 B2 JP7639381 B2 JP 7639381B2 JP 2021019964 A JP2021019964 A JP 2021019964A JP 2021019964 A JP2021019964 A JP 2021019964A JP 7639381 B2 JP7639381 B2 JP 7639381B2
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剛 塩谷
渉 田村
徳也 奥津
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Kurita Water Industries Ltd
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本発明は、土壌又は地下水の浄化方法に係り、特に土壌又は地下水中の揮発性有機化合物(VOCs)を電気発熱法により処理する方法に関する。 The present invention relates to a method for purifying soil or groundwater, and in particular to a method for treating volatile organic compounds (VOCs) in soil or groundwater using an electric heating method.

有機塩素系化合物等の揮発性化合物で汚染された土壌に間隔を隔てて電極を差し込み、電極間に電圧印加して通電し、通電によるジュール熱により揮発性化合物を溶出させて、除去する電気発熱法がある(特許文献1)。 There is an electric heating method in which electrodes are inserted at intervals into soil contaminated with volatile compounds such as organochlorine compounds, a voltage is applied between the electrodes to pass electricity, and the volatile compounds are dissolved and removed by Joule heat generated by the current (Patent Document 1).

電気発熱法により土壌又は地下水を浄化する方法においては、複数の電極を浄化対象となる土壌中に挿入し、電極間に電圧を印加してそれらの間の土壌に電流を流すことで、土壌の電気抵抗によりジュール熱を発生させて加温する。土壌の温度が上昇すると、土壌粒子に吸着しているテトラクロロエチレン(PCE)、トリクロロエチレン(TCE)、ジクロロエチレン(DCE)、トリクロロエタン等のVOCs(Volatile Organic Compounds/揮発性有機化合物)が土壌から脱離して地下水中に溶出する。この地下水を地上に汲み上げる揚水処理や、地下水からガス化したVOCsを含む地下ガスを吸引するガス吸引処理等を行うことにより、VOCsが土壌又は地下水から除去され、土壌又は地下水が浄化される。 In a method for purifying soil or groundwater using electrical heating, multiple electrodes are inserted into the soil to be purified, and a voltage is applied between the electrodes to pass an electric current through the soil between them, generating Joule heat due to the electrical resistance of the soil and heating it. When the temperature of the soil rises, VOCs (volatile organic compounds) such as tetrachloroethylene (PCE), trichloroethylene (TCE), dichloroethylene (DCE), and trichloroethane that are adsorbed to the soil particles are released from the soil and eluted into the groundwater. The VOCs are removed from the soil or groundwater, and the soil or groundwater is purified by performing a pumping process in which the groundwater is pumped to the surface, or a gas suction process in which underground gas containing VOCs that has been gasified from the groundwater is sucked in.

特開2016-159259号公報JP 2016-159259 A

土壌の不飽和層に電気発熱法を適用する場合、飽和層に比べて含水率が小さく、通電量が少ないために、温度が上昇しづらく、40℃程度までしか昇温しないことがある。VOCsは、沸点が50℃以上(PCE:121℃、TCE:87℃、DCE:55℃)であることが多いため、土壌ガス吸引法を適用してもVOCsの回収量が少ないという問題があった。 When applying the electric heating method to the unsaturated layer of soil, the water content is lower than in the saturated layer, and the amount of electricity passing through is small, so the temperature does not rise easily and may only rise to around 40°C. Since VOCs often have a boiling point of 50°C or higher (PCE: 121°C, TCE: 87°C, DCE: 55°C), there was a problem that the amount of VOCs recovered was small even when the soil gas suction method was applied.

本発明は、不飽和層の土壌又は地下水を電気発熱法により効率よく浄化することができる土壌又は地下水の浄化方法を提供することを目的とする。 The present invention aims to provide a method for purifying soil or groundwater that can efficiently purify unsaturated soil or groundwater using an electric heating method.

本発明の一態様の土壌又は地下水の浄化方法は、揮発性有機化合物で汚染された不飽和層を電気発熱法により浄化する方法において、該不飽和層に注水することを特徴とする。 One aspect of the present invention is a method for purifying soil or groundwater by using an electric heating method to purify an unsaturated layer contaminated with volatile organic compounds, and is characterized in that water is poured into the unsaturated layer.

本発明の一態様では、前記不飽和層を60℃以上にまで昇温させる。 In one embodiment of the present invention, the unsaturated layer is heated to 60°C or higher.

本発明の一態様では、前記揮発性有機化合物は、テトラクロロエチレン、トリクロロエチレン、ジクロロエチレン、及びトリクロロエタンの少なくとも1種を含む。 In one embodiment of the present invention, the volatile organic compound includes at least one of tetrachloroethylene, trichloroethylene, dichloroethylene, and trichloroethane.

本発明の土壌又は地下水の浄化方法の一態様によると、注入井戸等から不飽和層に注水し、不飽和層の含水率を上昇させた状態で電気発熱法を適用する。その結果、不飽和層に注水しない場合と比較して、通電量が増加し、温度が上昇する。これにより、VOCsの回収量を増加させることができる。また、浄化処理時間の短縮を図ることもできる。 According to one embodiment of the soil or groundwater purification method of the present invention, water is injected into the unsaturated layer from an injection well or the like, and the water content of the unsaturated layer is increased, and then an electric heating method is applied. As a result, the amount of electricity flow increases and the temperature rises compared to when water is not injected into the unsaturated layer. This makes it possible to increase the amount of VOCs recovered. It also makes it possible to shorten the purification process time.

実施の形態に係る土壌の浄化方法を説明する地盤の断面図である。1 is a cross-sectional view of ground illustrating a soil purification method according to an embodiment of the present invention. 実施例における測定結果を示すグラフである。1 is a graph showing measurement results in an example.

以下、図面を参照して本発明の一実施形態について詳細に説明する。 Below, one embodiment of the present invention will be described in detail with reference to the drawings.

本発明の一態様では、図1のように、飽和層11の上に不飽和層12が存在する土壌10において、不飽和層12のVOCsを電気発熱法により除去する。 In one embodiment of the present invention, as shown in FIG. 1, in soil 10 in which an unsaturated layer 12 exists above a saturated layer 11, VOCs in the unsaturated layer 12 are removed by an electrical heating method.

VOCsで汚染された不飽和層12に多数の孔1aが穿孔されたパイプ1と、複数の電極2を打ち込む。電極2に電源装置3を接続する。パイプ1に対し、タンク4内の水を給水ポンプ5及び配管6を介して供給可能とする。また、パイプ1の上端に、吸引配管7を接続し、吸引ポンプ8を介してVOCsガスをガス処理設備9に送気可能とする。 A pipe 1 with numerous holes 1a drilled therein and multiple electrodes 2 are driven into the unsaturated layer 12 contaminated with VOCs. A power supply unit 3 is connected to the electrodes 2. Water in a tank 4 can be supplied to the pipe 1 via a water supply pump 5 and piping 6. In addition, a suction piping 7 is connected to the upper end of the pipe 1, and VOCs gas can be sent to a gas treatment facility 9 via a suction pump 8.

なお、不飽和層12と飽和層11との界面深さについては、予めボーリング調査又は電気伝導計を有したプローブを土壌に打ち込んで行った電気伝導度調査などにより決定しておく。また、このボーリング調査又は電気伝導計の検出電気伝導度に基づいて不飽和層12の含水率を測定しておく。 The depth of the interface between the unsaturated layer 12 and the saturated layer 11 is determined in advance by a boring survey or an electrical conductivity survey conducted by driving a probe with an electrical conductivity meter into the soil. The moisture content of the unsaturated layer 12 is also measured based on the electrical conductivity detected by the boring survey or the electrical conductivity meter.

パイプ1及び電極2は、不飽和層12と飽和層11との界面直上まで打ち込むことが好ましい。 It is preferable to drive the pipe 1 and electrode 2 up to just above the interface between the unsaturated layer 12 and the saturated layer 11.

不飽和層12のVOCs除去作業を開始するに当っては、まず給水ポンプ5を作動させ、不飽和層12中に水を供給(圧入)し、不飽和層12の含水率を高めて電気伝導度を上昇させる。 When starting the VOCs removal work in the unsaturated layer 12, first operate the water supply pump 5 to supply (pressurize) water into the unsaturated layer 12, increasing the water content of the unsaturated layer 12 and increasing the electrical conductivity.

不飽和層12への水の注入量は、予め行ったボーリング調査又はプローブ打ち込み調査により測定した含水率により決定してもよく、パイプ1から所定距離離隔した地点において不飽和層12に打ち込んだプローブの電気伝導度計によって電気伝導度をモニタリングし、電気伝導度が所定値以上となるまで注水を行うようにしてもよい。 The amount of water injected into the unsaturated layer 12 may be determined based on the water content measured in a boring survey or a probe driving survey conducted in advance, or the electrical conductivity may be monitored using an electrical conductivity meter of a probe driven into the unsaturated layer 12 at a point a specified distance away from the pipe 1, and water may be injected until the electrical conductivity reaches a specified value or higher.

その後、又は注水開始前に、電源装置3により電極2,2間に通電し、ジュール熱により不飽和層12を加熱する。通電により、VOCsで汚染された不飽和層12の温度を好ましくは50℃以上、例えば50~90℃、特に好ましくは60~80℃に昇温させる。なお、電極2への通電開始前に給水ポンプ5を停止してもよく、電極2への通電開始途中において、給水ポンプ5を停止してもよく、通電の間も連続して注水してもよい。 After that, or before the start of water injection, a current is applied between the electrodes 2, 2 by the power supply unit 3, and the unsaturated layer 12 is heated by Joule heat. By applying current, the temperature of the unsaturated layer 12 contaminated with VOCs is raised to preferably 50°C or higher, for example, 50 to 90°C, and particularly preferably 60 to 80°C. Note that the water supply pump 5 may be stopped before the start of current application to the electrode 2, or the water supply pump 5 may be stopped halfway through the start of current application to the electrode 2, or water may be continuously injected during current application.

通電を開始した後、吸引ポンプ8を作動させ、パイプ1内からVOCs含有ガスを吸引し、ガス処理設備9に送って処理する。これにより、不飽和層12内のVOCsが除去される。なお、注水後、通電及び吸引を行なう工程を繰り返し行うようにしてもよい。ガス吸引は、不飽和層12が十分に昇温した後に行うのが好ましいが、これに限定されない。 After starting the current supply, the suction pump 8 is operated to suck the VOCs-containing gas from inside the pipe 1 and send it to the gas treatment facility 9 for treatment. This removes the VOCs from inside the unsaturated layer 12. Note that the process of applying current and suction may be repeated after water is poured in. It is preferable to suction the gas after the temperature of the unsaturated layer 12 has risen sufficiently, but this is not a limitation.

この実施の形態では、不飽和層12に注水することにより不飽和層12への通電量が増大し、不飽和層12が十分に昇温するので、不飽和層12のVOCsを短時間で十分に除去することができる。 In this embodiment, the amount of electricity flowing to the unsaturated layer 12 is increased by injecting water into the unsaturated layer 12, and the temperature of the unsaturated layer 12 is raised sufficiently, so that the VOCs in the unsaturated layer 12 can be sufficiently removed in a short period of time.

上記説明ではパイプ1を土壌に打ち込んで注水を行うようにしているが、土壌に設けた吸引井戸を利用して注水してもよい。 In the above explanation, water is injected by driving pipe 1 into the soil, but water may also be injected using a suction well installed in the soil.

上記実施の形態は本発明の一例であり、本発明は上記実施の形態に限定されない。 The above embodiment is an example of the present invention, and the present invention is not limited to the above embodiment.

[実施例1]
土壌ガス吸引井戸が設けられたVOCs汚染不飽和層(飽和層との界面の地表からの深さ2m、井戸深さ2m)において、電極を9本打ち込み、電気発熱法を適用した。電極間隔は2.5mとした。
[Example 1]
In the VOCs-contaminated unsaturated layer where a soil gas suction well was installed (2 m deep from the ground surface at the interface with the saturated layer, 2 m deep in the well), nine electrodes were driven in and an electric heating method was applied. The electrodes were spaced 2.5 m apart.

通電開始前の不飽和層温度は約15℃であった。通電開始後、不飽和層への注水開始前の不飽和層温度は約35℃であった。通電開始後、吸引井戸から不飽和層へ水道水10mを7時間かけて注入したところ、図2の通り、不飽和層温度は徐々に上昇し、38日後には60℃まで上昇した。43日目にガス吸引を開始したところ、不飽和層温度は徐々に低下し、51日目に45℃まで低下したので、ガス吸引を停止した。 The temperature of the unsaturated layer before the start of energization was about 15°C. After the start of energization, the temperature of the unsaturated layer before the start of water injection into the unsaturated layer was about 35°C. After the start of energization, 10 m3 of tap water was injected into the unsaturated layer from the suction well over a period of 7 hours. As shown in Figure 2, the temperature of the unsaturated layer gradually increased, reaching 60°C after 38 days. When gas suction was started on the 43rd day, the temperature of the unsaturated layer gradually decreased, reaching 45°C on the 51st day, and gas suction was stopped.

前回の通電開始から85日目に再度、水道水10mを7時間かけて注入したところ、102日目に不飽和層温度が53℃まで上昇したので、吸引井戸からのガス吸引を開始した。その後は、143日目まで不飽和層温度は約50℃であった。 On the 85th day after the start of the previous energization, 10 m3 of tap water was injected again over 7 hours, and the unsaturated layer temperature rose to 53°C on the 102nd day, so gas suction from the suction well was started. After that, the unsaturated layer temperature remained at about 50°C until the 143rd day.

以上の実験により、不飽和層への注水により不飽和層が十分に昇温することが確認された。 The above experiments confirmed that injecting water into the unsaturated layer sufficiently raises the temperature of the layer.

1 パイプ
1a 孔
2 電極
4 タンク
10 土壌
11 飽和層
12 不飽和層
Reference Signs List 1 Pipe 1a Hole 2 Electrode 4 Tank 10 Soil 11 Saturated layer 12 Unsaturated layer

Claims (4)

揮発性有機化合物で汚染された不飽和層を電気発熱法により浄化する方法において、
予めボーリング調査又は電気伝導計を有したプローブの打ち込みによる電気伝導度調査により、該不飽和層と飽和層との界面深さを特定すると共に、
該不飽和層の含水率を測定して該不飽和層への注水量を決定して該不飽和層に注水することを特徴とする土壌又は地下水の浄化方法。
1. A method for electrothermal purification of an unsaturated layer contaminated with volatile organic compounds, comprising:
The depth of the interface between the unsaturated layer and the saturated layer is identified in advance by a boring survey or an electrical conductivity survey by driving a probe having an electrical conductivity meter into the soil.
A method for purifying soil or groundwater , comprising measuring the water content of the unsaturated layer, determining the amount of water to be injected into the unsaturated layer, and injecting the water into the unsaturated layer.
揮発性有機化合物で汚染された不飽和層を電気発熱法により浄化する方法において、
予めボーリング調査又は電気伝導計を有したプローブの打ち込みによる電気伝導度調査により、該不飽和層と飽和層との界面深さを特定すると共に、
該不飽和層の電気伝導度をモニタリングし、該電気伝導度が所定値以上となるまで該不飽和層に注水することを特徴とする土壌又は地下水の浄化方法。
1. A method for electrothermal purification of an unsaturated layer contaminated with volatile organic compounds, comprising:
The depth of the interface between the unsaturated layer and the saturated layer is identified in advance by a boring survey or an electrical conductivity survey by driving a probe having an electrical conductivity meter into the soil.
A method for purifying soil or groundwater, comprising monitoring the electrical conductivity of the unsaturated layer and pouring water into the unsaturated layer until the electrical conductivity reaches a predetermined value or higher .
前記不飽和層を60℃以上にまで昇温させる請求項1又は2の土壌又は地下水の浄化方法。 3. The method for purifying soil or groundwater according to claim 1 , wherein the temperature of the unsaturated layer is raised to 60° C. or higher. 前記揮発性有機化合物は、テトラクロロエチレン、トリクロロエチレン、ジクロロエチレン、及びトリクロロエタンの少なくとも1種を含む請求項1~3のいずれかの土壌又は地下水の浄化方法。 4. The method for purifying soil or groundwater according to claim 1 , wherein the volatile organic compound comprises at least one of tetrachloroethylene, trichloroethylene, dichloroethylene, and trichloroethane.
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JP2000084535A (en) 1998-09-11 2000-03-28 Hazama Gumi Ltd Purification method of contaminated soil by volatile compounds
JP2001212551A (en) 2000-02-04 2001-08-07 Hazama Gumi Ltd How to clean contaminated soil with oil
JP2002001299A (en) 2000-06-23 2002-01-08 Hazama Gumi Ltd How to clean contaminated soil
JP2006026492A (en) 2004-07-14 2006-02-02 Fujita Corp Method for decontaminating contaminated ground
JP2006346549A (en) 2005-06-15 2006-12-28 Kubota Corp In-situ purification method for contaminated soil
JP2008272597A (en) 2007-03-14 2008-11-13 Dowa Eco-System Co Ltd Treatment method of contaminated soil
JP2014231050A (en) 2013-05-30 2014-12-11 株式会社島津製作所 Soil cleaning apparatus utilizing electrical warming means
JP2016159259A (en) 2015-03-04 2016-09-05 株式会社島津製作所 Soil purification method using electrical warming means, and electrode for the same
CN108114970A (en) 2017-12-21 2018-06-05 永清环保股份有限公司 A kind of contaminated soil original position thermal desorption repair system and method
JP2020044481A (en) 2018-09-18 2020-03-26 国際航業株式会社 Contaminated soil purification method
JP2020185554A (en) 2019-05-17 2020-11-19 株式会社島津製作所 Soil purification equipment and soil purification method

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000084535A (en) 1998-09-11 2000-03-28 Hazama Gumi Ltd Purification method of contaminated soil by volatile compounds
JP2001212551A (en) 2000-02-04 2001-08-07 Hazama Gumi Ltd How to clean contaminated soil with oil
JP2002001299A (en) 2000-06-23 2002-01-08 Hazama Gumi Ltd How to clean contaminated soil
JP2006026492A (en) 2004-07-14 2006-02-02 Fujita Corp Method for decontaminating contaminated ground
JP2006346549A (en) 2005-06-15 2006-12-28 Kubota Corp In-situ purification method for contaminated soil
JP2008272597A (en) 2007-03-14 2008-11-13 Dowa Eco-System Co Ltd Treatment method of contaminated soil
JP2014231050A (en) 2013-05-30 2014-12-11 株式会社島津製作所 Soil cleaning apparatus utilizing electrical warming means
JP2016159259A (en) 2015-03-04 2016-09-05 株式会社島津製作所 Soil purification method using electrical warming means, and electrode for the same
CN108114970A (en) 2017-12-21 2018-06-05 永清环保股份有限公司 A kind of contaminated soil original position thermal desorption repair system and method
JP2020044481A (en) 2018-09-18 2020-03-26 国際航業株式会社 Contaminated soil purification method
JP2020185554A (en) 2019-05-17 2020-11-19 株式会社島津製作所 Soil purification equipment and soil purification method

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