JP2006015202A - Purification apparatus of contaminated soil and purification method for contaminated soil using the apparatus - Google Patents

Purification apparatus of contaminated soil and purification method for contaminated soil using the apparatus Download PDF

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JP2006015202A
JP2006015202A JP2004193930A JP2004193930A JP2006015202A JP 2006015202 A JP2006015202 A JP 2006015202A JP 2004193930 A JP2004193930 A JP 2004193930A JP 2004193930 A JP2004193930 A JP 2004193930A JP 2006015202 A JP2006015202 A JP 2006015202A
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water
purification
purifying
contaminated
contaminated soil
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JP4344287B2 (en
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Kyo Nishio
経 西尾
Takeshi Ishiguro
健 石黒
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Onoda Chemico Co Ltd
Maeda Corp
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Onoda Chemico Co Ltd
Maeda Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a purification apparatus of contaminated soil and a purification method for contaminated soil using the apparatus surely purifying soil, friendly to the environment, meeting the construction term and economic performance. <P>SOLUTION: The purification apparatus 1 of contaminated soil is provided with a water circulation circuit 2, a purification agent injection circuit 3, and a water sucking/injecting device 4. The water sucking/injecting device 4 is pressedly set in the contaminated soil, and the water circulation circuit 2 and purification agent injection circuit 3 are connected to the water sucking/injecting device 4. By switching a three-way selector valve 5, the water circulation circuit 2 is made to communicate with the water sucking/injecting device 4, to suck and remove contaminants in the soil. Then, by switching the three-way selector valve 5, the purification agent injection circuit 3 is made to communicate with the water sucking/injecting device 4, to inject a purification agent into the soil for purifying the contaminants. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、汚染土壌浄化装置及びこの装置を用いた汚染土壌の浄化方法に関する。   The present invention relates to a contaminated soil purification apparatus and a method for purifying contaminated soil using the apparatus.

土壌汚染物質の一つである揮発性有機化合物(VOC)については、土壌汚染対策法において第一種特定有害物質に指定されており、その中には、トリクロロエチレン(TCE)、各種のジクロロエチレン、四塩化炭素等の10種類の物質が含まれている。これらの化合物は一般的に、比重が大きく、粘性が小さく、土壌への吸着性が小さく、揮発性が高い、といった特徴を持つ。そのため、土壌に浸入したVOCは、土粒子の空隙にガスとして存在するだけではなく、比重の大きい液状のVOCとして、間隙を抜けて地下水に入り地下水汚染を生じさせる。
また、VOCは常温で揮発しやすく水より比重が大きいため地中深く浸透し、さらに、VOCは水に溶解しにくいがある程度の量は溶解するため、土壌や地下水において最も拡散しやすい等の特徴がある。
Volatile organic compounds (VOC), one of the soil pollutants, are designated as Class 1 Specified Hazardous Substances by the Soil Contamination Countermeasures Law, and include trichlorethylene (TCE), various dichloroethylenes, four Ten kinds of substances such as carbon chloride are included. These compounds are generally characterized by high specific gravity, low viscosity, low adsorptivity to soil, and high volatility. Therefore, the VOC that has entered the soil not only exists as a gas in the voids of the soil particles, but also enters the groundwater through the gap as a liquid VOC having a large specific gravity, causing groundwater contamination.
In addition, VOC is easy to volatilize at normal temperature and has a higher specific gravity than water, so it penetrates deep into the ground. Furthermore, VOC is difficult to dissolve in water but dissolves to some extent, so it is most easily diffused in soil and groundwater. There is.

非特許文献1によれば、現在、土壌汚染対策技術として用いられる方法を概略大別すると、(1)遮断・遮水(隔離封じ込め、原位置封じ込め)、(2)固化・不溶化(化学的固化等)、(3)熱分解・固化(溶融固化・ガラス固化)、(4)分解(化学的酸化還元・バイオレメディエーション、透過性浄化壁等)、(5)分離・除去(掘削除去、地下水揚水、土壌洗浄、加熱吸引、土壌ガス吸引等)となる。
これらの技術のうち、(3)熱分解・固化(例えば、特許文献1)、(4)分解(例えば、特許文献2)、(5)分離・除去(例えば、特許文献3)が、VOCによる土壌汚染に用いられている。
According to Non-Patent Document 1, the methods currently used as soil contamination countermeasure technologies can be roughly classified as follows: (1) Blocking / water shielding (isolation containment, in-situ containment), (2) Solidification / insolubilization (chemical solidification) Etc.), (3) Pyrolysis / solidification (melt solidification / glass solidification), (4) Decomposition (chemical redox / bioremediation, permeable purification wall, etc.), (5) Separation / removal (excavation removal, groundwater pumping) Soil washing, heat suction, soil gas suction, etc.).
Among these technologies, (3) thermal decomposition / solidification (for example, Patent Document 1), (4) decomposition (for example, Patent Document 2), and (5) separation / removal (for example, Patent Document 3) are performed by VOC. Used for soil contamination.

「建築技術」,株式会社建築技術,平成15年4月1日,No.639,p.135,表1“Architecture Technology”, Architecture Technology Co., Ltd., April 1, 2003, No. 639, p. 135, Table 1 特開昭57−178023号公報Japanese Unexamined Patent Publication No. 57-178023 特開2003−305453号公報JP 2003-305453 A 特開2003−94037号公報JP 2003-94037 A

しかしながら、これらのVOCによる土壌汚染対策技術のうち、(3)熱分解・固化(溶融固化・ガラス固化)については、溶融固化が溶融スラグ化による汚染物質揮散と固形化による技術であり、ガラス固化については原位置あるいは掘削土壌での電極による溶融ガラス固化による技術であるため、現在のところ使用例が少ないことをみると、最適な技術ではないと考えられる。(4)分解については、周辺環境に与える影響は少ないものの、修復に要する期間が長期化する傾向があるといった問題点がある。(5)の分離・除去については、VOCが地中深く浸透しやすい特徴があることから、低温加熱法では汚染地盤の掘削処理が難しく、地下水揚水による方法では、必要揚程高が大きくなって揚水が難しくなったり、地下水に細粒分が多い場合には、通常吸水管の目詰まり対策に使用しているフィルタが目詰まりを生じて揚水能力を著しく低下させてしまうといった問題点がある。また、揚水量が過大になると地盤沈下等を誘発しやすいといった問題点もある。   However, among these VOC soil contamination countermeasure technologies, (3) thermal decomposition and solidification (melt solidification / glass solidification) is a technology by melting and solidifying the pollutants and solidification by melting slag. Is a technique based on molten glass solidification using electrodes in situ or in excavated soil, so it is considered that it is not the optimal technique considering that there are few examples of use at present. (4) The decomposition has a problem that although the influence on the surrounding environment is small, the period required for repair tends to be prolonged. Regarding the separation / removal of (5), since VOC easily penetrates deep into the ground, it is difficult to excavate contaminated ground by the low-temperature heating method. However, when there is a large amount of fine particles in the groundwater, there is a problem that the filter normally used for clogging of the water absorption pipe is clogged and the pumping capacity is significantly reduced. Another problem is that if the amount of pumped water is excessive, land subsidence is likely to occur.

これまで、VOCによる土壌汚染対策技術について述べてきたが、土壌汚染物質はVOCだけではなく、この他の重要な汚染物質として汚染油分が挙げられる。従って、VOCだけではなく、汚染油分を浄化する技術、あるいはVOCと汚染油分とを同じ装置あるいは同じ方法で浄化する技術も必要とされている。   So far, soil pollution control technology by VOC has been described, but soil pollution is not limited to VOC, and other important pollutants include contaminated oil. Therefore, not only the VOC but also a technology for purifying the contaminated oil, or a technology for purifying the VOC and the contaminated oil by the same apparatus or the same method is required.

この発明は、このような問題点を解決するためになされたもので、周辺環境に優しく、かつ工期と経済性を満足できる土壌の浄化を行うことができる汚染土壌浄化装置及びこの装置を用いた汚染土壌の浄化方法を提供することを目的とする。   The present invention has been made to solve such problems, and uses a contaminated soil purification apparatus capable of purifying soil that is friendly to the surrounding environment and satisfies the construction period and economy, and the apparatus. It aims at providing the purification method of contaminated soil.

この発明に係る汚染土壌浄化装置は、水槽に貯えられた水を昇圧して循環させる高圧ポンプ、及び循環された水を浄化する浄化手段を備えた水循環回路と、浄化剤を貯蔵する貯蔵槽及び浄化剤を注入する注入ポンプを備えた浄化剤注入回路と、ノズルを有する循環水管、及びノズルを内部に包含するように取り付けられノズル上方の位置にスリットを有する外管を備えた吸水・注入装置とを備え、水循環回路と浄化剤注入回路とは切り替え可能であって、いずれか一方が吸水・注入装置に連通され、吸水・注入装置は、水循環回路が選択された場合には、スリットから汚染物質を吸引可能であり、浄化剤注入回路が選択された場合には、スリットから浄化剤を注入可能であることを特徴とする。   A contaminated soil purification apparatus according to the present invention includes a high-pressure pump that boosts and circulates water stored in a water tank, a water circulation circuit that includes a purification means that purifies the circulated water, a storage tank that stores a purification agent, and A water-absorbing / injecting device comprising a purifying agent injection circuit having an infusion pump for injecting a purifying agent, a circulating water pipe having a nozzle, and an outer pipe attached to the nozzle so as to include the nozzle and having a slit at a position above the nozzle The water circulation circuit and the purifier injection circuit can be switched, and either one communicates with the water absorption / injection device, and the water absorption / injection device is contaminated from the slit when the water circulation circuit is selected. When the substance can be sucked and the cleaning agent injection circuit is selected, the cleaning agent can be injected from the slit.

この発明に係る汚染土壌の浄化方法は、この発明に係る汚染土壌浄化装置を用い、吸水・注入装置を、汚染物質が存在する深度まで貫入する工程と、水槽に貯えられた水が水循環回路を循環し、その循環された水がノズルにより流速を高められる際に発生する負圧によって、汚染物質がスリットから吸引され、循環された水と共に地上に運ばれた汚染物質が浄化手段によって浄化される工程と、汚染物質が吸引された後の地盤に、吸水・注入装置から前記浄化剤を注入する工程とを備える。
汚染物質が揮発性有機化合物を含む汚染水の場合には、浄化剤として、揮発性有機化合物を還元する還元剤を使用することが好ましい。
汚染物質が汚染油分を含む汚染水の場合には、浄化剤として、汚染油分を分解する分解剤を使用することが好ましい。
The method for purifying contaminated soil according to the present invention uses the contaminated soil purifying device according to the present invention, the step of penetrating the water absorption / injection device to the depth where the pollutant exists, and the water stored in the water tank The pollutant is sucked from the slit by the negative pressure generated when the circulating water is circulated and the flow velocity is increased by the nozzle, and the pollutant carried to the ground together with the circulated water is purified by the purification means. And a step of injecting the purification agent from the water absorption / injection device into the ground after the contaminant is sucked.
When the pollutant is contaminated water containing a volatile organic compound, it is preferable to use a reducing agent that reduces the volatile organic compound as a purification agent.
When the pollutant is contaminated water containing contaminated oil, it is preferable to use a decomposing agent that decomposes the contaminated oil as the purifier.

この発明によれば、吸水・注入装置に、水循環回路及び浄化剤注入回路を切り替えて接続することによって、土壌中の汚染物質を吸引除去した後、その土壌中へ浄化剤を注入して残留汚染物質に対して長期間の浄化効果を期待するようにしたので、周辺環境に優しく、かつ工期と経済性を満足できる土壌の浄化を行うことができる。   According to the present invention, by switching and connecting the water circulation circuit and the purification agent injection circuit to the water absorption / injection device, the contaminants in the soil are sucked and removed, and then the purification agent is injected into the soil to cause residual contamination. Since the substance is expected to have a long-term purification effect, it is possible to purify soil that is friendly to the surrounding environment and that satisfies the construction period and economy.

以下、この発明の実施の形態を添付図面に基づいて説明する。
図1に示されるように、この実施の形態に係る汚染土壌浄化装置1は、水循環回路2、浄化剤注入回路3、及び吸水・注入装置4を備えている。
水循環回路2は、水循環回路2を循環する水(以下、循環水と称する)が貯えられる水槽11、水槽11に貯えられた循環水を昇圧して水循環回路2中を循環させる高圧ポンプ12、循環水に混入する砂等を除去するサンドスクリーン13、循環水から汚染物質を除去する浄化槽14、及び浄化槽14において分離された汚染物質を貯蔵する貯溜槽15を備えている。ここで、サンドスクリーン13及び浄化槽14は、循環水を浄化する装置であり、浄化手段を構成する。
浄化剤注入回路3は、浄化剤を貯蔵する貯蔵槽16と、貯蔵槽16に貯蔵される浄化剤を土壌に注入する注入ポンプ17とを備えている。
Embodiments of the present invention will be described below with reference to the accompanying drawings.
As shown in FIG. 1, a contaminated soil purification device 1 according to this embodiment includes a water circulation circuit 2, a purification agent injection circuit 3, and a water absorption / injection device 4.
The water circulation circuit 2 includes a water tank 11 in which water circulating in the water circulation circuit 2 (hereinafter referred to as circulation water) is stored, a high-pressure pump 12 that boosts the circulating water stored in the water tank 11 and circulates in the water circulation circuit 2, and circulation A sand screen 13 for removing sand and the like mixed in water, a purification tank 14 for removing contaminants from the circulating water, and a storage tank 15 for storing the contaminants separated in the purification tank 14 are provided. Here, the sand screen 13 and the septic tank 14 are devices for purifying the circulating water, and constitute a purification means.
The purification agent injection circuit 3 includes a storage tank 16 that stores the purification agent, and an injection pump 17 that injects the purification agent stored in the storage tank 16 into the soil.

図2に示されるように、吸水・注入装置4は、H型鋼21のフランジ21aに沿うようにして、循環水管22と外管23とを備えている。循環水管22は、H型鋼21の下端部21b付近でコの字状に折り曲げられて180°向きを変え、その先端には、循環水をジェット水流として噴射するノズル24が設けられている。外管23は、ノズル24を内部に包含するように、循環水管22の先端に取り付けられ、ノズル24の上方にあたる位置にスリット25が形成されている。   As shown in FIG. 2, the water absorption / injection device 4 includes a circulating water pipe 22 and an outer pipe 23 along the flange 21 a of the H-shaped steel 21. The circulating water pipe 22 is bent in a U shape near the lower end portion 21b of the H-shaped steel 21 to change its direction by 180 °, and a nozzle 24 for injecting the circulating water as a jet water stream is provided at the tip thereof. The outer tube 23 is attached to the tip of the circulating water tube 22 so as to include the nozzle 24 therein, and a slit 25 is formed at a position above the nozzle 24.

また、図1に示されるように、水循環回路2と浄化剤注入回路3とは、三方弁5によって接続され、さらに、吸水・注入装置4と接続されている。三方弁5の切り替え操作によって、水循環回路2及び浄化剤注入回路3のいずれか一方が、吸水・注入装置4と連通するようになっている。   As shown in FIG. 1, the water circulation circuit 2 and the purification agent injection circuit 3 are connected by a three-way valve 5 and further connected to a water absorption / injection device 4. By switching the three-way valve 5, one of the water circulation circuit 2 and the purifier injection circuit 3 communicates with the water absorption / injection device 4.

次に、この実施の形態に係る汚染土壌浄化装置1の動作を説明する。
事前調査を行った結果、図3(a)に示されるように、地中の深度の深い所にVOCによって汚染された土壌及び地下水が、地中の浅い所に汚染油分が存在することが分かっていると仮定する。
この地盤上にクレーン6を設置し、吸水・注入装置4を地中へ垂直に圧入する。この際、吸水・注入装置4は、VOCにより汚染された土壌及び地下水を浄化するために地中の深いところへ圧入したもの4a、及び汚染油分を浄化するために地中の浅い所へ圧入したもの4bの2種類にわけられる。この2種類の吸水・注入装置4a,4bは、地盤を上方より見た図3(b)に示されるように、例えば地盤上を等ピッチで交互になるように圧入される。
Next, operation | movement of the contaminated soil purification apparatus 1 which concerns on this embodiment is demonstrated.
As a result of the preliminary survey, as shown in Fig. 3 (a), it was found that soil and groundwater contaminated by VOCs were deep in the ground and contaminated oil was present in shallow ground. Assuming that
A crane 6 is installed on the ground, and the water absorption / injection device 4 is press-fitted vertically into the ground. At this time, the water absorption / injection device 4 was pressed into a deep part of the ground in order to purify soil and groundwater contaminated by VOC, and pressed into a shallow part of the ground to purify contaminated oil. There are two types of thing 4b. The two types of water absorption / injection devices 4a and 4b are press-fitted so as to alternate on the ground at an equal pitch, for example, as shown in FIG. 3B when the ground is viewed from above.

このようにして、吸水・注入装置4を汚染土壌に圧入した後、水循環回路2及び浄化剤注入回路3を、VOCにより汚染された土壌及び地下水を浄化するための吸水・注入装置4aに接続し、三方弁5の切り替え操作を行うことによって、水循環回路2を吸水・注入装置4aに連通させる。
図1に示されるように、高圧ポンプ12を起動し、水槽11内の循環水を吸水・注入装置4aに送水する。吸水・注入装置4aに送水された循環水は、ノズル24(図2参照)から外管23(図2参照)中に噴射される。この際、ノズル24から噴射された循環水はジェット噴流となり、周囲に負圧を生じさせる。この負圧によって、外管23に形成されたスリット25(図2参照)から、土壌中のVOCによって汚染された地下水が吸引される。吸引されたVOCは外管23内を上昇し、サンドスクリーン13で土砂分を濾過された後、浄化槽14へ送られる。浄化槽14では、曝気処理等により揮発したVOCと水とに分離される。揮発したVOCは貯溜槽15へ送られ、活性炭による吸着処理がなされて適宜運搬処理される。一方、VOCと分離された循環水は、水槽11へ戻される。
この操作を、その他の吸水・注入装置4aにおいて繰り返すことにより、VOCにより汚染された地下水を除去する。
After the water absorption / injection device 4 is pressed into the contaminated soil in this way, the water circulation circuit 2 and the purifier injection circuit 3 are connected to the water absorption / injection device 4a for purifying the soil and groundwater contaminated by the VOC. By switching the three-way valve 5, the water circulation circuit 2 is communicated with the water absorption / injection device 4a.
As shown in FIG. 1, the high-pressure pump 12 is activated to feed the circulating water in the water tank 11 to the water absorption / injection device 4a. The circulating water sent to the water absorption / injection device 4a is jetted from the nozzle 24 (see FIG. 2) into the outer tube 23 (see FIG. 2). At this time, the circulating water jetted from the nozzle 24 becomes a jet jet, and creates a negative pressure around it. Under this negative pressure, groundwater contaminated by VOC in the soil is sucked from the slit 25 (see FIG. 2) formed in the outer tube 23. The sucked VOC ascends in the outer pipe 23, and after the earth and sand content is filtered by the sand screen 13, it is sent to the septic tank 14. In the septic tank 14, the volatile VOC and water are separated by aeration processing or the like. The volatilized VOC is sent to the storage tank 15 where it is adsorbed with activated carbon and appropriately transported. On the other hand, the circulating water separated from the VOC is returned to the water tank 11.
By repeating this operation in the other water absorption / injection device 4a, the groundwater contaminated by the VOC is removed.

この後、三方弁5の切り替え操作を行い、浄化剤注入回路3を吸水・注入装置4aに連通させる。
図1に示されるように、注入ポンプ17を起動することによって、貯蔵槽16内の浄化剤として鉄粉懸濁液のような還元剤が、循環水管22及び外管23の両方を通って、吸水・注入装置4aに送られる。吸水・注入装置4bに送られた鉄粉懸濁液は、VOCに汚染された地下水が吸引された土壌へ、スリット25から注入される。
土壌へ注入された鉄粉懸濁液は、残留した地下水に含まれるVOCや土粒子の空隙にガスとして存在するVOCと反応し、炭化水素へ還元する。例えば、トリクロロエチレン、ジクロロエチレン、四塩化炭素等のVOCは、炭化水素であるエチレンやエタンに還元される。
Thereafter, the switching operation of the three-way valve 5 is performed, and the purifier injection circuit 3 is communicated with the water absorption / injection device 4a.
As shown in FIG. 1, by starting the infusion pump 17, a reducing agent such as an iron powder suspension as a purifying agent in the storage tank 16 passes through both the circulating water pipe 22 and the outer pipe 23. It is sent to the water absorption / injection device 4a. The iron powder suspension sent to the water absorption / injection device 4b is injected from the slit 25 into the soil into which the groundwater contaminated with VOC has been sucked.
The iron powder suspension injected into the soil reacts with VOC contained in the residual groundwater and VOC present as gas in the voids of the soil particles, and is reduced to hydrocarbons. For example, VOCs such as trichlorethylene, dichloroethylene, and carbon tetrachloride are reduced to hydrocarbons such as ethylene and ethane.

このようにして、地中の深度の深い所を浄化した後、汚染油分によって汚染された地中の深度の浅い所の洗浄を行う。
水循環回路2及び浄化剤注入回路3を、汚染油分を浄化するための吸水・注入装置4bに接続する。この後、地中の深度の深い所を浄化した方法と同じ方法で、汚染油分を吸引除去した後、その土壌へ浄化剤を注入する。ここで、浄化剤として、VOCの場合と同じような還元剤を注入しても、汚染油分を分解することはできない。ここで、使用される浄化剤としては、汚染油分を分解する土壌中の微生物を増殖するための栄養塩溶液が最適である。このような栄養塩を土壌中に注入することによって、汚染油分を分解する土壌中の微生物が増殖・活性化され、汚染油分が炭素数の少ない炭化水素等へ分解される。栄養塩としては、例えば、栄養源となる窒素やリンを含んだ無機栄養塩、あるいはある種の水素供与剤等が挙げられる。
In this way, after purifying the deep depth in the ground, the shallow depth in the ground contaminated by the contaminated oil is washed.
The water circulation circuit 2 and the purification agent injection circuit 3 are connected to a water absorption / injection device 4b for purifying contaminated oil. Then, after removing the contaminated oil by suction in the same manner as the method of purifying deep underground, the purifier is injected into the soil. Here, even if a reducing agent similar to that in the case of VOC is injected as the purifying agent, the contaminated oil cannot be decomposed. Here, as the cleaning agent used, a nutrient solution for growing microorganisms in the soil that decomposes contaminated oil is optimal. By injecting such nutrients into the soil, microorganisms in the soil that decompose the contaminated oil are propagated and activated, and the contaminated oil is decomposed into hydrocarbons having a small number of carbon atoms. Examples of nutrient salts include inorganic nutrient salts containing nitrogen and phosphorus as nutrient sources, and certain hydrogen donors.

このように、吸水・注入装置4に、水循環回路2及び浄化剤注入回路3を切り替えて連通させることによって、土壌中の汚染物質を吸引除去した後、その土壌中へ浄化剤を注入して、残留汚染物質に対して長期間の浄化効果を期待することができるため、周辺環境に優しく、かつ工期と経済性を満足できる土壌の浄化を行うことができる。また、汚染物質の存在深度において、目詰まりなく確実に、汚染物質の吸引除去および浄化剤の注入が可能である。
また、水循環回路を循環する高圧水がノズルにより流速を高められる際に発生する負圧による吸水・注入装置4は、真空ポンプに比べてはるかに大きな揚水能力を有し、10m以上の深層部からも地上へ揚水することが容易にできる。さらに、吸水と同時に、スリット25の大きさ未満の砂礫等(粒径10mm程度以内)の土粒子類をもろとも、高速で循環する循環水と共に地上へ送られる。このため、スリット25には目詰まりが生じないため、確実に汚染物質の吸引除去が可能で、フィルタを備える不要にすることができる。
In this way, by switching the water circulation circuit 2 and the purification agent injection circuit 3 to communicate with the water absorption / injection device 4, after removing the contaminants in the soil by suction, the purification agent is injected into the soil, Since a long-term purification effect can be expected for residual pollutants, it is possible to purify soil that is friendly to the surrounding environment and that satisfies the construction period and economy. Further, it is possible to reliably remove the contaminants and inject the cleaning agent without clogging at the depth of presence of the contaminants.
Further, the water absorption / injection device 4 due to the negative pressure generated when the flow rate of the high-pressure water circulating in the water circulation circuit is increased by the nozzle has a much higher pumping capacity than a vacuum pump, and from a deep layer of 10 m or more. Can be easily pumped to the ground. Furthermore, simultaneously with water absorption, soil particles such as gravel (particle size within about 10 mm) less than the size of the slit 25 are sent to the ground together with circulating water circulating at high speed. For this reason, since clogging does not occur in the slit 25, the contaminants can be reliably removed by suction, and a filter can be omitted.

この実施の形態では、水循環回路2と浄化剤注入回路3とを三方弁5によって接続し、さらに、吸水・注入装置4に接続させ、三方弁5の切り替え操作によって、水循環回路2及び浄化剤注入回路3のいずれか一方を、吸水・注入装置4に連通するようにしたが、このような形態に限定されるものではない。水循環回路2と浄化剤注入回路3とを別々に設け、それぞれを別々に吸水・注入装置4に接続するようにしてもよい。それぞれを別々に吸水・注入装置4に接続することにより、水循環回路2及び浄化剤注入回路3のいずれか一方を、吸水・注入装置4に連通させることができる。   In this embodiment, the water circulation circuit 2 and the purification agent injection circuit 3 are connected by the three-way valve 5 and further connected to the water absorption / injection device 4, and the water circulation circuit 2 and the purification agent injection are switched by the switching operation of the three-way valve 5. Although either one of the circuits 3 is communicated with the water absorption / injection device 4, it is not limited to such a form. The water circulation circuit 2 and the purifier injection circuit 3 may be provided separately, and each may be connected to the water absorption / injection device 4 separately. By connecting each to the water absorption / injection device 4 separately, either the water circulation circuit 2 or the purifier injection circuit 3 can be communicated with the water absorption / injection device 4.

この実施の形態では、還元剤として鉄粉懸濁液を用いたが、これに限定されるものではない。その他の公知の還元剤を適宜選択することができ、必要に応じて二種類の還元剤を混合させて使用することもできる。二種類の還元剤を混合させて注入する場合には、貯蔵槽16及び注入ポンプ17を二系列設け、二種類の還元剤を、それぞれ循環水管22及び外管23を介して吸水・注入装置4に供給し、スリット25から注入される直前に混合させるようにすることもできる。   In this embodiment, the iron powder suspension is used as the reducing agent, but the present invention is not limited to this. Other known reducing agents can be appropriately selected, and two kinds of reducing agents can be mixed and used as necessary. When mixing and injecting two types of reducing agents, two series of storage tanks 16 and injection pumps 17 are provided, and the two types of reducing agents are supplied to the water absorption / injection device 4 via the circulating water pipe 22 and the outer pipe 23, respectively. It can also be made to mix immediately before injecting from the slit 25.

この実施の形態では、VOC及び汚染油分の双方が存在する場合について述べたが、VOCまたは汚染油分のいずれかが単独で存在しているときでも適用することができる。VOCまたは汚染油分のいずれかが単独で存在している場合についての実施の形態の概念図を、それぞれ図4及び図5に示す。   In this embodiment, the case where both the VOC and the contaminated oil are present has been described. However, the present invention can be applied even when either the VOC or the contaminated oil is present alone. A conceptual diagram of the embodiment in the case where either VOC or contaminated oil is present alone is shown in FIGS. 4 and 5, respectively.

この発明の実施の形態に係る汚染土壌浄化装置の構成図である。It is a block diagram of the contaminated soil purification apparatus which concerns on embodiment of this invention. この実施の形態に係る汚染土壌浄化装置の吸引・注入装置の全体図である。It is a general view of the suction / injection device of the contaminated soil purification device according to this embodiment. この実施の形態に係る汚染土壌浄化装置の吸引・注入装置を地盤に圧入する方法を説明するための図である。It is a figure for demonstrating the method to press-fit the suction / injection apparatus of the contaminated soil purification apparatus which concerns on this embodiment to the ground. 土壌中のVOCを浄化するために、この実施の形態に係る汚染土壌浄化装置の吸引・注入装置を地盤に圧入する方法を説明するための図である。It is a figure for demonstrating the method to press-fit the suction / injection apparatus of the contaminated soil purification apparatus which concerns on this embodiment in order to purify VOC in soil. 土壌中の汚染油分を浄化するために、この実施の形態に係る汚染土壌浄化装置の吸引・注入装置を地盤に圧入する方法を説明するための図である。It is a figure for demonstrating the method to press-fit the suction / injection apparatus of the contaminated soil purification apparatus which concerns on this embodiment in order to purify the contaminated oil in soil.

符号の説明Explanation of symbols

1 汚染土壌浄化装置、2 水循環回路、3 浄化剤注入回路、4,4a,4b 吸水・注入装置、11 水槽、12 高圧ポンプ、13 サンドスクリーン、14 浄化槽、15 貯溜槽、21 H型鋼、22 循環水管、23 外管、24 ノズル、25 スリット、31 貯蔵槽、32 注入ポンプ。   DESCRIPTION OF SYMBOLS 1 Contaminated soil purification apparatus, 2 Water circulation circuit, 3 Purification agent injection circuit, 4, 4a, 4b Water absorption / injection apparatus, 11 Water tank, 12 High pressure pump, 13 Sand screen, 14 Septic tank, 15 Reservoir tank, 21 H type steel, 22 Circulation Water pipe, 23 outer pipe, 24 nozzle, 25 slit, 31 storage tank, 32 infusion pump.

Claims (4)

水槽、前記水槽に貯えられた水を昇圧して循環させる高圧ポンプ、及び循環された前記水を浄化する浄化手段を備えた水循環回路と、
浄化剤を貯蔵する貯蔵槽及び前記浄化剤を注入する注入ポンプを備えた浄化剤注入回路と、
ノズルを有する循環水管、及び前記ノズルを内部に包含するように取り付けられノズル上方の位置にスリットを有する外管を備えた吸水・注入装置と
を備え、
前記水循環回路と前記浄化剤注入回路とは切り替え可能であって、いずれか一方が前記吸水・注入装置に連通され、
前記吸水・注入装置は、前記水循環回路が選択された場合には、前記スリットから汚染物質を吸引可能であり、前記浄化剤注入回路が選択された場合には、前記スリットから浄化剤を注入可能であることを特徴とする汚染土壌浄化装置。
A water circulation circuit comprising a water tank, a high-pressure pump for boosting and circulating the water stored in the water tank, and a purification means for purifying the circulated water;
A purifying agent injection circuit comprising a storage tank for storing the purifying agent and an infusion pump for injecting the purifying agent;
A circulating water pipe having a nozzle, and a water absorption / injection device provided with an outer pipe having a slit at a position above the nozzle attached so as to include the nozzle inside.
The water circulation circuit and the purifier injection circuit can be switched, and either one communicates with the water absorption / injection device,
The water absorption / injection device can suck contaminants from the slit when the water circulation circuit is selected, and can inject purification agent from the slit when the purification agent injection circuit is selected. The contaminated soil purification apparatus characterized by being.
請求項1に記載の汚染土壌浄化装置を用いた汚染物質を含む汚染土壌の浄化方法であって、
前記吸水・注入装置を、前記汚染物質が存在する深度まで貫入する工程と、
前記水槽に貯えられた前記水が前記水循環回路を循環し、その循環された前記水が前記ノズルにより流速を高められる際に発生する負圧によって、前記汚染物質が前記スリットから吸引され、前記循環された水と共に地上に運ばれた前記汚染物質が前記浄化手段によって浄化される工程と、
前記汚染物質が吸引された後の地盤に、前記吸水・注入装置から前記浄化剤を注入する工程と
を備える汚染土壌の浄化方法。
A method for purifying contaminated soil containing contaminants using the contaminated soil purification apparatus according to claim 1,
Penetrating the water absorption / injection device to a depth at which the contaminants are present;
The water stored in the water tank circulates in the water circulation circuit, and the pollutant is sucked from the slit by the negative pressure generated when the circulated water is increased in flow rate by the nozzle, and the circulation A step of purifying the pollutant carried on the ground together with the purified water by the purification means;
A method for purifying contaminated soil, comprising the step of injecting the purification agent from the water absorption / injection device into the ground after the contaminant is sucked.
前記汚染物質は、揮発性有機化合物を含む汚染水であり、
前記浄化剤は、前記揮発性有機化合物を還元する還元剤である
ことを特徴とする請求項2に記載の汚染土壌の浄化方法。
The pollutant is contaminated water containing volatile organic compounds,
The method for purifying contaminated soil according to claim 2, wherein the purification agent is a reducing agent that reduces the volatile organic compound.
前記汚染物質は、汚染油分を含む汚染水であり、
前記浄化剤は、前記汚染油分を分解する分解剤である
ことを特徴とする請求項2に記載の汚染土壌の浄化方法。
The pollutant is contaminated water containing contaminated oil,
The method for purifying contaminated soil according to claim 2, wherein the purification agent is a decomposition agent that decomposes the contaminated oil.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105107835A (en) * 2015-09-21 2015-12-02 中国科学院武汉岩土力学研究所 Contaminated soil treatment equipment through leaching

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105107835A (en) * 2015-09-21 2015-12-02 中国科学院武汉岩土力学研究所 Contaminated soil treatment equipment through leaching

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