JP3760494B2 - Soil purification method - Google Patents

Soil purification method Download PDF

Info

Publication number
JP3760494B2
JP3760494B2 JP35204895A JP35204895A JP3760494B2 JP 3760494 B2 JP3760494 B2 JP 3760494B2 JP 35204895 A JP35204895 A JP 35204895A JP 35204895 A JP35204895 A JP 35204895A JP 3760494 B2 JP3760494 B2 JP 3760494B2
Authority
JP
Japan
Prior art keywords
soil
well
groundwater
harmful substances
aquifer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP35204895A
Other languages
Japanese (ja)
Other versions
JPH09174034A (en
Inventor
幸生 福島
陽一郎 小野
明雄 田中
Original Assignee
日立プラント建設株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 日立プラント建設株式会社 filed Critical 日立プラント建設株式会社
Priority to JP35204895A priority Critical patent/JP3760494B2/en
Publication of JPH09174034A publication Critical patent/JPH09174034A/en
Application granted granted Critical
Publication of JP3760494B2 publication Critical patent/JP3760494B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Description

【0001】
【発明の属する技術分野】
本発明は揮発性の有害物質で汚染された土壌の浄化方法に係り、特に汚染された土壌内に抽出井戸を設けて汚染物質を除去する方法に関する。
【0002】
【従来の技術】
ドライクリ−ニング店などの敷地に含まれる有機塩素系溶剤などの、揮発性有害物質が地下水に溶解し地下汚染の原因となっている。この有害物質で汚染された土壌は例えば図3に示すように表土A、ロ−ム層B、粘土層C,れき層Dで構成されている。除去対象となる有害物質は表土Aやロ−ム層Bに多く存在しているが、一部は粘土層C内にも拡散している。粘土層Cに浸透した有害物質は帯水層であるれき層D内の地下水に溶解し拡散する。
【0003】
従来、この汚染された土壌から有害物質を除去する方法は、仕切板10をれき層Dに達する深さまで埋め込み汚染された地下水の拡散を防ぎ、次いで仕切板10の内側の地下水を揚水井戸11に備えてある揚水ポンプ12で汲み揚げ曝気槽14に送る。ここで地下水をエアレ−ションし有害物質を気化させる。気化した有害物質は排気管18を通り処理槽30に送られ活性炭に吸着される。一方曝気槽14で浄化された処理水は送水ポンプ16で地上に放流される。
更に、粘土層C及びロ−ム層Bに存在する有害物質は抽出井戸21から真空ポンプ23により吸引され、処理槽30に送られ活性炭に吸着される。揚水井戸11及び抽出井戸21の構造は下端部に多数の小径の穴が設けられており、この穴を介して地下水を揚水し、また、有害物質を真空抽出する。
【0004】
しかし、土壌内で液状のまま存在している有害物質や、土壌に吸着している有害物質を気化させ抽出するのは困難で、長期間の真空抽出が必要である。特に粘土層などの透気性が悪い土壌に含まれる有害物質の除去は難しく、真空抽出に3年以上要することもある。このため土壌を掘削して地上に取り出し、洗浄等の処理をすることもあるが、多大な費用が必要となり限界がある。
【0005】
【発明が解決しようとする課題】
本発明は、前記従来技術の欠点を解消し、土壌内で液状のまま存在している有害物質や、土壌に吸着している有害物質を短期間で気化させ除去できる土壌の浄化方法を提供するにある。
【0006】
【課題を解決するための手段】
本発明は前記課題を解決するために、土壌を加熱することによって有害物質の気化を促進させることが有効であることに着目し、その具体的手段として、帯水層中の地下水を汲み揚げる揚水井戸の他に圧入井戸を設けて、揚水井戸から汲み揚げた前記地下水を浄化した後、この処理水を加熱し前記圧入井戸を介し再度土壌の帯水層に圧入するとともに、加熱した処理水を圧入する圧入井戸の深さを、前記地下水を汲み揚げる揚水井戸の深さよりも浅くするように構成したものである。
【0007】
【発明の実施の形態】
次に、実施例に基づいて本発明を更に具体的に説明する。図1は本発明の実施例を示す系統図である。本実施例が図3の従来方法と違うところは、帯水層中の地下水を揚水ポンプ12で揚水し曝気槽14で浄化処理した後、この処理水を熱交換器15で40℃〜70℃に加熱し、送水ポンプ16により圧入井戸17から再度土壌の帯水層へ圧入する点にある。圧入井戸17はれき層Dの上部に開放端が位置し、この開放端には多数の小径の穴が設けられている。この穴から加熱された処理水が押し出されるが、処理水の温度が地下水よりも高く密度が小さいため帯水層であるれき層Dの最上部に拡散する。この加熱した処理水の拡散によって、上部の粘土層Cは加熱され徐々に温度が上昇する。このため、従来除去が困難とされていた粘土層Cに含まれる有害物質は気化し易くなり、短期間で真空抽出ができる。
【0008】
また、圧入井戸の深さを揚水井戸の深さよりも浅くすることによって、帯水層であるれき層Dは底部から低温の地下水を揚水井戸で吸入し、また、上部から加熱された処理水が混入することにより、温度差による密度層を形成する。このため、有害物質を比較的高濃度に含む低温の地下水を、加熱した処理水との混合が少ない状態で揚水することができ、地上での浄化処理の効率が向上する。
【0009】
図2は本発明による浄化方法と、浄化処理した処理水を地上に放流する従来の方法とを比較したものである。本発明による方法では粘土層C内に含まれる有害物質であるトリクレンの総除去量が多いだけでなく、除去速度が低下しにくい。これは処理水の加熱によって土壌に浸透したトリクレンの気化が促進されるだけでなく、土壌に吸着されているトリクレンや、土壌粒子間に捕捉されているトリクレンも、水分と共に気化させ除去できるためである。したがって、短期間で土壌を浄化でき、また、浄化後の土壌中の有害物質の濃度も低い。
【0010】
【発明の効果】
以上、本発明の方法によれば、地下水を揚水し浄化した後、この処理水を加熱し、予め設けた圧入井戸を介し再度土壌の帯水層に圧入するとともに、加熱した処理水を圧入する圧入井戸の深さを、前記地下水を汲み揚げる揚水井戸の深さよりも浅くすることにより、帯水層の上部に位置する土壌内の有害物質の気化を促進させることができ、短期間に土壌中の有害物質を除去できる。
【0011】
【図面の簡単な説明】
【図1】本発明の実施例を示す系統図
【図2】有害物質の除去に対する本発明と従来方法との比較
【図3】従来方法の系統図
【符号の説明】
10・・・仕切板
11・・・揚水井戸
14・・・曝気槽
15・・・熱交換器
17・・・圧入井戸
21・・・抽出井戸
23・・・真空ポンプ
30・・・処理槽
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for purifying soil contaminated with volatile harmful substances, and more particularly, to a method for removing contaminants by providing an extraction well in the contaminated soil.
[0002]
[Prior art]
Volatile toxic substances such as organic chlorinated solvents contained in sites such as dry cleaning stores dissolve in groundwater and cause underground pollution. For example, as shown in FIG. 3, the soil contaminated with this harmful substance is composed of a top soil A, a loam layer B, a clay layer C, and a gravel layer D. Although many harmful substances to be removed exist in the topsoil A and the loam layer B, some of them also diffuse in the clay layer C. The harmful substances that have permeated the clay layer C dissolve and diffuse in the groundwater in the gravel layer D, which is an aquifer.
[0003]
Conventionally, the method of removing harmful substances from this contaminated soil prevents the diffusion of contaminated groundwater by embedding the partition plate 10 to a depth reaching the gravel layer D, and then uses the groundwater inside the partition plate 10 to the pumping well 11. The water is pumped by the provided pump 12 and sent to the aeration tank 14. Here, groundwater is aerated to vaporize harmful substances. The vaporized harmful substance passes through the exhaust pipe 18 and is sent to the treatment tank 30 and is adsorbed by the activated carbon. On the other hand, the treated water purified in the aeration tank 14 is discharged to the ground by a water pump 16.
Furthermore, harmful substances present in the clay layer C and the loam layer B are sucked from the extraction well 21 by the vacuum pump 23, sent to the treatment tank 30, and adsorbed on the activated carbon. The structure of the pumping well 11 and the extraction well 21 is provided with a large number of small-diameter holes at the lower end portion, through which groundwater is pumped and harmful substances are vacuum extracted.
[0004]
However, it is difficult to vaporize and extract harmful substances that exist in a liquid state in the soil and harmful substances that are adsorbed on the soil, and vacuum extraction is required for a long period of time. In particular, it is difficult to remove harmful substances contained in soil with poor air permeability such as clay layers, and vacuum extraction may take 3 years or more. For this reason, soil may be excavated and taken out to the ground, and processing such as washing may be performed, but there is a limit because it requires a large amount of cost.
[0005]
[Problems to be solved by the invention]
The present invention provides a soil purification method that eliminates the disadvantages of the prior art and can vaporize and remove harmful substances present in liquid form in the soil and harmful substances adsorbed on the soil in a short period of time. It is in.
[0006]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the present invention pays attention to the fact that it is effective to promote the vaporization of harmful substances by heating the soil, and as a specific means, pumping up the groundwater in the aquifer In addition to the well, a press-in well is provided to purify the groundwater pumped from the pumping well, and then the treated water is heated and again injected into the soil aquifer through the press-in well, and the heated treated water is The depth of the press-fitting well to be press-fitted is configured to be shallower than the depth of the pumped well for pumping up the ground water .
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Next, the present invention will be described more specifically based on examples. FIG. 1 is a system diagram showing an embodiment of the present invention. This embodiment is different from the conventional method of FIG. 3 in that groundwater in the aquifer is pumped by a pump 12 and purified by an aeration tank 14, and then this treated water is heated at 40 ° C. to 70 ° C. by a heat exchanger 15. It is in the point which press-fits into the aquifer of soil again from the press-in well 17 with the water pump 16. The open well 17 has an open end located above the debris layer D, and a number of small-diameter holes are provided at the open end. Although the treated water heated from this hole is pushed out, the temperature of the treated water is higher than that of the groundwater and its density is small, so that it diffuses to the top of the gravel layer D that is an aquifer. Due to the diffusion of the heated treated water, the upper clay layer C is heated and the temperature gradually rises. For this reason, harmful substances contained in the clay layer C, which has conventionally been difficult to remove, are easily vaporized and can be vacuum extracted in a short period of time.
[0008]
In addition, by making the depth of the injection well shallower than the depth of the pumping well, the gravel layer D, which is an aquifer, draws low-temperature groundwater from the bottom through the pumping well, and the treated water heated from the top By mixing, a density layer due to a temperature difference is formed. For this reason, low-temperature groundwater containing a relatively high concentration of harmful substances can be pumped with little mixing with heated treated water, and the efficiency of purification treatment on the ground is improved.
[0009]
FIG. 2 shows a comparison between the purification method according to the present invention and a conventional method for discharging the treated water after purification treatment to the ground. In the method according to the present invention, not only the total removal amount of trichlene, which is a harmful substance contained in the clay layer C, is large, but also the removal rate is difficult to decrease. This is because heating of the treated water not only promotes the vaporization of trichrene that has penetrated into the soil, but also allows trichrene adsorbed on the soil and trichlene trapped between soil particles to be vaporized and removed together with moisture. is there. Therefore, soil can be purified in a short period of time, and the concentration of harmful substances in the soil after purification is low.
[0010]
【The invention's effect】
As described above, according to the method of the present invention, after pumping up and purifying the groundwater, the treated water is heated and again injected into the aquifer of the soil through a pre-installed injection well , and the heated treated water is injected. By making the depth of the injection well shallower than the depth of the pumping well for pumping up the groundwater, it is possible to promote the vaporization of harmful substances in the soil located above the aquifer, Can remove harmful substances.
[0011]
[Brief description of the drawings]
FIG. 1 is a system diagram showing an embodiment of the present invention. FIG. 2 is a comparison between the present invention and a conventional method for removing harmful substances. FIG. 3 is a system diagram of the conventional method.
DESCRIPTION OF SYMBOLS 10 ... Partition plate 11 ... Pumping well 14 ... Aeration tank 15 ... Heat exchanger 17 ... Press-in well 21 ... Extraction well 23 ... Vacuum pump 30 ... Processing tank

Claims (1)

揮発性の有害物質で汚染された上部層と、その下部の帯水層からなる土壌の所定区画を仕切板で囲み、その内側に上部層中の前記有害物質を真空ポンプでガス状で抽出する抽出井戸と、帯水層中の地下水を汲み揚げる揚水井戸を設け、これらの井戸で抽出したガス及び揚水した地下水を地上で浄化処理した後、この処理水を加熱し予め設けられた圧入井戸を介し再度土壌の帯水層に圧入する土壌の浄化方法において、
前記の加熱した処理水を圧入する圧入井戸の深さを、前記地下水を汲み揚げる揚水井戸の深さよりも浅くすることを特徴とする土壌の浄化方法。
A predetermined partition of soil consisting of an upper layer contaminated with volatile harmful substances and an aquifer below it is surrounded by a partition plate, and the harmful substances in the upper layer are extracted in the form of gas with a vacuum pump inside Establish an extraction well and a pumping well for pumping up groundwater in the aquifer. After purifying the gas extracted from these wells and the pumped-up groundwater on the ground, heat the treated water and install a pre-installed well. In the soil purification method, which is pressed again into the soil aquifer,
A method for purifying soil, characterized in that a depth of a press-fitting well into which the heated treated water is injected is shallower than a depth of a pumping well from which the groundwater is pumped.
JP35204895A 1995-12-27 1995-12-27 Soil purification method Expired - Fee Related JP3760494B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35204895A JP3760494B2 (en) 1995-12-27 1995-12-27 Soil purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35204895A JP3760494B2 (en) 1995-12-27 1995-12-27 Soil purification method

Publications (2)

Publication Number Publication Date
JPH09174034A JPH09174034A (en) 1997-07-08
JP3760494B2 true JP3760494B2 (en) 2006-03-29

Family

ID=18421431

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35204895A Expired - Fee Related JP3760494B2 (en) 1995-12-27 1995-12-27 Soil purification method

Country Status (1)

Country Link
JP (1) JP3760494B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4670029B2 (en) * 2001-07-17 2011-04-13 株式会社間組 Soil purification method
CN103706626A (en) * 2013-12-26 2014-04-09 江苏盖亚环境工程有限公司 System for treating organic pollutants in polluted soil
CN107328140B (en) * 2017-08-18 2020-04-28 吉林建筑大学 Seepage water-blocking structure and heat exchange structure
CN115055506B (en) * 2022-05-13 2024-04-19 北京建工环境工程咨询有限责任公司 Contaminated soil restoration system

Also Published As

Publication number Publication date
JPH09174034A (en) 1997-07-08

Similar Documents

Publication Publication Date Title
US5277518A (en) Contaminant remediation, biodegradation and removel methods and apparatus
JP2618579B2 (en) Method and apparatus for removing contaminants
JP2660307B2 (en) Methods for in situ decontamination of underground soil and groundwater
US5228804A (en) Method and apparatus for hydrocarbon-contaminated soil remediation
US5765964A (en) Submerged combustion process and apparatus for removing volatile contaminants from groundwater or subsurface soil
US6254310B1 (en) In-well air stripping and adsorption
KR100798763B1 (en) The method to remediate pol(petroleum, oil, lubricant) contaminated soil by in-situ thermal desorption approach, and the apparatus for the same
US5387057A (en) Contaminated ground site remediation system
EP1361002A2 (en) Method and apparatus for purifying a layer of contaminated soil
CN113102490A (en) Integrated system and method for monitoring and repairing soil and underground water pollution
JP3760494B2 (en) Soil purification method
JP4671073B2 (en) In-situ repair method for soil contaminated with organic matter
JP4398699B2 (en) In-situ purification system for contaminated groundwater
CN113172084A (en) Soil remediation system and method for enhancing thermal desorption effect
JPH0510083A (en) Method of electric vacuum purifying
JP4375592B2 (en) Soil and groundwater purification methods
BE1028844B1 (en) Combination of depollution techniques: In Situ Thermal Desorption and Immobilization
JP2007514534A (en) How to remove pollutants from contaminated soil
JPH0994558A (en) Recovery device for contaminant in ground
JP2006320842A (en) Method and device for cleaning contaminated soil
US5509760A (en) Method of rapid purging of contaminants from a contaminated area of soil or ground water
JPH09174033A (en) Vacuum extraction and purification of soil
JP3373788B2 (en) Contaminated groundwater purification equipment
JPH04501893A (en) On-site purification system for contaminated groundwater
Hutzler et al. Vaporizing VOCs

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050125

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050218

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20051220

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060102

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090120

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100120

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110120

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110120

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120120

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130120

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140120

Year of fee payment: 8

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees