JPH09234484A - Restoration method for polluted ground water and soil - Google Patents

Restoration method for polluted ground water and soil

Info

Publication number
JPH09234484A
JPH09234484A JP4336396A JP4336396A JPH09234484A JP H09234484 A JPH09234484 A JP H09234484A JP 4336396 A JP4336396 A JP 4336396A JP 4336396 A JP4336396 A JP 4336396A JP H09234484 A JPH09234484 A JP H09234484A
Authority
JP
Japan
Prior art keywords
pollutants
groundwater
soil
bioreactor
underground
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.)
Granted
Application number
JP4336396A
Other languages
Japanese (ja)
Other versions
JP3401660B2 (en
Inventor
Kazuo Okamura
和夫 岡村
Junichi Yagi
淳一 八木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shimizu Construction Co Ltd
Shimizu Corp
Original Assignee
Shimizu Construction Co Ltd
Shimizu Corp
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 Shimizu Construction Co Ltd, Shimizu Corp filed Critical Shimizu Construction Co Ltd
Priority to JP04336396A priority Critical patent/JP3401660B2/en
Publication of JPH09234484A publication Critical patent/JPH09234484A/en
Application granted granted Critical
Publication of JP3401660B2 publication Critical patent/JP3401660B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • Y02W10/12

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable rapid decomposition and removal and to enable the decomposition and removal of the contaminants of unsatd. strata as well at the time of purifying and restoring polluted ground water and soil by bioremediation. SOLUTION: Plural wells 11, 12, 13 are excavated in the saturation strate 17 near the underground polluted point 1 polluted with the contaminants and >=2 electrodes 14, 15, parted from each other, are enabedded near the underground polluted point 1. While voltage is impressed between the respective electrodes, the ground water contg. the contaminants is pumped up from the wells 11 to 13 and the pumped up water is introduced into a ground bioreactor 16, where the pollutants are subjected to the decomposition treatment. The treated water is released or the saturation stratum is impregnated with the water.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、トリクロロエチレ
ン、テトラクロロエチレンなどの有機塩素化合物や廃油
などの汚染物質によって汚染された土壌、地下水を修
復、浄化する技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for repairing and purifying soil and groundwater contaminated with organic chlorine compounds such as trichloroethylene and tetrachloroethylene and pollutants such as waste oil.

【0002】[0002]

【従来の技術】このような汚染土壌、地下水から汚染物
質を取り除く浄化方法として、最近、バイオテクロノジ
ーを利用したバイオレメディエーション(原位置バイオ
レメディエーションとも呼ばれる。)が注目を集めてい
る。バイオレメディエーションは、土壌中に生息する微
生物の機能を利用して汚染物質を分解し無害化する技術
であり、土壌生態系が本来有している浄化機能を人為的
に強化し利用するものである。
2. Description of the Related Art Recently, bioremediation (also called in-situ bioremediation) utilizing biotechnology has been attracting attention as a purification method for removing pollutants from such contaminated soil and groundwater. Bioremediation is a technology that decomposes and detoxifies pollutants by utilizing the function of microorganisms that live in the soil, and artificially enhances and uses the purification function originally possessed by the soil ecosystem. .

【0003】図3は、従来のバイオレメディエーション
技術による浄化方法の一例を模式的に示すものである。
この方法では、有機塩素化合物や油分などの汚染物質で
汚染された地下汚染箇所1の近傍の飽和層2に二本以上
の井戸3,4を掘削する。地下水流5の下流側に掘削さ
れた揚水井戸4から揚水した地下水の少なくとも一部を
基質添加手段6に導き、分解菌の生育基質であるメタン
やフェノールおよび空気(酸素)、栄養源等を加え、こ
れを上流側に掘削された注入井戸3へ注入し、循環す
る。これにより、飽和層2等に存在する汚染物質分解菌
の活性を高め、汚染物質の分解、除去を効率よく行うこ
とができ、コストパフォーマンスの高い修復方法とされ
ている。
FIG. 3 schematically shows an example of a purification method by a conventional bioremediation technique.
In this method, two or more wells 3 and 4 are excavated in the saturated layer 2 in the vicinity of the underground contaminated site 1 contaminated with pollutants such as organic chlorine compounds and oil. At least a part of the groundwater pumped from the pumping well 4 drilled on the downstream side of the groundwater flow 5 is guided to the substrate addition means 6, and methane, phenol and air (oxygen), which are growth substrates for the degrading bacteria, and nutrient sources are added. , And injects it into the injection well 3 that has been excavated upstream and circulates it. As a result, the activity of the pollutant-degrading bacteria present in the saturated layer 2 and the like can be enhanced, and the pollutant can be decomposed and removed efficiently, and the restoration method has high cost performance.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このバ
イオレメディエーションによる浄化方法にあっては、ト
リクロロエチレンなどの有機塩素化合物や油分等の汚染
物質は、粘土質や土壌中の有機物に吸着されやすく、こ
のため徐々にこれらが地下水中に離脱してくるため、除
去に比較的長時間を要する欠点がある。また、地下水が
飽和の状態で存在する飽和層での汚染物質の分解、除去
は可能であるが、地下水が不飽和で空気等の存在する間
隙が存在する不飽和層での分解、除去は困難であるなど
の問題を有している。
However, in this purification method by bioremediation, organic chlorine compounds such as trichlorethylene and pollutants such as oil are easily adsorbed by clay and organic matter in soil, and Since these are gradually released into the groundwater, there is a drawback that the removal takes a relatively long time. Also, although it is possible to decompose and remove pollutants in the saturated layer where groundwater is saturated, it is difficult to decompose and remove in the unsaturated layer where groundwater is unsaturated and there are gaps where air exists. It has problems such as

【0005】本発明の課題は、バイオレメディエーショ
ンによる浄化、修復を行う際、短時間で分解、除去が可
能であり、かつ不飽和層の汚染物質の分解除去も可能と
する方法の提供にある。
An object of the present invention is to provide a method capable of decomposing and removing in a short time when purifying and repairing by bioremediation and also capable of decomposing and removing contaminants in an unsaturated layer.

【0006】[0006]

【課題を解決するための手段】本発明の請求項1に係る
発明は、汚染物質で汚染された地下汚染箇所の近傍の飽
和層に複数の井戸を掘削するとともに、該地下汚染箇所
の近傍に2つ以上の電極を離間して埋設し、各電極間に
電圧を加えつつ、該井戸から汚染物質を含む地下水を揚
水し、該揚水を地上のバイオリアクターに導いて汚染物
質を分解処理し、該処理水を放流または飽和層に注入す
ることを特徴とする汚染地下水、土壌の修復方法であ
る。請求項2に係る発明は、前記処理水の少なくとも一
部に、酸素と土壌微生物の栄養源と基質のうちの少なく
とも1種を添加し、前記地下汚染箇所の地下水流上流側
に位置する注入井戸から飽和層に注入することを特徴と
する請求項1記載の汚染地下水、土壌の修復方法であ
る。請求項3に係る発明は、前記バイオリアクターが、
前記汚染物質を嫌気分解するように構成された嫌気的バ
イオリアクターであることを特徴とする請求項1または
2記載の汚染地下水、土壌の修復方法である。
According to a first aspect of the present invention, a plurality of wells are excavated in a saturated layer in the vicinity of an underground contaminated site contaminated with pollutants, and at the same time, in the vicinity of the underground contaminated site. By embedding two or more electrodes apart from each other, pumping groundwater containing pollutants from the well while applying a voltage between each electrode, and guiding the pumped water to a bioreactor on the ground to decompose pollutants, A method for repairing contaminated groundwater and soil, characterized in that the treated water is discharged or injected into a saturated layer. In the invention according to claim 2, at least one of a nutrient source and a substrate for oxygen and soil microorganisms is added to at least a part of the treated water, and the injection well is located upstream of the groundwater flow at the underground pollution location. The method for remediating contaminated groundwater and soil according to claim 1, wherein the method is to inject into the saturated layer. In the invention according to claim 3, the bioreactor is
It is an anaerobic bioreactor comprised so that the said pollutant may be decomposed anaerobically, It is a contaminated groundwater of the claim 1 or 2, The restoration method of soil.

【0007】[0007]

【発明の実施の形態】図1は、本発明による汚染地下
水、土壌の修復方法の一例を示すものである。この例で
は、有機塩素化合物や廃油などの汚染物質で汚染された
地下汚染箇所1の近傍の飽和層17に複数の井戸11,12,
13を掘削するとともに、それらの井戸11,12,13の地下水
流5の上流側と下流側とそれぞれ電極14,15を埋設し、
かつそれぞれの井戸11,12,13から揚水した地下水を、汚
染物質分解用のバイオリアクター16に導入して処理す
るように構成されている。
1 shows an example of a method for repairing contaminated groundwater and soil according to the present invention. In this example, a plurality of wells 11, 12, are formed in the saturated layer 17 near the underground pollution point 1 contaminated with pollutants such as organic chlorine compounds and waste oil.
Along with excavating 13 wells, burying the electrodes 14, 15 respectively on the upstream side and the downstream side of the groundwater flow 5 in those wells 11, 12, 13 respectively.
Moreover, the groundwater pumped from each well 11, 12, 13 is introduced into the bioreactor 16 for decomposing pollutants for treatment.

【0008】この地下汚染箇所1の地層は、地下水流5
に示すように、地下水が流れている飽和層17と、その
上層の不飽和層18と、飽和層17の下にある不透水層
19とからなっており、汚染物質は飽和層17と不飽和
層18に存在し、特にそれぞれの層の境界部分に多くな
っており、離脱し難い状態で存在している。トリクロロ
エチレンなどの有機塩素化合物の汚染物質は、粘土質や
土壌中の有機物に吸着されやすく、このため飽和層17
では、汚染物質が徐々に地下水中に離脱し、この地下水
中には汚染物質が含有されている。
[0008] The stratum at this underground pollution point 1 is composed of a groundwater flow 5
As shown in Fig. 2, the saturated layer 17 in which groundwater flows, the unsaturated layer 18 above it, and the impermeable layer 19 below the saturated layer 17 are included. It exists in the layer 18, especially in the boundary portion of each layer, and it exists in a state where it is difficult to separate. Contaminants of organochlorine compounds such as trichlorethylene are easily adsorbed by clay and organic matter in the soil.
Then, the pollutants gradually escape into the groundwater, and the groundwater contains the pollutants.

【0009】前記井戸11,12,13は、地下汚染箇所1の近
傍の飽和層17に十分達する深さに掘削されている。こ
れらの井戸11,12,13には揚水パイプが底の近くまで挿入
されており、これらの揚水パイプを通して地下水を地上
に揚水するようになっている。これらの井戸11,12,13の
本数は、地下汚染箇所1の汚染状況に応じて適宜設定さ
れる。また、これらの井戸11,12,13は揚水用のみでな
く、地下水流5の上流側に注水用の井戸を設け、この注
水井戸から基質としてメタンやフェノール等、空気、土
壌微生物の増殖用の栄養成分(窒素源、リン酸塩などの
無機塩類など)、あるいは界面活性剤を添加した水を供
給してもよい。
The wells 11, 12 and 13 are excavated to a depth enough to reach the saturated layer 17 near the underground pollution site 1. Pumping pipes are inserted into these wells 11, 12 and 13 up to near the bottom, and groundwater is pumped to the ground through these pumping pipes. The number of these wells 11, 12 and 13 is appropriately set according to the contamination status of the underground contamination site 1. Further, these wells 11, 12, 13 are not only for pumping water, but are also provided with wells for water injection on the upstream side of the groundwater flow 5, from which water wells for multiplication of methane, phenol, etc. Water supplemented with nutrients (nitrogen source, inorganic salts such as phosphate, etc.) or surfactant may be supplied.

【0010】前記電極14,15は、飽和層17に十分達す
る深さに挿入された導電体であればよく、材質や形状は
限定されない。例えば飽和層17に十分達する深さに打
ち込まれたグラファイトなどの電極が使用可能である。
また、不導電体からなる本体の外側に金属線や金属網を
取り付けた電極体を用いてもよい。
The electrodes 14 and 15 may be conductors inserted to a depth enough to reach the saturated layer 17, and the material and shape are not limited. For example, an electrode made of graphite or the like, which is driven to a depth sufficient to reach the saturated layer 17, can be used.
Moreover, you may use the electrode body which attached the metal wire or the metal net to the outer side of the main body which consists of non-conductive materials.

【0011】これらの電極14,15間には、地下水流5の
上流側の電極14を陽極(+)側とし、下流側の電極1
5を陰極(−)側とするように直流電流が加えられる。
これら電極14,15間に加える電圧は、汚染物質の離脱、
移動を促進させることができ、しかもロスが生じない範
囲とされ、地中の導電性に応じて数V〜数百Vの範囲で
適宜変更してよい。また、電極14,15の本数や設置位置
は、地下汚染箇所1の規模や地下水流5に応じて、地下
汚染箇所1の周囲に効率よく電圧を加えることができる
ように適宜設定してよいし、電極14,15の正負を随時切
り替えて処理を行ってもよい。
Between the electrodes 14 and 15, the electrode 14 on the upstream side of the groundwater flow 5 is the anode (+) side, and the electrode 1 on the downstream side is
A direct current is applied so that 5 is on the cathode (−) side.
The voltage applied between these electrodes 14 and 15 is
The range is such that the movement can be promoted and no loss occurs, and it may be appropriately changed within the range of several V to several hundred V depending on the conductivity of the ground. Moreover, the number and the installation positions of the electrodes 14 and 15 may be appropriately set depending on the scale of the underground pollution point 1 and the groundwater flow 5 so that a voltage can be efficiently applied around the underground pollution point 1. Alternatively, the positive and negative of the electrodes 14 and 15 may be switched at any time to perform the processing.

【0012】前記バイオリアクター16は、テトラクロ
ロエチレンなどの処理すべき物質を分解可能な微生物
と、井戸11,12,13から揚水された地下水とを接触させ、
該地下水に含まれる汚染物質を微生物によって生物学的
に分解するためのものである。このバイオリアクター1
6の装置構成や使用菌は汚染物質の種類に応じて適切な
タイプを選択使用することができる。例えば、嫌気性細
菌を用いたバイオリアクターとしては、通常の下水処理
や産業廃水処理で実施される嫌気性消化法(メタン発酵
法)の処理装置などを適用してよい。また、好気性菌を
用いた密閉式バイオリアクターを使用し、その他、汚染
物質の分解能を有する細菌を保持するための浮上性粒子
や多孔質支持体を備えたリアクターに、嫌気的または好
気的条件下で地下水を接触させるタイプのバイオリアク
ターを用いてもよい。
The bioreactor 16 brings microorganisms capable of decomposing substances to be treated, such as tetrachloroethylene, into contact with the groundwater pumped from the wells 11, 12, and 13,
It is for biologically decomposing pollutants contained in the groundwater by microorganisms. This bioreactor 1
As for the apparatus configuration of 6 and the bacteria to be used, an appropriate type can be selected and used according to the type of contaminant. For example, as a bioreactor using anaerobic bacteria, a treatment device of an anaerobic digestion method (methane fermentation method) or the like which is usually carried out in sewage treatment or industrial wastewater treatment may be applied. In addition, a closed bioreactor using aerobic bacteria is used, and in addition, a reactor equipped with buoyant particles or a porous support for retaining bacteria having the ability of degrading pollutants can be anaerobic or aerobic. A bioreactor of the type that contacts groundwater under conditions may be used.

【0013】このバイオリアクター16は、処理すべき
汚染物質の種類に応じて、嫌気的バイオリアクターと好
気的バイオリアクターのいずれか一方を備えていればよ
く、また嫌気的バイオリアクターと好気的バイオリアク
ターの両方を連設して配置してもよい。汚染物質がテト
ラクロロエチレンなどの有機塩素化合物である場合に
は、土壌中あるいは嫌気性汚泥などから分離される嫌気
性菌、例えば、Fathepureら(Fathepure,B.Z.,Nengu,J.
P. and Boyd,S.A.: Appl. Environ. Microbiol.,53,267
1-2674(1987);Fathepure,B.Z. and Boyd,S.A.: Appl.
Environ. Microbiol.,54,2976-2980(1988))により報告
された嫌気性細菌(Methanosarucina sp.,Methanosaruc
ina metai, Methanosarucina acetivorans, Methanothr
ix sp., Dechlorinating bacterium DCB-1, Methanosar
ucina sp.DCM)、Belayら(Belay,N. and Daniels,L.:A
ppl. Environ. Microbiol.,53,1604-1609(1987))によ
る報告されたメタン生成細菌(Methanococcus thermoli
thotrophics, M. thermodeltae, Methanobacterium the
rmoautotrophicum)、Egliら(Egli,C.E., Tschan,T.,
Scholtz,R.S., Cook,A.M. and Leisinger,T.: Appl. En
viron. Microbiol.,54,2819-2824(1988))により報告さ
れた硫酸還元細菌など(Desulfobacterium autotrophic
um, Acetobacterium woodii, Clostridium thermoaceti
cum)、Galliら(Galli,R. and McCaryt,P.L.:Appl. En
viron. Microbiol.,55,837-844(1989))により報告され
た嫌気性細菌(Clostridium sp.TCA2B株)、矢口ら(矢
口久美子、渡辺学、平田一郎、伊東武、浜田昭:水質汚
濁研究,14,479-486(1991))により報告されたグラム陰
性テトラクロロエチレン分解細菌T株などの細菌を用い
ることができる。
The bioreactor 16 may be equipped with either an anaerobic bioreactor or an aerobic bioreactor, depending on the type of pollutant to be treated, or may be an anaerobic bioreactor or an aerobic bioreactor. Both bioreactors may be arranged in series. When the pollutant is an organic chlorine compound such as tetrachloroethylene, anaerobic bacteria isolated in soil or from anaerobic sludge, for example, Fathepure et al. (Fathepure, BZ, Nengu, J.
P. and Boyd, SA: Appl. Environ. Microbiol., 53,267
1-2674 (1987); Fathepure, BZ and Boyd, SA: Appl.
Environ. Microbiol., 54, 2976-2980 (1988)), an anaerobic bacterium (Methanosarucina sp., Methanosaruc).
ina metai, Methanosarucina acetivorans, Methanothr
ix sp., Dechlorinating bacterium DCB-1, Methanosar
ucina sp.DCM), Belay et al. (Belay, N. and Daniels, L.:A
Microbiol., 53,1604-1609 (1987)), a reported methanogenic bacterium (Methanococcus thermoli).
thotrophics, M. thermodeltae, Methanobacterium the
rmoautotrophicum), Egli et al. (Egli, CE, Tschan, T.,
Scholtz, RS, Cook, AM and Leisinger, T .: Appl. En
viron. Microbiol., 54, 2819-2824 (1988)) and other sulfate-reducing bacteria (Desulfobacterium autotrophic
um, Acetobacterium woodii, Clostridium thermoaceti
cum), Galli et al. (Galli, R. and McCaryt, PL: Appl. En
Microbiol., 55,837-844 (1989)), an anaerobic bacterium (Clostridium sp.TCA2B strain), Yaguchi et al. (Kumiko Yaguchi, Manabu Watanabe, Ichiro Hirata, Takeshi Ito, Akira Hamada: Water Pollution Research, 14,479). -486 (1991)), such as Gram-negative tetrachloroethylene-degrading bacterium T strain, can be used.

【0014】また、トリクロロエチレンなどの有機塩素
化合物を好気的に分解する場合には、土壌中や好気的汚
泥中などから分離される好気性菌、例えば、Foxら(Fo
x,B.G. et al.:Biochemistry, 26, 6419-6427(1990))
によって報告された各種微生物(Pseudomonas mendocin
a, P. putida F1, Nitrosomonas europaea, Mycobacter
ium sp.など)を用いることができる。
In the case of aerobically decomposing organic chlorine compounds such as trichlorethylene, aerobic bacteria separated from soil or aerobic sludge, such as Fox et al.
x, BG et al .: Biochemistry, 26, 6419-6427 (1990))
Microorganisms reported by Pseudomonas mendocin
a, P. putida F1, Nitrosomonas europaea, Mycobacter
ium sp., etc.) can be used.

【0015】地下汚染箇所1の周囲に、このような設備
構成を構築しバイオレメディエーションにより地下汚染
箇所1の修復、すなわち汚染物質の分解除去を行うに
は、複数の電極14,15間に、地下水流5の上流側の電極
14が陽極(+)側、下流側の電極15が陰極(−)と
なるように電圧を加え、複数の井戸11,12,13から地下水
をポンプで揚水する。
In order to repair the underground pollution point 1 by bioremediation, that is, to decompose and remove the pollutants, by constructing such an equipment structure around the underground pollution point 1, the ground water is connected between the electrodes 14 and 15. A voltage is applied so that the electrode 14 on the upstream side of the stream 5 becomes the anode (+) side and the electrode 15 on the downstream side becomes the cathode (−), and groundwater is pumped from the plurality of wells 11, 12, 13.

【0016】これによって飽和層17中の汚染物質の離
脱、移動が著しく促進され、井戸11,12,13から揚水され
る地下水中の汚染物質の量を増大させることができると
ともに、汚染物質の離脱が困難であった不飽和層18や
不透水層19中との境界部分に含まれる汚染物質もそれ
ぞれの層から地下水流5中に離脱し、井戸11,12,13から
の揚水によって該汚染物質を回収することができるよう
になる。
As a result, desorption and migration of pollutants in the saturated layer 17 are significantly promoted, the amount of pollutants in the groundwater pumped from the wells 11, 12, 13 can be increased, and the desorption of pollutants can be achieved. The pollutants contained in the boundary between the unsaturated layer 18 and the impermeable layer 19 which were difficult to remove are also released from the respective layers into the groundwater flow 5, and the pollutants are pumped from the wells 11, 12, 13 by the pumping. Will be able to be collected.

【0017】それぞれの井戸11,12,13から揚水された地
下水は、バイオリアクター16に導いて、含有されてい
る有機塩素化合物等の汚染物質を生物学的に分解する。
バイオリアクター16では、汚染物質分解菌の生育に必
要な栄養源を添加したり、バイオリアクター内の温度、
酸素濃度を分解菌の生育に適する条件に維持して該菌を
増殖させる。
The groundwater pumped from each well 11, 12, 13 is guided to the bioreactor 16 to biologically decompose pollutants such as contained organic chlorine compounds.
In the bioreactor 16, the nutrient source necessary for the growth of the pollutant degrading bacteria is added, the temperature in the bioreactor,
The oxygen concentration is maintained under conditions suitable for the growth of the degrading bacterium to grow the bacterium.

【0018】バイオリアクター16において汚染物質を
分解、除去し、汚染物質が消失しまたは極めて低濃度と
なった水は、活性炭吸着などの処理を必要に応じて行っ
た後、放流される。
The water in which the pollutant is decomposed and removed in the bioreactor 16 and the pollutant disappears or has an extremely low concentration is discharged after performing treatment such as activated carbon adsorption as necessary.

【0019】この処理を継続して行うことにより、地下
汚染箇所1などに存在する汚染物質を効率よく地下水中
に離脱させ、分解菌によって安全に分解することがで
き、短期間のうちに地下汚染箇所1の汚染物質を除去
し、該箇所の修復を行うことができる。処理水は、地下
汚染箇所1の地下水流5の上流側に掘削された井戸か
ら、飽和層17に注入し、地下水流5を増加させるため
に用いても良い。
By continuing this treatment, the pollutants existing in the underground pollution site 1 and the like can be efficiently released into the groundwater and safely decomposed by the degrading bacteria, and the underground pollution can be achieved within a short period of time. It is possible to remove the contaminants at the point 1 and repair the point. The treated water may be used to increase the groundwater flow 5 by injecting it into the saturated layer 17 from a well drilled on the upstream side of the groundwater flow 5 at the underground pollution location 1.

【0020】図2は本発明による汚染地下水、土壌の修
復方法の他の例を示すものである。本例では、バイオリ
アクター16で処理された処理水を積極的に地下に注入
し、しかも、地中に存在する汚染物質分解菌の生育を促
進させるメタンやフェノールなどの基質、栄養源や空気
(酸素)を添加して注入することにより、地中に存在す
る汚染物質分解菌の活性を高め、より積極的な汚染物質
の分解除去を行うための方法である。
FIG. 2 shows another example of the method for repairing contaminated groundwater and soil according to the present invention. In this example, the treated water treated in the bioreactor 16 is actively injected underground, and substrates such as methane and phenol that promote the growth of pollutant degrading bacteria existing in the ground, nutrient sources and air ( This is a method for increasing the activity of pollutant degrading bacteria existing in the ground by adding and injecting (oxygen) to perform more aggressive decomposition and removal of pollutants.

【0021】本例では、図2に示す通り、地下汚染箇所
1の上流側に、少なくとも1本の注入井戸21と電極1
4とを設け、地下汚染箇所1の下流側に、少なくとも1
本の揚水井戸22と電極14とを設ける。揚水井戸22
には飽和層17に達する揚水パイプを挿入してあり、ポ
ンプによって揚水パイプを通して地下水を揚水し、この
水(汚染物質を含む地下水)を、地上に配したバイオリ
アクター16に導いて、汚染物質を生物学的に分解す
る。バイオリアクター16で処理された水は、栄養源、
空気、或いは界面活性剤などを適当量添加する基質添加
手段23に導き、分解菌のメタン、フェノール等の生育
基質、空気(酸素)、栄養源等を加えた後、注入井戸2
1から地下汚染箇所1の上流側に注入する。
In this example, as shown in FIG. 2, at least one injection well 21 and an electrode 1 are provided upstream of the underground contamination site 1.
4 is provided, and at least 1 is provided on the downstream side of the underground contamination point 1.
A pumping well 22 of a book and an electrode 14 are provided. Pumping well 22
A pumping pipe reaching the saturated layer 17 is inserted in the pump, groundwater is pumped through the pumping pipe by a pump, and this water (groundwater containing pollutants) is guided to the bioreactor 16 placed on the ground to remove pollutants. Biodegrades. The water treated in the bioreactor 16 is a nutrient source,
The injection well 2 is introduced to the substrate adding means 23 for adding an appropriate amount of air or a surfactant and the like, after adding growth substrates such as methane of decomposing bacteria and phenol, air (oxygen), nutrient sources, etc.
Inject from 1 to the upstream side of underground pollution point 1.

【0022】本例による処理では、地下汚染箇所1の下
流側の揚水井戸22から揚水した地下水を、バイオリア
クター16に導き、このバイオリアクター16内で汚染
物質の分解能の高い分解菌によって効率よく分解し、そ
の処理した水を注入井戸21を通して地下汚染箇所1の
上流側の注入井戸21から飽和層17に注入するので、
地下汚染箇所1の近傍に水を強制的に循環させることが
でき、地下汚染箇所1の上流側から下流側に向けて流れ
る地下水流5の量を増し、電極14,15間の電圧印加によ
る汚染物質の離脱効果と合わせて、汚染物質の地中から
の離脱をより一層促進することができる。しかも、地下
水流5が十分でない箇所においても汚染物質の処理を実
行することができる。
In the treatment according to this example, groundwater pumped from the pumping well 22 on the downstream side of the underground polluted site 1 is guided to the bioreactor 16 and efficiently decomposed by the degrading bacteria having high decomposing ability of pollutants in the bioreactor 16. Then, since the treated water is injected into the saturated layer 17 from the injection well 21 on the upstream side of the underground pollution place 1 through the injection well 21,
Water can be forcibly circulated in the vicinity of the underground pollution point 1, the amount of the groundwater flow 5 flowing from the upstream side to the downstream side of the underground pollution point 1 is increased, and the pollution caused by the voltage application between the electrodes 14 and 15 In addition to the effect of releasing the substance, the release of the pollutant from the ground can be further promoted. Moreover, the treatment of pollutants can be executed even in a place where the groundwater flow 5 is not sufficient.

【0023】また、本例では、地下汚染箇所1の上流側
の注入井戸21から飽和層17に処理水(別な水源から
の水でもよい)を注入する際に、地中に存在する汚染物
質分解菌の生育を促進させるメタン、フェノール等の基
質、栄養源、空気(酸素)を添加して注入することによ
り、地中に存在する汚染物質分解菌の活性を高め、地中
においても汚染物質の分解を行うことによって、汚染物
質の分解をより促進させることができる。さらに、必要
に応じて注入する処理水に界面活性剤を少量添加するこ
とにより、地中の粘土などに強固に吸着している汚染物
質を地下水中に極めて効果的に離脱させることができ
る。
Further, in this example, when the treated water (which may be water from another water source) is injected into the saturated layer 17 from the injection well 21 on the upstream side of the underground pollution point 1, contaminants existing in the ground Substrates such as methane and phenol that promote the growth of degrading bacteria, nutrient sources, and air (oxygen) are added and injected to enhance the activity of pollutant degrading bacteria existing in the ground, and pollutants even in the ground. The decomposition of the pollutants can promote the decomposition of the pollutants. Furthermore, by adding a small amount of a surfactant to the treated water to be injected as necessary, the pollutants strongly adsorbed on the clay in the ground can be very effectively released into the groundwater.

【0024】[0024]

【発明の効果】以上説明したように、本発明による汚染
地下水、土壌の修復方法は、汚染物質で汚染された地下
汚染箇所の近傍の飽和層に複数の井戸を掘削するととも
に、該地下汚染箇所の近傍に2つ以上の電極を離間して
埋設し、各電極間に電圧を加えつつ、該井戸から汚染物
質を含む地下水を揚水し、該揚水を地上のバイオリアク
ターに導いて汚染物質を分解処理し、該処理水を放流ま
たは飽和層に注入することにより、飽和層中の汚染物質
の離脱、移動を著しく促進することができるとともに、
従来法では汚染物質の離脱が困難であった飽和層以外の
地層中に含まれる汚染物質の離脱を促進させることがで
き、短期間で汚染物質を分解除去することができる。ま
た、前記処理水の少なくとも一部に、酸素と土壌微生物
の栄養源と基質のうちの少なくとも1種を添加し、前記
地下汚染箇所の地下水流上流側に位置する注入井戸から
飽和層に注入することによって、地下汚染個所近傍に存
在する汚染物質分解菌を生育させ、地下での汚染物質の
分解を促進させることができる。さらに、前記バイオリ
アクターを、前記汚染物質を嫌気分解するように構成さ
れた嫌気的バイオリアクターとしたので、好気的条件下
では分解不可能なテトラクロロエチレンをも分解するこ
とができる。
As described above, the method for remediating contaminated groundwater and soil according to the present invention excavates a plurality of wells in a saturated layer in the vicinity of a contaminated underground contaminated site, Two or more electrodes are buried in the vicinity of the space apart from each other, groundwater containing pollutants is pumped from the well while applying a voltage between each electrode, and the pumped water is guided to a bioreactor on the ground to decompose pollutants. By treating and then discharging or injecting the treated water into the saturated layer, it is possible to remarkably accelerate the desorption and migration of pollutants in the saturated layer,
It is possible to accelerate the removal of pollutants contained in formations other than the saturated layer, which was difficult to remove by conventional methods, and to decompose and remove the pollutants in a short period of time. Further, at least one of a nutrient source and a substrate for oxygen of soil microorganisms is added to at least a part of the treated water, and the saturated layer is injected from an injection well located upstream of the groundwater flow at the underground pollution location. As a result, the pollutant-degrading bacteria existing in the vicinity of the underground pollutant can be grown and the decomposition of the pollutant underground can be promoted. Furthermore, since the bioreactor is an anaerobic bioreactor configured to anaerobically decompose the pollutants, it is possible to decompose tetrachloroethylene, which cannot be decomposed under aerobic conditions.

【図面の簡単な説明】[Brief description of drawings]

【図1】図1は本発明の汚染地下水、土壌の修復方法の
一例を示す断面図である。
FIG. 1 is a sectional view showing an example of a method for repairing contaminated groundwater and soil according to the present invention.

【図2】図2は本発明の汚染地下水、土壌の修復方法の
一例を示す断面図である。
FIG. 2 is a cross-sectional view showing an example of a method for repairing contaminated groundwater and soil according to the present invention.

【図3】図3は従来のバイオレメディエーション法を示
す断面図である。
FIG. 3 is a cross-sectional view showing a conventional bioremediation method.

【符号の説明】[Explanation of symbols]

1……地下汚染箇所 17……飽和層 11,12,13……井戸 14,15……電極 16……バイオリアクター 21……注入井戸 22……揚水井戸 1 ... Underground contamination 17 ... Saturated layer 11, 12, 13 ... Well 14, 15 ... Electrode 16 ... Bioreactor 21 ... Injection well 22 ... Pumping well

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 汚染物質で汚染された地下汚染箇所の近
傍の飽和層に複数の井戸を掘削するとともに、該地下汚
染箇所の近傍に2つ以上の電極を離間して埋設し、各電
極間に電圧を加えつつ、該井戸から汚染物質を含む地下
水を揚水し、該揚水を地上のバイオリアクターに導いて
汚染物質を分解処理し、該処理水を放流または飽和層に
注入することを特徴とする汚染地下水、土壌の修復方
法。
1. A plurality of wells are excavated in a saturated layer in the vicinity of an underground polluted site contaminated with pollutants, and two or more electrodes are buried in the vicinity of the underground polluted site with a space between the electrodes. The groundwater containing pollutants is pumped from the well while applying a voltage to the well, the pollutants are decomposed by introducing the pumped water to an on-ground bioreactor, and the treated water is discharged or injected into a saturated layer. How to remediate contaminated groundwater and soil.
【請求項2】 前記処理水の少なくとも一部に、酸素と
土壌微生物の栄養源と基質のうちの少なくとも1種を添
加し、前記地下汚染箇所の地下水流上流側に位置する注
入井戸から飽和層に注入することを特徴とする請求項1
記載の汚染地下水、土壌の修復方法。
2. At least one of a nutrient source and a substrate for soil microorganisms is added to at least a part of the treated water, and a saturated layer is formed from an injection well located upstream of the groundwater flow at the underground pollution location. Injecting into
Remediation method for contaminated groundwater and soil described.
【請求項3】 前記バイオリアクターが、前記汚染物質
を嫌気分解するように構成された嫌気的バイオリアクタ
ーであることを特徴とする請求項1または2記載の汚染
地下水、土壌の修復方法。
3. The method for remediating contaminated groundwater and soil according to claim 1 or 2, wherein the bioreactor is an anaerobic bioreactor configured to anaerobically decompose the pollutants.
JP04336396A 1996-02-29 1996-02-29 How to restore contaminated groundwater and soil Expired - Fee Related JP3401660B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04336396A JP3401660B2 (en) 1996-02-29 1996-02-29 How to restore contaminated groundwater and soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04336396A JP3401660B2 (en) 1996-02-29 1996-02-29 How to restore contaminated groundwater and soil

Publications (2)

Publication Number Publication Date
JPH09234484A true JPH09234484A (en) 1997-09-09
JP3401660B2 JP3401660B2 (en) 2003-04-28

Family

ID=12661781

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04336396A Expired - Fee Related JP3401660B2 (en) 1996-02-29 1996-02-29 How to restore contaminated groundwater and soil

Country Status (1)

Country Link
JP (1) JP3401660B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004188406A (en) * 2002-04-02 2004-07-08 Eiichi Tashiro Anaerobic purifying method for soil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004188406A (en) * 2002-04-02 2004-07-08 Eiichi Tashiro Anaerobic purifying method for soil

Also Published As

Publication number Publication date
JP3401660B2 (en) 2003-04-28

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