JP2011000567A - Method and system for decomposing/purifying soil and groundwater polluting substances - Google Patents

Method and system for decomposing/purifying soil and groundwater polluting substances Download PDF

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JP2011000567A
JP2011000567A JP2009147704A JP2009147704A JP2011000567A JP 2011000567 A JP2011000567 A JP 2011000567A JP 2009147704 A JP2009147704 A JP 2009147704A JP 2009147704 A JP2009147704 A JP 2009147704A JP 2011000567 A JP2011000567 A JP 2011000567A
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injection
soil
groundwater
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Minoru Yoneda
稔 米田
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ARTHUR KK
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To provide a practical purification method which can purify substances polluting soil and ground water actually in a short time.SOLUTION: The method practiced in the site where soil or ground water is polluted by pollutants includes: a step in which an injection well 1 and a pumping well 2 are formed so that injection water passes through a pollution region, and ground water containing pollutants is pumped up from the pumping well 2; a step in which the pumped water is led into a bioreactor 15 on the ground for propagating microorganisms including the microorganisms in soil of the site to decompose the pollutants; and a step in which an apparatus 26 for generating ultrafine bubbles is arranged on the side of the injection well 1, and ultrafine bubbles are introduced into the decomposed pumped water and injected from the injection well 1.

Description

本発明は土壌・地下水汚染物質を浄化する方法及びそのシステムに関する。   The present invention relates to a method and system for purifying soil and groundwater contaminants.

従来、土壌、地下水から汚染物質を取り除く浄化方法として、バイオレメディエーションの開発研究が盛んに行われている。バイオレメディエーションとは土壌の掘削を行わず、原位置で微生物を利用して汚染物質を除去する技術である。
従来のバイオレメディエーションによる浄化方法としては、地下汚染領域の近くに複数本の井を掘削し、揚水管から揚水した地下水に微生物の活性を高める各種の基質(酸素、栄養など)を加えて、上流側に掘削された注入管へ戻す処理を繰り返す方法が知られている(特許文献1参照)。
近年では、注入水に超微細気泡を入れることで土壌に酸素を供給する構成が提案されている。
Conventionally, development research on bioremediation has been actively conducted as a purification method for removing contaminants from soil and groundwater. Bioremediation is a technology that removes pollutants using microorganisms in situ without excavating soil.
As a conventional purification method using bioremediation, several wells are drilled near the underground contamination area, and various substrates (oxygen, nutrients, etc.) that enhance the activity of microorganisms are added to the groundwater pumped from the pumping pipe. A method of repeating the process of returning to the injection tube excavated to the side is known (see Patent Document 1).
In recent years, a configuration has been proposed in which oxygen is supplied to soil by introducing ultrafine bubbles into the injected water.

特開平10−216696JP-A-10-216696

上記従来技術であっても揚水された汚染物質、例えば土壌等から剥離、分離された油などの汚染物質は最終的には産業廃棄処分をしなければならず、汚染が移動するだけであって環境汚染問題の根本的な解決にはならない。特に現実のバイオレメディエーションでは分離された油、例えばガソリン、軽油、重油などの処理に苦慮している。
また、現実の汚染土壌は多数の汚染物質が複雑に絡み合って汚染されており、単純に超微細気泡を注入するだけでは汚染土壌の個々の領域毎に汚染状況に応じた細やかで効果の高い浄化処理を行うことは難しい。
Even with the above prior art, the pollutants that have been pumped up, such as oil that has been peeled off and separated from the soil, etc., must finally be disposed of in an industrial waste, and only the contamination will be transferred. It is not a fundamental solution to environmental pollution problems. In particular, in actual bioremediation, it is difficult to process separated oils such as gasoline, light oil and heavy oil.
In addition, the actual contaminated soil is contaminated by many entangled pollutants, and by simply injecting ultra-fine bubbles, each area of the contaminated soil is refined and highly effective depending on the contamination status. It is difficult to process.

本発明は上記課題に鑑みなされたもので、本発明の目的は、土壌、地下水から分離された微生物のもつ発酵、分解機能を高めて、短期間で汚染物質に係わる産業廃棄物の発生を完全になくす、又は極めて低減できるシステムを提供することにある。
また、本発明の目的は、揚水によって回収される油などの汚染物質を微生物のもつ発酵、分解能力を活用したバイオリアクターシステムを開発することで、現実に短時間で浄化処理できる実用的なシステムを提供することである。
なお、上記に記載した以外の発明の課題、その解決手段及びその効果は、後述する明細書内の記載において詳しく説明する。
The present invention has been made in view of the above problems, and an object of the present invention is to enhance the fermentation and decomposition functions of microorganisms separated from soil and groundwater, and to completely generate industrial waste related to pollutants in a short period of time. It is an object of the present invention to provide a system that can be eliminated or extremely reduced.
In addition, the purpose of the present invention is to develop a bioreactor system that utilizes the fermentation and decomposition capabilities of microorganisms with pollutants such as oil recovered by pumping water, so that it can be practically purified in a short time. Is to provide.
In addition, the subject of invention other than having described above, its solution means, and its effect are demonstrated in detail in description in the specification mentioned later.

本発明は多面的に表現できるが、例えば、代表的なものを挙げると、次のように構成したものである。なお、下記各発明において、各符号は後述する実施形態との対応関係を分かりやすくするために一例として示したものであり、本発明の各構成要素は、実施形態に記載した符号に係る構成に限定されないことは言うまでもない。
本発明の土壌・地下水汚染物質の分解浄化方法は、土壌又は地下水が汚染物質で汚染されている原位置において行う方法であり、
注入水が汚染領域を通過するように注入井1と揚水井2を設け、前記揚水井2から汚染物質を含む地下水を揚水する行程と、
その原位置の土中微生物を含んだ微生物を増殖させる地上のバイオリアクター15に前記揚水を導いて汚染物質を分解する行程と、
超微細気泡発生装置26を前記注入井1側に配置して、前記分解された揚水に超微細気泡を入れて前記注入井1から注入する行程と、
を含むことを特徴とする。
Although the present invention can be expressed in many ways, for example, typical ones are configured as follows. In each of the following inventions, each symbol is shown as an example for easy understanding of the correspondence with the embodiment described later, and each component of the present invention corresponds to the configuration related to the symbol described in the embodiment. It goes without saying that it is not limited.
The method for decomposing and purifying soil and groundwater pollutants according to the present invention is a method for performing in situ where soil or groundwater is contaminated with pollutants,
A step of providing an injection well 1 and a pumping well 2 so that the injected water passes through the contaminated area, and pumping groundwater containing the pollutant from the pumping well 2;
A process of introducing the pumped water to a ground bioreactor 15 for growing microorganisms including soil microorganisms in its original position to decompose pollutants;
A step of placing the ultrafine bubble generating device 26 on the injection well 1 side, injecting ultrafine bubbles into the decomposed pumped water and injecting from the injection well 1;
It is characterized by including.

本発明であれば、少なくともその原位置の土中微生物を含んだ微生物を増殖させる地上のバイオリアクターに揚水を導くことにより、汚染物質を短時間でほぼ完全に分解することができる。従って汚染物質に係る産業廃棄物を著しく減らすことができる。また、嫌気性微生物、好気性微生物が働いている土中の状態であるか否かにかかわらず、超微細気泡発生装置を循環水経路の注入井側に配置して、超微細気泡を注入井から注入することで超微細気泡と微生物の相乗的な界面活性効果によって汚染物質の土壌構成物に対する剥離機能を高めて浄化速度を高めることができる。   According to the present invention, the pollutant can be almost completely decomposed in a short time by introducing the pumped water to the above-ground bioreactor for growing microorganisms containing soil microorganisms at least in situ. Therefore, industrial waste related to pollutants can be significantly reduced. Regardless of whether it is in the soil where anaerobic microorganisms or aerobic microorganisms are working, an ultrafine bubble generator is placed on the injection well side of the circulating water path to introduce the ultrafine bubbles into the injection well. It is possible to increase the decontamination function of the pollutant to the soil components and increase the purification rate by the synergistic interfacial effect of the ultrafine bubbles and the microorganisms.

上記構成において、前記バイオリアクター15で増殖された微生物を超微細気泡とともに前記注入井1から注入することもできる。
この構成であれば、汚染土壌中に存在する微生物はその汚染物質を分解する機能の高い細菌が集まっているので、その土中微生物をバイオリアクターで増殖させて超微細気泡とともに注入井から注入することで土中での分解速度を高めることができる。
上記構成において、前記バイオリアクター15の分解行程において、原位置の土中微生物に加えて汚染物質の種類を考慮してオペレータが選択した微生物を働かせることもできる。
この構成であれば、オペレータの経験を基にして汚染物質の分解に適した微生物を調合することでバイオリアクターでの分解速度を高めることができる。
In the above configuration, the microorganisms grown in the bioreactor 15 can be injected from the injection well 1 together with ultrafine bubbles.
With this configuration, the microorganisms present in the contaminated soil are gathered with bacteria that have a high function of decomposing the pollutants, so that the microorganisms in the soil are grown in the bioreactor and injected from the injection well together with ultrafine bubbles. This can increase the rate of decomposition in the soil.
In the above configuration, in the decomposition process of the bioreactor 15, in addition to the in-situ microorganisms, microorganisms selected by the operator in consideration of the types of contaminants can be used.
If it is this structure, the decomposition speed in a bioreactor can be raised by preparing the microorganisms suitable for decomposition | disassembly of a pollutant based on an operator's experience.

上記構成において、前記注入井1の注入口側に注入側バッファ槽12を設け、前記注入側バッファ槽12に超微細気泡発生装置26を配設し、前記注入側バッファ槽12内で超微細気泡の含有量を調整することもできる。
この構成であれば、汚染物質の分布状況に応じて注入側バッファ槽を設けることで、同じ原位置での汚染土壌であっても狭い汚染領域毎に注入液の条件を変えて細やかな浄化処理を行うことができる。
In the above-described configuration, the injection side buffer tank 12 is provided on the injection port side of the injection well 1, the ultrafine bubble generator 26 is provided in the injection side buffer tank 12, and the ultrafine bubbles are formed in the injection side buffer tank 12. The content of can also be adjusted.
With this configuration, by providing an injection-side buffer tank according to the state of contaminant distribution, even if it is contaminated soil at the same in-situ location, the conditions of the injection solution can be changed for each narrow contaminated area, and detailed purification processing can be performed. It can be performed.

上記構成において、前記注入側バッファ槽12に高濃度の微生物供給装置27を設け、前記注入側バッファ槽12内にオペレータが選択した微生物を供給することもできる。
この構成であれば、微生物を新たに加えることで分解条件を高めて、短期間に分解することが可能になる。
In the above configuration, a high concentration microorganism supply device 27 may be provided in the injection side buffer tank 12 to supply microorganisms selected by the operator into the injection side buffer tank 12.
If it is this structure, degradation conditions will be raised by adding microorganisms newly, and it will become possible to decompose in a short time.

本発明の土壌・地下水汚染物質の分解浄化システムは、土壌又は地下水が汚染物質で汚染されている原位置において、その汚染領域を注入水が通過するように設けられた注入井1及び揚水井2と、
前記揚水井2によって得られた揚水が導かれ、少なくともその原位置の土中微生物を含む微生物を増殖させる地上のバイオリアクター15と、
前記汚染物質の分布状況に対応して前記注入井1に連設して設けられた注入側バッファ槽12と、
前記注入側バッファ槽12に超微細気泡を供給する超微細気泡発生装置26と、
を備えたことを特徴とする。
The system for decomposing and purifying soil and groundwater pollutants of the present invention includes an injection well 1 and a pumping well 2 provided so that the injected water passes through the contaminated area in the original position where the soil or groundwater is contaminated with the contaminant. When,
A ground bioreactor 15 through which the pumped water obtained by the pumping well 2 is guided and grows microorganisms including soil microorganisms at least in its original position;
An injection-side buffer tank 12 connected to the injection well 1 corresponding to the state of distribution of the contaminants;
An ultrafine bubble generator 26 for supplying ultrafine bubbles to the injection side buffer tank 12,
It is provided with.

上記構成において、前記注入側バッファ槽12にオペレータが選択した微生物を供給する微生物供給装置27を設けることもできる。
上記構成において、前記揚水井2に揚水側バッファ槽13を設け、前記バイオリアクター15又は前記揚水側バッファ槽13に取付けられた汚染物質検出装置24の検出情報に基づいて、前記超微細気泡発生装置26、前記微生物供給装置22・27の少なくとも一つに駆動情報を出力する制御装置25を設けることもできる。
In the above configuration, a microorganism supply device 27 that supplies microorganisms selected by an operator to the injection side buffer tank 12 may be provided.
In the above configuration, a pumping-side buffer tank 13 is provided in the pumping well 2, and the ultrafine bubble generating device is based on detection information of the pollutant detecting device 24 attached to the bioreactor 15 or the pumping-side buffer tank 13. 26. At least one of the microorganism supply devices 22 and 27 may be provided with a control device 25 that outputs drive information.

本発明であれば、土壌、地下水から分離された汚染物質の微生物のもつ発酵、分解機能を高めて、短期間で汚染油の産業廃棄物の発生を完全になくすことができる。
また、現実に短時間で土壌・地下水の汚染物質を浄化処理できる実用的なシステムを提供できる。
According to the present invention, the fermentation and decomposition functions of the microorganisms of pollutants separated from soil and groundwater can be enhanced, and the generation of industrial waste of contaminated oil can be completely eliminated in a short period of time.
In addition, it is possible to provide a practical system that can purify contaminants of soil and groundwater in a short time.

以下、本発明の実施の形態を図面に基づき説明する。
図1は本発明に係る土壌・地下水汚染物質の分解浄化システムを示す概略構成図、図2は注入井と揚水井の平面配置の一例を示す図、図3は注入井と揚水井の断面図、図4は各井の作用部における注入,吸入の様子を示す図である。
この汚染物質分解浄化システムは、土壌又は地下水が汚染物質で汚染されている原位置において行われるものである。
図2に示すように、まず、汚染領域6を通過するように注入井1と揚水井2を例えば平面視において格子状に形成する。注入井1と揚水井2の配設間隔は汚染濃度が高いところは密度を高く設定し、汚染濃度が低いところは密度を低くするが図2においては等密度に設定した例が示してある。また、図4に示すように通常、各井1,2は管で構成され、各井1,2の作用部(主に先端部域)の周壁には孔3が多数設けられている。注入井1の孔3から放射状に放出された注入水4は土壌中を流れ、揚水井2の周壁の孔3から吸引される。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
1 is a schematic configuration diagram showing a system for decomposing and purifying soil and groundwater contaminants according to the present invention, FIG. 2 is a diagram showing an example of a plane arrangement of an injection well and a pumping well, and FIG. 3 is a cross-sectional view of the injection well and the pumping well. FIG. 4 is a view showing the state of injection and inhalation in the action part of each well.
This pollutant decomposition and purification system is carried out in situ where soil or groundwater is contaminated with pollutants.
As shown in FIG. 2, first, the injection well 1 and the pumping well 2 are formed in a lattice shape in plan view so as to pass through the contaminated region 6. The arrangement interval between the injection well 1 and the pumping well 2 is set such that the density is high when the contamination concentration is high, and the density is low when the contamination concentration is low, but FIG. Moreover, as shown in FIG. 4, each well 1 and 2 is normally comprised with the pipe | tube, and many holes 3 are provided in the surrounding wall of the action part (mainly tip part area) of each well 1 and 2. As shown in FIG. The injected water 4 radiated from the holes 3 of the injection well 1 flows through the soil and is sucked from the holes 3 on the peripheral wall of the pumping well 2.

図1及び図3に示すように、地中の構造は主に地下水が流れている地下水層7と、その上層の汚染土壌層8と地下水層7の下にある不透水層9とからなっている。汚染物質の多くは汚染土壌層8に存在し、特に各層の境界部分に多く存在している。例えば、油などの汚染物質は、粘土質や土壌中の有機物に吸着されやすく、汚染物質が徐々に地下水中に離脱していくので地下水層7にも汚染物質が含まれることになる。よって、注入井1と揚水井2は、地下の地下水層7にも十分達する深さに掘削される。また、浄化処理領域は遮水壁10によって周囲に拡散しないように区画する。   As shown in FIGS. 1 and 3, the underground structure is mainly composed of a groundwater layer 7 through which groundwater flows, a contaminated soil layer 8 above it, and an impermeable layer 9 below the groundwater layer 7. Yes. Most of the pollutants are present in the contaminated soil layer 8, and in particular, a large amount is present at the boundary portion of each layer. For example, contaminants such as oil are easily adsorbed by clay and organic matter in the soil, and the contaminants are gradually separated into the groundwater, so that the groundwater layer 7 also contains the contaminants. Therefore, the injection well 1 and the pumping well 2 are excavated to a depth that sufficiently reaches the underground groundwater layer 7. Further, the purification treatment area is partitioned by the water shielding wall 10 so as not to diffuse around.

図1に示すように、本実施形態に係る浄化システムは、注入井1及び揚水井2と、注入井1に連通される注入側バッファ槽12と、揚水井2に連通される揚水側バッファ槽13と、揚水側バッファ槽13からの揚水を一時的に溜める汚水槽14と、汚染物質を分解するバイオリアクター15と、水処理装置16と、水処理装置16で処理された水を溜める貯水槽17とを含んで構成してある。
この構成では揚水井2からの揚水の大部分は、揚水側バッファ槽13、汚水槽14、バイオリアクター15、水処理装置16、貯水槽17、注水側バッファ槽12を経て注入井1に再注入されるので循環管路18が形成されることになる。
As shown in FIG. 1, the purification system according to the present embodiment includes an injection well 1 and a pumping well 2, an injection-side buffer tank 12 that communicates with the injection well 1, and a pumping-side buffer tank that communicates with the pumping well 2. 13, a sewage tank 14 for temporarily storing pumped water from the pumping side buffer tank 13, a bioreactor 15 for decomposing pollutants, a water treatment device 16, and a water storage tank for storing water treated by the water treatment device 16 17.
In this configuration, most of the pumped water from the pumping well 2 is reinjected into the injection well 1 through the pumping side buffer tank 13, the sewage tank 14, the bioreactor 15, the water treatment device 16, the water storage tank 17, and the water injection side buffer tank 12. As a result, the circulation line 18 is formed.

注入井1と注水側バッファ槽12の間には弁装置29と注水用ポンプ30を設けてある。揚水井2と揚水側バッファ槽13の間にも弁装置31と注水用ポンプ32を設けてある。
注入側バッファ槽12は各注入井1に注入される水の性質、状態を変えるために設けられたものであり、超微細気泡発生装置26と後述する駆動情報によって選択された微生物を注入する微生物供給装置27を備えている。微生物供給装置27は複数個設けられる場合が多い。一方、揚水側バッファ槽13は必要によって設けられるものである。揚水側バッファ槽13は各揚水井2の揚水量や汚染物質の汚染濃度を検出するために水位計又は流量計(図示せず)や汚染濃度、汚染物質の特定などを行う汚染物質検出装置24が設けてある。
A valve device 29 and a water injection pump 30 are provided between the injection well 1 and the water injection side buffer tank 12. A valve device 31 and a water injection pump 32 are also provided between the pumping well 2 and the pumping side buffer tank 13.
The injection-side buffer tank 12 is provided to change the nature and state of the water injected into each injection well 1, and a microbe that injects a microbe selected by the ultrafine bubble generator 26 and drive information described later. A supply device 27 is provided. In many cases, a plurality of microorganism supply devices 27 are provided. On the other hand, the pumping side buffer tank 13 is provided if necessary. The pumping-side buffer tank 13 is a water level meter or a flow meter (not shown) for detecting the pumping amount of each pumping well 2 and the pollutant concentration, and a pollutant detection device 24 for identifying the pollutant concentration and pollutants. Is provided.

図1に示す構成では1本の注入井1に対して1個の注入側バッファ槽12が設けられている例が示してあるが、複数本の注入井1に対して1個の注入側バッファ槽12を連通させてもよい。この場合は複数本の注入井1の注入状態が単一の注入側バッファ槽12の状態で同じように変更されることになる。また、同様に複数本の揚水井2に対して1個の揚水側バッファ槽13を連通させてもよい。この場合は複数本の平均の揚水量や平均の汚染濃度が検出されることになる。前記複数本は2〜3本であることが好ましい。
水処理装置16は調整槽、浮上分離槽、沈殿槽、沈殿物滞在槽、フィルタープレス(全て図示せず)などで構成される。
In the configuration shown in FIG. 1, an example in which one injection-side buffer tank 12 is provided for one injection well 1 is shown, but one injection-side buffer is provided for a plurality of injection wells 1. The tank 12 may be communicated. In this case, the injection state of the plurality of injection wells 1 is changed in the same manner in the state of the single injection side buffer tank 12. Similarly, one pumping-side buffer tank 13 may be communicated with a plurality of pumping wells 2. In this case, an average amount of pumped water and an average contamination concentration are detected. The plurality is preferably 2 to 3 in number.
The water treatment device 16 includes an adjustment tank, a flotation separation tank, a sedimentation tank, a sediment residence tank, a filter press (all not shown), and the like.

バイオリアクター15は少なくともその原位置の土中微生物を含む微生物を増殖させる装置であり、短時間で油などの汚染物質を微生物の作用でほぼ完全に分解する能力のあるものが構成してある。本実施形態のバイオリアクター15は微生物培養装置20と微生物発酵分解槽21と微生物供給装置22を含んで構成してある。なお、バイオリアクター15にも汚染物質検出装置34が取り付けてある。汚染物質検出装置34は汚染物質の種類や濃度などを検出する。   The bioreactor 15 is a device for growing microorganisms including soil microorganisms at least in situ. The bioreactor 15 is configured to be capable of almost completely decomposing contaminants such as oil by the action of microorganisms in a short time. The bioreactor 15 according to the present embodiment includes a microbial culture apparatus 20, a microbial fermentation decomposition tank 21, and a microbial supply apparatus 22. The bioreactor 15 is also provided with a contaminant detection device 34. The contaminant detection device 34 detects the type and concentration of the contaminant.

このバイオリアクター15は、揚水井2から揚水された地下水に含まれる土中微生物を微生物培養装置20によって増殖させ、微生物発酵分解槽21において微生物によって発酵などによって分解するものである。このバイオリアクター15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、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15内の微生物培養装置20において温度、酸素濃度を分解細菌の生育に適する条件に維持してその細菌を増殖させる。   The bioreactor 15 is for growing microorganisms in the soil contained in the groundwater pumped from the pumping well 2 by the microorganism culturing apparatus 20 and decomposing the microorganisms by fermentation or the like in the microorganism fermentation decomposition tank 21. An appropriate type of bioreactor 15 can be selected and used according to the type of pollutant, and a nutrient source necessary for the growth of the pollutant-degrading bacteria can be added, or the temperature can be increased in the microorganism culture apparatus 20 in the bioreactor 15. The bacteria are propagated by maintaining the oxygen concentration at conditions suitable for the growth of the degrading bacteria.

バイオリアクター15は嫌気性バイオリアクターと好気性バイオリアクターの両方機能を備えている。例えば、好気性細菌と嫌気性細菌を用いる場合は超微細気泡を用いた分解槽を採用するとともに当該分解槽内又は別の分解槽において食物連鎖的な好気性細菌と嫌気性細菌の共同分解機能によって汚染物質を分解する。   The bioreactor 15 has both an anaerobic bioreactor function and an aerobic bioreactor function. For example, when aerobic bacteria and anaerobic bacteria are used, a decomposition tank using ultrafine bubbles is adopted, and a food chain-like aerobic and anaerobic bacteria decomposition function in the decomposition tank or in another decomposition tank To break down pollutants.

本実施形態において採用される汚染物質の分解能を有する微生物は、分解すべき汚染物質に応じて選択されるもので特に限定されない。
例えば、主な微生物を例示すると以下の通りである。
シュードモナス(Pseudomonas)属、バチルス(Bacillus)属、ニトロソモナス(Nitrosomonas)属、エシェリチア(Esherichia)属、バルクホルデリア(Burkholderia)属、アルカリゲネス(Alcaligenes)属、アシネトバクター(Acinetobacter)属、モラセラ(Moraxella)属、ビブリオ(Vibrio)属、ノカルジア(Nocardia)属、アルスロバクター(Arthrobacter)属、ミクロコッカス(Micrococcus)属、ラクトバチルス(Lactobacillus)属、アクロモバクター(Achromobacter)属、マイコバクテリウム(Mycobacterium)属、メチロシナス(Methylosinus)属、メチロモナス(Methylomonas)属、ベルキア(Welchia)属、メチロシスチス(Methylocystis)属などである。なお、投与する微生物は3〜15種類の混合で用いることが多い。原位置の細菌を増殖する場合は100種類を超える細菌を増殖する場合もある。
微生物供給装置22・27に加える微生物に関して、汚染物質がトリクロロエチレンや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好気性菌や、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、メタン生成細菌、フェノール資化性菌、トルエン資化性菌、アンモニア酸化細菌、硫酸還元細菌などの細菌を用いることができる。
The microorganism having the resolution of the pollutant employed in the present embodiment is not particularly limited and is selected according to the pollutant to be decomposed.
For example, examples of main microorganisms are as follows.
Pseudomonas genus, Bacillus genus, Nitrosomonas genus, Escherichia genus, Burkholderia genus, Alcaligenes genus, Acinetobacter genus Acinetobacter Vibrio genus, Nocardia genus, Arthrobacter genus, Micrococcus genus, Lactobacillus genus, Achromobacter genus, Mycobacterium ter , Methylocinus (Methy osinus) genus, Methylomonas (Methylomonas) genus, Berukia (Welchia) genus, Mechiroshisuchisu (Methylocystis) genus, and the like. In addition, the microorganisms to be administered are often used in a mixture of 3 to 15 types. When growing in situ bacteria, more than 100 types of bacteria may be grown.
Regarding microorganisms added to the microorganism supply devices 22 and 27, when the pollutant is an organic chlorine compound such as trichlorethylene or tetrachloroethylene, anaerobic bacteria, anaerobic bacteria separated from soil or anaerobic sludge, for example, methane Bacteria such as producing bacteria, phenol-utilizing bacteria, toluene-utilizing bacteria, ammonia-oxidizing bacteria, and sulfate-reducing bacteria can be used.

システムの制御については、揚水側バッファ槽13に設けられた汚染物質検出装置24の検出情報に基づいて、制御装置25がバイオリアクター15の微生物培養装置20、微生物発酵分解槽21及び微生物供給装置22に駆動情報(駆動信号を含む)を出力する。また、予め把握している汚染物質分布に基づいて、汚染物質領域に対応する注水側バッファ槽12に付設された超微細気泡発生装置26と微生物供給装置27にそれぞれ駆動情報を出力する。   Regarding the control of the system, based on the detection information of the pollutant detection device 24 provided in the pumping-side buffer tank 13, the control device 25 controls the microorganism culture device 20, the microorganism fermentation decomposition tank 21, and the microorganism supply device 22 of the bioreactor 15. Drive information (including drive signals) is output to Moreover, based on the pollutant distribution grasped in advance, the drive information is output to the ultrafine bubble generating device 26 and the microorganism supply device 27 attached to the water injection side buffer tank 12 corresponding to the pollutant region.

上記浄化システムの動作について簡単に説明する。
ボーリング調査から得られた3次元的な汚染物質分布情報に基づいて注入井1と揚水井1の差し込み形態が例えば、図2のように決定され、その汚染分布情報に基づいて注入井1に取り付けられる注入側バッファ槽12の注入井1に対する配設比率が決定される。例えば、図3に示す構成では2本の注入井1に対して1個の注入側バッファ槽12が設けてある。同様に揚水井1に対する揚水側バッフア槽13の配設比率も決定する。
The operation of the purification system will be briefly described.
Based on the three-dimensional pollutant distribution information obtained from the boring survey, the insertion form of the injection well 1 and the pumping well 1 is determined as shown in FIG. 2, for example, and attached to the injection well 1 based on the contamination distribution information. The arrangement ratio of the injection side buffer tank 12 to the injection well 1 is determined. For example, in the configuration shown in FIG. 3, one injection-side buffer tank 12 is provided for two injection wells 1. Similarly, the arrangement ratio of the pumping-side buffer tank 13 to the pumping well 1 is also determined.

この設定状態において、注入井1から注入用ポンプ30によって水を土壌等に注入して、図4に示すように噴出させて、超微細気泡を含んだ微生物の界面活性機能によって、石,砂利、岩、砂シルトなどの土壌構成物から汚染物質を剥離させて揚水井2からその汚染物質とともに揚水する。そして、汚水槽14を経てバイオリアクター15においてその土壌に住む土中微生物を含んで微生物培養装置20によって増殖させるとともに必要によって選択微生物を使用して微生物発酵分解槽21において汚染物質の分解を集中的に行う。実験では汚染地域に住む土中微生物を増殖させるとともに、選択して加える微生物の種類を経験則に従って調整することで、バイオリアクター15内においてガソリン、軽油などをほぼ100%分解することが可能であった。
汚染物質が除去された揚水は下流の水処理装置16を介して貯水槽17に蓄えられ、注入側バッファ槽12に再供給される。
In this set state, water is injected into the soil or the like from the injection well 1 by the injection pump 30 and ejected as shown in FIG. 4, and the surface active function of the microorganisms containing ultrafine bubbles allows the stone, gravel, The pollutant is peeled off from the soil components such as rocks and sand silt and pumped up from the pumping well 2 together with the pollutant. Then, in the bioreactor 15 through the sewage tank 14, the microorganisms in the soil that live in the soil are propagated by the microorganism culture apparatus 20, and if necessary, the decomposition of the pollutants is concentrated in the microorganism fermentation decomposition tank 21 using the selected microorganisms. To do. In the experiment, it was possible to decompose almost 100% of gasoline, light oil, etc. in the bioreactor 15 by growing microorganisms in the soil living in the contaminated area and adjusting the types of microorganisms selected and added according to empirical rules. It was.
The pumped water from which the pollutants have been removed is stored in the water storage tank 17 via the downstream water treatment device 16 and re-supplied to the injection side buffer tank 12.

一方、汚染領域の揚水側の要所に設けられた揚水側バッファ槽13の汚染物質検出装置24からは一定時間又は一定期間毎に揚水の揚水情報(揚水量、汚染物質の濃度等)が送られてくるので、その揚水情報に基づいて制御装置25は、バイオリアクター15の各槽の運転条件を所定のプログラム(動作テーブル等)に基づいて調整する。また、バイオリアクター15の運転条件を変えつつ、注入側バッファ槽12に供給する微生物の種類や、超微細気泡の有無及び量を変更するために、微生物供給装置27や超微細気泡発生装置26に駆動情報を送る。
このように一定時間又は一定期間毎に自動的にバイオリアクター15の運転条件と注入側バッファ槽12の条件を最適なものに変えることによって、従来の原位置での浄化所要時間を著しく短縮して1ヶ月〜3ヶ月程度で汚染土壌、汚染地下水を浄化することが可能になる。また、汚染物質であるをほぼ完全に分解できるので、産業廃棄物として処分する費用が不要になり、大きなコスト削減を実現できる。
On the other hand, from the pollutant detection device 24 of the pumping-side buffer tank 13 provided at a key point on the pumping side of the contaminated area, pumping information (pumping amount, concentration of pollutants, etc.) of pumped water is sent at fixed time intervals or fixed time intervals. Therefore, based on the pumping information, the control device 25 adjusts the operating conditions of each tank of the bioreactor 15 based on a predetermined program (operation table or the like). Further, in order to change the type of microorganisms supplied to the injection-side buffer tank 12 and the presence / absence and amount of ultrafine bubbles while changing the operating conditions of the bioreactor 15, the microorganism supply device 27 and the ultrafine bubble generator 26 are provided. Send drive information.
In this way, by automatically changing the operating conditions of the bioreactor 15 and the conditions of the injection side buffer tank 12 automatically for a certain time or every certain period, the time required for purification at the conventional in-situ position can be significantly shortened. It becomes possible to purify contaminated soil and contaminated groundwater in about one to three months. In addition, since the pollutant can be almost completely decomposed, the expense of disposing it as industrial waste becomes unnecessary, and a large cost reduction can be realized.

図1は実施形態に係る土壌・地下水汚染物質の分解浄化システムを示す概略構成図。FIG. 1 is a schematic configuration diagram illustrating a decomposition and purification system for soil and groundwater contaminants according to an embodiment. 図2は注入井と揚水井の平面配置の一例を示す図。FIG. 2 is a diagram showing an example of a planar arrangement of an injection well and a pumping well. 図3は注入井と揚水井の断面配置の一例を示す図。FIG. 3 is a diagram showing an example of a cross-sectional arrangement of an injection well and a pumping well. 図4は井の作用部における注入、吸入の様子を示す図。FIG. 4 is a view showing the state of injection and inhalation in the working part of the well.

1…注入井、2…揚水井、15…バイオリアクター、12…注入側バッファ槽、22・27…微生物供給装置、24・34…汚染物質検出装置、25…制御装置、26…超微細気泡発生装置。 DESCRIPTION OF SYMBOLS 1 ... Injection well, 2 ... Pumping well, 15 ... Bioreactor, 12 ... Injection side buffer tank, 22.27 ... Microorganism supply apparatus, 24.34 ... Contaminant detection apparatus, 25 ... Control apparatus, 26 ... Ultrafine bubble generation apparatus.

Claims (8)

土壌又は地下水が汚染物質で汚染されている原位置において行う方法であり、
注入水が汚染領域を通過するように注入井(1)と揚水井(2)を設け、前記揚水井(2)から汚染物質を含む地下水を揚水する行程と、
その原位置の土中微生物を含んだ微生物を増殖させる地上のバイオリアクター(15)に前記揚水を導いて汚染物質を分解する行程と、
超微細気泡発生装置(26)を前記注入井(1)側に配置して、前記分解された揚水に超微細気泡を入れて前記注入井(1)から注入する行程と、
を含むことを特徴とする、土壌・地下水汚染物質の分解浄化方法。
It is a method performed in situ where soil or groundwater is contaminated with pollutants,
Providing an injection well (1) and a pumping well (2) so that the injected water passes through the contaminated area, and pumping groundwater containing pollutants from the pumping well (2);
A process of decomposing pollutants by guiding the pumped water to a ground bioreactor (15) for growing microorganisms including soil microorganisms in its original position;
A step of disposing an ultrafine bubble generating device (26) on the injection well (1) side, injecting ultrafine bubbles into the decomposed pumped water and injecting from the injection well (1);
A method for decomposing and purifying soil and groundwater contaminants, characterized by comprising:
請求項1に記載の土壌・地下水汚染物質の分解浄化方法において、前記バイオリアクター(15)で増殖された微生物を超微細気泡とともに前記注入井(1)から注入する、土壌・地下水汚染物質の分解浄化方法。 The method for decomposing and purifying soil / groundwater pollutants according to claim 1, wherein microorganisms grown in the bioreactor (15) are injected from the injection well (1) together with ultrafine bubbles. Purification method. 請求項1に記載の土壌・地下水汚染物質の分解浄化方法において、前記バイオリアクター(15)の分解行程において、原位置の土中微生物に加えて汚染物質の種類を考慮してオペレータが選択した微生物を働かせる、土壌・地下水汚染物質の分解浄化方法。 The method for decomposing and purifying soil and groundwater pollutants according to claim 1, wherein in the bioreactor (15) decomposition process, the microorganism selected by the operator in consideration of the type of contaminant in addition to the soil microorganisms in situ Decomposing and purifying soil and groundwater pollutants. 請求項1から請求項3のいずれか一項に記載の土壌・地下水汚染物質の分解浄化方法において、前記注入井(1)の注入口側に注入側バッファ槽(12)を設け、前記注入側バッファ槽(12)に超微細気泡発生装置(26)を配設し、前記注入側バッファ槽(12)内で超微細気泡の含有量を調整する、土壌・地下水汚染物質の分解浄化方法。 The method for decomposing and purifying soil and groundwater contaminants according to any one of claims 1 to 3, wherein an injection-side buffer tank (12) is provided on the injection port side of the injection well (1), and the injection side A method for decomposing and purifying soil and groundwater pollutants, wherein an ultrafine bubble generating device (26) is disposed in a buffer tank (12), and the content of ultrafine bubbles is adjusted in the injection side buffer tank (12). 請求項4に記載の土壌・地下水汚染物質の分解浄化方法において、前記注入側バッファ槽(12)に高濃度の微生物供給装置(27)を設け、前記注入側バッファ槽(12)内にオペレータが選択した微生物を供給する、土壌・地下水汚染物質の分解浄化方法。 5. The method for decomposing and purifying soil and groundwater contaminants according to claim 4, wherein a high concentration microorganism supply device (27) is provided in the injection side buffer tank (12), and an operator is provided in the injection side buffer tank (12). A method for decomposing and purifying soil and groundwater contaminants that supplies selected microorganisms. 土壌又は地下水が汚染物質で汚染されている原位置において、その汚染領域を注入水が通過するように設けられた注入井(1)及び揚水井(2)と、
前記揚水井(2)によって得られた揚水が導かれ、少なくともその原位置の土中微生物を含む微生物を増殖させる地上のバイオリアクター(15)と、
前記汚染物質の分布状況に対応して前記注入井1に連設して設けられた注入側バッファ槽(12)と、
前記注入側バッファ槽(12)に超微細気泡を供給する超微細気泡発生装置(26)と、
を備えたことを特徴とする、土壌・地下水汚染物質の分解浄化システム。
An infusion well (1) and a pumping well (2) provided to allow the injected water to pass through the contaminated area at the site where the soil or groundwater is contaminated with the pollutant;
An above-ground bioreactor (15) to which the pumped water obtained by the pumping well (2) is guided and propagates microorganisms including soil microorganisms at least in its original position;
An injection-side buffer tank (12) provided continuously to the injection well 1 corresponding to the distribution of the contaminants;
An ultrafine bubble generator (26) for supplying ultrafine bubbles to the injection side buffer tank (12);
A system for decomposing and purifying soil and groundwater contaminants.
請求項6に記載の土壌・地下水汚染物質の分解浄化システムにおいて、前記注入側バッファ槽(12)にオペレータが選択した微生物を供給する微生物供給装置(27)を設ける、土壌・地下水汚染物質の分解浄化システム。 The soil / groundwater contaminant decomposition and purification system according to claim 6, wherein a microorganism supply device (27) for supplying microorganisms selected by an operator to the injection side buffer tank (12) is provided. Purification system. 請求項6に記載の土壌・地下水汚染物質の分解浄化システムにおいて、前記揚水井(2)に揚水側バッファ槽(13)を設け、前記バイオリアクター(15)又は前記揚水側バッファ槽(13)に取付けられた汚染物質検出装置(24)の検出情報に基づいて、前記超微細気泡発生装置(26)、前記微生物供給装置(22・27)の少なくとも一つに駆動情報を出力する制御装置(25)を設ける、土壌・地下水汚染物質の分解浄化システム。 The soil / groundwater contaminant decomposition and purification system according to claim 6, wherein a pumping-side buffer tank (13) is provided in the pumping well (2), and the bioreactor (15) or the pumping-side buffer tank (13) is provided. Based on the detection information of the attached pollutant detection device (24), the control device (25) outputs drive information to at least one of the ultrafine bubble generation device (26) and the microorganism supply device (22, 27). ), A system for decomposing and purifying soil and groundwater contaminants.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014069138A (en) * 2012-09-28 2014-04-21 Osaka Gas Co Ltd Underground fermentation facility
WO2015002302A1 (en) * 2013-07-05 2015-01-08 株式会社タカハタ電子 Method for activating oxygenase-containing composition, and contaminant detoxification method and device based on same
JP2017209599A (en) * 2016-05-23 2017-11-30 株式会社アーサーバイオ Purification method of oil contaminated soil and purification system thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014069138A (en) * 2012-09-28 2014-04-21 Osaka Gas Co Ltd Underground fermentation facility
WO2015002302A1 (en) * 2013-07-05 2015-01-08 株式会社タカハタ電子 Method for activating oxygenase-containing composition, and contaminant detoxification method and device based on same
JP2015012830A (en) * 2013-07-05 2015-01-22 株式会社タカハタ電子 Method for activating oxygenase-containing composition, and method and device for making contaminant harmless based on the method
JP2017209599A (en) * 2016-05-23 2017-11-30 株式会社アーサーバイオ Purification method of oil contaminated soil and purification system thereof

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