JP6750865B2 - Countermeasures against soil pollutants - Google Patents
Countermeasures against soil pollutants Download PDFInfo
- Publication number
- JP6750865B2 JP6750865B2 JP2016144184A JP2016144184A JP6750865B2 JP 6750865 B2 JP6750865 B2 JP 6750865B2 JP 2016144184 A JP2016144184 A JP 2016144184A JP 2016144184 A JP2016144184 A JP 2016144184A JP 6750865 B2 JP6750865 B2 JP 6750865B2
- Authority
- JP
- Japan
- Prior art keywords
- soil
- iron
- pollution
- pollutants
- reducing bacteria
- 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.)
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Description
本発明は、有害物質の取扱いのある事業者における、操業中からの土壌汚染の対策方法に関する。 The present invention relates to a method for coping with soil pollution during operation by a business operator handling hazardous substances.
我が国における土壌汚染対策事業は、1990年代より、多くの関連企業の業界参入が始まり、以後、関連法の法制化も図られて、2010年頃迄は、盛んに実施されてきたが、リーマンショックによる土地流動の硬直化や、収益の大きい大規模汚染サイト数の減少に伴って企業撤退が進み、業界は縮小傾向に向かった。
結果、業界創生から今日に至る約20余年において、約1割の汚染サイトの対策が完了したが、未だ9割程度の汚染サイトが残存する状況となった。
The soil pollution control business in Japan began to enter the industry by many related companies in the 1990s, and since then the related laws have been enacted, and it was actively implemented until around 2010, but due to the Lehman shock. The industry was heading for a shrinking trend as companies withdrew due to the stagnation of land flow and the decrease in the number of large-scale contaminated sites with large profits.
As a result, in about 20 years from the creation of the industry to the present day, measures for about 10% of contaminated sites have been completed, but about 90% of contaminated sites still remain.
この残存汚染サイトは、事業が継続中で浄化が思う様に進まない場合の他、汚染対策費が高額で土地売却が困難となり放置されているブラウンフィールドと呼ばれる不良債権化が進んだ土地である場合も多い。
いわゆる“塩漬け状態”となった土地であるが、我が国におけるブラウンフィールド化の懸念がある不良債権の総額は、約11兆円と推定されており、経済再生における土地流動化や地域再開発を推進する上で障害となる新たな社会問題として認知されている(環境省報道資料:土壌汚染をめぐるブラウンフィールド問題の実態等について中間とりまとめ/資料5(平成19年3月))。
This residual polluted site is a case where the project is ongoing and purification is not progressing as expected, and it is a land with bad debts called brown field which is abandoned due to high pollution control costs and difficult land sale There are also many.
Although the land is in a so-called "salted state", the total amount of bad debts that may cause brownfield in Japan is estimated to be about 11 trillion yen, promoting land mobilization and regional redevelopment during economic recovery. It has been recognized as a new social problem that will be an obstacle to doing so (Intermediate report on the actual situation of the Brownfield problem concerning soil pollution / Document 5 (March 2007)).
この様に、土壌汚染対策費が多額となるため、事業終了後の土地売却が困難となり放置されブラウンフィールド化が生じるならば、係るブラウンフィールド化対策は、想定される土地売却価格に見合った予算範囲内でのブラウンフィールド化予防対策を、事業終了以前の操業中からあらかじめ実施するか、或いは、廉価で有効なブラウンフィールド対策技術の上市を今後に待つ必要がある。但し、現状においては、後者は、その見込みさえも無く、前者の対策を重点的に図る選択肢しか無い状況にある。 In this way, the soil pollution countermeasure costs will be large, and if it becomes difficult to sell the land after the project is completed and it is left unattended and becomes brownfield, such a brownfield countermeasure is a budget that is commensurate with the expected land sale price. It is necessary to carry out brownfield prevention measures within the scope in advance from the start of operation before the end of the project, or to wait for the launch of inexpensive and effective brownfield countermeasure technology. However, in the present situation, the latter is not even promising, and there is only the option of focusing on the measures of the former.
前者の対策では、汚染拡大によってブラウンフィールド化する以前の「汚染漏洩の未然防止」と、係る未然防止対策を担保する「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」、更に、それでも汚染を生じてしまった場合は「操業中からの浄化対策等の実施」といった、汚染漏洩に対するフェイル・セーフ概念に基づく一連のブラウンフィールド化予防対策が、特に重要とされる。
係る「汚染漏洩の未然防止」に関する技術的/政策的アプローチとしては、平成24年に施行された改正水質汚濁防止法により、土壌地下水汚染を未然に防ぐ対策として、有害物質の地下浸透防止のための構造、設備及び使用の方法に関する基準が示され、法的拘束力を持った対策が図られる様になった。
また、「操業中からの浄化対策等の実施」においては、従来の汚染浄化技術における一部の原位置浄化技術に有効な対策技術が存在し、ブラウンフィールド化予防対策に一定の寄与を果たしている。
このように、汚染漏洩に対するブラウンフィールド化予防の取組みにおいて、その導入たる「汚染漏洩の未然防止」と最後段たる「操業中からの浄化対策等の実施」に関しては、ほぼ整備されつつある状況にあった。
The former measures include "prevention of pollution leaks" before brownfield due to the spread of pollution, and "early detection of pollution leaks and prevention of migration/diffusion of leaked pollutions (including local A series of brownfield preventive measures based on the fail-safe concept against pollution leakage, such as "low elution and pollution decomposition", and "continuation of purification measures during operation" if pollution still occurs. , Especially important.
As for the technical/policy approach regarding the “prevention of pollution leakage”, the revised Water Pollution Control Law enforced in 2012 is a measure to prevent soil and groundwater pollution. The standards for the structure, equipment, and method of use were provided, and legally binding measures were taken.
In addition, in "Implementation of purification measures during operation", there are some effective countermeasure techniques for in-situ purification techniques in conventional pollution purification techniques, and they contribute to a certain extent to brownfield prevention measures. ..
As described above, in the efforts to prevent brownfield conversion against pollution leaks, the introduction of "prevention of pollution leaks" and the final stage "implementation of purification measures from the start of operation" are almost ready. there were.
しかしながら、係る導入と最後段を繋ぐ技術、即ち、未然防止対策をフェイル・セーフの観点から担保し、本格対策に繋ぐ技術となる、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」に関する技術は、未だ発展途上であって、係る中継技術による補完が一連のブラウンフィールド化予防対策において望まれる状況にあった。
係る「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」技術における「汚染漏洩の早期検知」に関連する従来技術としては、特許文献1〜3に示す技術がある。また「漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」に関連する従来技術としては、特許文献4〜6に示す技術がある。
However, it is a technology that connects the introduction and the last stage, that is, a technology that guarantees preventive measures from the viewpoint of fail-safe and leads to full-scale measures, such as "early detection of pollution leakage and suppression of migration/diffusion of leakage pollution (including : Localized low elution/pollution decomposition) technology is still under development, and there was a situation where complementation by such relay technology was desired in a series of brownfield prevention measures.
As related arts related to "early detection of pollution leakage" in such "early detection of pollution leakage and movement/diffusion suppression of leakage pollution (including local low elution and pollution decomposition)", there are Patent Documents 1 to 1. There is a technology shown in 3. Further, as related arts related to “movement/diffusion suppression of leaked pollution (including: local low elution/decomposition of pollution)”, there are technologies shown in Patent Documents 4 to 6.
しかしながら、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」技術における「汚染漏洩の早期検知」に関連する従来技術としては、特許文献1〜3に示す技術は、後述する様な種々の問題点を有していた。 However, as a conventional technique related to "early detection of pollution leak" in "early detection of pollution leak and movement/diffusion control of leaked pollution (including local low elution and pollution decomposition)", Patent Document 1 The techniques shown in to 3 have various problems as described later.
特許文献1は、注入した検査用流体に汚染物質を捕捉し、検査用流体を含む地下水を回収して汚染を検知する技術であるが、地下水深度が深く存在する場合、メッシュ調査にはボーリングマシン等を用いた多数の観測井戸の設置を必要とすることとなり、係るコストからの実用性や汎用性に難があった。
また、本技術は、注入した検査用流体が均等に周囲に広がり、また確実に戻ってくることを前提とする調査であるが、この前提には地層が均質である必要性があり、自然状態において、このような理想的な条件は、まず存在しえない。本技術は、極めて環境依存性が高く、検査用流体の広がり方によっては、汚染が見過ごされ、或いは過小評価される懸念を有する技術であった。
Patent Document 1 is a technique for capturing pollutants in the injected inspection fluid and collecting groundwater containing the inspection fluid to detect contamination. However, when the groundwater depth is deep, the drilling machine is used for mesh investigation. Therefore, it was necessary to install a large number of observation wells using the above, and there was a difficulty in practicality and versatility from the cost.
In addition, the present technology is a study that assumes that the injected test fluid spreads evenly around the periphery and returns reliably, but this premise requires that the stratum be homogeneous and In such an ideal condition, there can hardly exist. The present technology is highly dependent on the environment, and there is a concern that contamination may be overlooked or underestimated depending on how the inspection fluid spreads.
また特許文献2は、地下水中の各種微生物の呼吸源となるイオン種の濃度分布から汚染の存在を推定する技術であるが、特許文献1と同様に、地下水深度が深く存在する場合、メッシュ調査には多数の観測井戸を設置する必要があり、コスト面からの実用性や汎用性に難があった。
加えて、汚染分解微生物の呼吸源となる硝酸イオンや硫酸イオンが、初期条件にて調査サイトにおいてほぼ均一の濃度で存在しなければ、汚染量に応じた定量的評価を適切に実施することは困難であり、汚染を過小評価してしまう、或いは見誤ってしまう等、不確実性を有する技術でもあった。
総じて、本技術は、極めて環境依存性が高く、汚染を過小評価してしまう、或いは見誤ってしまう、不確実性を有する技術であった。
Moreover, although patent document 2 is a technique which estimates the existence of pollution from the concentration distribution of the ion species used as the respiration source of various microorganisms in groundwater, like patent document 1, when groundwater depth exists deeply, a mesh investigation will be carried out. Since it was necessary to install a large number of observation wells, there was difficulty in practicality and versatility in terms of cost.
In addition, if nitrate ions and sulfate ions, which are respiration sources of pollutant-degrading microorganisms, do not exist at the survey site under the initial conditions in a substantially uniform concentration, it is not possible to appropriately carry out a quantitative evaluation according to the amount of contamination. It was also a technology with uncertainty, such as being difficult to underestimate pollution or making a mistake.
In general, the present technology is highly environment-dependent and has an uncertainty of underestimating the pollution or making a mistake.
また更に、特許文献3は、表層ガスを用いた調査方法であり、施工が容易で低コストを期待できる実施形態であるが、こちらも特許文献2同様に、調査サイトにおいて、呼吸源や栄養塩に不足が無く微生物代謝を担保する基本条件が整っていなければ、汚染量に応じた評価を適切に実施することは困難であり、汚染を過小評価してしまう不確実性を有する技術でもあった。
総じて、本技術もまた、極めて環境依存性が高く、汚染を過小評価してしまう、或いは見誤ってしまう、不確実性を有する技術であった。
Furthermore, Patent Document 3 is an investigation method using surface gas, and is an embodiment in which construction is easy and low cost can be expected. If there is no shortage and basic conditions to ensure microbial metabolism are not in place, it is difficult to properly carry out an evaluation according to the amount of pollution, and it was also a technique with the uncertainty of underestimating pollution. ..
In general, the present technology is also highly dependent on the environment and has an uncertainty of underestimating or misidentifying pollution.
このように、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」技術における「汚染漏洩の早期検知」に関連する従来技術は、いずれも極めて環境依存性が高く、汚染が見過ごされる、或いは過小評価される懸念を有する、おおむね高コストな技術であった。 As described above, the conventional technologies related to “early detection of pollution leakage” in “early detection of pollution leakage and movement/diffusion control of leakage pollution (including local low elution and pollution decomposition)” are all It was a highly expensive technology, which is highly dependent on the environment and could cause pollution to be overlooked or underestimated.
ところで、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」技術における「漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」に関連する従来技術である、特許文献4〜6に示す技術も、後述する様な種々の問題点を有していた。 By the way, in the "Early detection of pollution leakage and migration/diffusion control of leakage pollution (including local low elution and pollution decomposition)" technology, "Movement/diffusion suppression of leakage pollution (including local low elution/local decomposition)" The technologies disclosed in Patent Documents 4 to 6, which are conventional technologies related to "decomposition of pollution", also have various problems as described below.
たとえば、特許文献4に示される技術の様に、有機性化合物による土壌汚染から汚染物質の移動/拡散抑制(含:局所的な低溶出化・汚染分解)を図るための方法として、錠剤状の活性炭含有物を用いた低溶出化手法が提案されている。 For example, as in the technique disclosed in Patent Document 4, as a method for suppressing migration/diffusion of pollutants from soil pollution by organic compounds (including local low elution and pollution decomposition) A method for reducing elution using a material containing activated carbon has been proposed.
ところが、特許文献4に示されている錠剤状の活性炭含有物を用いた汚染物質の移動/拡散抑制(含:局所的な低溶出化・汚染分解)を図るための方法は、汚染された表層土壌や河川底泥等への散布による対策用の技術であり、地質構造を有する汚染された飽和帯へ適用するためには、錠剤状の活性炭含有物の形状から、掘削し混合する方法等に限定され、適用性が限定される技術であった。
加えて、本技術は、単に活性炭錠剤に汚染物質を吸着させ局所的な低溶出化を図る技術であって、汚染物質の低減が可能な浄化技術では無い、即ち、汚染物質の含有量を低減することが困難な技術であった。
However, a method for suppressing migration/diffusion of pollutants (including: local low elution/pollution decomposition) using a tablet-shaped active carbon-containing material disclosed in Patent Document 4 is a contaminated surface layer. It is a technology for countermeasures by spraying on soil or river bottom mud, and in order to apply it to a polluted saturated zone having a geological structure, it is necessary to use a method such as excavating and mixing from the shape of tablet-like activated carbon-containing material. It was a technology with limited and limited applicability.
In addition, this technology is a technology that simply adsorbs contaminants to activated carbon tablets to achieve local low elution, and is not a purification technology that can reduce contaminants, that is, reduces the content of contaminants. It was a difficult technique to do.
また、係る汚染含有量の低減が困難な点は、特許文献5の汚染吸着能を有する微細炭素系粒子を用いた汚染対策技術も同様であった。
即ち、汚染吸着能を有する微細炭素系粒子に吸着した汚染を分解除去する機能がなければ、散布した汚染吸着能を有する微細炭素系粒子は、いずれは吸着量の限界に至り、その場合は、汚染吸着能を有する微細炭素系粒子を繰り返し投入する様な、不経済な処理となってしまいかねない技術であった。
Further, the difficulty of reducing the contamination content is also the same as the contamination countermeasure technology using fine carbon-based particles having a contamination adsorbing ability of Patent Document 5.
That is, if there is no function of decomposing and removing the contaminants adsorbed on the fine carbon-based particles having a contaminant adsorption capacity, the dispersed fine carbon-based particles having a contaminant adsorption capacity eventually reach the limit of the adsorption amount, and in that case, It was a technique that could result in an uneconomical treatment, such as repeatedly charging fine carbonaceous particles having a contaminant adsorption capacity.
特許文献6に示される汚染土壌浄化後における再汚染防止方法は、土壌地下水汚染対策後の不用意な汚染溶出を対象とした技術であるが、特許文献5同様に、汚染吸着能を有する活性炭やゼオライトが、単に汚染物質の吸着のみに使用されており、本技術においても、汚染吸着能を有する吸着粒子に吸着した汚染を分解除去する機能がなく、これらの吸着粒子は、いずれは吸着量の限界に至り、その場合は、汚染吸着能を有する吸着粒子を繰り返し投入する様な、不経済な処理となってしまいかねない技術であった。 The method for preventing recontamination after purification of contaminated soil shown in Patent Document 6 is a technique aimed at inadvertent contamination elution after soil groundwater pollution countermeasures. Zeolite is used only for the adsorption of pollutants, and even in the present technology, there is no function of decomposing and removing the contaminants adsorbed by the adsorbent particles having a contaminant adsorbing ability. The technique reached the limit, and in that case, the technique could be an uneconomical treatment such as repeatedly introducing adsorbent particles having a contaminant adsorption ability.
総じて、従来の土壌汚染に対して土壌へ種々の汚染吸着能を有する微細炭素系粒子を添加して汚染対策を実施する技術は、一定量の汚染に対し「移動/拡散抑制・低溶出化」を図ることは可能であるが、汚染含有量の低減たる「分解」までを考慮した、効果の継続性や費用対効果を兼ね備えた技術では無かった。 Generally speaking, the technology of adding fine carbon particles with various adsorption capacity to soil for conventional soil pollution and implementing countermeasures against pollution is "movement/diffusion suppression/low elution" for a certain amount of pollution. Although it is possible to achieve this, it was not a technology that has both continuity of effects and cost-effectiveness in consideration of “decomposition” that reduces the pollutant content.
この様な背景から、本発明の目的を、汚染が過小評価される懸念が少ない環境依存性が低い廉価な「汚染漏洩の早期検知」技術、また、移動/拡散抑制・低溶出化は元より、汚染含有量の低減たる汚染分解までを考慮した「漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」技術の上市化と設定した。 From such a background, the purpose of the present invention is to reduce the risk of underestimation of pollution, to provide an inexpensive “early detection of pollution leakage” technology with low environmental dependency, and to prevent migration/diffusion suppression/low elution. , It was set as the market launch of the technology of "movement/diffusion control of leaked pollution (including: local low elution/pollution decomposition)" in consideration of pollution decomposition to reduce the pollution content.
上記の課題を解決するために、本件発明者らが鋭意開発を進めたところ、導電性資材による立体導電網を活用して、鉄還元細菌が有する機能を応用したバイオプリベンション法(生物学的汚染予防法)とその付帯対策技術群による、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」を一連で達成する以下の発明に至った。
即ち、本発明の要旨とするところは、次の(1)〜(14)である。
In order to solve the above-mentioned problems, the inventors of the present invention have eagerly developed the bio-prevention method applying the function of the iron-reducing bacteria (biological The following inventions have been achieved to achieve "early detection of pollution leakage and suppression of migration/diffusion of leakage pollution (including local low elution and pollution decomposition)" by means of the Pollution Prevention Law) It was
That is, the gist of the present invention is the following (1) to (14).
(1)生分解性を呈し有害物質を包含する汚染物質の取扱い履歴、或いは予定がある敷地において、鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材と培養基材を、対策対象の土壌に添加し、連通する立体導電網を地中に形成して、該立体導電網に導通する鉄還元細菌を包含する微生物群集と汚染物質との接触を通じて、汚染物質の代謝や分解を図る土壌汚染物質の対策方法であって、前記鉄還元細菌の代謝に由来する不溶性鉄化合物の生成と集積を図り、土壌間隙の閉塞を促して、前記汚染物質の移動の抑制を図り、該移動が抑制された該汚染物質に対し、更なる微生物代謝や分解を図る前記土壌汚染物質の対策方法。 (1) A material containing a porous carbon-based material that mediates extracellular electron transfer of iron-reducing bacteria at least partly in a site where biodegradable pollutants including harmful substances are handled or planned And, a culture substrate is added to the soil to be treated, a three-dimensional conductive net that communicates is formed in the ground, and a contact is made with a microbial community including iron-reducing bacteria that conducts to the three-dimensional conductive net and contaminants, metabolism or degradation of the pollutants to a countermeasure method of FIG Ru soil contaminants, achieving generation and accumulation of insoluble iron compounds derived from the metabolism of the iron-reducing bacteria, to encourage blockage of soil pore, said pollution The method for controlling soil pollutants, which aims to suppress the migration of the pollutants and further metabolizes or decomposes the pollutants whose migration is suppressed .
(2)前記敷地において、前記汚染物質による土壌汚染が既知である土壌汚染エリアとその周辺部を対象として、前記立体導電網と鉄還元細菌を包含する微生物群集を形成することを特徴とする(1)に記載された土壌汚染物質の対策方法である。 ( 2 ) On the site, a microbial community including the steric conductive net and iron-reducing bacteria is formed for a soil-contaminated area where soil contamination by the pollutant is known and its surrounding area ( This is the countermeasure method for soil pollutants described in 1 ) .
(3)前記汚染物質を代謝可能な微生物、および/或いは、前記鉄還元細菌を別途培養し、前記鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材、および/或いは、前記培養基材と共に、対策対象の土壌に添加することを特徴とする(1)から(2)の少なくとも1項に記載された土壌汚染物質の対策方法である。 ( 3 ) A microorganism that can metabolize the pollutant and/or a material containing at least a part of a porous carbon-based material that mediates extracellular electron transfer of the iron-reducing bacterium by separately culturing the iron-reducing bacterium And/or, together with the culture substrate, the method for controlling soil pollutants described in at least one of (1) to ( 2 ), which is added to the soil to be treated.
(4)微生物代謝に応じた電子供与体、および/或いは、電子受容体を、対策対象の土壌に添加することを特徴とする(1)から(3)の少なくとも1項に記載された土壌汚染物質の対策方法である。 (4) an electron donor according to the microorganism metabolism, and / or an electron acceptor, which is according to at least one of adding to the soil measures a subject from and wherein (1) and (3) Soil This is a countermeasure for pollutants.
(5)前記鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材が、活性炭であることを特徴とする(1)から(4)の少なくとも1項に記載された土壌汚染物質の対策方法である。 ( 5 ) The material containing a porous carbon-based material that mediates extracellular electron transfer of iron-reducing bacteria in at least a part thereof is activated carbon, according to at least one of (1) to ( 4 ). This is a countermeasure method for the listed soil pollutants.
(6)前記活性炭および鉄粉を、また前記培養基材として脂溶性有機資材を少なくとも一部に含む資材を添加して、汚染物質の代謝や分解を還元条件下で促進化する操作を、任意のタイミングで実施することを特徴とする(5)に記載された土壌汚染物質の対策方法である。 ( 6 ) The operation of accelerating the metabolism and decomposition of pollutants under reducing conditions by adding the activated carbon and iron powder, and a material containing a fat-soluble organic material as at least a part of the culture substrate, is performed . It is the method for controlling soil pollutants described in ( 5 ), which is carried out at any time.
(7)前記活性炭および鉄粉を対策対象の土壌に添加し、更に過酸化物を少なくとも一部に含む資材を添加して、汚染物質の代謝や分解を酸化条件下で促進化する操作を、任意のタイミングで実施することを特徴とする(5)に記載された土壌汚染物質の対策方法である。 ( 7 ) An operation of adding the activated carbon and iron powder to the soil to be treated, and further adding a material containing at least a part of peroxide to accelerate the metabolism and decomposition of pollutants under oxidizing conditions , is been countermeasures soil contaminants described which comprises carrying out at the timing of arbitrary (5).
(8)前記鉄還元細菌が用いる、電子受容体の供給、および/或いは、電子受容体の賦活化を目的として、空気または酸素を含む気体を、対策対象の土壌に供給することを特徴とする(1)から(7)の少なくとも1項に記載された土壌汚染物質の対策方法である。 ( 8 ) It is characterized in that a gas containing air or oxygen is supplied to the soil to be treated for the purpose of supplying electron acceptors and/or activating electron acceptors used by the iron-reducing bacteria. It is the method for controlling soil pollutants described in at least one of (1) to ( 7 ).
(9)井戸様構造物を介して、過酸化物を対策対象の土壌に添加して、前記鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材の付着性物質による機能低下の再生を図る操作を実施することを特徴とする(1)から(8)の少なくとも1項に記載された土壌汚染物質の対策方法である。 (9) Material via wells like structures, with the addition of the peroxide into the soil measures a subject, comprising at least a portion of the porous carbonaceous material which mediate extracellular electron transfer of the iron-reducing bacteria The method for remedying soil pollutants described in at least one of (1) to ( 8 ) is characterized in that the operation for regenerating the functional deterioration due to the adherent substance is carried out.
(10)前記井戸様構造物が、1本の管構造物で構成され、観測井戸機能と共に、該ストレーナ区間から、過酸化物溶液、および/或いは、気体を対策対象の土壌に注入する機能を有する、少なくとも2区間以上のストレーナを配することを特徴とする(9)に記載された土壌汚染物質の対策方法である。 ( 10 ) The well-like structure is composed of one tube structure, and has a function of observing well and a function of injecting a peroxide solution and/or gas from the strainer section into the soil to be treated. The method for controlling soil pollutants described in ( 9 ) is characterized by disposing strainers for at least two sections.
(11)前記過酸化物が過硫酸化合物であることを特徴とする(7)、(9)、或いは(10)の少なくとも1項に記載された土壌汚染物質の対策方法である。 ( 11 ) The method for preventing soil pollutants according to at least one of ( 7 ), ( 9 ), or ( 10 ), wherein the peroxide is a persulfate compound.
(12)前記鉄還元細菌を包含する微生物群集の代謝を通じて発生した二酸化炭素ガスを少なくとも含む1種類以上の地中ガス成分濃度を測定して、該ガス成分の濃度分布から前記汚染物質の地下漏洩地点の推定を、加えて実施することを特徴とする(1)から(11)の少なくとも1項に記載された土壌汚染物質の対策方法である。 ( 12 ) The concentration of at least one underground gas component containing at least carbon dioxide gas generated through the metabolism of a microbial community including the iron-reducing bacteria is measured, and the underground leakage of the pollutant is determined from the concentration distribution of the gas component. the estimation of the location, a countermeasure soil pollutants according to at least one of which comprises carrying out pressurized strong point (1) (11).
(13)前記有害物質が、1,4-ジオキサンであることを特徴とする(1)から(12)の少なくとも1項に記載された土壌汚染物質の対策方法である。 ( 13 ) The method for controlling soil pollutants described in at least one of (1) to ( 12 ), wherein the harmful substance is 1,4-dioxane.
以下、本発明について更に詳述する。
本発明では、鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材による立体導電網を活用して、鉄還元細菌が有する機能を応用したバイオプリベンション法(生物学的汚染予防法)とその付帯対策技術群による、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」たる一連の汚染対策を実施することを前提とする。
Hereinafter, the present invention will be described in more detail.
In the present invention, a bioprevention method applying the function of an iron-reducing bacterium by utilizing a steric conductive network of a material containing at least a part of a porous carbon-based material that mediates extracellular electron transfer of the iron-reducing bacterium. (Biological Pollution Prevention Law) and its incidental countermeasure technology group to implement a series of pollution countermeasures such as "early detection of pollution leakage and suppression of migration/diffusion of leakage pollution (including local low elution and pollution decomposition)" It is assumed to be implemented.
本発明のうち(1)に係る土壌汚染物質の対策方法によれば、鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材と培養基剤を、対象土地の飽和帯或いは不飽和帯に添加して、連通する立体導電網を地中に形成することにより、立体導電網に導通する鉄還元細菌を包含する微生物群集の代謝によって、生分解性を呈し有害物質を包含する汚染物質の代謝を促し、汚染物質の低減を図ることができる。 According to the method for controlling soil pollutants according to (1) of the present invention, a material containing a porous carbon-based material that mediates extracellular electron transfer of iron-reducing bacteria in at least a part and a culture base are used as a target land. By adding it to the saturated or unsaturated zone of spores to form a communicating steric conductive network in the ground, it is biodegradable and harmful by the metabolism of a microbial community including iron-reducing bacteria that conducts to the steric conductive network. It is possible to promote metabolism of pollutants including substances and reduce pollutants.
なお、土壌中には、豊富な三価鉄が存在するとしても、「鉄還元細菌(を包含する微生物群集)」及び「汚染物質」並びに「電子受容体」の三者が同地点に存在しなければ、高い代謝活性を得ることはできない。更に、この三者が同地点に存在したとしても、時間経過に従い代謝が進行し、相対量として「汚染物質」>「電子受容体」となった場合は、その地点において「電子受容体」の不足を生じることとなり、結果、「鉄還元細菌(を包含する微生物群集)」の代謝は低下し「汚染物質」の代謝も停止する。
しかしながら、本発明であるところの、連通する立体導電網を土壌中に張り巡らせることにより、少なくとも、「鉄還元細菌(を包含する微生物群集)」及び「汚染物質」並びに「立体導電網」の三者が同地点に存在すれば、鉄還元細菌由来の電子を、この立体導電網が近傍の数多の電子受容体迄の電子移動を仲介する。
また更に、培養が進み鉄還元細菌の存在量が増加すれば、導通状態に無い立体導電網同士が、鉄還元細菌が仲立ちすることで導通状態となり、立体導電網同士が有機的に連結するので、係る立体導電網の敷設が叶った範囲の三価鉄を、あまねく電子受容体として活用することが可能となる。
係る機構によって、本発明によるところの立体導電網を地中に設置することにより、代謝収支における相対量として「汚染物質」<「電子受容体」の状態となるので、鉄還元細菌等による汚染物質の代謝が、その場で継続し、より多くの汚染物質の浄化を継続的に図ることができる。
Even if abundant trivalent iron is present in soil, there are three parties, "iron-reducing bacteria (including microbial community),""pollutants," and "electron acceptor" at the same location. Without it, high metabolic activity cannot be obtained. Furthermore, even if these three are present at the same point, if the metabolism progresses over time and the relative amount becomes "pollutant">"electronacceptor", the "electron acceptor" As a result, the metabolism of "iron-reducing bacteria (including microbial community)" is lowered and the metabolism of "pollutants" is stopped.
However, according to the present invention, by spreading a communicating three-dimensional conductive network in the soil, at least "iron-reducing bacteria (including microbial community)", "pollutants" and "three-dimensional conductive network" can be obtained. If a person exists at the same point, this steric conductive network mediates the transfer of electrons from iron-reducing bacteria to many electron acceptors in the vicinity.
Furthermore, as the culture progresses and the amount of iron-reducing bacteria increases, the three-dimensional conductive networks that are not in conduction are brought into conduction by the intermediary of iron-reducing bacteria, and the three-dimensional conduction networks are organically linked to each other. It becomes possible to utilize the ferric iron in the range where the three-dimensional conductive network is laid as a general electron acceptor.
By installing the three-dimensional conductive network according to the present invention in the ground by such a mechanism, the relative amount in the metabolic balance becomes “pollutant”<“electron acceptor”, and therefore pollutants due to iron-reducing bacteria etc. Metabolism continues on the spot, and more pollutants can be continuously purified.
ところで、本発明によるところの立体導電網を敷設し、鉄還元細菌を包含する微生物群集の代謝によって、生分解性を呈し有害物質を包含する汚染物質の分解と浄化が図られる過程において、二酸化炭素や三価鉄由来の種々の鉄化合物が、周囲の土壌間隙中に蓄積される。 By the way, by laying a three-dimensional conductive network according to the present invention, by the metabolism of a microbial community including iron-reducing bacteria, in the process of decomposing and purifying pollutants that exhibit biodegradability and include harmful substances, carbon dioxide Various iron compounds derived from iron and trivalent iron accumulate in the surrounding soil voids.
係る、前者の蓄積する二酸化炭素を利用すれば、(12)に係る方法であるところの、地上と連通する地中孔を通じて土壌ガスを採取し、二酸化炭素を少なくとも含む1種類以上のガス成分濃度を、定期的に測定することにより、係るガス成分の濃度分布から該汚染物質の地下漏洩とその漏洩地点を早期に検知できるので、その後の一連の土壌汚染物質対策を有効且つ効果的に実施することができる。
また、係る汚染物質の地下漏洩調査を精度良く定期的に実施することにより、汚染漏洩の存在と漏洩地点を、漏洩を生じた極初期の段階で検知することにより、広範・深部に移動/拡散し重篤な汚染被害を引き起こす可能性のあるリスクを回避し、結果的には浄化対策コストを格段に低減した汚染対策を実施することができる。
実際、浅層での1立米の汚染土壌の掘削除去と処理には数万円程度が掛かる。地下水流速が0.3m/日、垂直/水平方向への移動速度がこの1/10だとして、これを1年間放置すれば、汚染長は100m超、汚染深度/幅は10m超にも及ぶ。単純に1年間で0.5〜1万立米程度の汚染土壌が生じることとなり、この対策処理には、高々1年の放置で億単位の費用損失が想定される深刻な損害状況となる。
If the former accumulated carbon dioxide is used, the soil gas is collected through the underground hole that communicates with the ground, which is the method according to ( 12 ), and the concentration of one or more gas components containing at least carbon dioxide. By measuring periodically, the underground leakage of the pollutant and its leakage point can be detected early from the concentration distribution of the gas component concerned, so a series of subsequent measures for soil pollutants will be implemented effectively and effectively. be able to.
In addition, by conducting underground leakage surveys of such pollutants with high accuracy and regularity, the presence and location of the contamination leakage can be detected at the very early stage of the leakage, so that it can be moved/extended to a wide area/deep area. However, it is possible to avoid the risk of causing serious pollution damage, and as a result, it is possible to implement pollution control measures that significantly reduce purification cost.
Actually, excavation and removal of contaminated soil of 1 cubic meter in the shallow layer costs tens of thousands of yen. Assuming that the groundwater flow velocity is 0.3 m/day and the vertical/horizontal movement speed is 1/10 of this, if left unattended for 1 year, the pollution length will exceed 100 m and the pollution depth/width will exceed 10 m. Simply, about 0.5 to 10,000 cubic meters of contaminated soil will be produced in one year, and this treatment will result in a serious damage situation in which a loss of 100 million units is expected if left unattended for at most one year.
一方、後者の三価鉄由来の鉄化合物類は、上述した立体導電網の機能によって、鉄還元細菌を包含する微生物群集の代謝によって汚染物質の分解と浄化が図られる部位に蓄積するとは限らない。その多くは、鉄還元細菌を包含する微生物群集が存在する周縁の、三価鉄が存在する酸化環境近傍の土壌と立体導電網が接触する部分にて、三価鉄由来の種々の鉄化合物の蓄積が図られる。
即ち、(1)に係る方法であるところの、嫌気的環境の周囲に存在する酸化的環境に近い部位にて三価鉄由来の種々の鉄化合物、例えば、マグネタイトや、酸素と二価鉄の反応にて生じた水酸化鉄等の不溶性鉄化合物類を蓄積させることにより、その汚染近傍の土壌間隙の閉塞が促され、汚染物質の移動/拡散抑制を図りながら、鉄還元細菌を包含する微生物群集の近傍に係る汚染物質を留め、更に係る鉄還元細菌を包含する微生物群集の代謝により汚染物質の低減を効率良く図ることができる。
On the other hand, the latter iron compounds derived from ferric iron do not always accumulate at the site where decomposition and purification of pollutants are achieved by metabolism of the microbial community including iron-reducing bacteria due to the function of the above-mentioned steric conductive network. .. Many of them are composed of various ferric iron-derived iron compounds in the periphery where microbial communities including iron-reducing bacteria are present, at the part where the steric conductive network comes into contact with the soil near the oxidizing environment where ferric iron exists. Accumulation is planned.
That is, in the method according to ( 1 ), various iron compounds derived from ferric iron, such as magnetite, oxygen and divalent iron, are present in the vicinity of the oxidative environment existing around the anaerobic environment. By accumulating insoluble iron compounds such as iron hydroxide generated in the reaction, the soil voids near the contamination are promoted to be blocked, and microorganisms containing iron-reducing bacteria while suppressing migration/diffusion of contaminants. The pollutants in the vicinity of the crowd can be retained, and the pollutants can be efficiently reduced by metabolism of the microbial community including the iron-reducing bacteria.
また、係る土壌間隙の閉塞により汚染物質の移動は極めて緩やかになるが、鉄還元細菌を包含する微生物群集による汚染物質の代謝速度は変わらないので、係る周囲の二酸化炭素濃度をスポット的に高く維持することができ、(12)に係る方法であるところの、土壌ガス調査による汚染漏洩地点検出の確度を、本機構により格段に高めることができる。 In addition, although the migration of pollutants becomes extremely slow due to the blockage of the soil gap, since the metabolic rate of pollutants by the microbial community including iron-reducing bacteria does not change, the carbon dioxide concentration in the surroundings can be maintained at a high spot. The accuracy of detection of a pollution leak point by soil gas survey, which is the method according to ( 12 ), can be significantly increased by this mechanism.
ところで、(2)に係る土壌汚染物質の対策方法によれば、すでに汚染が既知となっている場合においても、未知の場合と同様に、鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材と培養基材を、対象土地の飽和帯或いは不飽和帯に添加して、連通する立体導電網を地中に形成することにより、立体導電網に導通する鉄還元細菌を包含する微生物群集の汚染物質の代謝によって、更なる汚染の移動/拡散を防止しながら、既知汚染の浄化を図ることができる。 By the way, according to the method for controlling soil pollutants according to ( 2 ), even when the pollution is already known, as in the unknown case, it is a porous medium that mediates extracellular electron transfer of iron-reducing bacteria. A material containing at least part of a carbonaceous material and a culture substrate are added to a saturated zone or an unsaturated zone of the target land to form a communicating three-dimensional conductive network in the ground, thereby conducting the three-dimensional conductive network. Metabolism of contaminants in microbial communities, including iron-reducing bacteria, allows for purification of known contaminants while preventing further contamination migration/diffusion.
また更に、(5)に係る土壌汚染物質の対策方法によれば、多孔質な炭素系資材を、より好ましくは活性炭とすることで、汚染物質の吸着能をより高めることにより、より精度の高い汚染物質の移動/拡散抑制と土壌からの低溶出化を実現できる。 Furthermore, according to the method for controlling soil pollutants according to ( 5 ), the porous carbonaceous material is more preferably activated carbon to increase the adsorption ability of pollutants, resulting in higher accuracy. It is possible to suppress migration/diffusion of pollutants and reduce elution from soil.
ところで、汚染物質の取扱い履歴のある敷地において土壌汚染が既知であれば、この既知汚染は、浄化対策が叶うタイミングを見計らって優先的に浄化することが好ましい。
本発明であるところの(6)と(7)に示す土壌汚染物質の対策方法によれば、任意のタイミングにおいて、導電性資材として活性炭および鉄粉を選択し、更に必要に応じて過酸化物等を併せて活用することにより、安価で迅速なスポット浄化を効果的に実施することができる。
By the way, if soil contamination is known at a site where there is a history of handling pollutants, it is preferable to preferentially purify this known contamination in consideration of the timing at which purification measures are realized.
According to countermeasures soil contaminants in this invention is that where the (6) (7), at the timing of the arbitrary, selected activated carbon and iron powder as a conductive material, if necessary peroxidation It is possible to effectively carry out spot purification inexpensively and promptly by utilizing things and the like together.
また、(3)に係る土壌汚染物質の対策方法によれば、汚染物質の微生物代謝を司る微生物、および/或いは、前記鉄還元細菌を別途培養し、該土壌に添加することによって、本発明を展開する対象地における汚染の移動/拡散抑制や微生物分解を、より強化し確実に実施することができる。 In addition, according to the method for controlling soil pollutants according to ( 3 ), the present invention can be performed by separately culturing a microorganism that controls microbial metabolism of a pollutant and/or the iron-reducing bacterium and adding the soil-reducing bacteria to the soil. It is possible to further strengthen and surely carry out migration/diffusion control of pollution and microbial decomposition in the target area to be deployed.
ところで、(4)に係る土壌汚染物質の対策方法によれば、汚染物質の微生物代謝を司る微生物や鉄還元細菌の電子供与体、および/或いは、電子受容体を、浄化対象の土壌に不足なく添加することによって、本発明を展開する対象地における汚染の微生物分解や鉄還元細菌による移動/拡散抑制をより確実に実施することができる。 By the way, according to the method for controlling soil pollutants according to ( 4 ), the electron donors and/or electron acceptors of the microorganisms and iron-reducing bacteria that control the microbial metabolism of pollutants are not insufficient in the soil to be purified. By adding, it is possible to more surely carry out microbial decomposition of contamination in the target area to which the present invention is applied, and migration/diffusion suppression by iron-reducing bacteria.
また、(8)に係る土壌汚染物質の対策方法によれば、空気または酸素を含む気体を土壌に供給することによって、嫌気性の鉄還元細菌に対しては、電子受容体の酸化による賦活化を図り、一方、好気性を呈する鉄還元細菌や好気性微生物に対しては、電子受容体たる酸素の供給が図られることにより、このワンステップ操作をもって、土壌中の嫌気/好気の両領域における汚染物質の微生物分解を極めて効率的に促すことができる。 Further, according to the method for controlling soil pollutants according to ( 8 ), by supplying a gas containing air or oxygen to the soil, anaerobic iron-reducing bacteria are activated by oxidation of electron acceptors. On the other hand, oxygen is supplied as an electron acceptor to aerobic iron-reducing bacteria and aerobic microorganisms, and by this one-step operation, both anaerobic/aerobic regions in soil can be obtained. Microbial decomposition of pollutants can be very efficiently promoted.
例えば、ベンゼンは、嫌気性の鉄還元細菌によっても、好気性菌によっても生物学的分解が可能であるが、従来技術では、主として土壌を掘削してスタティックパイル等を形成して、パイル中央下部からの連続吸気による好気的分解により浄化が図られていた。
但し、この従来技術たるスタティックパイルを用いた純然たる好気的分解では、スタティックパイル内に均一に通気を実施することは、ほぼ不可能であり、酸素の供給は、一部の土壌間隙が通気道となり、局所的に実施されるに過ぎなかった。このため、連続通気によって、酸素供給と共に土壌の乾燥を図り、更に一定期間毎にパイルの切り返し作業を繰り返して実施して、乾燥状態にある土壌の団粒構造や土塊を更に砕くことにより、対象土壌に満遍なく酸素が行き渡る様な作業の併用が必須であった。
ところが、本発明であるところの連通する立体導電網を土壌中に形成することによって、鉄還元細菌にとっての電子受容体たる土壌中に存在する三価鉄を、余すところなく利用することができるので、好気的分解では必須であった、酸素たる電子受容体を満遍なく汚染土壌の隅々まで行き渡らせる為の切返し作業や連続吸気を大幅に減じた作業にて、ベンゼン汚染の浄化を図ることができる。
For example, benzene can be biodegraded by both anaerobic iron-reducing bacteria and aerobic bacteria, but in the prior art, soil is mainly excavated to form static piles, etc. Purification was achieved by aerobic decomposition by continuous inhalation from.
However, it is almost impossible to evenly ventilate the inside of the static pile by pure aerobic decomposition using this static pile, which is the conventional technique. It became a way and was only implemented locally. Therefore, continuous aeration is used to dry the soil with oxygen supply, and the pile cutting operation is repeated at regular intervals to further crush the aggregated structure and soil mass of the soil in a dry state. It was essential to combine the work so that oxygen was evenly distributed throughout the soil.
However, by forming a three-dimensional conductive network in the soil, which is the present invention, the ferric iron present in the soil, which is an electron acceptor for iron-reducing bacteria, can be fully utilized. , Which was essential for aerobic decomposition, can be used to purify benzene pollution by turning work to spread oxygen electron acceptors evenly throughout the contaminated soil and by greatly reducing continuous intake. it can.
この場合、重機を多用する切返や大型送気装置を用いた吸気(通気)は、鉄還元細菌の電子受容体たる三価鉄の多くが還元された場合に、最少回数で実施し、係る還元された鉄化合物の一部を酸素によって再酸化して、鉄還元細菌の電子受容体となる三価鉄の再生を図る程度に実施することで、低エネルギー且つ低コストを特徴とした浄化を実施できる。 In this case, the inversion (ventilation) using heavy-duty heavy-duty turning and a large air supply device is performed at the minimum number of times when most of the ferric iron, which is an electron acceptor of iron-reducing bacteria, is reduced. By reoxidizing a part of the reduced iron compound with oxygen to regenerate trivalent iron, which is an electron acceptor of iron-reducing bacteria, purification with low energy and low cost is performed. Can be implemented.
この様に、本発明であるところの立体導電網を適切に設置することにより、より多くの土壌中の三価鉄を電子受容体として活用できるので、通常の汚染濃度であり、一般的な三価鉄含有を有する土壌であれば、特段の切返や大型の送気装置を用いた吸気(通気)を行わずとも、初期の立体導電網設置の混合作業を含めた最少工数にて、汚染浄化を実施することができる。
理論上では、一般の土壌に含まれる三価鉄の含有量からすれば、最大で1g/kg濃度で存在するベンゼンの嫌気的代謝分解を満たす電子受容体量が存在する。これは、一般に見られるベンゼン汚染土壌の汚染濃度よりも遥かに高い濃度である。
As described above, by properly installing the three-dimensional conductive network of the present invention, more ferric iron in the soil can be utilized as an electron acceptor, which is a normal pollutant concentration, If the soil contains valent iron, it will be contaminated with minimum man-hours including mixing work in the initial installation of the three-dimensional conductive network without special turning back or intake (aeration) using a large air supply device. Purification can be carried out.
Theoretically, from the content of trivalent iron contained in general soil, there is an electron acceptor amount satisfying the anaerobic metabolic decomposition of benzene present at a maximum concentration of 1 g/kg. This is a much higher concentration than that found in benzene-contaminated soils commonly found.
ところで、上述する様な、酸素と三価鉄の両者が存在する環境においては、この両者を電子受容体として利用可能な一部の鉄還元細菌の増殖を特異的に促すことができる。
この一部の鉄還元細菌は、三価鉄を電子受容体として用いる場合には二価鉄と有機酸を生成し、一方、酸素を電子受容体として用いる場合には、過酸化水素を生成する性質が知られており、本発明であるところの(8)に係る土壌汚染物質の対策方法にて、空気または酸素を含む気体を対策対象の土壌に、一定間隔を持って供給することによって、二価鉄と有機酸と過酸化水素が同時に存在するタイミングを形成して、これら生成物を基材とする化学酸化機構たるフェントン反応により、更なる汚染物質の分解を促すことができる。
By the way, in the environment where both oxygen and trivalent iron are present as described above, it is possible to specifically promote the growth of some iron-reducing bacteria that can use both of them as electron acceptors.
Some of these iron-reducing bacteria produce ferric iron and organic acids when ferric iron is used as an electron acceptor, while hydrogen peroxide is produced when oxygen is used as an electron acceptor. In the method for controlling soil pollutants according to ( 8 ), which is known in nature and is the present invention, by supplying air or a gas containing oxygen to the soil to be countermeasured at regular intervals, By forming the timing when ferric iron, an organic acid and hydrogen peroxide are present at the same time, it is possible to promote the decomposition of further pollutants by the Fenton reaction which is a chemical oxidation mechanism based on these products.
また、(9)と(10)に示す土壌汚染物質の対策方法によれば、井戸様構造物、好ましくは、1本の管構造物で構成され、観測井戸機能と共に、該ストレーナ区間から、過酸化物溶液、および/或いは、気体を対策対象の土壌に注入する機能を有する井戸様構造物を用いて、過酸化物を、対策対象の土壌に、効果的に満遍なく添加することにより、前記鉄還元細菌の細胞外電子伝達を仲介する多孔質な炭素系資材を少なくとも一部に含む資材の付着性物質による機能低下の再生を可能とし、正常稼働を維持することができる。 Further, according to the countermeasures soil contaminants shown in (9) and (10), wells like structures, preferably, consists of one tube structure, with observation wells functions, from the strainer section, By using a well-like structure having a function of injecting a peroxide solution and/or a gas into the soil to be treated, the peroxide can be effectively and evenly added to the soil to be treated. the porous carbon-based materials that mediate extracellular electron transfer iron-reducing bacteria to allow regeneration of reduced function by adhesive substance of the material comprising at least a portion, it is possible to maintain the normal operation.
また更に、(7)と(9)と(10)に示す土壌汚染物質の対策方法において、過酸化物として、過硫酸化合物を利用することで、より良い汚染浄化・洗浄効果を得ることができる。 Furthermore, in the method for controlling soil pollutants shown in ( 7 ), ( 9 ) and ( 10 ), by using a persulfate compound as a peroxide, a better pollution purification/washing effect can be obtained. ..
ところで、平成21年の環境省告示により環境基準化が図られた1,4-ジオキサンは、一般には、生分解性が低いと評価されてきた有害物質であり、特にバイオ浄化対策方法に関する知見は未だ少ない状況にあった。
本発明であるところの(13)に示す土壌汚染物質の対策方法によれば、有害物質である1,4-ジオキサンに対し、鉄還元細菌を活用した「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」迄の、一貫した汚染対策を実施することができる。
By the way, 1,4-dioxane, which has been environmentally standardized by the Ministry of the Environment Notification in 2009, is a harmful substance that has generally been evaluated to have low biodegradability, and there are no particular findings regarding bio-purification measures. There were still few situations.
According to the method for controlling soil pollutants shown in ( 13 ), which is the present invention, it is possible to detect early detection of pollution leakage and transfer of leakage pollution by utilizing iron-reducing bacteria against 1,4-dioxane, which is a harmful substance. /Diffusion suppression (including: local low elution and pollution decomposition)" can be implemented.
本発明により、法定の第一種特定有害物質及びそれに類する有害物質による、既知、あるいは未知の土壌汚染に対し、導電性資材による立体導電網を活用して、鉄還元細菌が有する機能を応用したバイオプリベンション法(生物学的汚染予防法)とその付帯対策技術群による、「汚染漏洩の早期検知と漏洩汚染の移動/拡散抑制(含:局所的な低溶出化・汚染分解)」を一連で達成することができる。 According to the present invention, the known or unknown soil pollution by the statutory first class specific harmful substances and similar harmful substances is applied to the function of the iron-reducing bacteria by utilizing the three-dimensional conductive network of the conductive material. A series of "early detection of pollution leak and suppression of migration/diffusion of leak pollution (including local low elution and pollution decomposition)" by the bioprevention method (biological pollution prevention method) and its incidental countermeasure technology group Can be achieved with.
以下、本発明を代表する実施の基本形態について図1から図3の図面を用いて説明する。
特に本発明の本旨とするところは、導電性資材1により、連通する立体導電網2を地中に形成し、鉄還元細菌を包含する微生物群集3の代謝を、立体導電網2と生分解性を呈し有害物質を包含する汚染物質4が共存する範囲にて活性化することにより、漏洩汚染に対し、下記を要素とする一連の汚染対策を実施することにある。
Hereinafter, a basic embodiment representative of the present invention will be described with reference to the drawings of FIGS. 1 to 3.
In particular, the gist of the present invention is that the conductive material 1 forms a communicating steric conductive network 2 in the ground, and the metabolism of the microbial community 3 including iron-reducing bacteria is biodegradable with the steric conductive network 2. By activating the pollutant 4 including the toxic substance in a range where it coexists, a series of pollution countermeasures including the following elements are taken against leakage pollution.
(A)汚染漏洩地点の推定、好ましくは漏洩の早期検知。
(B)不溶性鉄化合物等の生成による汚染の移動/拡散抑制。
(C)有害物質の土壌からの低溶出化。
(D)鉄還元細菌を包含する微生物群集によるバイオプリベンション。
(E)アプローチの容易な既知汚染に対する導電性資材を活用したスポット浄化。
(A) Estimating the location of pollution leaks, preferably early detection of leaks.
(B) Suppression of migration/diffusion of contamination due to generation of insoluble iron compound or the like.
(C) Low elution of harmful substances from soil.
(D) Bioprevention by a microbial community including iron-reducing bacteria.
(E) Spot purification using a conductive material against known contamination that is easy to approach.
なお、地表17で漏洩した生分解性を呈し有害物質を包含する汚染物質4は、漏洩地点12から不飽和帯18へ、また不飽和帯18から更に飽和帯20に浸透する経過をたどるのが一般的であるが、飽和帯20に達した生分解性を呈し有害物質を包含する汚染物質4が、自然地下水流向に応じて流下し、広域汚染を引き起こすと、より深刻な問題となる。
本発明の本旨とするところの、立体導電網2は、地表17から不飽和帯18、更に飽和帯20に至る、いずれの土壌区分にも形成することが可能であるが、ここでは、より深刻な問題が懸念される飽和帯20での適用を例に挙げて、以下、係る実施の形態について述べる。
It should be noted that the pollutant 4, which leaks on the surface of the earth 17 and exhibits biodegradability and contains harmful substances, traces the process of penetrating from the leak point 12 to the unsaturated zone 18 and from the unsaturated zone 18 to the saturated zone 20. Generally, if the pollutant 4, which reaches the saturation zone 20 and exhibits biodegradability and contains harmful substances, flows down according to the natural groundwater flow direction and causes wide-area pollution, it becomes a more serious problem.
The three-dimensional conductive net 2, which is the gist of the present invention, can be formed in any soil section from the ground surface 17 to the unsaturated zone 18 and further to the saturated zone 20, but here, it is more serious. Such an embodiment will be described below by taking as an example the application in the saturation zone 20 where various problems are concerned.
さて、飽和帯20に存在する鉄還元細菌を包含する微生物群集3は、飽和帯嫌気的環境域において三価の鉄化合物であるゲータイトやフェリハイドライト等を構成物とする酸化的土壌粒子5に対し、直接ないし間接的に電子を付与し、二価鉄イオンやマグネタイト等の二価鉄を含む鉄化合物類を生成する呼吸を行う。 By the way, the microbial community 3 including the iron-reducing bacteria present in the saturated zone 20 becomes oxidative soil particles 5 composed of trivalent iron compounds such as goethite and ferrihydrite in the saturated zone anaerobic environment. On the other hand, by directly or indirectly imparting electrons, breathing is performed to generate iron compounds containing divalent iron such as divalent iron ions and magnetite.
ここに、鉄還元細菌を包含する微生物群集3と共に立体導電網2が存在すると、鉄還元細菌を包含する微生物群集3から立体導電網2に付与された電子は、立体導電網2に接する全ての酸化的土壌粒子5に対し電子を付与することが可能となり、呼吸源たる電子受容体として機能する酸化的土壌粒子5を潤沢に用いて、生分解性を呈し有害物質を包含する汚染物質4の浄化が図られ、更に、係る電子付与により還元的な不溶性鉄化合物11や二価鉄イオンを生成する。 If the steric conductive net 2 is present together with the microbial community 3 containing the iron-reducing bacteria, the electrons imparted to the steric conductive net 2 from the microbial community 3 containing the iron-reducing bacteria are all in contact with the steric conductive net 2. It becomes possible to donate electrons to the oxidative soil particles 5, and the oxidative soil particles 5 that function as an electron acceptor serving as a respiratory source are used in abundance, and thus pollutants 4 that are biodegradable and include harmful substances Purification is achieved, and further, by the electron donation, a reductive insoluble iron compound 11 and divalent iron ions are generated.
汚染の初期状態は、正に酸化的土壌粒子5で構成される土壌間隙に、生分解性を呈し有害物質を包含する汚染物質4が滲入した状況であり、この時点においては、酸化的土壌粒子5、生分解性を呈し有害物質を包含する汚染物質4、鉄還元細菌を包含する微生物群集3が、ほぼ同じ地点に存在し、この地点で不溶性鉄化合物11や二価鉄イオンを生成する。 The initial state of pollution is a situation in which the pollutant 4, which is biodegradable and contains harmful substances, has infiltrated into the soil gap that is exactly composed of the oxidative soil particles 5. At this point, the oxidative soil particles are 5. Pollutants 4, which are biodegradable and contain harmful substances, and microbial communities 3, which contain iron-reducing bacteria, exist at almost the same point, and insoluble iron compounds 11 and divalent iron ions are produced at this point.
一方、時間経過と共に、鉄還元細菌を包含する微生物群集3の汚染物質の代謝が進むと、汚染漏洩地点の酸化的土壌粒子5は、鉄還元細菌を包含する微生物群集3の呼吸源として使われると、還元的土壌粒子6に変化し、ついには、本地点での呼吸源が枯渇する。この時点から立体導電網2を介した、更に周囲の酸化的土壌粒子5への電子付与する呼吸が始まる。 On the other hand, when the metabolism of pollutants in the microbial community 3 including iron-reducing bacteria progresses over time, the oxidative soil particles 5 at the pollution leak point are used as a respiratory source for the microbial community 3 including iron-reducing bacteria. Then, it changes into reducing soil particles 6, and finally the respiratory source at this point is depleted. At this point, electron-releasing respiration starts via the three-dimensional conductive network 2 and to the surrounding oxidative soil particles 5.
この結果、不溶性鉄化合物11は、鉄還元細菌を包含する微生物群集3が生育する飽和帯嫌気的環境域7ではなく、周囲の飽和帯好気的環境域8との境界域にて生成・蓄積され、この集積の結果、土壌間隙の閉塞化が促される。また、併せて生じた二価鉄イオンに関しても、周囲の清浄表層地下水9に含まれる分子状酸素との反応から、三価の鉄化合物である不溶性鉄化合物11が生成され、鉄還元細菌を包含する微生物群集3の増殖した菌体も相まって、これら不溶性の粒子群によって土壌間隙の閉塞化が促される。 As a result, the insoluble iron compound 11 is produced and accumulated in the boundary area with the surrounding saturated zone aerobic environment area 8 instead of the saturated zone anaerobic environment area 7 where the microbial community 3 including iron-reducing bacteria grows. As a result of this accumulation, the closure of the soil gap is promoted. In addition, regarding the divalent iron ions generated together, the insoluble iron compound 11 that is a trivalent iron compound is produced from the reaction with the molecular oxygen contained in the surrounding clean surface groundwater 9, and the iron-reducing bacteria are included. The insoluble particle group promotes the clogging of the soil gap in combination with the bacterial cells of the microbial community 3 that grow.
ところで、環境省「平成20年度土壌汚染対策法の施行状況及び土壌汚染調査・対策事例等に関する調査結果」によれば、一般に、土壌汚染は、配管の破損や不適切な取扱いの様な一過性のトラブルによって生じる場合が多く、排水の地下浸透等、連続・継続的な漏洩事例の割合は少ないことが示されている。 By the way, according to the Ministry of the Environment "Survey of the Soil Contamination Countermeasures Act of 2008 and the results of surveys on soil pollution surveys and cases of countermeasures," soil pollution is generally a cause of temporary damage such as pipe damage or improper handling. It has been shown that it is often caused by sexual problems, and the proportion of continuous and continuous leakage cases such as infiltration of drainage underground is low.
このように、一過性のトラブルが、ブラウンフィールド化が懸念される様な重篤な汚染へと進行する一つの原因として、従来技術においては、未然に防止できなかった係る一過性の汚染に対し、適切な早期検知、移動/拡散抑制を図る技術が存在しなかったことが原因として挙げられる。
結果、一過性の僅かな汚染漏洩であっても、見過ごされ汚染が拡大すれば、放置された時間経過によっては、上述した様に想像もつかない様な対策費が掛かる、重篤な汚染へと進行してしまう。
したがって、一過性の個々の少量規模の漏洩トラブルに対し、いかに早期に検知し、移動/拡散抑制を施すかが、汚染の重篤化を防止する、即ちブラウンフィールド化を防止する上で重要となる。
As described above, as one of the causes for the temporary trouble to progress to the serious pollution in which the brown field is feared, in the conventional technology, the temporary pollution that cannot be prevented in advance. On the other hand, there is no suitable technology for early detection and movement/diffusion suppression.
As a result, even if a temporary leak of a small amount of pollution occurs, if it is overlooked and the pollution spreads, depending on the elapsed time, the cost of countermeasures that cannot be imagined as described above will be applied to serious pollution. And it progresses.
Therefore, it is important to detect how quickly a temporary small-scale leakage problem occurs and to control the movement/diffusion to prevent serious pollution, that is, to prevent brownfield. Becomes
本発明によるところの、漏洩汚染に対する早期検知は、係る生分解性を呈し有害物質を包含する汚染物質4の漏洩を契機として、鉄還元細菌を包含する微生物群集3の代謝が活発化して生じる、大量の二酸化炭素ガス13を指標として(A)汚染漏洩地点の推定を実施するものである。 The early detection of leakage pollution according to the present invention is caused by activation of metabolism of the microbial community 3 including iron-reducing bacteria, triggered by the leakage of the pollutant 4 which is biodegradable and includes harmful substances. The large amount of carbon dioxide gas 13 is used as an index to estimate (A) the pollution leakage point.
例えば、ベンゼン原液0.1L程度が地中に漏洩し、鉄還元細菌を包含する微生物群集3によって、完全に二酸化炭素ガス13まで分解されたと仮定すれば、1モルのベンゼンから最大6モルの二酸化炭素を生じるので、概ね100Lを超える二酸化炭素ガス13が生成する。
そして、表層地中ガスの二酸化炭素は、大気圧変化によって生じる大気とのガス交換によって、漏洩地点12の周囲を最大濃度として、濃度分布を生じながら、次第に周囲に拡散する。
For example, assuming that about 0.1 L of benzene stock solution leaked into the ground and was completely decomposed to carbon dioxide gas 13 by the microbial community 3 including iron-reducing bacteria, 1 mol of benzene up to 6 mol of dioxide. Since carbon is generated, the carbon dioxide gas 13 generally exceeds 100 L.
Then, the carbon dioxide of the surface underground gas gradually diffuses to the surroundings while generating a concentration distribution with the maximum concentration around the leakage point 12 by gas exchange with the atmosphere caused by the atmospheric pressure change.
この希釈拡散された二酸化炭素ガス13を、例えば10ppmオーダー程度で精度良く測定するとすれば、最大で数百倍希釈、即ち元の生成二酸化炭素体積の数百倍の体積である数十立米の地中ガスに希釈された場合においても、大気中濃度レベルからしても十分な有意差を持った、ダイナミックレンジの広い地中ガス中の二酸化炭素ガス濃度分布14を生じる。 If this diluted and diffused carbon dioxide gas 13 is to be accurately measured, for example, on the order of 10 ppm, it will be diluted several hundred times at the maximum, that is, several tens of cubic meters of ground, which is several hundred times the volume of the original carbon dioxide produced. Even when diluted with medium gas, a carbon dioxide concentration distribution 14 in the underground gas having a wide dynamic range and having a significant difference from the atmospheric concentration level is generated.
この二酸化炭素ガス濃度分布14の形成原理から、大気中濃度レベルとは有意差を持つ二酸化炭素ガス濃度地点を検出し、この地点を起点として、更により濃度の高い地点を更にメッシュを狭めて体系的に追求して漏洩地点12を追求する。 From the principle of formation of this carbon dioxide gas concentration distribution 14, a carbon dioxide gas concentration point having a significant difference from the atmospheric concentration level is detected, and from this point, the point with a higher concentration is further narrowed to a system In pursuit of the leakage point 12.
以下、本発明を代表する実地の表層土壌ガス調査について図2を用いて説明する。 Hereinafter, the actual surface soil gas survey representing the present invention will be described with reference to FIG.
具体的には、対象地を、調査メッシュ15で分割して調査地点16を地表17に設定し、不飽和帯18に1m深度程度の採取孔19を作成後、地中ガスを採取し、地中ガス中の二酸化炭素ガス13の濃度を測定して、メッシュ上における二酸化炭素ガス濃度分布14から、基本メッシュにおいて相対的に濃度の高い濃度地点を抽出すると共に各地点のガス濃度から、対象メッシュ上における二酸化炭素ガス濃度分布14を明らかにする。なお、飽和帯20が浅層に存在し、所定深度の採取孔19を設置できない場合は、より浅い深度に採取孔19を設置して、地中ガスを採取する。 Specifically, the target site is divided by the survey mesh 15, the survey point 16 is set on the ground surface 17, the sampling hole 19 having a depth of about 1 m is created in the unsaturated zone 18, and the underground gas is sampled. The concentration of the carbon dioxide gas 13 in the medium gas is measured, and the concentration points of relatively high concentration in the basic mesh are extracted from the carbon dioxide gas concentration distribution 14 on the mesh, and the target mesh is determined from the gas concentration of each point. The carbon dioxide gas concentration distribution 14 above is clarified. In addition, when the saturation zone 20 exists in a shallow layer and the sampling hole 19 of a predetermined depth cannot be installed, the sampling hole 19 is installed in a shallower depth, and underground gas is sampled.
次に、調査メッシュ15上でのガス濃度分布に応じて、特に最大濃度地点周辺のメッシュ幅を、更に、1/2(図中のX1地点)、1/4(図中のY1地点とY2地点)と、順次狭めて、更なる最高二酸化炭素濃度の検出地点を追求し、絞込んで、漏洩地点12を推定する。 Next, according to the gas concentration distribution on the survey mesh 15, the mesh width around the maximum concentration point is further divided into ½ (X1 point in the figure) and ¼ (Y1 point and Y2 in the figure). Point)), and the detection point of the highest maximum carbon dioxide concentration is further pursued and narrowed down to estimate the leakage point 12.
ここで、より具体的なところでは、本発明であるところの二酸化炭素ガス13を用いた表層土壌ガス調査では、経験的に8mメッシュを基本メッシュとして用いる。このように、初期メッシュを8mで設定すると、8→4→2→1mと、3段階にメッシュを絞込んでも、以後の地点出しにおけるメジャーの目盛をm単位の整数値で簡便に設定できるので、この様なメッシュ設定を心掛けて調査の効率化を図る。
また、生分解性を呈し有害物質を包含する汚染物質4の使用や漏洩が、ほぼ無いと想定されるエリアに関しては、8mの倍数である16mや32mを採用しても良い。
Here, more specifically, in the surface soil gas investigation using the carbon dioxide gas 13 according to the present invention, an 8 m mesh is empirically used as the basic mesh. In this way, if the initial mesh is set to 8 m, even if the mesh is narrowed down to 3 levels of 8 → 4 → 2 → 1 m, the scale of the measure at the subsequent spotting can be easily set with an integer value of m unit. , Make the mesh setting like this to improve the efficiency of the survey.
Further, for areas where it is assumed that the pollutant 4 exhibiting biodegradability and containing harmful substances is hardly used or leaked, 16 m or 32 m, which is a multiple of 8 m, may be adopted.
なお、本発明であるところの表層ガス調査時の、地面への削孔作業、ガス試料の採取作業等は、上述した土壌汚染対策法での土壌ガス調査(環境省告示第16号調査)の方法に準じたガス調査機材(削孔機、ガス採取管、採取バッグ等)にて、代用することが可能である。 In the surface gas investigation, which is the present invention, the drilling work on the ground, the sampling work of the gas sample, etc. are the same as those of the soil gas investigation (the Ministry of the Environment Notification No. 16 investigation) under the above-mentioned soil pollution control method. It is possible to substitute gas survey equipment (drilling machine, gas sampling pipe, sampling bag, etc.) according to the method.
なお、係る表層ガス調査の際、二酸化炭素ガス濃度のみならず、ベンゼンの様に揮発性がある漏洩物質であれば、ベンゼンをターゲットとした、ベンゼンガス検知管、PID検出器、FID検出器、IR吸光検出器等を用いて、地中のベンゼンガス濃度を二酸化炭素ガス濃度と共に測定しても良い。 In the surface gas investigation, not only the carbon dioxide gas concentration but also a benzene-like leaking substance such as benzene can be targeted with benzene gas detector tubes, PID detectors, FID detectors, The benzene gas concentration in the ground may be measured together with the carbon dioxide gas concentration using an IR absorption detector or the like.
但し、揮発したベンゼンガスは、地中ガスとして、上述した二酸化炭素ガスと同様の挙動で希釈拡散が図られるが、ベンゼンガスの理論上での最大発生量は、上記の二酸化炭素発生量の1/6程度でしかない。また、ベンゼンガスは、その希釈拡散過程において、土壌微生物によって容易に分解され二酸化炭素ガスに変換され消失してしまう可能性が高い事に留意する。 However, the volatilized benzene gas dilutes and diffuses as underground gas in the same behavior as the carbon dioxide gas described above, but the theoretical maximum generation amount of benzene gas is 1% of the above carbon dioxide generation amount. Only about /6. It should be noted that benzene gas is likely to be easily decomposed by soil microorganisms to be converted to carbon dioxide gas and disappear during the dilution and diffusion process.
経験的には、二酸化炭素ガスの水平分布は、揮発性汚染物質ガスの水平分布より、明らかに広く分布する傾向にあり、実際、揮発性汚染物質ガスは、漏洩地点12の極近傍でないと検出されない場合が多い。従って、揮発性汚染物質ガスを併用した測定は、メッシュを絞り込む段階から始め、総じて効率の良い調査を実施する。
また、揮発性汚染物質のガス濃度測定の目的を、漏洩地点12の確定のクロスチェックと位置付けると、二酸化炭素ガス調査結果を検証する上での有意義な測定となる。二酸化炭素ガス調査は精度が高いので、汚染物質以外の有機物の分解によって生じた非汚染物質由来の二酸化炭素ガスを検出する場合もあり、係るクロスチェックは、特定の有害物質汚染の漏洩地点の確定には、重要な操作となる。
Empirically, the horizontal distribution of carbon dioxide gas tends to be clearly wider than the horizontal distribution of volatile pollutant gas, and in fact, it is detected that the volatile pollutant gas is not in the immediate vicinity of the leakage point 12. It is often not done. Therefore, the measurement using volatile pollutant gas together starts with the step of narrowing down the mesh, and generally conducts an efficient survey.
Further, if the purpose of measuring the gas concentration of volatile pollutants is positioned as a cross-check for confirming the leakage point 12, it will be a meaningful measurement for verifying the carbon dioxide gas survey results. Since the carbon dioxide gas survey is highly accurate, carbon dioxide gas derived from non-pollutants generated by the decomposition of organic substances other than pollutants may be detected. Is an important operation.
上述から明らかな様に、測定対象として二酸化炭素ガス13の選択、調査メッシュ15の精度、漏洩地点12の絞り込み作業の実施という点において、或いは、導電性資材1で構成される立体導電網2での鉄還元細菌を包含する微生物群集3の代謝活用、また代謝産物による土壌間隙閉塞を促し漏洩汚染の高濃度維持を図るという点において、本発明によるところの表層ガス調査は、公定調査たるフェーズ2土壌ガス調査(環境省告示第16号調査)や従来の表層ガス調査方法等とは大きく異なる。 As is clear from the above, in terms of selection of the carbon dioxide gas 13 as the measurement target, accuracy of the investigation mesh 15, implementation of the work of narrowing down the leakage point 12, or by using the three-dimensional conductive net 2 composed of the conductive material 1. In terms of the metabolic utilization of the microbial community 3 including the iron-reducing bacteria of the present invention, and the aim of maintaining the high concentration of leakage pollution by promoting the soil gap clogging by the metabolites, the surface gas investigation according to the present invention is the official investigation Phase 2 It is significantly different from the soil gas survey (Ministry of the Environment Notification No. 16 survey) and conventional surface gas survey methods.
本発明であるところの表層ガス調査法は、生分解性を呈し有害物質を包含する汚染物質4における漏洩汚染の検知、漏洩汚染地点の推定等、一連の汚染機構の推定を精度高く実施することに主眼が置かれた調査方法と位置付けられる。
また、本法は、公定のフェーズ2の土壌ガス調査よりも高精度にて、生分解性を呈し有害物質を包含する汚染物質4の存在と漏洩地点の検知が可能である特徴を有する。後述する様な、公定のフェーズ2の土壌ガス調査対策に向けた事前基本情報として活用する他、以降のあらゆる汚染対策の設計に有効に活用することが好ましい。
The surface gas investigation method which is the present invention is to carry out highly accurate estimation of a series of pollution mechanisms, such as detection of leakage pollution in pollutant 4 which is biodegradable and includes harmful substances, and estimation of leakage pollution points. It is positioned as a survey method with a focus on.
In addition, this method has a feature that it is possible to detect the presence of the pollutant 4 that exhibits biodegradability and includes harmful substances and the leakage point with higher accuracy than the official phase 2 soil gas survey. It is preferable to use it as the basic information for the official phase 2 soil gas survey countermeasures, which will be described later, and to effectively use it for the design of all subsequent pollution countermeasures.
以下、第一種特定有害物質を取り扱う工場・事業所等の操業中の段階から計画的に一連の土壌汚染対策に取り組むための、本発明を代表する実施の形態について説明する。 Hereinafter, an embodiment representative of the present invention for systematically addressing a series of soil pollution countermeasures from the stage of operation of factories, business establishments, etc. that handle first-class specified hazardous substances will be described.
後述する様に、第一種特定有害物質等の有害物質を取り扱う工場・事業所を廃止する場合や、工事等で敷地の範囲が変わったり、土を掘り返したりする場合等、土壌汚染対策法で規定される要件を満たす場合は、同法に規定される所定の調査が必須となる。
係る調査での、フェーズ2土壌ガス調査にて、「定量下限値以上の濃度検出」地点が存在すれば、以後、フェーズ3のボーリング調査による汚染の存在確定、更に汚染レベルに応じた汚染区域指定を経て、区域解除を目的とした浄化対策という一連を実施する義務を負い、行政指導下にて、数百万〜数億円規模の浄化対策費、手間、時間を要する事業的負担を要求されかねないレールが、所定の手順や監督署の指導に従って、敷かれることとなる。
As will be described later, the Soil Contamination Countermeasures Act is used when factories and business establishments that handle hazardous substances such as Class I Specified Hazardous Substances are abolished, when the site area changes due to construction, and when the soil is dug up. If the prescribed requirements are met, the prescribed investigation prescribed in the law is mandatory.
If there is a point of "concentration detection above the lower limit of quantification" in the Phase 2 soil gas survey, the presence of contamination is confirmed by the boring survey in Phase 3 and the contaminated area is designated according to the contamination level. After that, it is obliged to implement a series of purification measures for the purpose of removing the area, and under the administrative guidance, purification measures costs of several million to several hundred million yen, labor and time-consuming business burden are required. The possible rails will be laid according to the prescribed procedure and the guidance of the supervision office.
まずは、係るフェーズ2土壌ガス調査をクリアーすることを念頭に、本発明であるところの(A)〜(D)の汚染物質の対策方法をもって、操業中の段階から計画的に土壌汚染対策に取り組み、土壌汚染の早期発見、早期対策の見地に立った一連の汚染対策を執り行うことが好ましい。 First of all, in consideration of clearing the Phase 2 soil gas survey, the method of countermeasures for pollutants (A) to (D) according to the present invention is used to systematically tackle soil pollution countermeasures from the stage of operation. It is preferable to take a series of pollution countermeasures from the viewpoint of early detection of soil pollution and early countermeasures.
ところで、最も好ましい本発明であるところの汚染対策の運用方法は、第一種特定有害物質の取扱いが、今後に予定される敷地に対し、汚染が未然な更地の状態から、汚染対策をスタートすることである。 By the way, the most preferable method of operating the pollution control according to the present invention is to start the pollution control from the state of vacant land where the handling of Class I specified hazardous substances is planned for the future. It is to be.
具体的には、第一種特定有害物質の取扱いが予定される敷地の表層土壌に対し、地盤改良を施すがごとく、バックホウ、パワーブレンダー、トレンチャー型スタビライザー、汎用スタビライザー等の重機を用いて効率良く地中に導電性資材や培養基材を表層土壌に混合し、連通する立体導電網を、表層土壌中に形成する。 Specifically, the soil on the surface of the site where the Class 1 Specified Hazardous Substances are scheduled to be handled is improved efficiently by using heavy equipment such as backhoes, power blenders, trencher type stabilizers, general-purpose stabilizers, etc. An electrically conductive material and a culture substrate are mixed in the surface soil to form a three-dimensional conductive network that communicates with the surface soil.
なお、この様に、広い敷地に対し導電性資材を添加する場合は、特に黒色の強い海砂等、多量に導電性のマグネタイト(砂鉄)等を含む安価な土木資材を用いて、価格を抑えた立体導電網の施工となる様に心掛ける。 In addition, when adding conductive materials to a large site in this way, use inexpensive civil engineering materials that contain a large amount of conductive magnetite (sand iron), such as sea sand, which has a strong black color, to reduce the price. Make sure that the three-dimensional conductive net is installed.
その後は、定期的に上述した表層ガス調査を実施して、土壌ガスに有意に大気レベルを超える二酸化炭素ガスや汚染ガスが検知された場合を契機として、漏洩対策をリアルタイムで実施する。
また、係る表層ガス測定地点が建屋内に存在する、或いは舗装や被覆面に存在する場合は、ガソリンスタンドの地中タンク周囲に設置されている様な漏洩検知孔のごとくのガス採取孔を常設し、以後は、都度の穿孔作業無しの土壌ガス採取と分析のみを実施する、効率の良い定期的表層ガス調査を実施することが好ましい。
After that, the above-mentioned surface gas survey will be carried out regularly, and the leakage countermeasure will be carried out in real time when the carbon dioxide gas or the pollutant gas significantly exceeding the atmospheric level is detected in the soil gas.
If the surface gas measurement point exists in the building, or on the pavement or covered surface, a gas sampling hole such as a leak detection hole installed around the underground tank of the gas station is permanently installed. However, after that, it is preferable to carry out an efficient periodical surface gas survey, in which only soil gas sampling and analysis are performed without drilling work each time.
ところで、既に、建屋が存在し、有害物質等の取扱いが始まっている場合は、まず、地表面に導電性資材と共に培養基材を含む水溶液を地表面に散布した後、一定時間を経過した後に、本発明であるところの表層ガス調査を実施する。
第一種特定有害物質を取扱いが始まっており、既に漏洩汚染が発生している可能性が高い状況において、導電性資材の大規模な添加施工を実施して現場の土壌ガスを大きく撹乱してしまうと、本来の調査目的たる漏洩地点情報を失してしまいかねないので、ここでの施工優先順位には、注意を要する。
By the way, if the building already exists and the handling of harmful substances etc. has begun, first, after spraying the aqueous solution containing the culture base material with the conductive material on the ground surface, after a certain time has elapsed The surface gas investigation, which is the present invention, is carried out.
In the situation where the handling of Class I specified harmful substances has started and there is a high possibility that leakage pollution has already occurred, large-scale addition of conductive materials will be carried out to greatly disturb the soil gas at the site. If this happens, the leak point information, which is the original purpose of the investigation, may be lost, so caution should be exercised in the construction priority here.
係る表層ガス調査にて、汚染漏洩の存在が否定されるエリアであれば、自走式ボーリングマシンや打撃式簡易機械ボーリングマシンを活用して、導電性資材を分散状態で含む水溶液等を、当該敷地の飽和帯或いは不飽和帯の間隙を通じて土壌に注入して、連通する立体導電網を地中の広範囲に形成しても良いし、粒子状の導電性資材等をバックホウ、パワーブレンダー、トレンチャー型スタビライザー、汎用スタビライザー等の重機を用いて土壌と混合し、連通する立体導電網を、表層土壌中に形成しても良い。施工場所の状況に応じて導電資材等と施工機器を選択し、適切な立体導電網の設置を図る。 In the area where the presence of pollution leakage is denied in the surface gas survey, a self-propelled boring machine or a percussion-type simple mechanical boring machine is used to remove an aqueous solution containing conductive materials in a dispersed state. It may be injected into the soil through the gap between the saturated zone and the unsaturated zone of the site to form a three-dimensional conductive network that communicates with the soil over a wide area in the ground, or particulate conductive material etc. may be used as a backhoe, power blender, or trencher type. It is also possible to use a heavy machine such as a stabilizer or a general-purpose stabilizer to mix with the soil to form a three-dimensional conductive network that communicates with the soil in the surface soil. Select conductive materials and construction equipment according to the situation of the construction site, and install an appropriate three-dimensional conductive net.
最後に、既に汚染漏洩の存在が認知されるエリアであれば、まず、(E)アプローチの容易な既知汚染に対する導電性資材を活用したスポット浄化を積極的に図ることが好ましい。
一方、現状ではアプローチが困難な汚染に対しては、その周囲の土壌に対し、本発明であるところの、活性炭や多孔質黒鉛等の低溶出型導電性資材他を、上記の要領で土壌に添加し、鉄還元細菌を包含する微生物群集の代謝を活性化して、(B)不溶性鉄化合物等の生成による汚染の移動/拡散抑制、(C)有害物質の土壌からの低溶出化、(D)鉄還元細菌を包含する微生物群集によるバイオプリベンションを図る。
係る施工後は、定期的な表層ガス調査を実施して、更なる漏洩汚染の早期検知と早期対策を図ると共に、浄化施工を施したエリアに関しては、浄化経過を、ガス調査を通じて経過観察する。
Finally, in an area where the presence of contamination leakage has already been recognized, it is preferable to first actively perform spot purification using an electrically conductive material against known contamination that is easy to approach (E).
On the other hand, for pollution that is difficult to approach at present, for the soil around it, low elution type conductive material etc. such as activated carbon or porous graphite, which is the present invention, is applied to the soil in the above manner. (B) Suppression of migration/diffusion of pollution due to generation of insoluble iron compounds, etc., (C) Low elution of harmful substances from soil, (D) ) Bio-prevention by a microbial community including iron-reducing bacteria.
After such construction, regular surface gas surveys will be conducted to further detect early leakage pollution and early countermeasures, and in the areas where purification construction has been carried out, the purification progress will be observed through gas surveys.
なお、第一種特定有害物質等の揮発性有機化合物を含む汚染である場合、汚染中心部の高濃度領域は、切削油やグリース等を伴う汚染である場合が多い。油分の多い汚染中心部の汚染に対しては、多孔質黒鉛を主体とした油汚染を考慮した施工を、また、飽和帯にて地下水流によって流下し、主として有害物質のみとなった汚染に対しては活性炭を主体とした施工を行うなど、汚染状態に応じた、最適な汚染吸着能を有する多孔質な炭素系導電性材料を選択する。 In the case of pollution containing a volatile organic compound such as a first-class specified harmful substance, the high-concentration region at the central part of the pollution is often accompanied by cutting oil, grease, or the like. For the pollution of the central part with a large amount of oil content, the construction considering the oil pollution mainly consisting of porous graphite, and the pollution mainly flowing only the harmful substances that flowed down by the groundwater flow in the saturated zone For example, select a porous carbon-based conductive material that has the optimum adsorption capacity for pollutants depending on the polluted state, such as performing construction mainly on activated carbon.
なお、これらの選定やブレンド比率等に関しては、あらかじめラボ等での事前試験等を行う必要があり、また現地施工時においても、定期的な確認を実施して、より確実な施工となるように心掛ける。 Regarding the selection and blending ratio of these, it is necessary to carry out a preliminary test in a laboratory in advance.Also, at the time of on-site construction, conduct regular checks to ensure more reliable construction. aim to do.
また、有害物質の種類に応じて、鉄還元細菌を包含する微生物群集による分解が最適となる様に、添加する肥料資材、電子供与体、電子受容体等の調整を実施する。例えば、有害物質が有機塩素系のテトラクロロエチレンならば、鉄還元細菌を包含する微生物群集による分解は、呼吸と共役する脱塩素反応により進行し、それぞれの相対的な濃度によっては、三価鉄の還元反応と競合する可能性もある。ラボの事前検討によってこの様な現象が見られた場合は、鉄還元細菌を包含する微生物群集における、鉄還元細菌以外の微生物による脱塩素化反応も併せて考慮し、応じた電子供与体や分解菌等の添加を検討する。 In addition, fertilizer materials, electron donors, electron acceptors, etc. to be added are adjusted so that decomposition by a microbial community including iron-reducing bacteria is optimal depending on the type of harmful substance. For example, if the harmful substance is an organochlorine tetrachloroethylene, decomposition by a microbial community including iron-reducing bacteria will proceed by a dechlorination reaction coupled with respiration, and depending on the relative concentration of each, reduction of trivalent iron will occur. There is also the possibility of competing with the reaction. If such a phenomenon is observed in the laboratory, the dechlorination reaction by microorganisms other than iron-reducing bacteria in the microbial community including iron-reducing bacteria should also be considered, and appropriate electron donors and decomposition Consider adding bacteria.
ところで、既に有害物質の取扱いや管理を終了した、或いは終了を予定する敷地である場合も、汚染の恐れが高い状況と判断し、上記と同様の考え方で対策に臨む。 By the way, even in the case of a site where the handling or management of harmful substances has already been completed or is scheduled to be completed, it is judged that there is a high risk of contamination, and countermeasures will be taken in the same way as above.
これら一連を、係る事業が終了した後に実施される、公定調査たるフェーズ2調査をクリアーするための対策として実施する。 This series will be implemented as a measure to clear the Phase 2 study, which is an official study that will be implemented after the project is completed.
なお、係るフェーズ2土壌ガス調査にて、所定の基準値を超えなければ、そこで公定調査たる汚染区域判定は終了し、土地利用、売買等に関し、汚染が無き土地とほぼ同等の活用が可能となる。 In addition, if the specified standard value is not exceeded in the Phase 2 soil gas survey, the polluted area judgment, which is the official survey, will be completed, and it will be possible to use land in the same way as land without pollution regarding land use and sale. Become.
一方、このフェーズ2土壌ガス調査にて「定量下限値以上の濃度検出」とスクリーニングされた地点が存在し、その後のフェーズ3調査での汚染確定を経て、汚染区域として「要措置区域」或いは「形質変更時要届出区域」が指定された場合は、この一連の区域解除を目的とした更なる浄化対策を実施する。 On the other hand, there are points that were screened as "detection of concentration above the lower limit of quantitation" in this Phase 2 soil gas survey, and after the contamination was confirmed in the Phase 3 survey, the "measured area" or If the “Notification Required Area for Character Change” is designated, further purification measures will be implemented with the aim of releasing this series of areas.
具体的には、本発明であるところの、(B)不溶性鉄化合物等の生成による汚染の移動/拡散抑制、(C)有害物質の土壌からの低溶出化、(D)鉄還元細菌を包含する微生物群集によるバイオプリベンションを継続し、また必要に応じて(E)アプローチの容易な既知汚染に対する導電性資材を活用したスポット浄化を実施して、まずは、汚染区域指定区分である、「要措置区域」から「形質変更時要届出区域」への変更、続いて、「形質変更時要届出区域」の解除といった順次の区域解除を目標とする浄化対策を図ることが好ましい。 Specifically, the present invention includes (B) suppression of migration/diffusion of pollution due to generation of insoluble iron compounds, (C) low elution of harmful substances from soil, and (D) iron-reducing bacteria. Continuation of bioprevention by microbial communities that carry out, and (E) if necessary, spot purification using electrically conductive materials against known contamination with an easy approach is carried out. It is preferable to take purification measures aiming at the sequential removal of areas, such as changing from the "measure area" to the "notification area required for changing traits", and then releasing the "notification area requiring notification when changing traits".
なお、土壌汚染対策法での各種調査にて、汚染区画が明確に示されている場合において、本発明であるところの(A)汚染漏洩地点の推定が実施されていない場合は、汚染漏洩地点を確認するために、本発明に準じた表層土壌ガス調査を実施し、係る汚染漏洩地点を必ず浄化対象に含める様にする。 In addition, when various surveys under the Soil Contamination Countermeasures Law clearly indicate the contaminated section, if the (A) pollution leakage point of the present invention is not estimated, the pollution leakage point is In order to confirm the above, a surface soil gas survey according to the present invention is carried out, and the pollution leak point is always included in the purification target.
現行の土壌汚染対策法施行後の浄化対策では、施工事業者によっては、汚染漏洩地点を確認せずに、フェーズ2土壌ガス調査結果とフェーズ3のボーリング調査結果に基づいて、汚染漏洩地点の把握か省みられることなく浄化対策が計画・実施される場合も少なく無い。
結果、公定調査結果で確定された汚染地点範囲の浄化が完了し、しばらく経った後に、同地点で再度汚染が検出され、施工不良が問われる係争事例も発生している。
汚染は、原因があって結果を生じるものであり、汚染機構を判じ得ない別観点での汚染調査結果だけを見て対処し、原因を究明しなかった場合に起こり得る、典型的な浄化施工業者の過失事例である。現時点における土壌汚染対策法の調査は、敷地に対する汚染の有無を調査する目的で実施される調査であり、汚染機構を明確に反映する調査ではないことに留意する。
漏洩地点が明確ではない場合は、本発明であるところの(A)汚染漏洩地点の推定を実施、又は応用し、汚染機構を明確とした、確度の高い浄化対策を実施する。
In the purification measures after the enforcement of the current Soil Contamination Countermeasures Act, some construction companies do not confirm the pollution leak point, but grasp the pollution leak point based on the Phase 2 soil gas survey result and the Phase 3 boring survey result. There are many cases where purification measures are planned and implemented without being omitted.
As a result, after the purification of the polluted point area confirmed by the official survey results was completed, and after a while, pollution was detected again at the same point, and there are also disputed cases where construction defects are asked.
Contamination has a cause and produces a result, and it is a typical purification that can occur if the cause is not determined, by dealing with it only by looking at the result of the contamination investigation from another viewpoint where the contamination mechanism cannot be understood. This is a negligent case of a contractor. It should be noted that the survey on the Soil Contamination Countermeasures Law at this time is a survey conducted for the purpose of investigating the presence or absence of pollution on the site and does not clearly reflect the pollution mechanism.
If the leak point is not clear, the (A) pollution leak point, which is the present invention, is estimated or applied to implement a highly accurate purification measure with a clear pollution mechanism.
なお、このように既に汚染の存在が明確である状況では、土壌に添加する導電性資材として、多孔質黒鉛等、特に多孔質な炭素系の導電性資材を用いて、立体導電網の構築によって生じる不溶性鉄化合物の生成による汚染の移動/拡散抑制作用と共に、多孔質な炭素系資材が有する物質吸着能により、更なる汚染の土壌からの低溶出化を図る様に心掛ける。施工方法も上述のごとく、施工場所や汚染状況に応じて、適切な方法を選択する。 In addition, in such a situation that the presence of contamination is already clear, as a conductive material to be added to the soil, by using a porous carbon-based conductive material, such as porous graphite, by constructing a three-dimensional conductive network. In addition to the effect of suppressing the migration/diffusion of pollution due to the formation of the insoluble iron compound that occurs, the substance adsorption capacity of the porous carbonaceous material is taken into consideration to further reduce the pollution from soil. As for the construction method, as described above, an appropriate method is selected according to the construction site and the pollution situation.
特に対象地が「要措置区域」を指定された場合は、所定の溶出基準を満たす経口摂取経路の遮断措置が求められ、行政対応としては、係る汚染地下水の飲用・利用の制限を実施するのが一般的であり、一方、事業サイドとしては、係る汚染の移動/拡散抑制と第二溶出基準を満たす土壌からの低溶出化と共に浄化を図る対策を、本発明によるところの対策方法にて確度高く実施し、まずは「要措置区域」から「形質変更時要届出区域」への早急なる区分変更が図られる様に努める。 In particular, if the target area is designated as a "required measure area", it is required to take measures to block the ingestion route that meets the prescribed elution criteria, and the administrative response is to restrict drinking and use of the contaminated groundwater. On the other hand, on the business side, on the other hand, the measures to prevent the migration/diffusion of such pollution and to reduce the amount of soil from the soil satisfying the second elution standard and to purify the same can be achieved with the accuracy of the countermeasure method according to the present invention. We will implement it at a high cost, and first try to quickly change the category from the "measure area" to the "notification area required for changing traits".
この「要措置区域」から「形質変更時要届出区域」への区分変更によって、当該区域への人の立ち入りや、建屋の建設等の形質変更に対する規制要件が、大幅に減免され、実質的な商業的生産活動が可能となる。係る商業的生産活動を、対象区域にて早急に再開し、以後、積極的な商業展開を実施する等、今後の浄化費用負担の軽減を図る様に心掛ける。 By changing the classification from the "necessary measure area" to the "characteristic change required notification area", the regulatory requirements for entering the area and changing the character such as building construction are substantially exempted. Enables commercial production activities. Such commercial production activities will be promptly resumed in the target area, and after that, aggressive commercial development will be carried out to reduce the burden of purification costs in the future.
なお、その後の「形質変更時要届出区域」の解除には、更に所定の溶出基準濃度までの浄化が求められ、また一定期間の予後調査が要求される。この場合は、本発明であるところの、(C)有害物質の土壌からの低溶出化、(D)鉄還元細菌を包含する微生物群集によるバイオプリベンションを継続し、また必要に応じて(E)アプローチの容易な既知汚染に対する導電性資材を活用したスポット浄化を実施して、所定の溶出基準を満たす浄化を図り、一定の期間を経た後の区域指定解除を目指す。 Further, in order to release the "notification area required for changing traits" thereafter, further purification up to a predetermined elution standard concentration is required and a prognosis study for a certain period is required. In this case, according to the present invention, (C) the low elution of harmful substances from soil, (D) bioprevention by a microbial community including iron-reducing bacteria is continued, and (E) ) We will carry out spot purification using a conductive material against known pollution that is easy to approach, pursuing purification that meets prescribed elution standards, and aiming to release the area designation after a certain period of time.
係る生物学的浄化の完了には、汚染程度にもよるが、一般に半年から数年の時間を要する。「形質変更時要届出区域」の状況で、実質的な商業的生産活動を再開するなどの土地利用の改善を図り浄化費用負担の軽減を図りながら、一定期間「形質変更時要届出区域」の状態で、生物学的浄化の完了を待つことが可能であれば、現状にて主流である「要措置区域」から一足飛びの「浄化対策完了」を早急に図る、費用対効果の薄い浄化対策に、莫大な費用を掛ける必要性は無くなる。 Depending on the degree of contamination, completion of such biological purification generally takes from half a year to several years. In the situation of "notification area required for change of characteristics", improvement of land use, such as resumption of substantial commercial production activities, and reduction of burden of purification costs, If it is possible to wait for the completion of biological purification in a state, it is a cost-effective purification measure that promptly takes a step away from the “mainly required area” which is currently the mainstream , There is no need to spend a huge amount of money.
なお、浄化対策費用が、その対象地の土地価格の2割を超えると、浄化対策を実施した上での土地売買が成立せずに、土地の塩漬けたるブラウンフィールド化する可能性を示す市場調査結果がある。 In addition, if the cost of cleanup measures exceeds 20% of the land price of the target area, a market survey showing the possibility that the land will be salted and becomes brownfield without the sale of land after implementing the cleanup measures. There is a result.
有害物質の取扱いがあって、ブラウンフィールド化が懸念される敷地であることがあらかじめ想定されるのであれば、有害物質を取り扱う事業の操業中の段階から、まずは、事業終了後の公定試験たるフェーズ2の土壌ガス調査にて「汚染無し」と判定される様な、早期検知と早期対策を特徴とする本発明であるところの(A)から(E)の土壌汚染対策を、係る調査に先んじて計画的に実施することが極めて重要である。 If it is assumed in advance that there is a concern that there will be brownfield conversion of hazardous substances, from the stage of operation of the project dealing with hazardous substances, first, the official test phase after the project is completed. Prior to the investigation, the soil pollution countermeasures (A) to (E) of the present invention, which are characterized by early detection and early countermeasures, which are determined to be “no pollution” in the soil gas survey 2) It is extremely important to implement this systematically and systematically.
ここで実施の形態に係る、導電性資材としては、具体的には例えば、鉱物系導電材であれば、マグネタイト、ヘマタイト、レピドクロサイト、ゲータイト等が、金属系導電材であれば、鉄粉、アルミ粉、マグネシウム粉等が、炭素系導電材であれば、黒鉛、カーボンブラック、黒炭、白炭、オガ炭、竹炭、バイオ炭等の粉末、または、これらの繊維様製品、多孔質炭素系粒子たる活性炭等を利用することができるが、導電性を呈し、鉄還元細菌の細胞表面での電子伝達を仲介できる導電性資材であれば、本発明にて利用することが可能であり、上記に具体的に示した資材に限定されることはない。また、他の資材を混合し、これらの導電性資材を一部に含む資材であれば、本発明での導電性資材として活用可能であることは言うまでもない。 Here, as the conductive material according to the embodiment, specifically, for example, if it is a mineral-based conductive material, magnetite, hematite, lepidocrocite, goethite, etc., if it is a metal-based conductive material, iron powder. If aluminum, aluminum powder, magnesium powder, etc. are carbon-based conductive materials, powders of graphite, carbon black, black charcoal, white charcoal, ogre charcoal, bamboo charcoal, biochar, etc., or fiber-like products thereof, porous carbon-based particles Although it is possible to use a barrel of activated carbon or the like, any conductive material that exhibits conductivity and can mediate electron transfer on the cell surface of iron-reducing bacteria can be used in the present invention. The materials are not limited to those specifically shown. Further, needless to say, a material containing other electrically conductive materials and partially containing these electrically conductive materials can be used as the electrically conductive material in the present invention.
ここで実施の形態に係る、導電性資材の形状は、展開する土壌や形成条件によりサイズも様々に存在する不定型ではあるものの、導電性資材が土壌粒子の表面に付着し、土壌間隙中にて互いに連通することで立体導電網の基礎が形成され、更に土壌粒子の表面での鉄還元細菌の仲介で拡大・補強される共通性質を有する。この土壌間隙をトンネルに例えれば、このトンネルの内壁面に沿って立体導電網が形成される。
また、係る立体導電網の立体的な外観形状は、スポンジ樹脂形状に近似される。本来のスポンジ樹脂は、多くの空隙を内包する網目状の樹脂構造で外観が形成されるが、係る立体導電網及び土壌間隙の外観は、この網目状の樹脂の外観に近似できる。なお、実際のスポンジを形成する樹脂は中空構造を採らないが、中空構造を有すると仮定すれば、近似される土壌間隙は、この中空部分に該当し、同様に近似される立体導電網は、中空を規定する外表面に相当する。
即ち、立体導電網は、その形状が土壌間隙と土壌粒子との境界形状に近似され、外観がスポンジ樹脂構造に近似される網目状に連なった立体物が、中空たるトンネル形状を呈する網糸によって形成されたごとくの構造物と説明される。
Here, according to the embodiment, the shape of the conductive material is an atypical type in which there are various sizes depending on the soil to be developed and the forming conditions, but the conductive material adheres to the surface of the soil particles, and in the soil gap. Have a common property that they form the basis of a three-dimensional conductive network by communicating with each other, and are expanded and reinforced by mediating iron-reducing bacteria on the surface of soil particles. If this soil gap is compared to a tunnel, a three-dimensional conductive network is formed along the inner wall surface of this tunnel.
Further, the three-dimensional appearance shape of the three-dimensional conductive network is similar to the sponge resin shape. The original sponge resin has a mesh-like resin structure that encloses a large number of voids, but the appearance of the three-dimensional conductive net and the soil gap can be similar to that of the mesh-like resin. Incidentally, the resin forming the actual sponge does not have a hollow structure, but assuming that it has a hollow structure, the approximated soil gap corresponds to this hollow part, and the similarly approximated three-dimensional conductive network is It corresponds to the outer surface defining the hollow.
That is, the three-dimensional conductive net, the shape of which is approximated to the boundary shape between the soil gap and the soil particles, the three-dimensional object in which the appearance is approximated to the sponge resin structure, is a hollow tunnel-shaped net thread. Described as a structure as formed.
また、ここで実施の形態に係る、培養基材としては、窒素肥料(アンモニウム塩、硝酸塩、尿素等)、リン酸肥料(リン酸塩、過燐酸石灰等)、カリウム肥料、各種金属塩(マグネシウム、マンガン、モリブデン、コバルト等)、ビタミン類等の培地成分の他、これら培地成分を吸着し徐放的に供給するための鉱物系粒子(ゼオライト、鹿沼土、タルク等)等や、電子供与体(有機物等、零価鉄等の金属粒子等)、電子受容体(有機物、硝酸塩、硫酸塩、鉄化合物、マンガン化合物、フミン酸等の有機酸、炭酸化合物等)を利用することができるが、鉄還元細菌を包含する微生物群集の増殖や代謝を促す資材であれば、本発明にて利用することが可能であり、上記に具体的に示した資材に限定されることはない。また、他の資材を混合し、これらの培養基材を一部に含む資材であれば、本発明にて培養基材として活用可能であることは言うまでもない。 Further, here, as the culture substrate according to the embodiment, nitrogen fertilizer (ammonium salt, nitrate, urea, etc.), phosphate fertilizer (phosphate, superphosphate, etc.), potassium fertilizer, various metal salts (magnesium) , Manganese, molybdenum, cobalt, etc.), vitamins, and other medium components, as well as mineral particles (zeolite, Kanuma soil, talc, etc.) for adsorbing and gradually releasing these medium components, and electron donors. (Organic substances, metal particles such as zero-valent iron, etc.), electron acceptors (organic substances, nitrates, sulfates, iron compounds, manganese compounds, organic acids such as humic acid, carbonic acid compounds, etc.) can be used, Any material that promotes the growth and metabolism of a microbial community including iron-reducing bacteria can be used in the present invention, and is not limited to the materials specifically shown above. In addition, it goes without saying that other materials can be mixed and used as a culture substrate in the present invention as long as they are materials containing a part of these culture substrates.
また更に、ここで実施の形態に係る有害物質としては、土壌汚染対策法における第一種特定有害物質である、四塩化炭素、1,2-ジクロロエタン、1,1-ジクロロエチレン、シス-1,2-ジクロロエチレン、1,3-ジクロロプロペン、ジクロロメタン、テトラクロロエチレン、1,1,1-トリクロロエタン、1,1,2-トリクロロエタン、トリクロロエチレン、ベンゼンが挙げられ、本発明の対策対象とすることが可能である。その他、水質環境基準や土壌環境基準に定められる、1,4-ジオキサンや塩ビモノマー等も、本発明の対策にて適用可能である。なお、上記の第一種特定有害物質の他にも、化審法等で定められる対象物質を含む汚染が、生分解性を呈し有害物質を包含する汚染物質の態様を示すものであれば該当し、言うまでもなく上記に具体的に示した化学物質に限定されることはない。 Furthermore, as the harmful substances according to the embodiment, carbon tetrachloride, 1,2-dichloroethane, 1,1-dichloroethylene, cis-1,2, which are the first-class specified harmful substances in the Soil Contamination Countermeasures Act, are used. -Dichloroethylene, 1,3-dichloropropene, dichloromethane, tetrachloroethylene, 1,1,1-trichloroethane, 1,1,2-trichloroethane, trichloroethylene, and benzene can be mentioned, and they can be the object of the present invention. In addition, 1,4-dioxane, vinyl chloride monomer, etc., which are defined in the water quality environmental standard and the soil environmental standard, are also applicable in the measure of the present invention. Note that, in addition to the above-mentioned Class I specified harmful substances, if the pollution containing the target substances specified by the Chemical Substances Control Law, etc. is biodegradable, it shows the mode of pollutants including harmful substances. However, it goes without saying that the chemical substances are not limited to the chemical substances specifically shown above.
ここで、本発明にて用いることが可能な鉄還元細菌としては、具体的には例えば、ゲオバクター属細菌、ペロバクター属細菌、フェリモナス属細菌、シュワネラ属細菌、ロドフェラックス属細菌、フェリバクテリウム属細菌、アナエロミクソバクター属細菌、デスルフロムサ属細菌、デスルフロモナス属細菌、デスルフィトバクテリウム属細菌、ゲオグローブス属細菌、バチルス属細菌、フェログロブス属細菌、ゲオバチルス属細菌、及び、ゲオスリックス属細菌等が挙げられる。
なお、細胞表面や導電性ワイヤ等の細胞構成器官を介して導電性資材や他の細菌に対し電子伝達できる微生物であれば、本発明にて利用することが可能であり、上記に具体的に示した微生物に限定されることはない。
Here, as the iron-reducing bacteria that can be used in the present invention, specifically, for example, Geobacter bacteria, Perobacter bacteria, Felimonas bacteria, Schwanella bacteria, Rhodoferrax bacteria, and Ferribacterium. Bacteria, Anaeromyxobacter bacteria, Desulfromus bacteria, Desulfromonas bacteria, Desulfitobacterium bacteria, Geoglobus bacteria, Bacillus bacteria, Ferroglobus bacteria, Geobacillus bacteria, and Geoslix bacteria and the like. ..
It should be noted that any microorganism capable of electron transfer to a conductive material or another bacterium through a cell constituting organ such as a cell surface or a conductive wire can be used in the present invention, and is specifically described above. It is not limited to the microorganisms shown.
また、本発明では、鉄還元細菌と共生関係にある他の嫌気性細菌を含めた、鉄還元細菌を包含する微生物群集3による生物学的浄化を図ることを主旨の一つとする。以下、本発明であるところの鉄還元細菌を包含する微生物群集の詳細について、図3を用いて説明する。 Further, one of the gist of the present invention is to achieve biological purification by a microbial community 3 including iron-reducing bacteria, including other anaerobic bacteria having a symbiotic relationship with iron-reducing bacteria. Hereinafter, details of the microbial community including the iron-reducing bacteria, which is the present invention, will be described with reference to FIG.
鉄還元細菌群23は、環境中において、他の嫌気性(共生)細菌群24と共にバイオマットを形成し、生分解性を呈し有害物質を包含する汚染物質4を、電子供与体として、或いは電子受容体として消費する。この消費を促すことにより、汚染物質の浄化が図られる。
生分解性を呈し有害物質を包含する汚染物質4という表現が示す通り、汚染物質は、少なくとも1種類以上の有害物質を含む複合物質で構成され、この複合物質の総合的な代謝を図る上で、多様な細菌の機能をもって対処する必要がある、本発明においては、鉄還元細菌群23を主体とし嫌気性(共生)細菌群24を包含する微生物群集にて、係る総合的な代謝を図る。
The iron-reducing bacteria group 23 forms a biomat together with other anaerobic (symbiotic) bacteria group 24 in the environment, and uses the pollutant 4 that is biodegradable and contains harmful substances as an electron donor or as an electron donor. It is consumed as an acceptor. By promoting this consumption, purification of pollutants can be achieved.
As the expression "pollutant 4 which is biodegradable and contains harmful substances" indicates that the pollutant is composed of a complex substance containing at least one or more kinds of harmful substances, and it is necessary for the comprehensive metabolism of this complex substance. In the present invention, which needs to be dealt with by the functions of various bacteria, the microbial community mainly including the iron-reducing bacteria group 23 and including the anaerobic (symbiotic) bacteria group 24 is used to achieve such comprehensive metabolism.
ここで、例えば、対象が有機塩素化合物汚染であれば、鉄還元細菌群23の他、硫酸還元細菌群やメタン細菌群、デハロコッコイデス等の脱塩素細菌群、或いはビタミンB12産生菌等から構成される嫌気性(共生)細菌群24で構成される、鉄還元細菌を包含する微生物群集3によって脱塩素化を図る。
ここで、本発明にて用いることが可能な、鉄還元細菌以外の有機塩素化合物の脱塩素化菌として、具体的には例えば、デハロコッコイデス属細菌、メタノサルシナ属細菌、デスルフィトバクテリウム属細菌、デハロバクター属細菌等が挙げられ、これらは、有機塩素化合物を電子受容体として利用し、適切な電子供与体と培養基剤を併せて供給することで有機塩素化合物に対して脱塩素化たる浄化を(ビタミンB12産生菌等との共生によって)図る特徴を有する。
Here, for example, if the target is an organic chlorine compound contamination, in addition to the iron-reducing bacteria group 23, a sulfate-reducing bacteria group, a methane bacteria group, a dechlorinating bacteria group such as dehalococcoides, or a vitamin B12-producing bacteria, etc. Dechlorination is achieved by the microbial community 3 including iron-reducing bacteria, which is composed of the anaerobic (symbiotic) bacteria group 24.
Here, as the dechlorinating bacterium of an organic chlorine compound other than iron-reducing bacteria that can be used in the present invention, specifically, for example, Dehalococcocides bacteria, Methanosarcina bacteria, Desulfitobacterium Genus bacterium, Dehalobacterus bacterium, etc. are used, which utilize an organochlorine compound as an electron acceptor and dechlorinate an organochlorine compound by supplying an appropriate electron donor and a culture base together. It has the characteristic of purifying (by coexistence with vitamin B12-producing bacteria).
ここで、鉄還元細菌群23を主体とする微生物群集とすることで、一部の嫌気性(共生)細菌群24と、細胞表面、導電性ワイヤ22、その他導電物質を通じて、係る電子の授受を行なって、エネルギー効率の良いバイオ浄化を図ることが期待される。
例えば、嫌気性(共生)細菌群24の一部として存在する脱塩素細菌群と鉄還元細菌との電子授受を介した、より緊密な共生関係が築かれた鉄還元細菌を包含する微生物群集3を、現場土着の菌叢によって構築しバイオスティミュレーションを実施する、或いは係る電子授受が図られる共生系が成立した集積培養系をあらかじめ取得し、バイオオーグメンテーション的手法を現場で展開することにより、鉄還元細菌より生じた電子を脱塩素細菌群の脱塩素化に利用させるエネルギー効率の良い脱塩素化バイオ浄化が期待される。
Here, by making the microbial community mainly composed of the iron-reducing bacteria group 23, transfer of such electrons is performed through a part of the anaerobic (symbiotic) bacteria group 24, the cell surface, the conductive wire 22, and other conductive substances. It is hoped that this will lead to energy-efficient bio-purification.
For example, a microbial community 3 that includes iron-reducing bacteria with which a closer symbiotic relationship is established through electron transfer between the dechlorinating bacteria existing as a part of the anaerobic (symbiotic) bacteria group 24 and the iron-reducing bacteria 3 To conduct biostimulation by constructing a local indigenous flora, or to obtain in advance an integrated culture system in which a symbiotic system capable of electronic transfer is established and to develop a bioaugmentation method on site. Therefore, energy-efficient dechlorination biopurification in which electrons generated from iron-reducing bacteria are used for dechlorination of dechlorination bacteria is expected.
また、例えば、対象がガソリン汚染であれば、ガソリン中のベンゼンは、バイオマット中の鉄還元細菌群23により分解され、一方、他のガソリン成分は、バイオマット中の硝酸還元菌群、硫酸還元細菌群やメタン細菌群等から構成される嫌気性(共生)細菌群24により分解が図られる。このように、ガソリン汚染に対しては、鉄還元細菌を包含する微生物群集3による多様な微生物を介した生物学的浄化を図る。 Further, for example, when the target is gasoline pollution, benzene in gasoline is decomposed by the iron-reducing bacteria group 23 in the biomat, while other gasoline components are nitrate-reducing bacteria group in the biomat and sulfuric acid reduction. Degradation is achieved by the anaerobic (symbiotic) bacterial group 24 composed of bacterial groups, methane bacterial groups, and the like. In this way, for gasoline pollution, biological purification through various microorganisms by the microbial community 3 including iron-reducing bacteria is attempted.
なお、鉄還元細菌群23の一部には、バイオマット境界21付近に伸びた導電性ワイヤ22を通じて、分子状酸素に対し電子伝達が可能なことも知られ、この様に、鉄還元細菌は、好気環境から嫌気環境に至る幅広い環境において、多様でユニークな電子伝達を行うことを可能とする。 It is also known that a part of the iron-reducing bacteria group 23 can transfer electrons to molecular oxygen through the conductive wire 22 extending near the biomat boundary 21. , It enables diverse and unique electron transfer in a wide range of environments from aerobic to anaerobic environments.
ところで、燃料油汚染の浄化に関しては、嫌気性の油分解菌のみならず、好気性の油分解菌による浄化事例も多くの実績がある。本発明であるところの嫌気性の鉄還元細菌と好気性の油分解菌を用いた、嫌気/好気条件のハイブリッド浄化を実施する場合は、汚染の移動/拡散抑制が担保された条件にて、対象汚染土壌に対し、嫌気分解を阻害しない程度の断続的な酸素を含むガスの通気を実施して、還元された鉄還元細菌の電子受容体の再生と、好気性油分解菌に対しては電子受容体たる酸素の供給を実施して効率の良い浄化を実施する。 By the way, regarding purification of fuel oil pollution, there are many actual cases of purification by not only anaerobic oil-decomposing bacteria but also aerobic oil-decomposing bacteria. When carrying out a hybrid purification under anaerobic/aerobic conditions using an anaerobic iron-reducing bacterium and an aerobic oil-degrading bacterium according to the present invention, under the condition that migration/diffusion suppression of pollution is secured. , The target polluted soil is intermittently ventilated with a gas containing oxygen that does not inhibit anaerobic decomposition, to regenerate the electron acceptor of the reduced iron-reducing bacteria and to aerobic oil-degrading bacteria. Supplies oxygen as an electron acceptor to carry out efficient purification.
なお、本ハイブリッド浄化を実施する場合は、できれば、対象土を掘削し、掘削土をパイルに成型し、適切な通気(吸気)配管を設置して、実施することが好ましいが、原位置にて土壌改良を実施するがごとくの切返しを実施して、簡便な通気装置での断続的な通気を実施するだけでも、十分に時間を掛けることで、浄化が達成される。 When performing this hybrid purification, it is preferable to excavate the target soil, form the excavated soil into a pile, and install an appropriate ventilation (intake) pipe, if possible, but at the original position. Purification can be achieved by taking a sufficient amount of time even by simply performing a cut-back to perform soil improvement and performing intermittent ventilation with a simple ventilation device.
ところで、本発明にて利用可能な、燃料油や油脂分を分解可能な好気性微生物としては、具体的には例えば、ロドコッカス属、ゴルドニア属、ノカルディア属、シュードモナス属、マイコバクテリウム属、ノカルディオイデス属、プラウセレラ属、バークホールデリア属、アルカニボラックス属、キサントモナス属、アシネートバクター属、ラルストニア属、オレイフィラス属、タラソリタス属、キサントバクター属、アシディスファエラ属、バチルス属、ゲオバチルス属細菌等が挙げられる。なお、燃料油や油脂分を分解できる好気性微生物であれば、本発明にて利用することが可能であり、上記に具体的に示した細菌群に限定されることはない。 By the way, as the aerobic microorganism capable of decomposing fuel oil and fats and oils usable in the present invention, specifically, for example, Rhodococcus, Gordonia, Nocardia, Pseudomonas, Mycobacterium, No Cardioides genus, Plaucerella genus, Burkholderia genus, Alkaniborax genus, Xanthomonas genus, Acinetobacter genus, Ralstonia genus, Oleophilus genus, Thalassolitas genus, Xanthobacter genus, Acidis faera genus, Bacillus genus, Geobacillus genus Examples include genus bacteria. It should be noted that any aerobic microorganism capable of decomposing fuel oil or fat and oil can be used in the present invention, and is not limited to the bacteria group specifically shown above.
この様に、ベンゼンを含む複合汚染を例にとっても、鉄還元細菌と様々な微生物群との組合せたる鉄還元細菌を包含する微生物群集3により、多様な浄化方法を提案できる。
現場状況、土着微生物の汚染分解能、分解菌添加の有効性の確認を、施工前にラボで確認するなど、適切な浄化設計を実施すると共に、納期、浄化コストに鑑み、最適な浄化を実施する様に心掛ける。
Thus, even in the case of complex pollution containing benzene, various purification methods can be proposed by the microbial community 3 including iron-reducing bacteria, which is a combination of iron-reducing bacteria and various microbial groups.
Appropriate purification design will be carried out, such as confirmation of the site situation, contamination resolution of indigenous microorganisms, confirmation of effectiveness of degrading bacteria addition in the lab before construction, etc., as well as optimal purification in view of delivery time and purification cost Like that.
なお、特殊なケースではあるが、呼吸基質として酸素と三価鉄の両方を用いることができるシュワネラ属細菌等の一部の鉄還元細菌の現場適用が可能であれば、空気または酸素を含む気体を対策対象の土壌に対し一定間隔を持って供給する。結果、係る特殊な鉄還元細菌は、酸素を呼吸基質として用いる時間帯には過酸化水素を生成し、また通気をストップして嫌気的に三価鉄を呼吸基質として用いる時間帯には、二価鉄と有機酸を生成する。
この操作を交互に繰り返すことで、二価鉄と有機酸と過酸化水素が同時に存在する時間帯を形成し、これら生成物群を基材とする非生物学的な化学酸化分解たるフェントン反応を生じやすい条件を設定して、更なる汚染物質浄化の促進を図る様に心掛ける。
Although it is a special case, if some iron-reducing bacteria such as Schwanella bacteria that can use both oxygen and trivalent iron as respiratory substrates can be applied in the field, air or gas containing oxygen can be used. Are supplied to the soil to be treated at regular intervals. As a result, such a special iron-reducing bacterium produces hydrogen peroxide during the time period when oxygen is used as a respiratory substrate, and it is reduced during the time period when anaerobically using ferric iron as a respiratory substrate. It produces valent iron and organic acids.
By repeating this operation alternately, a time zone in which divalent iron, organic acid, and hydrogen peroxide simultaneously exist is formed, and the Fenton reaction, which is a non-biological chemical oxidative decomposition based on these products, is performed. Set conditions that are likely to occur and try to promote further purification of pollutants.
以上、想定される汚染状況や対策目的に応じた本発明の発明を実施するための形態や実施例を説明してきたが、少なくとも導電性資材と培養基材を用いて、対策対象の土壌に連通する立体導電網を地中に形成し、鉄還元細菌を包含する微生物群集と汚染物質との接触を通じて汚染物質の代謝や分解を図るバイオプリベンション技術(生物学的汚染予防技術)を基本構成とする汚染対策であれば、本発明の要旨を逸脱しない範囲における変更や追加があっても本発明に含まれることはいうまでもない。 As described above, the mode and the embodiment for carrying out the invention of the present invention according to the assumed pollution situation and the purpose of the countermeasure have been described, but at least the conductive material and the culture substrate are used to communicate with the soil to be the countermeasure. basic to form a three-dimensional conductive network in the ground, FIG metabolism and decomposition of pollutants through contact with including microbial community the iron-reducing bacteria and contaminants Luba Io prevention technology (biological pollution prevention technologies) to if that is contamination countermeasures to the configuration and it is needless to say that also included in the present invention there are changes or additions without departing from the scope of the present invention.
また、後述する浄化対策の付帯技術(任意のタイミングでの汚染浄化技術や井戸様構造物を用いた導電性資材の再生技術)に関しても、本発明の要旨を逸脱しない範囲における変更や追加があっても本発明に含まれることはいうまでもない。 Further, with regard incidental art purification Mitigation later (reproduction technique conductive material using a decontamination technology and well-like structures at any time), changes and additions without departing from the scope of the present invention Needless to say, these are included in the present invention.
係る付帯技術である、任意のタイミングでの汚染浄化を実施する場合は、導電性資材として、特に活性炭および鉄粉を選択的に用いる。この場合の汚染浄化方法として、化学酸化分解法と還元脱塩素法を選択できるが、方法の選択は、必ず適用可能性試験を施工前に実施して、その効能の確認と必要資材の施用量を決定する。 In the case of carrying out pollution purification at an arbitrary timing, which is an accompanying technique, activated carbon and iron powder are selectively used as the conductive material. In this case, the chemical oxidative decomposition method and the reductive dechlorination method can be selected as the pollution purification method, but the method must be selected by conducting an applicability test before construction, confirming its efficacy and applying the necessary materials. To decide.
化学酸化分解法では、導電性資材の他に過酸化物や有機酸の種類を検討して適切な条件を設定する。過酸化物としては、例えば、過酸化水素、オゾン、次亜塩素酸塩、過マンガン酸塩、マグネシウム過酸化物、過硫酸塩などを含む資材を挙げることができる。これらの過酸化物は単独で使用してもよいし、2種以上を組み合わせて使用してもよい。過酸化物としては、特に過硫酸化合物を用いることが好ましい。
また、有機酸としては、例えば、コハク酸、クエン酸、ピルビン酸、マレイン酸、フマル酸、乳酸、酢酸、蟻酸、シュウ酸、リンゴ酸、グルコン酸、酒石酸などから選ばれる有機酸またはその塩を含む資材を単独で使用してもよいし、2種以上を組み合わせて使用してもよい。
なお、活性炭と鉄粉との組合せによって汚染・有害物質を分解できる過酸化物および/或いは、有機酸を含む資材であれば、本発明にて利用することが可能であり、上記に具体的に示した資材に限定されることはない。
In the chemical oxidative decomposition method, in addition to the conductive material, the types of peroxides and organic acids are examined and appropriate conditions are set. Examples of peroxides include materials containing hydrogen peroxide, ozone, hypochlorite, permanganate, magnesium peroxide, persulfate, and the like. These peroxides may be used alone or in combination of two or more. As the peroxide, it is particularly preferable to use a persulfate compound.
Further, as the organic acid, for example, an organic acid selected from succinic acid, citric acid, pyruvic acid, maleic acid, fumaric acid, lactic acid, acetic acid, formic acid, oxalic acid, malic acid, gluconic acid, tartaric acid or a salt thereof. The contained materials may be used alone or in combination of two or more.
It should be noted that any material containing peroxide and/or organic acid capable of decomposing pollutant/hazardous substances by the combination of activated carbon and iron powder can be used in the present invention. It is not limited to the materials shown.
また、還元脱塩素法では、導電性資材の他に脂溶性有機資材を少なくとも一部に含む資材を添加して適切な条件を設定する。脂溶性有機資材を用いる利点は、地下水流や雨水浸透による流下・流出を最少とできることにあり、比較的長期間を要する還元脱塩素法の実施において汚染土壌に対し長期に亘って本剤の供給を図る目的で用いる。
一方、展開する土壌環境が酸化雰囲気にあり、短期間で還元条件に移行させる必要がある場合等には、脂溶性有機資材を主とした構成であって、一部に水溶性有機物を含む様な資材構成にて還元脱塩素法を実施する方法を採用しても良い。
脂溶性有機資材としては、植物油(菜種油、大豆油、コーン油、ゴマ油、米油、係る植物油の廃油等)、動物油(ラード、牛脂、係る動物脂の廃油等)、脂肪酸などを含む資材を単独で使用してもよいし、2種以上を組み合わせて使用してもよい。
Further, in the reductive dechlorination method, in addition to the conductive material, a material containing a fat-soluble organic material in at least a part thereof is added to set an appropriate condition. The advantage of using a fat-soluble organic material is that it can minimize the flow down and outflow due to the infiltration of groundwater and rainwater, and in the implementation of the reductive dechlorination method, which requires a relatively long period of time, the supply of this product to contaminated soil over a long period of time. Used for the purpose of
On the other hand, when the soil environment to be developed is in an oxidizing atmosphere and it is necessary to shift to reducing conditions in a short period of time, etc., the structure is mainly composed of fat-soluble organic materials, and some of them may contain water-soluble organic substances. A method of implementing the reductive dechlorination method with various material configurations may be adopted.
As fat-soluble organic materials, vegetable oil (rapeseed oil, soybean oil, corn oil, sesame oil, rice oil, waste oil of such vegetable oil, etc.), animal oil (lard, beef fat, waste oil of such animal fat, etc.), fatty acid, etc. May be used, or two or more kinds may be used in combination.
また、もう一つの付帯技術である、導電性資材の再生方法を、図4に記載した井戸様構造物の概略図を用いて説明する。
井戸様構造物は、4aに示す多重分配継手25によって仕切られ、仕切られた区間に配置されたストレーナ(有孔)管26から、過酸化物溶液、および/或いは、気体を、流体移送管27を介して、対策対象の土壌に注入する機能を有する。注入された過酸化物溶液は、注入気体流28によって注入過酸化物溶液の撹拌流29を生じ、対象土壌たる帯水層中への浸透・拡散が図られる。この気体を用いた過酸化物溶液の撹拌は、1本の井戸に複数のストレーナを配して実施したほうが、影響範囲をより広く取ることができる。
A method of regenerating a conductive material, which is another accessory technique, will be described with reference to the schematic view of the well-like structure shown in FIG.
The well-like structure is partitioned by the multiple distribution joint 25 shown in 4a, and the peroxide solution and/or the gas is transferred from the strainer (perforated) pipe 26 arranged in the partitioned section to the fluid transfer pipe 27. It has the function of injecting it into the soil of the countermeasure target via. The injected peroxide solution causes a stirring flow 29 of the injected peroxide solution by the injection gas flow 28, and permeates and diffuses into the aquifer, which is the target soil. The stirring of the peroxide solution using this gas can have a wider influence range when a plurality of strainers are arranged in one well.
この複数のストレーナを配する1本の井戸は、4aや4bに示す様に多重分配継手25を1本の井戸内に複数配置して、仕切られた複数のストレーナ区間を設置し、更に流体移送外管群30と流体移送内管31を包含する多重管構造を有する流体移送管27を、多重分配継手25とストレーナ(有孔)管26に通じた後に、流体移送管固定具32にて固定し、最後にストレーナ(有孔)管26や無孔管33を固定して製作する(4c)。 One well in which a plurality of strainers are arranged has a plurality of multiple distribution joints 25 arranged in one well as shown in 4a and 4b, and a plurality of partitioned strainer sections are installed to further carry out fluid transfer. A fluid transfer pipe 27 having a multiple pipe structure including an outer pipe group 30 and a fluid transfer inner pipe 31 is connected to a multiple distribution joint 25 and a strainer (perforated) pipe 26, and then fixed by a fluid transfer pipe fixture 32. Finally, the strainer (perforated) pipe 26 and the non-perforated pipe 33 are fixed and manufactured (4c).
この対象土壌に浸透・拡散された過酸化物溶液にて、導電性資材に付着した機能損壊物質の洗浄・分解を行い、導電性資材の機能たる、導電特性、表面吸着特性、空間特性等の諸機能の回復を図る。なお、過酸化物としては、例えば、過酸化水素、オゾン、次亜塩素酸塩、過マンガン酸塩、マグネシウム過酸化物、過硫酸塩などを含む資材を挙げることができる。これらの過酸化物は単独で使用してもよいし、2種以上を組み合わせて使用してもよい。但し、過酸化物としては、特に過硫酸化合物を用いることが好ましい。 The peroxide solution that has permeated and diffused into the target soil is used to wash and decompose the functionally damaging substances adhering to the conductive material, and to determine the function of the conductive material, such as the conductive characteristics, surface adsorption characteristics, and spatial characteristics. To restore various functions. Examples of peroxides include materials containing hydrogen peroxide, ozone, hypochlorite, permanganate, magnesium peroxide, persulfate, and the like. These peroxides may be used alone or in combination of two or more. However, it is particularly preferable to use a persulfate compound as the peroxide.
なお、本井戸様構造物は、導電性資材の再生を行っていない期間には、各ストレーナ区間における観測井戸として活用し、多区間のモニタリングによって精度の高いモニタリングを実施する。また、地層構造が破壊されていない互層構造を有する汚染土壌に本井戸様構造物を適用する場合であれば、本井戸様構造物の特徴である多数のストレーナ区間を、互層構造の各地層に分配して配置することで、各層に対する個別のモニタリングや各層に特化した流体の注入・回収操作を実施できる多目的井戸として活用する。 This well-like structure will be used as an observation well in each strainer section during the period when the conductive material is not regenerated, and highly accurate monitoring will be carried out by monitoring multiple sections. If the well-like structure is to be applied to contaminated soil that has an alternating structure in which the stratum structure is not destroyed, the multiple strainer sections that are characteristic of the well-like structure should By distributing and arranging, it will be utilized as a multi-purpose well that can carry out individual monitoring for each layer and fluid injection/recovery operations specialized for each layer.
以上、本発明の発明を実施するための形態や実施例を説明してきたが、具体的な構成は前述した形態や事例に限られるものではなく、本発明の要旨を逸脱しない範囲における変更や追加があっても本発明に含まれる。 Although the embodiments and examples for carrying out the invention of the present invention have been described above, the specific configurations are not limited to the above-described embodiments and examples, and modifications and additions are made within the scope not departing from the gist of the present invention. Even so, it is included in the present invention.
以下に、実施例により本発明について具体的に説明するが、本発明は以下の実施例に何ら限定されるものではない。 Hereinafter, the present invention will be specifically described with reference to Examples, but the present invention is not limited to the following Examples.
本実験では、導電性資材の添加量が異なるローム土壌を容器内に入れ、係る土壌の一部に灯油・ガソリンの混合油を添加して、鉄還元細菌による呼吸量の違いを、容器内の二酸化炭素濃度から評価した。 In this experiment, loam soil with different amounts of conductive materials added was placed in a container, and a mixed oil of kerosene/gasoline was added to a part of the soil to determine the difference in respiration rate due to iron-reducing bacteria. It was evaluated from the carbon dioxide concentration.
試験手順を以下に示す。
(a)基本培養土の調整を、窒素ガス置換した嫌気グローブボックス内にて、ローム土壌1Lに対し、鉄還元細菌用の培地(脱塩素水道水100m1、NH4Cl:0.15g、NaH2PO4:0.06g、CaCl2・2H2O:0.01g、KCl:0.01g、MgCl2・6H2O:0.2mg)を添加・混合して作成した。
引き続き、同グローブボックス内にて、この基本培養土を5等分し、土壌1kg当たり、10mg、50mg、100mg、500mgのナノ活性炭(<1nmφ)を加えた4系統の試験土壌と、1系統の活性炭無添加土壌を作成し、セプタムで仕切られたガス放出・採取孔を有する500ml容のガラス瓶に各試験土壌を充填した。
続いて、充填した土壌の中央部に、灯油とガソリンを1:1で混合した混合油1mlを、瓶中央の地表部から周囲への広がりを最少として垂直に浸透させる様、ゆっくりとスパイクし、更に全体の土壌構造を乱さない様に注意しながら蓋を取付け、摂氏15℃のインキュベータで静置状態での培養試験に供した。
The test procedure is shown below.
(A) In the anaerobic glove box in which the nitrogen gas was replaced, the basic culture soil was adjusted with respect to 1 L of the loamy soil, a medium for iron-reducing bacteria (dechlorination tap water 100 m1, NH 4 Cl: 0.15 g, NaH 2 PO 4 : 0.06 g, CaCl 2 ·2H 2 O: 0.01 g, KCl: 0.01 g, MgCl 2 ·6H 2 O: 0.2 mg) were added and mixed to prepare.
Subsequently, in the same glove box, this basic culture soil was divided into 5 equal parts, and 4 mg of the test soil to which 10 mg, 50 mg, 100 mg, and 500 mg of nano activated carbon (<1 nmφ) were added per 1 kg of soil, and 1 strain of the Activated carbon-free soil was created, and each test soil was filled in a 500 ml glass bottle having a gas discharge/collection hole partitioned by a septum.
Then, in the center of the filled soil, 1 ml of mixed oil of kerosene and gasoline mixed 1:1 was slowly spiked so that it spreads vertically from the surface of the center of the bottle to the surroundings, Furthermore, a lid was attached while being careful not to disturb the entire soil structure, and the culture test was performed in a static state in an incubator at 15°C.
(b)続いて、経過時間毎に、各試験区のガス放出・採取孔から0.5mlのガスをガスタイトシリンジにて採取し、TCDガスクロマトグラフィーに供して、採取ガス中の二酸化炭素濃度を求めた。 (B) Subsequently, for each elapsed time, 0.5 ml of gas was sampled from the gas release/collection hole of each test section with a gas tight syringe and subjected to TCD gas chromatography to measure the carbon dioxide concentration in the sampled gas. I asked.
上記の実験結果を図4に示す。
図4のグラフより明らかなように、活性炭濃度が高い程、二酸化炭素濃度上昇が早期に始まることが分かった。また、到達時間の差はあるものの、二酸化炭素濃度の到達濃度は、活性炭添加量が50mgを超えるとほぼ変わらなくなり、80〜90%近辺で頭打ちとなった。
The above experimental results are shown in FIG.
As is clear from the graph of FIG. 4, it was found that the higher the activated carbon concentration, the earlier the carbon dioxide concentration rises. Further, although there was a difference in arrival time, the arrival concentration of carbon dioxide concentration remained almost unchanged when the amount of activated carbon added exceeded 50 mg, and reached a peak around 80 to 90%.
なお、試験終了時点で、試験土壌を冷凍固定した後に容器から取出し、更に、解凍して観察に供したところ、活性炭添加量が50mgを超えた試験区では、試験初期には黒掛かった褐色であった土色が、試験土壌の全面が黒掛かった青色に変化している様子が観察された。一方、無添加区と10mg添加区では、全面の青色変化は観察されず、青色化は中央部付近に限定されていた。また10mg添加区での青色部と褐色部の境界に、放射状に伸びる糸状の青色ラインが複数観察された。 At the end of the test, the test soil was frozen and fixed, then taken out of the container, thawed and subjected to observation. In the test section where the amount of activated carbon added exceeded 50 mg, the test soil had a dark brown color at the beginning of the test. It was observed that the soil color that had existed changed to blue, which was black over the entire surface of the test soil. On the other hand, in the non-addition group and the 10 mg addition group, no blue color change was observed on the entire surface, and the bluing was limited to the vicinity of the central portion. In addition, a plurality of thread-shaped blue lines extending radially were observed at the boundary between the blue part and the brown part in the 10 mg addition group.
これらの実験結果から、少なくとも、係る活性炭を適切に土壌に混合して、土壌中に立体導電網を形成することにより、汚染存在部のみならず離れた場所の電子受容体も併せて活用して、系全体としての鉄還元細菌の代謝活性を高められることが分かった。また係る代謝では、顕著な二酸化炭素の発生を伴うことが確認された。 From these experimental results, at least, by appropriately mixing the activated carbon with the soil to form a three-dimensional conductive network in the soil, it is possible to utilize not only the contaminated portion but also the electron acceptor at a remote place. , It was found that the metabolic activity of iron-reducing bacteria in the whole system can be enhanced. It was also confirmed that such metabolism is accompanied by remarkable generation of carbon dioxide.
実施例1では、二酸化炭素の発生、及び、立体導電網の形成に関する評価を実施したが、係る実施例2では、導電性資材を用いた効果としての、汚染移動/拡散抑制、土壌からの低溶出化、微生物浄化に関する評価について、土壌カラム試験を用いて実施した。 In Example 1, generation of carbon dioxide and evaluation of formation of a three-dimensional conductive network were carried out, but in Example 2 concerned, pollution transfer/diffusion suppression, reduction from soil as an effect of using a conductive material. The soil column test was used to evaluate elution and microbial purification.
試験手順を以下に示す。
(a)重量比95の粒径0.1mmのガラスビーズと重量比5の腐葉土を良く混合して充填した内径φ5cm×1m有効長の温調ジャケット付模擬土壌カラムを3本用意し、続いて、煮沸・脱気処理と活性炭処理を施し、更にスチールウールを充填したプレカラムを通じて脱酸素化を図った嫌気除塩素水道水を、嫌気グローブボックス内で調整し、シリンジポンプを用いて、カラム間隙体積の3倍量分を通水してコンディショニングを実施した。なお、コンディショニングは、カラム通過線速が、概ね30cm/日となるように、シリンジポンプの流量を調整した。
The test procedure is shown below.
(A) Prepare three simulated soil columns with an inner diameter of φ5 cm×1 m effective length and a temperature control jacket, in which glass beads having a weight ratio of 95 and a particle diameter of 0.1 mm and well-known soil having a weight ratio of 5 are well mixed and packed, and subsequently, The anaerobic dechlorinated tap water, which has been subjected to boiling/deaeration treatment and activated carbon treatment and deoxygenation through a pre-column filled with steel wool, is adjusted in the anaerobic glove box and the column gap volume is adjusted using a syringe pump. Conditioning was carried out by passing water in an amount of 3 times the amount of the above. In the conditioning, the flow rate of the syringe pump was adjusted so that the linear velocity passing through the column was approximately 30 cm/day.
(b)また、上述の「嫌気除塩素水道水」に対し1,4-ジオキサンを1mg/L濃度となる様に添加し、更に栄養塩の添加の有無の違いから2種類の供給溶液を、嫌気グローブボックス内で作成し、カラム試験の各試験区に供した。各試験区における培養条件の違いを表1に示す。 (B) In addition, 1,4-dioxane was added to the above-mentioned "anaerobic dechlorinated tap water" to a concentration of 1 mg/L, and two types of feed solutions were added depending on whether nutrient salts were added or not, It was prepared in an anaerobic glove box and provided for each column test section. Table 1 shows the difference in the culture conditions in each test section.
ところで、本来であれば、自然界の土壌中には、少なからず不溶性の三価鉄が含まれ、必ずしも培地を通じた三価鉄成分の供給は必要としないが、今回は、試験の途中から、鉄還元細菌の寄与を評価するために、敢えて溶解性鉄成分を通水に加えて供給する系にて実験を行った。
なお、各試験区の通水は、初期のカラム通過線速が、概ね30cm/日となるように設定したが、その後の経過に従って、供給圧力が上昇した場合を想定し、供給圧力が50kPaで通水自動停止、10kPa迄、圧力が低下すると通水自動復帰となる様な圧力調整による断続的な通水を設定した。また、カラム温度は、温調ジャケットを通じて摂氏15℃の恒温となるように調整した。
この様な設定の下で、10日間のコンディショニングを実施し、また、経時的にカラム通過水中の1,4-ジオキサン濃度を、PID/GCを用いたヘッドスペース法にて測定した。
By the way, originally, natural soil contains a considerable amount of insoluble trivalent iron, and it is not always necessary to supply the ferric iron component through the medium, but this time, from the middle of the test, iron In order to evaluate the contribution of reducing bacteria, experiments were carried out in a system in which a soluble iron component was supplied in addition to water.
The water flow in each test section was set so that the initial column passing linear velocity was approximately 30 cm/day, but assuming that the supply pressure increased with the passage of time, the supply pressure was 50 kPa. Automatic water supply was stopped, and intermittent water supply was set by adjusting the pressure so that when the pressure drops to 10 kPa, the water supply automatically returns. The column temperature was adjusted to a constant temperature of 15°C through a temperature control jacket.
Under these settings, conditioning was carried out for 10 days, and the 1,4-dioxane concentration in the water passing through the column was measured over time by the headspace method using PID/GC.
(c)係る10日間のコンディショニング後、試験区1と試験区2の各カラムに対し、カラム体積の0.1倍量の5%重量濃度のナノ活性炭スラリー溶液をカラムに通過させ、活性炭粒子をガラスビーズ表面に吸着させる操作を実施した。 (C) After conditioning for 10 days, a nano activated carbon slurry solution having a concentration of 5% by weight, which is 0.1 times the column volume, was passed through each column of the test section 1 and the test section 2 to remove the activated carbon particles. The operation of adsorbing on the surface of the glass beads was performed.
(d)以後、経時的なカラム通過水中の1,4-ジオキサン濃度を、PID/GCを用いたヘッドスペース法での測定を継続した。また、活性炭添加後90日から100日迄の10日間は、試験区1に対し、通水溶液の栄養塩中からFe(III)‐EDTAを除いた溶液の通液を実施して通過水中の1,4-ジオキサン濃度を観察した。 (D) After that, the 1,4-dioxane concentration in the water passing through the column with time was continuously measured by the headspace method using PID/GC. In addition, for 10 days from 90 days to 100 days after the addition of activated carbon, test solution 1 was passed through a solution obtained by removing Fe(III)-EDTA from the nutrient salt of the passing solution, and The concentration of 4,4-dioxane was observed.
結果を、図5から図7のグラフに示す。図5は、各試験区における供給1,4-ジオキサン濃度と経時的なカラム流出水中の1,4-ジオキサン濃度から求めた濃度比である。−10日から0日目迄は、各試験区共に、活性炭添加前のコンディショニング期間であり、試験区1と2に対しては、0日目に活性炭の添加を実施した。 The results are shown in the graphs of FIGS. FIG. 5 is a concentration ratio calculated from the 1,4-dioxane concentration supplied in each test section and the 1,4-dioxane concentration in the column outflow water over time. From -10th day to 0th day, each test section was in the conditioning period before the addition of activated carbon, and for test sections 1 and 2, the addition of activated carbon was carried out on the 0th day.
図5にて明らかな様に、活性炭添加区である試験区1と2に関しては、活性炭添加後、数日を経て、濃度比が減少傾向に移行し、更に数日を経て、ほぼ検出が見られなくなった。詳細には、試験区1は、活性炭添加後34日目に、また試験区2は56日目に、水質環境基準である0.05mg/L以下となった。以後、試験区1は97日目迄、試験区2は57日目迄の2日間にて、係る基準値以下を達成した。 As is clear from FIG. 5, with regard to the test groups 1 and 2 which are the activated carbon-added groups, the concentration ratio changed to a decreasing tendency several days after the addition of the activated carbon, and the detection was almost observed after several days. I can no longer. Specifically, the test plot 1 had a water environmental standard of 0.05 mg/L or less on the 34th day after the addition of activated carbon and the test plot 2 on the 56th day. After that, the test section 1 achieved the standard value or less by the 97th day and the test section 2 by the 57th day for two days.
この両試験区における、地下水基準を達成する迄の日数、及び、継続期間の違いは、栄養塩添加の有無の違いであり、鉄還元細菌、或いは鉄還元細菌を包含する微生物群集の増殖に伴う1,4-ジオキサン分解の有無の違いによるものと推察された。
なお、微生物分解の関与がほとんど無いと想定される試験区2の濃度比の変化に関しては、主として活性炭の吸着効果による1,4-ジオキサン濃度の減少と想定されるが、70日目以降で観察される急激な1,4-ジオキサン濃度比の上昇は、添加した活性炭の吸着容量が限界となる破過状態に達した結果であると推察される。
The difference in the number of days until the groundwater standard is reached and the duration of these two test plots is the difference in the presence or absence of the addition of nutrient salts, which is associated with the growth of iron-reducing bacteria or microbial communities including iron-reducing bacteria. It was inferred that this was due to the presence or absence of decomposition of 1,4-dioxane.
Regarding the change in the concentration ratio of test area 2 which is assumed to have almost no involvement in microbial degradation, it is assumed that the 1,4-dioxane concentration decreases mainly due to the adsorption effect of activated carbon, but it is observed after 70 days. It is speculated that the rapid increase in the 1,4-dioxane concentration ratio that is caused is the result of reaching a breakthrough state where the adsorption capacity of the added activated carbon reaches its limit.
一方、試験区1に関しては、70日を超えてもなお、環境基準値以下を保っており、係る現象の比較からも、1,4-ジオキサンの分解・浄化に、鉄還元細菌、或いは鉄還元細菌を包含する微生物群集の一定の寄与が示唆される。
この鉄還元細菌等の寄与を更に明確にする為に、通水からFe(III)‐EDTAを除いた試験を90日目から100日目迄の10日間実施したところ、111日目をピークとする一過性の1,4-ジオキサン濃度比の戻りが観察され、カラム流出水中の1,4-ジオキサン濃度が環境基準値以下を保つ上で、鉄還元菌等は、分解を担う一定の寄与を果たしていることが明確となった。
On the other hand, in Test Zone 1, the environmental standard value is still maintained even after 70 days. From the comparison of such phenomena, iron-reducing bacteria or iron-reducing bacteria can be used for the decomposition and purification of 1,4-dioxane. A certain contribution of microbial communities, including bacteria, is suggested.
In order to further clarify the contribution of this iron-reducing bacterium, etc., a test in which Fe(III)-EDTA was removed from the water flow was carried out for 10 days from 90th day to 100th day, and the peak was found on the 111th day. A temporary return of the 1,4-dioxane concentration ratio was observed, and iron-reducing bacteria, etc., contributed to a certain degree of contribution in keeping the 1,4-dioxane concentration in the column effluent below the environmental standard value. It became clear that it fulfilled.
ところで、試験区3は、試験区1同様にカラム通水に栄養塩が存在する試験区であるが、試験区1で観察された様な明瞭な1,4-ジオキサン濃度の低下は観察されなかった。この試験区3と試験区1との条件の差は、活性炭添加の有無であるが、図6に示す1,4-ジオキサン除去能の比較では、試験区1と試験区2&3の和との除去能を比較すると、後者が74日目以降、急激な能力低下を示すのに対し、前者は74日以降も高い除去能力を維持している(111日目を負のピークとする別目的での評価期間を除く)ことが明瞭に示されている。
この結果が示すところは、試験区2に示される活性炭の吸着による1,4-ジオキサン除去効果と、試験区3に示される鉄還元細菌等の分解による1,4-ジオキサン除去効果、双方の効果の和以上の効果が、活性炭と鉄還元細菌等の組み合わせによって生じることが、試験区1が示す結果との比較によって明らかとなった。
今回の実験では、電子受容体は通水液から連続的に供給しているので、立体導電網形成程度の違いから生じる電子受容体律速による差では無い。活性炭による汚染濃縮効果、或いは、付着やバイオマット形成等の促進効果が、鉄還元細菌等の増殖や分解促進に寄与した等、別観点における1,4-ジオキサン除去の促進効果の存在が示唆される。
By the way, although the test section 3 is a test section in which nutrient salts are present in the column water as in the test section 1, no clear decrease in the 1,4-dioxane concentration as observed in the test section 1 is observed. It was The difference between the conditions of test section 3 and test section 1 is the presence or absence of addition of activated carbon, but in the comparison of the 1,4-dioxane removal ability shown in FIG. 6, the removal of test section 1 and the sum of test sections 2 & 3 Comparing the performances, the latter shows a sharp decline in capacity after the 74th day, while the former maintains a high removal capacity even after the 74th day (for another purpose, with the negative peak on the 111th day). (Excluding the evaluation period) is clearly shown.
These results show that 1,4-dioxane removal effect by adsorption of activated carbon shown in test section 2 and 1,4-dioxane removal effect by decomposition of iron-reducing bacteria shown in test section 3 It was clarified by the comparison with the results shown in Test Group 1 that the above-mentioned effect is caused by the combination of activated carbon and iron-reducing bacteria.
In this experiment, since the electron acceptor is continuously supplied from the water flow liquid, it is not the difference due to the rate-determining electron acceptor caused by the difference in the degree of formation of the steric conductive network. Contamination concentration effect by activated carbon, or promotion effect of adhesion and biomat formation, etc. contributed to the promotion and decomposition of iron-reducing bacteria. It
また、図7に示す各カラムの供給圧の経時的変化を比較すると、活性炭のみを添加した試験区2の供給圧力に変化は無く、また、栄養塩のみを添加した試験区3の供給圧力にも幾分の上昇傾向が観察されたものの、試験区1の供給圧力の上昇が最も顕著であった。
係る圧力上昇の差は、鉄還元細菌の代謝によって生じる不溶性鉄化合物の生成や増殖した鉄還元細菌等による土壌間隙の閉塞化によって生じたものと推察され、試験区1の鉄還元細菌等の代謝活性は、試験区3と比較して、より顕著であったと考察される。
In addition, comparing the changes over time in the supply pressure of each column shown in FIG. 7, there was no change in the supply pressure of the test section 2 to which only activated carbon was added, and to the supply pressure of the test section 3 to which only nutrient salts were added. Although a slight increase tendency was observed, the increase in the supply pressure in the test area 1 was the most remarkable.
It is speculated that the difference in the increase in pressure was caused by the formation of insoluble iron compounds generated by the metabolism of the iron-reducing bacteria and the clogging of the soil gap by the proliferated iron-reducing bacteria, and the metabolism of the iron-reducing bacteria and the like in test section 1. It is considered that the activity was more remarkable as compared with the test group 3.
総じて、系への活性炭添加は、立体導電網形成も相まって、系全体での鉄還元細菌等の代謝活性を高める作用があり、これにより、1,4-ジオキサン浄化能の向上と、土壌間隙の閉塞化たる透水係数の低下が図られ、汚染地下水に含まれる有害物質の、移動/拡散抑制(含:局所的な低溶出化・汚染分解)たる、流下量の抑制を促すものと推察された。 In general, the addition of activated carbon to the system, together with the formation of a steric conductive network, has the effect of enhancing the metabolic activity of iron-reducing bacteria and the like in the entire system, which improves the 1,4-dioxane purification capacity and soil pores. It was conjectured that the permeability coefficient, which is a blockage, would be reduced, and that the flow rate of harmful substances contained in contaminated groundwater would be suppressed, including migration/diffusion suppression (including local low elution and pollution decomposition). ..
実施例2の成果に基づき、1,4-ジオキサンを、ベンゼン或いはテトラエチレンに変更し、培養液成分はそれぞれの分解に適した組成に変更して、実施例2と同様の試験を実施したところ、両有害物質共に、1,4-ジオキサンとほぼ同様の結果が示され、有害物質種を芳香族炭化水素系物質や有機ハロゲン化合物に替えても、同様な効果を再現できることが示された(データ不載)。 Based on the results of Example 2, 1,4-dioxane was changed to benzene or tetraethylene, the composition of the culture solution was changed to a composition suitable for each decomposition, and the same test as in Example 2 was carried out. , Both harmful substances showed almost the same results as 1,4-dioxane, and it was shown that the same effect can be reproduced by replacing the harmful substance species with aromatic hydrocarbon compounds and organic halogen compounds ( No data).
本実験では、導電性資材としてマグネタイト(砂鉄)を用いた立体導電網を地中に形成し、導通する鉄還元細菌を包含する微生物群集を活用して、過酸化水素と二価鉄と有機酸の生成を促して、フェントン反応を誘導し、難生分解性汚染物質の分解を図る方法に関する検証を実施した。 In this experiment, a three-dimensional conductive net using magnetite (sand iron) as a conductive material is formed in the ground, and a microbial community including conducting iron-reducing bacteria is utilized to utilize hydrogen peroxide, divalent iron, and organic acids. The verification of the method that promotes the generation of methane, induces the Fenton reaction, and decomposes the hardly biodegradable pollutants was conducted.
試験手順を以下に示す。
(a)難生分解性汚染物質を含む土壌として、好気性のバイオレメディエーションの実施履歴があるC重油汚染土で、汚染浄化が不調で汚染が残存してしまった汚染未完了土(汚染濃度:約3千mg/kg)を選択した。この難生分解性油分を含む土壌に対し、米糠とマグネタイト(砂鉄)をそれぞれ重量比0.2%で添加し、更に、窒素とリンを0.01%の割合で添加(窒素肥料として尿素、リン肥料として過リン酸石灰を使用)し、供試土壌を作成した。
The test procedure is shown below.
(A) As a soil containing hardly biodegradable pollutants, it is a C heavy oil contaminated soil that has a history of aerobic bioremediation, and uncontaminated soil (pollution concentration: Approximately 3000 mg/kg) was selected. Rice bran and magnetite (sand iron) were added to the soil containing the hardly biodegradable oil at a weight ratio of 0.2%, respectively, and nitrogen and phosphorus were added at a ratio of 0.01% (urea as a nitrogen fertilizer, Calcium superphosphate was used as phosphorus fertilizer) to prepare the test soil.
(b)続いて、上記供試土壌を、5台の2L容のステンレス製容器の口一杯まで装填して5系統の試験区を設定し、培養温度20度のインキュベータ内にて培養に供した。培養開始後、各試験区での油分濃度を経時的に測定した。
また、試験開始後、油分の減少が観察された試験区の土壌試料(500ml程度)を用いて、係る分解効果がフェントン反応で生じたヒドロキシラジカル由来の分解反応であることを判定するために、土壌重量の0.5%量のマンニトール(ヒドロキシラジカルのスカベンジャーとして:マスキング試験)を添加し、その後、500ml容の容器に充填し、本試験条件と同様の操作にてインキュベーションとその後の経時的な油分濃度の測定を実施した(なお、マンニトール添加前後で、添加による土壌微生物の呼吸活性に変化がないことを確認済。)。
(B) Subsequently, the test soil was loaded up to the mouth of five stainless steel containers of 2 L volume to set up test sections of 5 lines, and the test soil was cultured in an incubator at a culture temperature of 20 degrees. .. After the start of culture, the oil concentration in each test section was measured over time.
Further, after the start of the test, using a soil sample (about 500 ml) in a test section where a decrease in oil content was observed, in order to determine that the decomposition effect is a decomposition reaction derived from a hydroxy radical generated in the Fenton reaction, Mannitol (as a scavenger for hydroxy radicals: masking test) was added in an amount of 0.5% of the soil weight, and then filled in a 500 ml container, and incubation and subsequent aging were performed under the same operation as the test conditions. The oil concentration was measured (it was confirmed that the addition of mannitol did not change the respiratory activity of soil microorganisms before and after addition).
上記の実験結果を表2に示す。表2から明らかな様に、通気条件によってC重油の浄化性能が異なる結果を得た。1日毎の撹拌を実施した試験区2の通気サイクルにて、C重油汚染土由来の難生分解性汚染物質の分解を最も顕著に図ることができた。 The results of the above experiment are shown in Table 2. As is clear from Table 2, the result that the purification performance of the C heavy oil was different depending on the ventilation condition was obtained. In the aeration cycle of the test section 2 in which the stirring was performed every day, the decomposition of the hardly biodegradable pollutant derived from the C heavy oil-contaminated soil could be most remarkably achieved.
実施例5では、各種汚染物質分解で用いられる資材(過酸化物、有機酸鉄、脂肪酸)と代表的な導電性資材(活性炭、鉄粉)とを組み合わせた場合の汚染浄化性能について評価した。表3にその概要を示す。試験区1〜3は活性炭のみの系、試験区7〜9は鉄粉のみの系、試験区4〜6は鉄粉と活性炭を組み合わせた系を設定した。 In Example 5, the pollution purification performance was evaluated in the case where materials (peroxides, organic acid iron, fatty acids) used for decomposing various pollutants and typical conductive materials (activated carbon, iron powder) were combined. Table 3 shows the outline. Test sections 1 to 3 were set up with a system containing only activated carbon, test sections 7 to 9 were set up with a system containing only iron powder, and test sections 4 to 6 were set up with a system combining iron powder and activated carbon.
なお、各試験区の詳細な設定は、以下とした。黒ボク土を重量濃度で50%含む地下水100mlに対し、「過酸化水素+クエン酸鉄添加」系の試験では、最終濃度として、過酸化水素濃度:10g/L、クエン酸鉄濃度:1g/Lとなるように試験系に添加した。「過硫酸ナトリウム添加」系の試験では、最終濃度として、過硫酸ナトリウム濃度:10g/Lとなるように試験系に添加した。「脂肪酸添加」系の試験では、最終濃度として、市販の脂肪酸資材であるアムテクリーンP(パナソニック環境社製):10g/Lとなるように試験系に添加した。そして、鉄粉および活性炭を、最終濃度総量として10g/Lとなるように、また、全ての系に、培養基材としてIMK培地(和光純薬社製):252mg/Lとなるように、添加した。 The detailed settings for each test section are as follows. In 100 ml of groundwater containing 50% by weight of black soil, in the test of "adding hydrogen peroxide + iron citrate", the final concentrations were hydrogen peroxide concentration: 10 g/L, iron citrate concentration: 1 g/ L was added to the test system. In the test of the "sodium persulfate addition" system, the final concentration was added to the test system so that the sodium persulfate concentration was 10 g/L. In the test of the "fatty acid addition" system, a commercially available fatty acid material, Amteclean P (manufactured by Panasonic Environment Co., Ltd.): 10 g/L was added to the test system as a final concentration. Then, iron powder and activated carbon were added so that the total final concentration was 10 g/L, and IMK medium (manufactured by Wako Pure Chemical Industries, Ltd.): 252 mg/L as a culture substrate was added to all systems. did.
それぞれの反応液を調整後、反応液100mlを500ml容の密栓瓶に入れ、還元系の密栓瓶に対しては、気相を純窒素ガスで置換した後に密栓して、更にテトラクロロエチレン濃度:40mg/Lとなるようにテトラクロロエチレン標準溶液(1mg/ml)を500ml容の密栓瓶の試験系に添加して、15℃に保ったインキュベータ内に保管し、試験を開始した。続いて、反応開始から10日後と30日後に、各試験系の塩素イオン濃度をイオン電極により測定し各試験系におけるテトラクロロエチレンの塩素イオンまでの分解程度を観察した。結果を表4に示す。 After adjusting each reaction solution, 100 ml of the reaction solution was placed in a 500 ml capacity sealed bottle, and for the reducing system sealed bottle, the gas phase was replaced with pure nitrogen gas and then the bottle was sealed, and the tetrachloroethylene concentration was 40 mg/ The tetrachloroethylene standard solution (1 mg/ml) was added to the test system in a 500 ml capacity sealed bottle so as to give L and stored in an incubator kept at 15° C. to start the test. Then, 10 and 30 days after the reaction was started, the chlorine ion concentration of each test system was measured with an ion electrode, and the degree of decomposition of tetrachloroethylene to chlorine ion in each test system was observed. The results are shown in Table 4.
今回の30日間の試験では、分解速度や終点濃度から、程度の差こそあれ、全ての試験系で、それぞれの対照区と比較して有意な塩素イオンの生成たるテトラクロロエチレンの分解が観察された。また、各試験区の比較から、活性炭或いは鉄粉を単独に添加した試験系よりも活性炭と鉄粉の両者が存在する試験系で顕著なテトラクロロエチレンの分解が観察され、特に過硫酸ナトリウムを加えた系で顕著な分解が観察された。
In the present 30-day test, in all test systems, significant decomposition of tetrachloroethylene, which produces chlorine ions, was observed in comparison with the respective control groups, although there was a difference in degree depending on the decomposition rate and the end point concentration. Further, from the comparison of each test section, remarkable decomposition of tetrachloroethylene was observed in the test system in which both activated carbon and iron powder were present, as compared to the test system in which activated carbon or iron powder was added alone, and especially sodium persulfate was added. Significant degradation was observed in the system.
なお、テトラクロロエチレン濃度:40mg/L条件において、完全分解によって生じる塩素イオン濃度は、理論上34.2mg/Lと計算されるが、過硫酸ナトリウムを加えた試験区2、5、8の30日後の塩素イオン濃度は、係る完全分解に近い濃度が観察された。また、これらの過硫酸ナトリウムを加えた系では、10日目の結果を見る限り、活性炭と鉄粉の両者が存在する試験系での分解速度が、最も良いことが分かった。 The concentration of tetrachlorethylene under the condition of 40 mg/L, the chlorine ion concentration generated by complete decomposition is theoretically calculated to be 34.2 mg/L, but after 30 days of test groups 2, 5, and 8 to which sodium persulfate was added, Regarding the chlorine ion concentration, a concentration close to the complete decomposition was observed. In addition, it was found that the system containing these sodium persulfates had the best decomposition rate in the test system in which both activated carbon and iron powder were present as far as the results on the 10th day were seen.
この様に、活性炭存在下でテトラクロロエチレンが完全分解に近い状態までに至ったことから、添加された過硫酸ナトリウムによって、活性炭に吸着されたテトラクロロエチレンまでもが分解されたことが示唆された。即ち、過硫酸ナトリウム添加によって活性炭の再生が可能であることが分かった。 In this way, since tetrachloroethylene reached a state close to complete decomposition in the presence of activated carbon, it was suggested that sodium persulfate added also decomposed tetrachloroethylene adsorbed on the activated carbon. That is, it was found that the activated carbon can be regenerated by adding sodium persulfate.
総じて、各種汚染物質分解で用いられる資材(過酸化物、有機酸鉄、脂肪酸)と代表的な導電性資材(活性炭、鉄粉)とを組み合わせて汚染浄化性能を評価した結果、導電性資材として活性炭と鉄粉の両者が存在する条件下にて、各種汚染物質分解で用いられる資材(過酸化物、有機酸鉄、脂肪酸)を添加することにより、汚染浄化の促進をより一層図ることができること、また、過酸化物としては、過硫酸ナトリウムが好ましく、本剤を用いることによって、汚染が吸着した活性炭の再生が可能であることが分かった。 In general, as a result of evaluating the pollution purification performance by combining materials used for decomposing various pollutants (peroxides, organic acid iron, fatty acids) and typical conductive materials (activated carbon, iron powder), as a conductive material It is possible to further promote pollution purification by adding materials (peroxides, organic iron oxides, fatty acids) used in the decomposition of various pollutants under the condition that both activated carbon and iron powder are present. Also, it was found that sodium persulfate is preferable as the peroxide, and the use of this agent makes it possible to regenerate the activated carbon having adsorbed the pollution.
実施例6では、導電性資材の付着性物質による機能低下の再生を、井戸様構造物を利用して図る際の通気・撹拌操作に関する評価を実施した。 In Example 6, an evaluation was carried out regarding aeration/agitation operation when the well-like structure was used to regenerate the functional deterioration of the conductive material due to the adherent substance.
(実験1)本実験は、井戸様構造物が有する多区間のストレーナからの通気影響範囲に関する考察を得るために実施した。
地下水位がGL‐1.8mに存在し、GL‐9.5mの粘土シルト層を基底とする、細砂〜中砂を主体として構成される第一帯水層を有するサイトにて、25cmストレーナ区間4箇所(井戸底から、A区間:25−50、B区間:100−125、C区間:175−200、D区間:250−275cm区間)を有するφ50mmの井戸様構造物を設置した。
また、その井戸様構造物から直線距離で、0.5m、1.0m、1.5m、2.0mの位置に全層ストレーナを有する観測井戸を設置した。続いて、各ストレーナからの通気量を、圧縮空気を用いて10L/分の強度となるようにマスフローメータを用いて調整した。上記設定の下、最下部のストレーナから順次通気を実施して、1昼夜経過後における観測井戸での発泡状況から、各通気条件における通気影響範囲を求めた。
また上記にて一連の試験を実施した後に、A区間のみから40L/分の強度での通気を行なう実験を併せて実施した。結果を表5に示す。
(Experiment 1) This experiment was conducted in order to obtain a consideration on the range of the influence of ventilation from the strainer in multiple sections of the well-like structure.
A 25 cm strainer is located at a site with a groundwater level of GL-1.8 m and a GL-9.5 m clay silt layer as the base and a first aquifer mainly composed of fine sand to medium sand. A φ50 mm well-like structure having four sections (from the bottom of the well, section A: 25-50, section B: 100-125, section C: 175-200, section D: 250-275 cm) was installed.
In addition, observation wells having all-layer strainers were installed at positions of 0.5 m, 1.0 m, 1.5 m, and 2.0 m in a linear distance from the well-like structure. Subsequently, the air flow rate from each strainer was adjusted using compressed air using a mass flow meter so that the strength was 10 L/min. Under the above settings, ventilation was sequentially performed from the bottom strainer, and the ventilation influence range under each ventilation condition was determined from the foaming condition in the observation well after one day and night.
In addition, after conducting a series of tests as described above, an experiment was also conducted in which ventilation was performed from only section A at a strength of 40 L/min. The results are shown in Table 5.
(実験2)続いて、井戸様構造物からの通気による撹拌効果を検証する目的で、過酸化物の代用として、約1%食塩溶液を400L用意し、通気開始前の4区間のストレーナからそれぞれ100Lを注入後、4区間のストレーナから10L/分の強度となるように通気を実施した。以後、経過時間毎に各観測井戸における電気伝導度を測定し、通気の撹拌効果について考察を実施した。 (Experiment 2) Subsequently, for the purpose of verifying the stirring effect by aeration from the well-like structure, 400 L of a 1% saline solution was prepared as a substitute for the peroxide, and each strainer from the 4 sections before the start of aeration was used. After injecting 100 L, ventilation was performed from a strainer in 4 sections so that the strength was 10 L/min. After that, the electrical conductivity of each observation well was measured at each elapsed time, and the stirring effect of aeration was considered.
結果、本試験条件において概ね3日間を経過すると、各観測井戸での電気伝導度が50〜100μS/cmの範囲に収束することが分かり、多区間ストレーナを有する井戸様構造物からの気体通気による一定エリア内の撹拌が可能であることが示された。 As a result, it was found that the electric conductivity in each observation well converges in the range of 50 to 100 μS/cm after about 3 days under the test conditions, and the gas aeration from the well-like structure having a multi-section strainer It was shown that stirring within a certain area is possible.
以上、本発明の実施例を説明してきたが、具体的な構成は前述した実施例に限られるものではなく、本発明の要旨を逸脱しない範囲における変更や追加があっても本発明に含まれる。 Although the embodiments of the present invention have been described above, the specific configuration is not limited to the above-described embodiments, and modifications and additions within the scope of the present invention are included in the present invention. ..
本発明は、法定の第一種特定有害物質及びそれに類する有害物質による未知の土壌汚染に対し、初期汚染の早期発見と早期移動/拡散抑制対策を可能とする、未然措置に対するフェイル・セーフを果たす、応急対策技術として、特に適用することができる。
また、既知の汚染に関しては、有害物質の移動/拡散抑制、土壌からの低溶出化、鉄還元細菌叢によるバイオプリベンション、導電性資材を活用したスポット浄化を図る応急対策技術として、特に適用することができる。
The present invention achieves fail-safe against unanticipated measures that enables early detection of early pollution and early migration/dispersion suppression measures against unknown soil pollution caused by legally designated Class I specified harmful substances and similar substances. It can be applied especially as an emergency measure technology.
In addition, regarding known pollution, it is especially applied as an emergency measure technology for suppressing migration/diffusion of harmful substances, low elution from soil, bioprevention by iron-reducing bacterial flora, and spot purification using conductive materials. be able to.
1…導電性資材
2…立体導電網
3…鉄還元細菌を包含する微生物群集
4…生分解性を呈し有害物質を包含する汚染物質
5…酸化的土壌粒子
6…還元的土壌粒子
7…飽和帯嫌気的環境域
8…飽和帯好気的環境域
9…清浄表層地下水
10…自然地下水流向
11…不溶性鉄化合物
12…漏洩地点
13…二酸化炭素ガス
14…二酸化炭素ガス濃度分布
15…調査メッシュ
16…調査地点
17…地表
18…不飽和帯
19…採取孔
20…飽和帯
21…バイオマット境界
22…導電性ワイヤ
23…鉄還元細菌群
24…嫌気性(共生)細菌群
25…多重分配継手
26…ストレーナ(有孔)管
27…流体移送管
28…注入気体流
29…注入過酸化物溶液の撹拌流
30…流体移送外管群
31…流体移送内管
32…流体移送管固定具
33…無孔管
DESCRIPTION OF SYMBOLS 1... Conductive material 2... Steric conductive net 3... Microbial community 4 containing iron-reducing bacteria 4... Pollutant 5 exhibiting biodegradability and containing harmful substances 5... Oxidizing soil particles 6... Reducing soil particles 7... Saturation zone Anaerobic environment area 8... Saturated zone Aerobic environment area 9... Clean surface groundwater 10... Natural groundwater flow direction 11... Insoluble iron compound 12... Leakage point 13... Carbon dioxide gas 14... Carbon dioxide gas concentration distribution 15... Survey mesh 16... Survey point 17... Surface 18... Unsaturated zone 19... Collection hole 20... Saturation zone 21... Biomat boundary 22... Conductive wire 23... Iron-reducing bacteria group 24... Anaerobic (symbiotic) bacteria group 25... Multiple distribution joint 26... Strainer (perforated) pipe 27... Fluid transfer pipe 28... Injection gas flow 29... Stirring flow of injected peroxide solution 30... Fluid transfer outer tube group 31... Fluid transfer inner tube 32... Fluid transfer tube fixture 33... No hole tube
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