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JP7557428B2 - Method for culturing purifying bacteria and purification method - Google Patents
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JP7557428B2 - Method for culturing purifying bacteria and purification method - Google Patents

Method for culturing purifying bacteria and purification method Download PDF

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JP7557428B2
JP7557428B2 JP2021087384A JP2021087384A JP7557428B2 JP 7557428 B2 JP7557428 B2 JP 7557428B2 JP 2021087384 A JP2021087384 A JP 2021087384A JP 2021087384 A JP2021087384 A JP 2021087384A JP 7557428 B2 JP7557428 B2 JP 7557428B2
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雅子 伊藤
陽 高畑
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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NPMD NPMD NITE P-1471NITE P-1471

本発明は、揮発性有機塩素化合物で汚染された地下水を浄化するための浄化菌の培養方法および浄化方法に関する。 The present invention relates to a method for culturing purification bacteria and a purification method for purifying groundwater contaminated with volatile organic chlorine compounds.

微生物を用いる浄化技術は、排水処理における活性汚泥法や嫌気処理法などに広く利用されている。また、近年では、有害化学物質で汚染された土壌や地下水を微生物により浄化する技術(バイオレメディエーション)が、環境負荷および浄化コストの小さい浄化方法として着目されている。
代表的な揮発性有機塩素化合物(VOCs)であるテトラクロロエチレン(PCE)やトリクロロエチレン(TCE)などの塩素化エチレン類は、油に対する洗浄力の強い安価な溶剤として、金属産業、半導体産業、ドライクリーニング店など幅広い分野で使用されている。その一方、塩素化エチレン類による土壌や地下水汚染について多くの報告があり、社会問題となっている。
塩素化エチレン類のバイオレメディエーションには、「テトラクロロエチレン(PCE)→トリクロロエチレン(TCE)→シス-1,2-ジクロロエチレン(cis-DCE)→クロロエチレン(VCM)→エチレン」という還元的脱塩素化反応(化1)により塩素化エチレン類を無害化する嫌気性脱塩素化菌を利用している。
Purification technologies using microorganisms are widely used in the activated sludge and anaerobic treatment processes for wastewater treatment, etc. In recent years, bioremediation, a technology that uses microorganisms to purify soil and groundwater contaminated with hazardous chemicals, has been attracting attention as a purification method with low environmental impact and purification costs.
Chlorinated ethylenes such as tetrachloroethylene (PCE) and trichloroethylene (TCE), which are representative volatile organic compounds (VOCs), are used as inexpensive solvents with strong cleaning power against oil in a wide range of fields such as the metal industry, semiconductor industry, dry cleaning shops, etc. On the other hand, there have been many reports of soil and groundwater contamination by chlorinated ethylenes, which has become a social problem.
The bioremediation of chlorinated ethylenes utilizes anaerobic dechlorinating bacteria that render chlorinated ethylenes harmless through the reductive dechlorination reaction (chemical formula 1) of tetrachloroethylene (PCE) → trichloroethylene (TCE) → cis-1,2-dichloroethylene (cis-DCE) → chloroethylene (VCM) → ethylene.

Figure 0007557428000001
Figure 0007557428000001

嫌気性脱塩素化菌の一種であるデハロコッコイデス(Dehalococcoides)属細菌は、cis-DCE以降の脱塩素化を進行できることが報告されている唯一の細菌である。すなわち、塩素化エチレン類のバイオレメディエーションにおいて、処理対象土壌中にデハロコッコイデス属細菌が存在しないと、cis-DCEまでしか脱塩素化できない。また、デハロコッコイデス属細菌が存在していたとしても、環境中でのデハロコッコイデス属細菌の菌体量は非常に少なく、その増殖速度も遅いため、浄化期間が長期化するという課題がある。
このような課題を解決するために、デハロコッコイデス属細菌を人為的に培養して増加させ、浄化対象とする環境に導入して浄化を促進させる方法(バイオオーグメンテーション)が期待されている。本発明者らは、特許文献1において、国内で初めて、デハロコッコイデス・エスピーUCH007株(NITE P-1471、以下、UCH007株ともいう)を単離し、このUCH007株を用いる塩素化エチレン類の浄化方法を提案している。
また、デハロコッコイデス属細菌は、電子供与体として水素のみを利用するとされている(非特許文献1)。そのため、これまでデハロコッコイデス属細菌の培養は、窒素と水素の混合ガス雰囲気下のみで行われていた。しかし、本発明者らは、ピルビン酸又はその塩を含む培地を用いる培養方法を提案している(特許文献2)。この培養方法によれば、ピルビン酸を炭素源としてだけでなく、電子供与体としても作用させることができるため、水素ガスが不要となり、安全な環境下でデハロコッコイデス属細菌を培養できる。更に、本発明者らは、上記方法で純粋培養した培養液を汚染地盤に注入する方法として、不活性ガス(窒素ガス)と注入管を利用して、絶対嫌気性の浄化菌が死滅しないように、空気(酸素)に触れずに供給する方法を提案している(特許文献3)。
UCH007株を用いる一連の浄化技術は、揮発性有機塩素化合物(VOCs)汚染サイトにおいて浄化効果が実証されている。しかし、当該技術は、浄化菌を導入せずに土着のデハロコッコイデス属細菌を活性化させる浄化方法(バイオスティミュレーション)よりもコストが高いものである。その原因として、浄化菌の培養費用が高いことが挙げられる(非特許文献2参照)。
Dehalococcoides bacteria, a type of anaerobic dechlorinating bacteria, are the only bacteria that have been reported to be capable of dechlorinating chloroethylenes to cis-DCE and beyond. In other words, in bioremediation of chlorinated ethylenes, if Dehalococcoides bacteria are not present in the soil to be treated, dechlorination can only be performed to cis-DCE. Even if Dehalococcoides bacteria are present, the amount of Dehalococcoides bacteria in the environment is very small and their proliferation rate is slow, which results in a problem of a long purification period.
In order to solve such problems, a method of artificially culturing and increasing bacteria of the genus Dehalococcoides and introducing them into the environment to be purified to promote purification (bioaugmentation) is expected. In Patent Document 1, the present inventors isolated Dehalococcoides sp. UCH007 strain (NITE P-1471, hereinafter also referred to as UCH007 strain) for the first time in Japan, and proposed a method for purifying chlorinated ethylenes using this UCH007 strain.
In addition, Dehalococcoides bacteria are said to use only hydrogen as an electron donor (Non-Patent Document 1). Therefore, Dehalococcoides bacteria have been cultivated only under a mixed gas atmosphere of nitrogen and hydrogen. However, the present inventors have proposed a cultivation method using a medium containing pyruvic acid or a salt thereof (Patent Document 2). According to this cultivation method, pyruvic acid can be used not only as a carbon source but also as an electron donor, making hydrogen gas unnecessary and allowing Dehalococcoides bacteria to be cultivated in a safe environment. Furthermore, the present inventors have proposed a method of injecting the culture solution purely cultivated by the above method into the contaminated ground by using an inert gas (nitrogen gas) and an injection pipe to supply the culture solution without contacting air (oxygen) so that the absolutely anaerobic purification bacteria are not killed (Patent Document 3).
A series of purification techniques using the UCH007 strain have been demonstrated to be effective in purifying sites contaminated with volatile organic chlorine compounds (VOCs). However, this technique is more expensive than a purification method that activates indigenous Dehalococcoides bacteria without introducing purification bacteria (biostimulation). The reason for this is the high cost of culturing the purification bacteria (see Non-Patent Document 2).

特許第6103518号公報Patent No. 6103518 特開2021-016368号公報JP 2021-016368 A 特願2020-073529号公報Patent Application No. 2020-073529 特許第6698357号公報Patent No. 6698357 特開2021-016369号公報JP 2021-016369 A

Loffler, F.E., Yan, J., Ritalahti, K.M., Adrian, L., Edwards, E.A., Konstantinidis, K.T., Muller, J.A., Fullerton, H., Zinder, S.H. & Spormann, A.M. " Dehalococcoides mccartyi gen. nov., sp. nov., obligately organohalide-respiring anaerobic bacteria relevant to halogen cycling and bioremediation, belong to a novel bacterial class, Dehalococcoidia classis nov., order Dehalococcoidales ord. nov. and family Dehalococcoidaceae fam. nov., within the phylum Chloroflexi." Int. J. Syst. Evol. Microbiol.,2013年,63: p.625-635.Loffler, F.E., Yan, J., Ritalahti, K.M., Adrian, L., Edwards, E.A., Konstantinidis, K.T., Muller, J.A., Fullerton, H., Zinder, S.H. & Spormann, A.M. " Dehalococcoides mccartyi gen. nov., sp. nov., obligately organohalide-respiring anaerobic bacteria relevant to halogen cycling and bioremediation, belong to a novel bacterial class, Dehalococcoidia classis nov., order Dehalococcoidales ord. nov. and family Dehalococcoidaceae fam. nov., within the phylum Chloroflexi." Int. J. Syst. Evol. Microbiol.,2013,63: p.625-635. https://www.env.go.jp/press/108518.htmlにおける添付書類(114877)Attached document (114877) at https://www.env.go.jp/press/108518.html Journal of Environmental Biotechnology, Vol.13, No.1, p13-18, 2013Journal of Environmental Biotechnology, Vol.13, No.1, p13-18, 2013

先に、本発明者らは、必要とする浄化菌を浄化サイトに設けられた簡易施設で培養して、迅速に供給する方法を提案した(特許文献4)。本技術は、培養過程にオートクレーブを用いず、蒸留水が入った容器で浄化菌の培養を現地で行う技術である。しかしながら、本技術は通性嫌気性細菌を対象としており、酸素に触れると死滅する絶対嫌気性細菌には適用できない。 Previously, the inventors proposed a method for cultivating the necessary purification bacteria in a simple facility set up at the purification site and quickly supplying it (Patent Document 4). This technology does not use an autoclave in the cultivation process, but cultivates the purification bacteria on-site in a container filled with distilled water. However, this technology targets facultative anaerobic bacteria and cannot be applied to obligate anaerobic bacteria that die when exposed to oxygen.

純粋培養ではない様々な細菌が存在する中でデハロ菌を含む菌液を浄化に用いて、浄化効果が得られることが明らかとなっている(非特許文献3)。様々な細菌が存在する混合菌の中で特定の有用菌の培養を行う場合、厳重に管理された大型培養槽(ファーメンター)が用いられている。ファーメンターを浄化サイトに設置することはコストが高く難しいため、菌液は専用の培養施設に設置されているファーメンターで培養したものを容器に移し替えて現地に輸送している。 It has been revealed that a purification effect can be obtained by using a bacterial liquid containing Dehalobacteria in the presence of various bacteria that are not pure cultures (Non-Patent Document 3). When culturing specific useful bacteria in a mixture of various bacteria, a large, strictly controlled culture tank (fermenter) is used. Since it is costly and difficult to install a fermenter at the purification site, the bacterial liquid is cultured in a fermenter installed in a dedicated cultivation facility, transferred to a container, and transported to the site.

特許文献2、特許文献5では、培養容器としてビア樽を用いている。この方法によれば、培養したものをそのまま輸送して現地に持ち込み、特許文献3に記載の方法で浄化サイトに注入することができる。図1に具体的な操作のフロー図を示した。浄化サイトに、オートクレーブ、水道施設、窒素ボンベなどの装置を有する温度管理可能な培養室があれば、現地で培養が行えるため、菌液の輸送が不要となる。しかし、培養室の設置には一定のコストがかかる。また、培養基質となる蒸留水を大量に確保する必要もあるため、浄水器もしくは蒸留水を購入する必要がある。 In Patent Document 2 and Patent Document 5, beer barrels are used as the culture vessels. With this method, the cultured material can be transported as is to the site and then injected into the purification site using the method described in Patent Document 3. A specific operation flow diagram is shown in Figure 1. If the purification site has a temperature-controlled culture room equipped with equipment such as an autoclave, water supply system, and nitrogen cylinder, the culture can be carried out on-site, eliminating the need to transport the bacterial liquid. However, setting up a culture room incurs a certain cost. In addition, it is necessary to secure a large amount of distilled water as the culture substrate, so a water purifier or distilled water must be purchased.

培養におけるコスト分析を行うと、特許文献5で用いる還元剤(グルタチオン)のコスト比率が高い。還元剤を用いる理由は、培地中の酸素を除去して培養液を嫌気性のデハロ菌が増殖できる還元状態に培養液を調整するためである。培養基質に蒸留水の代わりに水道水を用いれば浄水器は不要になるが、水道水は酸素濃度が高く、ほぼ飽和状態で酸素が存在しているため、還元剤を多く入れなければ嫌気状態を形成できないという課題があった。 When a cost analysis of the culture is performed, the cost ratio of the reducing agent (glutathione) used in Patent Document 5 is high. The reason for using a reducing agent is to remove oxygen from the medium and adjust the culture liquid to a reducing state in which anaerobic Dehalobacteria can grow. If tap water is used instead of distilled water as the culture substrate, a water purifier is not necessary, but tap water has a high oxygen concentration and oxygen is present in a nearly saturated state, so there is a problem that an anaerobic state cannot be created unless a large amount of reducing agent is added.

本発明は、上記の事情に鑑みてなされたものである。すなわち、本発明の課題は、培養液の滅菌処理や還元剤の添加を必要とせずに、浄化に必要な浄化菌を簡便に培養することができ、絶対嫌気性細菌にも適用可能であり、浄化菌を地盤に導入した際に良好な浄化効果を得ることが可能な浄化菌の培養方法および当該浄化菌を用いた浄化方法を提供することである。 The present invention has been made in consideration of the above circumstances. That is, the object of the present invention is to provide a method for culturing purifying bacteria that can easily culture the purifying bacteria necessary for purification without requiring sterilization of the culture solution or the addition of a reducing agent, that is also applicable to obligate anaerobic bacteria, and that can obtain a good purification effect when the purifying bacteria are introduced into the ground, and a purification method using the purifying bacteria.

本発明者らは、培養基質となる蒸留水の代わりに、現地で入手できる地下水を培養液として用いることによって、上記課題を解決できることを見出し、本発明に到達することができた。すなわち、本発明は以下のような構成を有するものである。
(1)揮発性有機塩素化合物で汚染された地下水を浄化するための浄化菌の培養方法であって、前記浄化菌が、嫌気性の浄化菌であり、前記地下水が存在する帯水層から採取した前記地下水にトリクロロエチレンを添加して培養液として用い、前記培養液の滅菌処理を行わず、前記地下水と有機物と酸化還元指示薬を含む培養液を密栓可能な容器に入れ、気相部を窒素で置換した後に一定期間静置し、前記培養液の酸化還元指示薬が変色して酸化還元電位が低下したことを確認した後に、前記培養液に前記浄化菌を添加することを特徴とする浄化菌の培養方法。
(2)揮発性有機塩素化合物で汚染された地下水を浄化するための浄化菌の培養方法であって、前記浄化菌が、嫌気性の浄化菌であり、前記地下水が存在する帯水層から採取した前記地下水にトリクロロエチレンを添加して培養液として用い、前記培養液に還元剤を添加せず、前記地下水と有機物と酸化還元指示薬を含む培養液を密栓可能な容器に入れ、気相部を窒素で置換した後に一定期間静置し、前記培養液の酸化還元指示薬が変色して酸化還元電位が低下したことを確認した後に、前記培養液に前記浄化菌を添加することを特徴とする浄化菌の培養方法。
(3)前記培養液に還元剤を添加しない(1)に記載の浄化菌の培養方法。
(4)前記浄化菌が、デハロコッコイデス属細菌のデハロコッコイデス・エスピーUCH007株(NITE P-1471)である(1)~(3)のいずれか1項に記載の浄化菌の培養方法。
(5)揮発性有機塩素化合物で汚染された地下水を浄化菌を用いて浄化する浄化方法であって、前記浄化菌が、嫌気性の浄化菌であり、培養容器内において、培養液の中から酸素を除去する培養液酸素除去工程と、前記培養容器内の前記培養液中で前記浄化菌を増殖させる培養工程と、前記地下水が存在する帯水層に前記培養液を注入するための注入管を設置する注入管設置工程と、前記注入管の内部の酸素を除去する注入管内酸素除去工程と、前記帯水層に有機物溶液を供給して一定期間放置することで嫌気的な地盤を形成する有機物溶液供給工程と、前記帯水層に前記浄化菌を増殖させた前記培養液を供給する培養液供給工程と、を備え、前記培養液供給工程で供給される前記浄化菌が、前記培養工程において、(1)~(4)のいずれか1項に記載された浄化菌の培養方法を用いて培養されたものであることを特徴とする浄化方法。
The present inventors have found that the above-mentioned problems can be solved by using locally available groundwater as a culture solution instead of distilled water as a culture substrate, and have arrived at the present invention. That is, the present invention has the following configuration.
(1) A method for culturing purification bacteria for purifying groundwater contaminated with volatile organic chlorine compounds, the purification bacteria being anaerobic purification bacteria, the purification bacteria being characterized in that trichloroethylene is added to the groundwater collected from an aquifer in which the groundwater exists to prepare a culture solution, the culture solution containing the groundwater, organic matter, and an oxidation-reduction indicator is placed in a sealable container without sterilizing the culture solution, the gas phase is replaced with nitrogen, and the culture solution is allowed to stand for a certain period of time, and after confirming that the oxidation-reduction indicator in the culture solution has changed color and the oxidation-reduction potential has decreased, the purification bacteria are added to the culture solution .
(2) A method for culturing purification bacteria for purifying groundwater contaminated with volatile organic chlorine compounds, the purification bacteria being anaerobic purification bacteria, the purification bacteria being characterized in that trichloroethylene is added to the groundwater collected from an aquifer in which the groundwater exists to prepare a culture solution, no reducing agent is added to the culture solution, the culture solution containing the groundwater, organic matter, and an oxidation-reduction indicator is placed in a sealable container, the gas phase is replaced with nitrogen, and the culture solution is allowed to stand for a certain period of time, and after confirming that the oxidation-reduction indicator in the culture solution has changed color and the oxidation-reduction potential has decreased, the purification bacteria are added to the culture solution.
(3) The method for culturing a purifying bacterium according to (1), in which no reducing agent is added to the culture solution.
(4) The method for culturing a purifying bacterium according to any one of (1) to (3), wherein the purifying bacterium is a Dehalococcoides sp. UCH007 strain (NITE P-1471) belonging to the genus Dehalococcoides.
(5) A method for purifying groundwater contaminated with volatile organic chlorine compounds using purification bacteria, the purification bacteria being anaerobic purification bacteria, the purification method comprising: a culture solution oxygen removal step of removing oxygen from a culture solution in a culture vessel; a culture step of growing the purification bacteria in the culture solution in the culture vessel; an injection pipe installation step of installing an injection pipe for injecting the culture solution into an aquifer in which the groundwater is present; an injection pipe oxygen removal step of removing oxygen inside the injection pipe; an organic solution supply step of supplying an organic solution to the aquifer and leaving it for a certain period of time to form an anaerobic ground; and a culture solution supply step of supplying the culture solution in which the purification bacteria have grown to the aquifer, the purification bacteria supplied in the culture solution supply step being cultured in the culture step using the purification bacteria culture method described in any one of (1) to (4) .

本発明の浄化菌の培養方法及び浄化方法は、培養液の滅菌処理や還元剤の添加を必要とせずに、浄化に必要な浄化菌を簡便に培養することができ、絶対嫌気性細菌にも適用可能であり、浄化菌を地盤に導入した際に良好な浄化効果を得ることができる。 The method for cultivating and purifying purifying bacteria of the present invention can easily cultivate the purifying bacteria necessary for purification without the need for sterilization of the culture solution or the addition of a reducing agent, and can also be applied to strictly anaerobic bacteria, and can provide a good purification effect when the purifying bacteria are introduced into the ground.

従来の浄化菌の培養方法のフロー図である。FIG. 1 is a flow diagram of a conventional method for cultivating purifying bacteria. 本発明の浄化菌の培養方法のフロー図である。FIG. 1 is a flow chart of a method for culturing purifying bacteria according to the present invention. 実験例1の地下水培地、通常培地における増殖後のデハロコッコイデス属細菌(UCH007株)の菌数を示す図である。FIG. 1 is a graph showing the number of bacteria of the genus Dehalococcoides (UCH007 strain) after growth in groundwater medium and normal medium in Experimental Example 1. 実験例2の地下水培地、通常培地における増殖後のデハロコッコイデス属細菌(UCH007株)の菌数を示す図である。FIG. 13 is a graph showing the number of bacteria of the genus Dehalococcoides (UCH007 strain) after growth in groundwater medium and normal medium in Experimental Example 2. 実験例3の地下水培地におけるVOCs分解活性を示す図である。FIG. 13 is a graph showing VOCs decomposition activity in a groundwater medium in Experimental Example 3. 実験例3の通常培地におけるVOCs分解活性を示す図である。FIG. 1 shows the VOCs decomposition activity in a normal medium in Experimental Example 3. 実験例4の地下水培地、通常培地における増殖後のデハロコッコイデス属細菌(UCH007株)の菌数を示す図である。FIG. 13 is a graph showing the number of bacteria of the genus Dehalococcoides (UCH007 strain) after growth in groundwater medium and normal medium in Experimental Example 4. 実験例5の培養7日目の地下水のVOCs濃度を示す図である。FIG. 13 is a graph showing the VOCs concentration in groundwater on the 7th day of culture in Experimental Example 5. 実験例5の培養16日目の地下水のVOCs濃度を示す図である。FIG. 13 is a graph showing the VOCs concentration in groundwater on the 16th day of culture in Experimental Example 5. 実験例5の培養16日目における初期濃度からのVOCsの残存率を示す図である。FIG. 13 is a graph showing the residual rate of VOCs from the initial concentration on the 16th day of culture in Experimental Example 5. 実験例5の培養16日目のUCH007の遺伝子コピー数を示す図である。FIG. 13 shows the gene copy number of UCH007 on the 16th day of culture in Experimental Example 5. 実験例5の培養開始から培養16日目におけるUCH007遺伝子コピー数の増加率を示す図である。FIG. 13 shows the increase rate of UCH007 gene copy number from the start of culture to day 16 of culture in Experimental Example 5. 実験例5の培養16日目における地下水中のvcrAの濃度を示す図である。FIG. 13 is a graph showing the concentration of vcrA in groundwater on the 16th day of culture in Experimental Example 5.

本発明の実施形態について説明する。但し、本発明の実施形態は、以下の実施形態に限定されるものではない。
本発明は、絶対嫌気性細菌であるデハロコッコイデス属細菌等の培養において、還元剤を添加せず、最低限の装置を用いて、現地で菌液を培養する方法を考案したものである。本発明の浄化菌の培養方法における代表的な手順1~5を以下に示す。以下では、培養の対象となる浄化菌として、絶対嫌気性の浄化菌であるデハロコッコイデス属細菌を例に挙げて、説明する。
An embodiment of the present invention will be described below. However, the embodiment of the present invention is not limited to the following embodiment.
The present invention has devised a method for culturing obligate anaerobic bacteria such as Dehalococcoides bacteria on-site using a minimum amount of equipment without adding a reducing agent. Representative steps 1 to 5 in the method for culturing purifying bacteria of the present invention are shown below. In the following, an explanation will be given using obligate anaerobic purifying bacteria, Dehalococcoides bacteria, as an example of the purifying bacteria to be cultured.

[手順1] 培養基質(培養液の溶媒)
培養基質として酸素濃度ができるだけ低い液体を用いて培養するため、浄化を行うサイトもしくはサイト近傍で帯水層から揚水した酸素濃度の低い地下水を用いる。当該地下水は、酸素濃度が低ければ、汚染されていなくても、浄化対象とする汚染物質(例えばトリクロロエチレン)で汚染されていても、どちらでも良い。また、微生物浄化等を行った結果、有機物が混入している状態の地下水を用いても良い。
[Step 1] Culture substrate (solvent for culture medium)
In order to use a liquid with as low an oxygen concentration as possible as the culture substrate, groundwater with a low oxygen concentration pumped from an aquifer at or near the site where purification is performed is used. As long as the groundwater has a low oxygen concentration, it may be either uncontaminated or contaminated with the pollutant to be purified (e.g., trichloroethylene). In addition, groundwater that has been contaminated with organic matter as a result of microbial purification or the like may be used.

菌液の地盤への注入が可能な密閉可能な培養容器に、予め必要な薬剤を入れて、地下水と混合して溶解させて、培養液を作成する。地下水に溶解させる薬剤は、例えば、窒素、リンなどの無機塩類(表1~3参照)、還元剤、有機物等である。表1には無機栄養源である基礎培地の成分組成を示した。表2と表3にはそれぞれ、基礎培地中の成分である微量元素溶液Aと微量元素溶液Bの成分組成を示した。培養容器については、特許文献3や特許文献5に記載があるが、5ガロンのビア樽(コーネリアスタイプ)などが使用できる。還元剤は添加することもできるが、添加しなくてもよい。これにより、蒸留水や水道水を使用する必要がなくなり、コストを低減できるだけでなく、水道施設が整っていないサイトにおいても現地で培養を行うことが可能となる。 The necessary chemicals are added to a sealable culture vessel that can be used to inject the bacterial liquid into the ground, and the mixture is mixed with groundwater to dissolve the chemicals, creating a culture solution. Examples of chemicals to be dissolved in groundwater include inorganic salts such as nitrogen and phosphorus (see Tables 1 to 3), reducing agents, and organic substances. Table 1 shows the composition of the basal medium, which is an inorganic nutrient source. Tables 2 and 3 show the composition of trace element solutions A and B, which are components of the basal medium. The culture vessel is described in Patent Document 3 and Patent Document 5, but a 5-gallon beer barrel (Cornelius type) can be used. A reducing agent can be added, but it is not necessary to add one. This eliminates the need to use distilled water or tap water, which not only reduces costs but also makes it possible to culture on-site at sites without water facilities.

Figure 0007557428000002
Figure 0007557428000002

Figure 0007557428000003
Figure 0007557428000003

Figure 0007557428000004
Figure 0007557428000004

[手順2] 窒素パージ
培養容器に地下水を所定量入れて密栓した状態で、窒素ガス発生装置を用いて、培養容器中の気相部を窒素パージ(窒素置換)する。窒素ガス発生装置としては、PSA(Pressure Swing Adsorption)方式の窒素ガス発生装置を用いることが好ましい。
窒素パージする方法として、培養容器中に作成した培養液500mLに対して、窒素ガス発生装置から発生した窒素ガスを0.5L/minの供給量で10分間パージを行い、培養容器中の酸素を極力低減させることができる。
[Step 2] Nitrogen purging: With a specified amount of groundwater in the culture vessel and the vessel sealed, the gas phase in the culture vessel is purged with nitrogen (nitrogen replacement) using a nitrogen gas generator. As the nitrogen gas generator, a PSA (Pressure Swing Adsorption) type nitrogen gas generator is preferably used.
The nitrogen purging method involves purging 500 mL of culture solution prepared in a culture vessel with nitrogen gas generated from a nitrogen gas generator at a supply rate of 0.5 L/min for 10 minutes, thereby minimizing oxygen in the culture vessel.

[手順3] TCEの添加
培養液中に、トリクロロエチレン(TCE)溶液を終濃度が0.6~2.5ml/Lになるように添加する。
[Procedure 3] Addition of TCE Add a trichloroethylene (TCE) solution to the culture medium to a final concentration of 0.6 to 2.5 ml/L.

[手順4] 嫌気状態の形成
デハロコッコイデス属細菌が増殖しやすい20~30℃の温度(温度に関する情報は、特開2021-13911号公報参照)で静置培養を行う。そして、培地中のデハロコッコイデス属細菌以外の細菌によって、培養容器中に残存する酸素や硝酸性窒素が消費されて、培養容器内のデハロコッコイデス属細菌が増殖可能な嫌気状態となるのを待つ。還元剤を使用せず、滅菌処理をしないことで、地下水に含まれる細菌群が有機物を消費して、嫌気状態を形成することとなる。嫌気状態の確認には、培養液中に添加した酸化還元指示薬(たとえばレサズリンナトリウムなど)が青紫色(ピンク)から透明に変色していることを目視で確認する。
[Step 4] Creation of anaerobic conditions Static culture is performed at a temperature of 20 to 30 ° C (for information on temperature, see JP 2021-13911 A), at which the Dehalococcoides bacteria are likely to grow. Then, wait until the remaining oxygen and nitrate nitrogen in the culture vessel are consumed by bacteria other than the Dehalococcoides bacteria in the medium, creating an anaerobic state in which the Dehalococcoides bacteria in the culture vessel can grow. By not using a reducing agent and not sterilizing the culture vessel, the bacteria in the groundwater consume organic matter and create an anaerobic state. To confirm the anaerobic state, visually check that the redox indicator (such as resazurin sodium) added to the culture solution has changed color from blue-purple (pink) to transparent.

培養に用いる密閉容器は、コストと安全面を考慮し、通常はステンレス製のものを使用することが多い。ステンレス製の密閉容器を使用すると、外側から内部の状況を視認できない。そのような容器の場合には、注射針付の透明な注射器を用いる。具体的には、開口部から注射針を空気が入らないように刺し、刺した注射針が培養液面に届くように培養容器を傾ける、又は容器を逆さにする。そして、培養液の着色の様子が確認できるように、プランジャーを僅かに引いて、注射器内部に培養液を取り出し、培養液中に添加した酸化還元指示薬による着色の状況を目視で確認する。確認後は、引いたプランジャーを押し戻して、培養液を容器内に戻し、容器内に空気が入らないようにして、注射針を開口部から抜く。 In consideration of cost and safety, stainless steel sealed containers are usually used for culturing. When a stainless steel sealed container is used, the inside cannot be seen from the outside. In the case of such a container, a transparent syringe with a needle is used. Specifically, the needle is inserted from the opening without allowing air to enter, and the culture container is tilted or turned upside down so that the inserted needle reaches the surface of the culture fluid. Then, the plunger is slightly pulled back to remove the culture fluid into the syringe so that the color of the culture fluid can be confirmed, and the color caused by the redox indicator added to the culture fluid is visually confirmed. After confirmation, the plunger is pushed back to return the culture fluid to the container, and the needle is removed from the opening while making sure that no air enters the container.

[手順5] 純粋培養した浄化菌の植菌・静置培養
培養液が還元状態になっていることを確認した後、純粋培養した種菌(UCH007株:1×10cells/ml程度、UCH001株:1×10cells/ml程度)を培地に対して0.1~1%の割合で植菌して、再び静置で培養する。その後、培養14日以内にデハロコッコイデス属細菌を10cells/ml以上の濃度まで増殖させる。
[Step 5] Inoculation and static culture of pure cultured purifying bacteriaAfter confirming that the culture solution is in a reducing state, pure cultured seed bacteria (UCH007 strain: approximately 1 x 10 cells/ml, UCH001 strain: approximately 1 x 10 cells/ml) are inoculated into the medium at a ratio of 0.1 to 1% and again cultured statically.Then, the Dehalococcoides bacteria are multiplied to a concentration of 10 cells/ml or more within 14 days of culture.

以上、説明してきた本発明の培養方法におけるフロー図を図2に示した。
地下水が存在する帯水層から採取した地下水を直ちに密閉して、残存する微生物によって地下水を嫌気化することにより、従来必須としていた高価な還元剤(グルタチオン)を添加しなくても、デハロコッコイデス属細菌を含む菌液を増殖させることが可能である。
尚、増殖させた浄化菌の汚染サイトへの注入時には、培養液の使用前に窒素パージを行い、注入管に活性炭フィルターを付けて、培養液中のVOCを除去する必要がある。
A flow diagram of the above-described culture method of the present invention is shown in FIG.
By immediately sealing groundwater collected from an aquifer where groundwater exists and anaerobicizing the groundwater using the remaining microorganisms, it is possible to grow a bacterial liquid containing Dehalococcoides bacteria without the need to add an expensive reducing agent (glutathione), which was previously required.
Furthermore, when injecting the grown purification bacteria into a contaminated site, it is necessary to purge the culture solution with nitrogen before use and to attach an activated carbon filter to the injection tube to remove VOCs in the culture solution.

以下、従来方法(従来の浄化菌の培養方法のフロー図、図1)で培養する場合と、本発明の方法で培養する場合(本発明の浄化菌の培養方法のフロー図、図2)を対比させながら、以下の実験を行った。いずれの実験でも、デハロコッコイデス属細菌を含む培養液を作成することができた。 The following experiments were carried out, comparing the conventional method (flow chart of the conventional method for culturing purifying bacteria, Figure 1) with the method of the present invention (flow chart of the method for culturing purifying bacteria, Figure 2). In both experiments, a culture solution containing Dehalococcoides bacteria was successfully produced.

[実験例1] 地下水培地と通常培地との比較
1)目的
実験例1では、浄化対象とする帯水層から採取した地下水を用いて、従来の手順(図1)で浄化菌の培養が可能であるかについて確認する。
[Experimental Example 1] Comparison of groundwater medium and normal medium
1) Objective In Experimental Example 1, we will confirm whether it is possible to cultivate purification bacteria using conventional procedures (Figure 1) using groundwater collected from the aquifer to be purified.

2)試験方法
地下水培地:全量720mlのガラスバイアル瓶に、基質となる汚染地下水500ml、ピルビン酸ナトリウム0.23g、炭酸水素ナトリウム1.25g、グルタチオン(還元剤)0.5g、0.1%レサズリンナトリウム0.5mlを投入した。ガラスバイアル瓶をブチルゴム栓で密栓して、窒素ガスを15分間パージし、滅菌処理を行った(121℃、20分)。冷却後、ビタミン溶液0.5ml、TCE溶液2.0ml(終濃度1.2mg/L)を添加し、UCH007株とUCH001株のコカルチャー培養液(UCH007:1.05×10cells/ml、UCH001:1.0×10cells/ml)を2ml植菌した。ビタミン溶液の成分組成を表4に示した。
通常培地:基質となる水を変え、従来方法の培地を作成した。ガラスバイアル瓶に、基質となる蒸留水500ml、無機栄養源(表1)の他に上記地下水培地にも添加したピルビン酸ナトリウム0.23g、グルタチオン(還元剤)0.5g、0.1%レサズリンナトリウム0.5mlを添加した。15分間の窒素パージの後に、滅菌処理し、冷却後に、ビタミン溶液0.5ml、TCE溶液2.0ml(終濃度1.2mg/L)を添加して培地を調整し、UCH007株とUCH001株のコカルチャー培養液(UCH007:1.05×10cells/ml、UCH001:1.0×10cells/ml)を2ml植菌した。
2) Test method Groundwater medium: 500 ml of contaminated groundwater as a substrate, 0.23 g of sodium pyruvate, 1.25 g of sodium bicarbonate, 0.5 g of glutathione (reducing agent), and 0.5 ml of 0.1% sodium resazurin were added to a 720 ml glass vial. The glass vial was sealed with a butyl rubber stopper and sterilized by purging with nitrogen gas for 15 minutes (121°C, 20 minutes). After cooling, 0.5 ml of vitamin solution and 2.0 ml of TCE solution (final concentration 1.2 mg/L) were added, and 2 ml of coculture culture solution of UCH007 and UCH001 strains (UCH007: 1.05 x 10 8 cells/ml, UCH001: 1.0 x 10 9 cells/ml) was inoculated. The composition of the vitamin solution is shown in Table 4.
Conventional medium: A conventional medium was prepared by changing the water substrate. 500 ml of distilled water as the substrate, 0.23 g of sodium pyruvate, 0.5 g of glutathione (reducing agent), and 0.5 ml of 0.1% resazurin sodium were added to a glass vial in addition to inorganic nutrient sources (Table 1). After 15 minutes of nitrogen purging, the medium was sterilized and cooled, and 0.5 ml of vitamin solution and 2.0 ml of TCE solution (final concentration 1.2 mg/L) were added to adjust the medium, and 2 ml of coculture culture solution of UCH007 and UCH001 strains (UCH007: 1.05 x 10 8 cells/ml, UCH001: 1.0 x 10 9 cells/ml) was inoculated.

Figure 0007557428000005
Figure 0007557428000005

3)試験結果
地下水培地、通常培地ともに22℃の恒温庫で静置培養し、培養14日目には、10cells/ml以上のデハロコッコイデス属細菌(UCH007株)が増殖した(図3)。実験例1により、浄化対象とする帯水層から採取した地下水を用いれば、通常培地と同等以上の浄化菌を培養できることが確認できた。
3) Test results Both the groundwater medium and the regular medium were statically cultured in a thermostatic chamber at 22°C, and on the 14th day of culture, Dehalococcoides genus bacteria (UCH007 strain) had proliferated to over 107 cells/ml (Figure 3). Experimental Example 1 confirmed that by using groundwater collected from the aquifer to be purified, it was possible to cultivate purification bacteria equivalent to or better than those in the regular medium.

[実験例2] 地下水の滅菌処理を行わずに還元剤を用いて培養する試験
1)試験目的
実施例1の方法から、更に滅菌処理を省略して浄化菌の培養が可能であるかを確認する。
[Experimental Example 2] Test to culture groundwater using a reducing agent without sterilizing it
1) Purpose of the test To confirm whether it is possible to culture purifying bacteria without the sterilization process, in addition to the method of Example 1.

2)試験方法
地下水培地:全量60mlのガラスバイアル瓶に、基質となる地下水40ml、ピルビン酸ナトリウム40mg、炭酸水素ナトリウム0.1g、グルタチオン(還元剤)40mg、ビタミン溶液40μL、無機栄養源(表1)、0.1%レサズリンナトリウム40μLを投入した。ブチルゴム栓で密栓して、窒素ガスを5分間パージし、TCE溶液0.2ml(終濃度1.2mg/L)を添加し、UCH007株とUCH001株のコカルチャー培養液(UCH007:7.7×10cells/ml、UCH001:1.0×10cells/ml)を0.4ml植菌した。
通常培地:上記地下水培地の場合と同様に、ガラスバイアル瓶に、基質となる蒸留水40ml、ピルビン酸ナトリウム40mg、炭酸水素ナトリウム0.1g、グルタチオン(還元剤)40mg、無機栄養源(表1)、0.1%レサズリンナトリウム40μLを投入した。ブチルゴム栓で密栓して、窒素ガスを5分間パージした後、滅菌処理(121℃、20分)した。冷却後に、ビタミン溶液40μL、TCE溶液0.2ml(終濃度1.2mg/L)を添加し、UCH007株とUCH001株のコカルチャー培養液(UCH007:7.7×10cells/ml、UCH001:1.0×10cells/ml)を0.4ml植菌した。
2) Test method Groundwater medium: 40 ml of groundwater as substrate, 40 mg of sodium pyruvate, 0.1 g of sodium bicarbonate, 40 mg of glutathione (reducing agent), 40 μL of vitamin solution, inorganic nutrient source (Table 1), and 40 μL of 0.1% resazurin sodium were placed in a 60 ml glass vial. The vial was sealed with a butyl rubber stopper and purged with nitrogen gas for 5 minutes, after which 0.2 ml of TCE solution (final concentration 1.2 mg/L) was added, and 0.4 ml of coculture culture solution of UCH007 and UCH001 strains (UCH007: 7.7 x 107 cells/ml, UCH001: 1.0 x 109 cells/ml) was inoculated.
Normal medium: As in the case of the groundwater medium, 40 ml of distilled water as a substrate, 40 mg of sodium pyruvate, 0.1 g of sodium bicarbonate, 40 mg of glutathione (reducing agent), inorganic nutrient source (Table 1), and 40 μL of 0.1% resazurin sodium were added to a glass vial. The vial was sealed with a butyl rubber stopper, purged with nitrogen gas for 5 minutes, and then sterilized (121°C, 20 minutes). After cooling, 40 μL of vitamin solution and 0.2 ml of TCE solution (final concentration 1.2 mg/L) were added, and 0.4 ml of coculture culture solution of UCH007 and UCH001 strains (UCH007: 7.7 x 107 cells/ml, UCH001: 1.0 x 109 cells/ml) was inoculated.

3)試験結果
地下水培地、通常培地ともに25℃の恒温庫で静置培養し、培養14日目には、共に10cells/ml以上のデハロコッコイデス属細菌(UCH007株)が増殖していることが確認された(図4)。
3) Test results Both the groundwater medium and the regular medium were cultured statically in an incubator at 25°C, and on the 14th day of culture, it was confirmed that Dehalococcoides bacteria (UCH007 strain) had proliferated at more than 10 8 cells/ml in both media (Figure 4).

[実験例3] 実験例2で得られた滅菌処理を行っていない培地の揮発性有機塩素化合物(VOCs)分解活性を確認する試験
1)試験目的
実験例2において、滅菌処理を行っていない地下水培地でも滅菌処理を行った通常培地と同様に浄化菌が増殖した。滅菌処理を行っていない地下水には、浄化菌以外の細菌が多く存在している。非滅菌状態(他の細菌が存在する状態)の菌液を用いて、純粋培養した通常培地と同等の浄化効果が得られることを確認するため、培養した菌液を実汚染地下水に導入して浄化効果を確認する。
[Experimental Example 3] Test to confirm the decomposition activity of volatile organic chlorine compounds (VOCs) in the medium not subjected to sterilization treatment obtained in Experimental Example 2
1) Test Objectives In Experimental Example 2, the purifying bacteria grew in the unsterilized groundwater medium in the same way as in the sterilized normal medium. Unsterilized groundwater contains many bacteria other than the purifying bacteria. In order to confirm that a purification effect equivalent to that of a normal medium in which pure culture is performed using a non-sterile bacterial solution (a state in which other bacteria are present), the cultured bacterial solution is introduced into actual contaminated groundwater to confirm the purification effect.

2)試験方法
本試験では、全量60mlのガラス培養容器に実汚染地下水40mlを投入し、あらかじめ有機資材を添加して嫌気化した。嫌気化した地下水の水質を表5に示した。この嫌気化した地下水にUCH007株を増殖させた地下水培地と通常培地を添加して、VOCsの分解活性を比較した。なお汚染地下水に添加した時の地下水培地、通常培地のUCH007株は共に1×10cells/mlであり、汚染地下水に対して、0.4ml(1%)添加した。培養は25℃の静置培養とした。
2) Test method In this test, 40 ml of actual contaminated groundwater was placed in a 60 ml glass culture vessel and anaerobicized by adding organic materials beforehand. The quality of the anaerobic groundwater is shown in Table 5. A groundwater medium in which UCH007 strain had been grown and a normal medium were added to this anaerobic groundwater, and the decomposition activity of VOCs was compared. The UCH007 strain in both the groundwater medium and the normal medium when added to the contaminated groundwater was 1 x 10 8 cells/ml, and 0.4 ml (1%) was added to the contaminated groundwater. Cultivation was performed as a static culture at 25°C.

Figure 0007557428000006
Figure 0007557428000006

3)試験結果
試験の結果を図5、図6に示した。非滅菌地下水で増殖させたUCH007株を用いた場合(図5)も、通常培地(純粋培養)で増殖させたUCH007株を用いた場合(図6)も、14日目にはTCEの濃度が大幅に低下しており、実汚染地下水に対する浄化効果に差が生じなかった。したがって、浄化菌以外に増殖した細菌が存在する菌液を用いても浄化できることが確認できた。
3) Test results The test results are shown in Figures 5 and 6. Whether using the UCH007 strain grown in non-sterile groundwater (Figure 5) or the UCH007 strain grown in normal medium (pure culture) (Figure 6), the TCE concentration had dropped significantly by the 14th day, meaning there was no difference in the purification effect on actual contaminated groundwater. This confirmed that purification was possible even when using a bacterial solution containing bacteria grown other than the purification bacteria.

[実験例4] 地下水の滅菌処理を行わず、還元剤も使用せずに培養する試験
1)試験目的
実験例2(地下水を非滅菌条件で培養する条件)において、価格が高い還元剤(グルタチオン)を使わずに浄化菌を培養できるかについて確認する。
[Experimental Example 4] Test to culture groundwater without sterilization or reducing agents
1) Purpose of the test In Experimental Example 2 (cultivating groundwater under non-sterile conditions), we will confirm whether purification bacteria can be cultivated without using an expensive reducing agent (glutathione).

2)試験方法
地下水培地:全量120mlのガラスバイアル瓶に、基質となる地下水100ml、ピルビン酸ナトリウム100mg、ビタミン溶液100μL、無機栄養源(表1)、0.1%レサズリンナトリウム100μLを投入した。ブチルゴム栓で密栓して、窒素ガスを10分間パージし、TCE溶液0.5ml(終濃度1.4mg/L)を添加し、UCH007株とUCH001株のコカルチャー培養液(UCH007:7.7×10cells/ml、UCH001:1.0×10cells/ml)を1.0ml植菌した。
通常培地:上記地下水培地と同様に、ガラスバイアル瓶に、基質となる蒸留水80ml、ピルビン酸ナトリウム80mg、炭酸水素ナトリウム0.2g、グルタチオン(還元剤)80mg、無機栄養源(表1)、0.1%レサズリンナトリウム80μLを投入した。ブチルゴム栓で密栓して、窒素ガスを10分間パージした後、滅菌処理(121℃、20分)を行った。冷却後に、ビタミン溶液80μL、TCE溶液0.3ml(終濃度0.52mg/L)添加し、UCH007株とUCH001株のコカルチャー培養液(UCH007:7.7×10cells/ml、UCH001:1.0×10cells/ml)を1.0ml植菌した。
2) Test method Groundwater medium: 100 ml of groundwater as a substrate, 100 mg of sodium pyruvate, 100 μL of vitamin solution, inorganic nutrient source (Table 1), and 100 μL of 0.1% resazurin sodium were placed in a 120 ml glass vial. The vial was sealed with a butyl rubber stopper and purged with nitrogen gas for 10 minutes, after which 0.5 ml of TCE solution (final concentration 1.4 mg/L) was added and 1.0 ml of coculture culture solution of UCH007 and UCH001 strains (UCH007: 7.7 x 107 cells/ml, UCH001: 1.0 x 109 cells/ml) was inoculated.
Normal medium: As with the above groundwater medium, 80 ml of distilled water as a substrate, 80 mg of sodium pyruvate, 0.2 g of sodium bicarbonate, 80 mg of glutathione (reducing agent), inorganic nutrient source (Table 1), and 80 μL of 0.1% resazurin sodium were added to a glass vial. The vial was sealed with a butyl rubber stopper, purged with nitrogen gas for 10 minutes, and then sterilized (121°C, 20 minutes). After cooling, 80 μL of vitamin solution and 0.3 ml of TCE solution (final concentration 0.52 mg/L) were added, and 1.0 ml of coculture culture solution of UCH007 and UCH001 strains (UCH007: 7.7×10 7 cells/ml, UCH001: 1.0×10 9 cells/ml) was inoculated.

3)試験結果
地下水培地、通常培地ともに25℃の恒温庫で静置培養し、培養14日目には、共に10cells/ml以上のUCH007が増殖していることを確認した(図7)。したがって、非滅菌条件では還元剤を用いなくても浄化菌を必要量培養できることが確認できた。
3) Test results: Both groundwater medium and normal medium were cultured in a thermostatic chamber at 25℃, and on the 14th day of culture, it was confirmed that UCH007 had proliferated to more than 107 cells/ml in both media (Figure 7). Therefore, it was confirmed that the necessary amount of purification bacteria can be cultured under non-sterile conditions without using a reducing agent.

以上の検討結果から、本発明の浄化菌の培養方法では、地下水を培養の基質として使用する。その結果、従来の培養方法に比べて、滅菌処理が不要となり、還元剤も使用せずに培養可能であることが判明した。
本発明の浄化菌の培養方法では以下の効果が期待できる。
(1)地下水を用いるので蒸留水を使わなくて良い(コスト削減、浄化サイトで水道等がない場合でも現地で培養可能)。
(2)容器と種菌と温度管理できる部屋があれば培養可能である。
(3)還元剤が不要(安価)である。
(4)現地で培養可能(輸送費無し)である。
(5)管理が容易(純粋培養ではない)である。
(6)安全性が高い。浄化を行うサイトの地下水(細菌)と安全性が確認されている細菌(単離株)のみを用いて培養している。
(7)培養期間が短い(容器数の減少)。
From the above results, it was found that the method for culturing purifying bacteria of the present invention uses groundwater as a culture substrate, and as a result, compared to conventional culture methods, sterilization is not required and it is possible to culture without using a reducing agent.
The method for culturing purifying bacteria of the present invention is expected to have the following effects.
(1) Since groundwater is used, there is no need to use distilled water (cost reduction; cultivation is possible on-site even if the purification site does not have a running water supply).
(2) Cultivation is possible if you have a container, seed culture, and a room where the temperature can be controlled.
(3) No reducing agent is required (cheap).
(4) It can be cultivated locally (no transportation costs).
(5) It is easy to manage (it is not a pure culture).
(6) High safety. Only groundwater (bacteria) from the site where the purification is carried out and bacteria (isolated strains) that have been confirmed to be safe are used for cultivation.
(7) The cultivation period is short (reduced number of containers).

[実験例5] 地下水に添加するVOCsの濃度の浄化菌増殖への影響
1)試験目的
地下水に添加するVOCs(TCE)の濃度として、最適な濃度の範囲について検討する。
[Experimental Example 5] Effect of concentration of VOCs added to groundwater on the proliferation of purification bacteria
1) Purpose of the test To investigate the optimal concentration range for VOCs (TCE) to be added to groundwater.

2)試験方法
表6に記載の組成で、TCE、地下水、ピルビン酸ナトリウム、無機栄養源(表1)、ビタミン類、炭酸水素ナトリウム、0.1%レサズリンナトリウムを含有する培養液を調製した。
全量120mlのガラスバイアル瓶10個に、表6に記載の10種類の培養液をそれぞれ添加した。気相部を5分間窒素パージし、各条件のTCE溶液を添加して25℃で静置培養した。1週間培養後に、UCH007株のコカルチャー培養液(UCH007:4.7×10cells/ml、UCH001:6.0×10cells/ml)を各バイアル瓶に0.2mlを植菌して、その後のUCH007株の増殖を確認した。
2) Test method A culture solution containing TCE, groundwater, sodium pyruvate, inorganic nutrient sources (Table 1), vitamins, sodium bicarbonate, and 0.1% resazurin sodium was prepared according to the composition shown in Table 6.
The 10 types of culture medium listed in Table 6 were added to 10 glass vials with a total volume of 120 ml. The gas phase was purged with nitrogen for 5 minutes, and TCE solution of each condition was added and cultured at 25°C. After one week of culture, 0.2 ml of coculture medium of UCH007 strain (UCH007: 4.7 x 107 cells/ml, UCH001: 6.0 x 108 cells/ml) was inoculated into each vial, and the subsequent growth of UCH007 strain was confirmed.

Figure 0007557428000007
Figure 0007557428000007

3)試験結果
培養開始から7日目のVOCs濃度を図8に示した。添加したTCEは高濃度になるにつれて、初期濃度よりも低くなり、殆ど全ての条件でTCEからcis-1,2-DCEに脱塩素化されていた。さらに、その後培養を継続して、培養開始から16日目のVOCs濃度を図9に示した。TCEの初期濃度が3.0mg/Lの場合を除き、VOCsの脱塩素化がさらに進捗していることが確認された。
3) Test results Figure 8 shows the VOCs concentration on the 7th day after the start of cultivation. As the concentration of added TCE increased, the concentration became lower than the initial concentration, and under almost all conditions TCE was dechlorinated to cis-1,2-DCE. Cultivation was continued thereafter, and the VOCs concentration on the 16th day after the start of cultivation is shown in Figure 9. It was confirmed that the dechlorination of VOCs had progressed further, except when the initial TCE concentration was 3.0 mg/L.

また、培養開始から16日目における初期濃度からのVOCsの残存率を図10に示した。培養開始から16日目のUCH007の遺伝子コピー数を図11に示した。培養開始から培養16日目におけるUCH007遺伝子コピー数の増加率を図12に示した。
以上の検討結果から、以下のことが判明した。
(1)VOCs初期濃度(添加濃度)を3.0mg/L以下で培養することでUCH007を地下水で優占的に増殖させることが可能である。
(2)図10、図12の結果から、地下水に添加するVOCsの終濃度は、0.6~2.5mg/Lが好ましく、1.0~2.5mg/Lがより好ましい。
図13は、培養開始から16日目の地下水中のvcrA(脱塩素化の機能遺伝子)の濃度を測定した結果である。この結果から、TCE添加率が低く、UCH007株がそれほど増えていない条件でも脱塩素化率が進行した理由は、UCH007株以外にも、もとの地下水に脱塩素化菌が存在したためと考えられる。
Furthermore, the residual rate of VOCs from the initial concentration on the 16th day from the start of culture is shown in Figure 10. The gene copy number of UCH007 on the 16th day from the start of culture is shown in Figure 11. The rate of increase in the gene copy number of UCH007 from the start of culture to the 16th day of culture is shown in Figure 12.
From the above investigation, the following became clear:
(1) It is possible to grow UCH007 predominantly in groundwater by culturing it at an initial VOCs concentration (additive concentration) of 3.0 mg/L or less.
(2) From the results shown in Figures 10 and 12, the final concentration of VOCs added to groundwater is preferably 0.6 to 2.5 mg/L, and more preferably 1.0 to 2.5 mg/L.
Figure 13 shows the results of measuring the concentration of vcrA (the functional gene for dechlorination) in groundwater on the 16th day after the start of cultivation. From these results, the reason why the dechlorination rate progressed even under conditions where the TCE addition rate was low and the UCH007 strain did not increase significantly is thought to be because dechlorinating bacteria other than the UCH007 strain were present in the original groundwater.

次に、前記の浄化菌の培養方法によって得られた浄化菌の培養液を用いて行う、揮発性有機塩素化合物で汚染された地下水の浄化方法について説明する。
本実施形態の浄化方法は、培養容器内において、培養液の中から酸素を除去する培養液酸素除去工程と、培養容器内の培養液中で浄化菌を増殖させる培養工程と、地下水が存在する帯水層に培養液を注入するための注入管を設置する注入管設置工程と、注入管の内部の酸素を除去する注入管内酸素除去工程と、帯水層に有機物溶液を供給して一定期間放置することで嫌気的な地盤を形成する有機物溶液供給工程と、帯水層に浄化菌を増殖させた培養液を供給する培養液供給工程という工程を有している。
Next, a method for purifying groundwater contaminated with volatile organic chlorine compounds using the culture solution of the purifying bacteria obtained by the above-mentioned method for culturing the purifying bacteria will be described.
The purification method of this embodiment includes a culture solution oxygen removal process for removing oxygen from the culture solution in a culture vessel; a cultivation process for growing purification bacteria in the culture solution in the culture vessel; an injection pipe installation process for installing an injection pipe for injecting the culture solution into an aquifer where groundwater exists; an injection pipe oxygen removal process for removing oxygen inside the injection pipe; an organic solution supply process for forming an anaerobic ground by supplying an organic solution to the aquifer and leaving it for a certain period of time; and a culture solution supply process for supplying the culture solution in which purification bacteria have grown to the aquifer.

培養液の中から酸素を除去する培養液酸素除去工程は、前記した培養容器を密栓して、窒素ガスをパージする工程に相当する。
培養容器内の培養液中で浄化菌を増殖させる培養工程は、前記した地下水を用いた培養液にTCE溶液を添加し、浄化菌を植菌して、恒温庫で静置培養する工程に相当する。
The culture solution oxygen removal step of removing oxygen from the culture solution corresponds to the above-mentioned step of tightly sealing the culture vessel and purging with nitrogen gas.
The culture process for growing the purifying bacteria in the culture solution in the culture vessel corresponds to the process of adding a TCE solution to the culture solution using the above-mentioned groundwater, inoculating the purifying bacteria, and allowing it to undergo static culture in an incubator.

地下水が存在する帯水層に注入管を設置する注入管設置工程では、浄化菌を増殖させた培養液を地下水の帯水層に注入するために、注入管を地盤に設置する。注入管は、汚染地下水が存在する帯水層に到達するように、帯水層の深度に相当する長さのものを設置する。注入管の地中への設置方法は限定されるものではなく、例えば、地盤を削孔することにより形成された掘削孔に注入管を挿入してもよい。 In the injection pipe installation process, an injection pipe is installed in the ground to inject the culture solution in which the purification bacteria have been grown into the groundwater aquifer. The injection pipe is installed to a length equivalent to the depth of the aquifer so that it reaches the aquifer where the contaminated groundwater exists. There are no limitations on the method of installing the injection pipe underground, and for example, the injection pipe may be inserted into a borehole formed by drilling the ground.

注入管の内部の酸素を除去する注入管内酸素除去工程では、地盤に設置した注入管の内部の酸素を除去する。具体的には、窒素ガス発生装置から注入管の底部に窒素ガスを供給することで、注入管内の酸素を除去する。注入管の管内の体積の3倍以上の窒素ガスを供給することが好ましい。 In the injection pipe oxygen removal process, oxygen is removed from inside the injection pipe installed in the ground. Specifically, oxygen is removed from inside the injection pipe by supplying nitrogen gas from a nitrogen gas generator to the bottom of the injection pipe. It is preferable to supply nitrogen gas at least three times the volume inside the injection pipe.

有機物溶液供給工程では、帯水層に有機物溶液を供給して、一定期間放置することで嫌気的な地盤を形成する。地盤内に有機物を供給することで、地盤内に存在する好気性細菌が酸素を消費しながら有機物を分解するため、地盤内に嫌気環境が形成される。放置する期間は、1~2か月間程度であり、硫酸イオン濃度をモニタリングすることによって決定される。硫酸イオン濃度の低下が確認されたら、次の工程に進む。有機物は特に限定されない(例えば、乳酸ナトリウム、等)。有機物溶液中の有機物濃度は、500mg/L~50g/Lの範囲内とすることが好ましい。注入管に有機物溶液を注入する際には、窒素ガス発生装置による窒素ガスの圧力を利用する。 In the organic solution supply process, an anaerobic ground is formed by supplying an organic solution to the aquifer and leaving it for a certain period of time. By supplying organic matter to the ground, aerobic bacteria present in the ground consume oxygen and decompose the organic matter, creating an anaerobic environment in the ground. The leaving period is about 1 to 2 months and is determined by monitoring the sulfate ion concentration. Once a decrease in the sulfate ion concentration is confirmed, proceed to the next step. There are no particular restrictions on the organic matter (e.g., sodium lactate, etc.). The organic matter concentration in the organic solution is preferably within the range of 500 mg/L to 50 g/L. When the organic solution is injected into the injection tube, nitrogen gas pressure from a nitrogen gas generator is used.

帯水層に浄化菌を増殖させた培養液を供給する培養液供給工程では、地盤(帯水層)に前記の培養工程で培養された浄化菌の培養液を供給する。培養液供給工程で供給される浄化菌は、前記培養工程において、前記した浄化菌の培養方法を用いて培養されたものである。注入管に培養液を注入する際には、窒素ガス発生装置による窒素ガスの圧力を利用する。 In the culture solution supplying process, in which a culture solution in which purifying bacteria have been grown is supplied to the aquifer, the culture solution of the purifying bacteria cultivated in the above-mentioned cultivation process is supplied to the ground (aquifer). The purifying bacteria supplied in the culture solution supplying process are those cultivated in the above-mentioned cultivation process using the above-mentioned cultivation method for the purifying bacteria. When the culture solution is injected into the injection pipe, the pressure of nitrogen gas from a nitrogen gas generator is used.

本実施形態の浄化方法によれば、地盤内に有機物を含む培養液を供給すると、地盤内に存在する好気性細菌が酸素を消費しながら培養液中の有機物を分解するため、地盤内に嫌気環境が形成される。地盤内に嫌気環境が形成されると、嫌気性細菌が活性化して有機物を分解し、水素(電子供与体)が供給される。そして、嫌気性の浄化菌がこの水素を利用して浄化(脱塩素化)を進行させる。 According to the purification method of this embodiment, when a culture solution containing organic matter is supplied into the ground, aerobic bacteria present in the ground consume oxygen while decomposing the organic matter in the culture solution, forming an anaerobic environment in the ground. When an anaerobic environment is formed in the ground, the anaerobic bacteria become activated and decompose the organic matter, supplying hydrogen (electron donor). The anaerobic purification bacteria then use this hydrogen to proceed with purification (dechlorination).

Claims (5)

揮発性有機塩素化合物で汚染された地下水を浄化するための浄化菌の培養方法であって、
前記浄化菌が、嫌気性の浄化菌であり、
前記地下水が存在する帯水層から採取した前記地下水にトリクロロエチレンを添加して培養液として用い
前記培養液の滅菌処理を行わず、
前記地下水と有機物と酸化還元指示薬を含む培養液を密栓可能な容器に入れ、気相部を窒素で置換した後に一定期間静置し、前記培養液の酸化還元指示薬が変色して酸化還元電位が低下したことを確認した後に、前記培養液に前記浄化菌を添加することを特徴とする浄化菌の培養方法。
A method for culturing purification bacteria for purifying groundwater contaminated with volatile organic chlorine compounds, comprising:
The purification bacteria are anaerobic purification bacteria,
The groundwater is collected from an aquifer in which the groundwater exists, and trichloroethylene is added to the groundwater to be used as a culture solution ;
The culture medium is not sterilized,
The method for cultivating purifying bacteria is characterized in that a culture solution containing the groundwater, organic matter, and an oxidation-reduction indicator is placed in a sealable container, the gas phase is replaced with nitrogen, and the solution is allowed to stand for a certain period of time. After confirming that the oxidation-reduction indicator in the culture solution has changed color and the oxidation-reduction potential has decreased, the purifying bacteria are added to the culture solution .
揮発性有機塩素化合物で汚染された地下水を浄化するための浄化菌の培養方法であって、A method for culturing purification bacteria for purifying groundwater contaminated with volatile organic chlorine compounds, comprising:
前記浄化菌が、嫌気性の浄化菌であり、The purification bacteria are anaerobic purification bacteria,
前記地下水が存在する帯水層から採取した前記地下水にトリクロロエチレンを添加して培養液として用い、The groundwater is collected from an aquifer in which the groundwater exists, and trichloroethylene is added to the groundwater to be used as a culture solution;
前記培養液に還元剤を添加せず、No reducing agent is added to the culture medium,
前記地下水と有機物と酸化還元指示薬を含む培養液を密栓可能な容器に入れ、気相部を窒素で置換した後に一定期間静置し、前記培養液の酸化還元指示薬が変色して酸化還元電位が低下したことを確認した後に、前記培養液に前記浄化菌を添加することを特徴とする浄化菌の培養方法。The method for cultivating purifying bacteria is characterized in that a culture solution containing the groundwater, organic matter, and an oxidation-reduction indicator is placed in a sealable container, the gas phase is replaced with nitrogen, and the solution is allowed to stand for a certain period of time. After confirming that the oxidation-reduction indicator in the culture solution has changed color and the oxidation-reduction potential has decreased, the purifying bacteria are added to the culture solution.
前記培養液に還元剤を添加しない請求項1に記載の浄化菌の培養方法。The method for culturing purifying bacteria according to claim 1 , wherein no reducing agent is added to the culture solution. 前記浄化菌が、デハロコッコイデス属細菌のデハロコッコイデス・エスピーUCH007株(NITE P-1471)である請求項1~3のいずれか1項に記載の浄化菌の培養方法。 The method for culturing a purifying bacterium according to any one of claims 1 to 3 , wherein the purifying bacterium is a Dehalococcoides sp. UCH007 strain (NITE P-1471) belonging to the genus Dehalococcoides. 揮発性有機塩素化合物で汚染された地下水を浄化菌を用いて浄化する浄化方法であって、
前記浄化菌が、嫌気性の浄化菌であり、
培養容器内において、培養液の中から酸素を除去する培養液酸素除去工程と、
前記培養容器内の前記培養液中で前記浄化菌を増殖させる培養工程と、
前記地下水が存在する帯水層に前記培養液を注入するための注入管を設置する注入管設置工程と、
前記注入管の内部の酸素を除去する注入管内酸素除去工程と、
前記帯水層に有機物溶液を供給して一定期間放置することで嫌気的な地盤を形成する有機物溶液供給工程と、
前記帯水層に前記浄化菌を増殖させた前記培養液を供給する培養液供給工程と、を備え、
前記培養液供給工程で供給される前記浄化菌が、前記培養工程において、請求項1~のいずれか1項に記載された浄化菌の培養方法を用いて培養されたものであることを特徴とする浄化方法。
A method for purifying groundwater contaminated with volatile organic chlorine compounds using purification bacteria, comprising:
The purification bacteria are anaerobic purification bacteria,
A culture solution oxygen removal step of removing oxygen from the culture solution in the culture vessel;
A culture step of growing the purifying bacteria in the culture solution in the culture vessel;
An injection pipe installation step of installing an injection pipe for injecting the culture solution into an aquifer where the groundwater exists;
an oxygen removal process in the injection tube for removing oxygen from inside the injection tube;
an organic solution supplying step of supplying an organic solution to the aquifer and leaving it for a certain period of time to form an anaerobic ground;
A culture solution supplying step of supplying the culture solution in which the purification bacteria have been grown to the aquifer,
The purification method, characterized in that the purification bacteria supplied in the culture solution supplying step are cultured in the culturing step using the purification bacteria culture method described in any one of claims 1 to 4 .
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014046269A (en) 2012-08-31 2014-03-17 Kurita Water Ind Ltd Method for decontaminating contaminated soil
JP2014108061A (en) 2012-11-30 2014-06-12 Taisei Corp New microorganism that dechlorinate volatile organochlorine compounds
JP5668916B2 (en) 2010-10-21 2015-02-12 栗田工業株式会社 Soil and groundwater purification methods

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Publication number Priority date Publication date Assignee Title
JP5668916B2 (en) 2010-10-21 2015-02-12 栗田工業株式会社 Soil and groundwater purification methods
JP2014046269A (en) 2012-08-31 2014-03-17 Kurita Water Ind Ltd Method for decontaminating contaminated soil
JP2014108061A (en) 2012-11-30 2014-06-12 Taisei Corp New microorganism that dechlorinate volatile organochlorine compounds

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大成建設技術センター報,第45号,2007年,pp.51-1~51-4

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