JP5747371B2 - Lipophilic solvent treatment method using Rhodococcus bacteria - Google Patents
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本発明は、炭化水素の処理方法及び炭化水素の処理システムに関し、詳細には、ロドコッカス(Rhodococcus)属細菌を利用した効率のよい炭化水素の処理方法及び炭化水素の処理システムに関する。 The present invention relates to a hydrocarbon treatment method and a hydrocarbon treatment system, and more particularly, to an efficient hydrocarbon treatment method and a hydrocarbon treatment system using Rhodococcus bacteria.
ロドコッカス(Rhodococcus)属細菌は、土壌や海洋などにありふれて存在するグラム陽性細菌、高G+C含量のコリネ型細菌の一種である。ロドコッカス(Rhodococcus)属細菌には、石油系炭化水素やポリ塩化ビフェニール類(PCB)などをはじめとした数多くの難分解性化合物に対して分解・資化能力をもつことに加え、アクリルアミドや有用酵素群、あるいは細胞外多糖をはじめとした機能性バイオポリマーなどの生産菌が多く存在することが知られている。 Rhodococcus (genus Rhodococcus) is a kind of gram-positive bacteria commonly found in soil and the ocean, and a coryneform bacterium with a high G + C content. Rhodococcus bacteria have the ability to decompose and assimilate a number of persistent compounds including petroleum hydrocarbons and polychlorinated biphenyls (PCB), as well as acrylamide and useful enzymes. It is known that there are many producing bacteria such as functional biopolymers including group or extracellular polysaccharides.
それゆえ、産業的に重要な菌群として位置づけられており、低エネルギー化や環境負荷を削減できるバイオプロセスによる環境浄化・物質生産への応用などが期待されている(非特許文献1)。 Therefore, it is positioned as an industrially important fungus group, and is expected to be applied to environmental purification and substance production by a bioprocess capable of reducing energy and reducing environmental burden (Non-patent Document 1).
特に、バイオプロセスを考える場合、応用が期待される微生物には、有機溶媒を含む特殊な環境下での良好な生育や活発な代謝活動などの性質が求められる。また、石油流出事故などによる石油汚染環境の浄化に必要な微生物にも、高濃度難揮発性化合物存在下でこれらの分解を行いながら良好な生育を示すために、これらに対する分解能だけでなく、共存する難揮発性化合物の毒性に対する耐性能が高いことが求められる。 In particular, when considering a bioprocess, microorganisms that are expected to be applied are required to have properties such as good growth and active metabolic activity in a special environment containing an organic solvent. In addition, in order to show good growth while decomposing these microorganisms in the presence of high-concentration non-volatile compounds, microorganisms necessary for purification of the oil-contaminated environment due to an oil spill accident, etc., not only have the ability to resolve them but also coexist. Therefore, it is required to have high resistance to toxicity of the hardly volatile compound.
上述したこれらの性質を解析するためには、まず、その切り口として微生物の有機溶媒耐性が必要であり、特にバイオプロセスにおいては、高濃度有機溶媒存在下での生育が求められる。 In order to analyze the above-described properties, first, the organic solvent resistance of the microorganism is required as a starting point, and particularly in a bioprocess, growth in the presence of a high concentration organic solvent is required.
微生物の有機溶媒耐性に関する研究では、これまでにグラム陰性菌の大腸菌やシュードモナス(Pseudomonas)属細菌などのモデル微生物を中心に遺伝生化学的な研究が行われ、細胞表層構造の変化やエプラックスポンプ、ベシクルの形成などの耐性機構が提案されている(非特許文献2)。 In the research on organic solvent resistance of microorganisms, genetic biochemical research has been conducted mainly on model microorganisms such as Escherichia coli and Pseudomonas bacteria, which are Gram-negative bacteria. A resistance mechanism such as vesicle formation has been proposed (Non-patent Document 2).
一方、グラム陽性菌においては、炭化水素分解遺伝子などに関する遺伝性化学的研究は進んできたが、有機溶媒耐性に関した研究は多くない。このことは、一般にグラム陽性菌は陰性菌に比べ有機溶媒耐性レベルが低いと考えられていることに起因していると予想される。 On the other hand, in gram-positive bacteria, genetic chemical research on hydrocarbon degrading genes has progressed, but there are not many studies on organic solvent resistance. This is presumably due to the fact that Gram-positive bacteria are generally considered to have a lower level of organic solvent resistance than negative bacteria.
しかしながら、バイオプロセスを考える場合には、極めて応用に近い段階の微生物において、実際の利用環境に近い条件での有機溶媒耐性に関する情報が求められる。上述したようにロドコッカス(Rhodococcus)属細菌はバイオプロセスへの応用が期待されていることから、同菌の有機溶媒耐性に関する知見の蓄積が必要である。 However, when considering a bioprocess, information on resistance to organic solvents under conditions close to the actual use environment is required for microorganisms at a very close to application stage. As described above, since Rhodococcus bacteria are expected to be applied to bioprocesses, it is necessary to accumulate knowledge about the organic solvent resistance of the bacteria.
岩淵らは、ロドコッカス・ロドクラウス(Rhodococcus rhodochrous)S−2株が高濃度石油耐性石油分解菌であることを見出し、その石油耐性に検討を加えた結果、同菌の生産する細胞外多糖(以下、「EPS」という)が長鎖アルカンなどの難揮発性有機溶媒の耐性に深く関与していることを明らかにした。 Iwabuchi et al. Found that Rhodococcus rhodochrous S-2 strain is a high-concentration oil-resistant oil-degrading bacterium, and as a result of investigating its oil resistance, an extracellular polysaccharide produced by the bacterium (hereinafter, It was revealed that "EPS" is deeply involved in the resistance of hardly volatile organic solvents such as long-chain alkanes.
さらに、ロドコッカス(Rhodococcus)属細菌のコロニー形態と溶媒耐性について検討したところ、EPS生産量の少ないラフ型菌は溶媒に親和性が高く結果的に溶媒感受性であり、一方で、EPS生産量の多いムコイド型菌は耐性を示したことから、同属細菌においては、コロニー形態と有機溶媒耐性に高い相関があることを明らかにした。 Furthermore, when the colony morphology and solvent resistance of Rhodococcus genus bacteria were examined, rough type bacteria with a low EPS production amount have high affinity for the solvent and as a result are solvent-sensitive. On the other hand, the EPS production amount is large. Since mucoid bacteria showed resistance, it was clarified that there is a high correlation between colony morphology and organic solvent resistance in bacteria belonging to the same genus.
また、EPSは溶媒に感受性のラフ型菌にも溶媒耐性を与えることが示されており、これらのことから、ムコイド型コロニーの形成が同属細菌の溶媒耐性を考える上での一つの指標であることが見出された(非特許文献3)。 EPS has also been shown to impart solvent resistance to solvent-sensitive rough bacteria, and from these, the formation of mucoid colonies is one index for considering the solvent resistance of the genus bacteria. (Non-Patent Document 3).
ロドコッカス・エリスロポリス(Rhodococcus erythropolis)PR4株は分岐アルカンの一種であるプリスタン(2,6,10,14-tetramethyl-pentadecane)分解菌として単離された株であり(非特許文献4)、培養の経過と共にEPSの生産に基づいた自身のコロニー形態をラフ型→ムコイド型→ラフ型へと変化させる株である。同株は難揮発性有機溶媒に耐性を示すことが知られていることから、ゲノム解析株に選定され、また、宿主−ベクター系の開発にも着手されている。従って、ロドコッカス・エリスロポリス(Rhodococcus erythropolis)PR4株(以下、「Rh-PR4」又は、「PR4株」という。)は、近い将来、ロドコッカス(Rhodococcus)属細菌の中で、遺伝子操作系の発達した株になることが予想される。 Rhodococcus erythropolis PR4 strain is a strain isolated as a degrading bacterium of pristane (2,6,10,14-tetramethyl-pentadecane) which is a kind of branched alkane (Non-patent Document 4). It is a strain that changes its colony form based on the production of EPS over time from rough type to mucoid type to rough type. Since this strain is known to exhibit resistance to a hardly volatile organic solvent, it has been selected as a genome analysis strain and has also begun to develop a host-vector system. Accordingly, the Rhodococcus erythropolis PR4 strain (hereinafter referred to as “Rh-PR4” or “PR4 strain”) has developed a genetic manipulation system in the near future in the genus Rhodococcus. It is expected to become a stock.
一般に、有機溶媒を細菌で処理する場合、有機溶媒と培地成分を含む水性溶媒との二層培養系で行う。しかしながら、水性溶媒中に添加された細菌は、有機溶媒−水性溶媒界面でしか反応できないため、バイオプロセスによる環境浄化・物質生産への応用には、菌体の親油性を改善し、菌体が炭化水素に転移するようにしての処理効率を向上させる必要がある。 In general, when an organic solvent is treated with bacteria, it is carried out in a two-layer culture system of an organic solvent and an aqueous solvent containing medium components. However, since the bacteria added in the aqueous solvent can only react at the interface between the organic solvent and the aqueous solvent, it is necessary to improve the lipophilicity of the microbial cells for application to environmental purification and substance production by bioprocess. It is necessary to improve the treatment efficiency by transferring to hydrocarbons.
R .erythropolis PR4株は培地/アルカンの二層培養系において、添加するアルカンの炭素数によって、アルカン粒子表面へ吸着する「吸着型」とアルカン粒子内へ転移する「転移型」の二つの異なる局在性を示す株であり、バイオリメディエーションやバイオプロセスの宿主として期待されている。 R. erythropolis strain PR4 is a two-layer culture system of culture medium / alkane, and it has two different stations, “adsorption type” that adsorbs to the surface of alkane particles and “transfer type” that transfers into alkane particles, depending on the number of carbons of the added alkane. It is a strain exhibiting sexuality and is expected as a host for bioremediation and bioprocesses.
岩淵らは、Rh-PR4が前記炭素数14以上のテトラデカン、ペンタデカン、ヘキサデカン、プリスタン、スクワラン等に転移して、これらの炭化水素を代謝・分解できることを明らかにした(特許文献1)。 Iwabuchi et al. Revealed that Rh-PR4 can be transferred to tetradecane, pentadecane, hexadecane, pristane, squalane and the like having 14 or more carbon atoms to metabolize and decompose these hydrocarbons (Patent Document 1).
既述のように、ロドコッカス属微生物は炭化水素の分解・代謝に有用であるものの、炭素数が一定以下の炭化水素には転移出来ないなど、分解・代謝できる炭化水素には制限があるという課題があった。 As mentioned above, Rhodococcus microorganisms are useful for hydrocarbon decomposition and metabolism, but there are restrictions on hydrocarbons that can be decomposed and metabolized, such as being unable to transfer to hydrocarbons with a certain number of carbon atoms or less. was there.
そこで、本願発明は、ロドコッカス属微生物の親油性溶媒に対する親和性を制御、即ち、親油性溶媒に吸着する状態からこれに転移する状態に変化させることにより、新油性溶媒を効率よく分解することができる方法を提供することを目的とするものである。 Therefore, the present invention is capable of efficiently decomposing a new oily solvent by controlling the affinity of the microorganism of the genus Rhodococcus to the lipophilic solvent, that is, by changing from the state of being adsorbed to the lipophilic solvent to the state of transfer to this. It is intended to provide a method that can be used.
前記目的を達成するために、本発明は、ロドコッカス属細菌を用いた対象物の処理方法であって、当該細菌の培地に添加されるマグネシウム塩の濃度を制限することによって、前記培地に添加される代謝対象新油性化合物に対する前記細菌の局在性を、前記化合物に吸着する形態から前記化合物に転移する形態に変更することを特徴とするものである。 To achieve the above object, the present invention provides a method for treating an object using Rhodococcus bacteria, which is added to the medium by limiting the concentration of magnesium salt added to the medium of the bacteria. The localization of the bacterium with respect to the metabolized new oily compound is changed from a form adsorbed to the compound to a form transferred to the compound.
さらに、本発明は、実質的にマグネシウム塩を含有しないか、又は、制限された濃度以下のマグネシウ塩を含有する水溶性培地に、ロドコッカス属細菌を添加する工程と、前記水溶性培地に、代謝対象物を添加して、当該代謝対象物を前記細菌によって代謝する工程と、を備えることを特徴とするものである。 Furthermore, the present invention includes a step of adding Rhodococcus bacteria to a water-soluble medium substantially free of magnesium salt or containing magnesium salt at a concentration not more than a limited concentration; Adding an object and metabolizing the object to be metabolized by the bacterium.
ロドコッカス属細菌は、ロドコッカス・エリスロポリス(Rhodococcus erythropolis)であり、好ましくはそのPR4株である。ロドコッカス・エリスロポリス(Rhodococcus erythropolis)属細菌は、天然に由来する菌株の他、炭化水素を分解・代謝する性質を維持・向上した形質転換体を含む。 The Rhodococcus bacterium is Rhodococcus erythropolis, preferably its PR4 strain. Rhodococcus erythropolis genus bacteria include transformants that maintain and improve the properties of decomposing and metabolizing hydrocarbons, in addition to naturally occurring strains.
ロドコッカス・エリスロポリス(Rhodococcus erythropolis)属細菌が、炭化水素内に転移して、これを分解できる場合の炭化水素には、特に制限はないが、このましくは、常温・常圧で液体状又は半固形状であり、炭素数が16以好ましくは13以下のn−アルカンと分岐アルカンが好ましい。 There are no particular restrictions on the hydrocarbons in which Rhodococcus erythropolis bacteria can be transferred to and decomposed into hydrocarbons. Preferred are n-alkanes and branched alkanes that are semi-solid and have 16 or less carbon atoms, preferably 13 or less carbon atoms.
前記特許文献1で説明したように、従来、低炭素数の炭化水素、例えば、炭素数が13以下の炭化水素に対しては、ロドコッカス・エリスロポリス(Rhodococcus erythropolis)属細菌は通常吸着するだけで、それに転移することはできず、これを代謝・分解することはできなかったが、本発明に従って、同細菌の培地に添加される無機塩の濃度を制限することによって、当該細菌を低炭素数の炭化水素に転移させることができる。 As described in Patent Document 1, conventionally, Rhodococcus erythropolis genus bacteria only adsorb to hydrocarbons having a low carbon number, for example, hydrocarbons having 13 or less carbon atoms. However, it was not possible to metabolize and decompose it, but according to the present invention, by limiting the concentration of inorganic salts added to the bacterial culture medium, Can be transferred to the hydrocarbon.
前記マグネシウムの濃度は、88.5 nM以下、好ましくは、8.9 nM以下、さらに好ましくは、0.9 nM以下である。前記マグネシウム塩は、特に、塩化マグネシウムである。 The concentration of magnesium is 88.5 nM or less, preferably 8.9 nM or less, and more preferably 0.9 nM or less. The magnesium salt is in particular magnesium chloride.
以上説明したように、本願発明によれば、ロドコッカス属微生物の炭化水素などの代謝対象成分に対する親和性を制御、即ち、当該成分に吸着する状態からこれに転移する状態に変化させることにより、これを効率よく分解することができる方法を提供することができる。 As described above, according to the present invention, by controlling the affinity of the Rhodococcus microorganism to the metabolic target component such as hydrocarbons, that is, by changing from the state adsorbed to the component to the state transferred to this, Can be efficiently decomposed.
1.ロドコッカス・エリスロポリス(Rhodococcus erythropolis)PR4株ロドコッカス属細菌を用いた代謝方法は、独立行政法人製品評価技術基盤機構バイオテクノロジー本部生物遺伝資源部門より入手できる。 1. A metabolic method using Rhodococcus erythropolis PR4 strain Rhodococcus genus bacteria can be obtained from the Biogenetic Resource Division, Biotechnology Division, National Institute of Technology and Evaluation.
2.培養液の作成
Rh-PR4の培地、溶液を以下のように作製した。
2. Preparation of culture solution
A medium and solution of Rh-PR4 were prepared as follows.
IB 液体培地: 約700 mlのミリQ水(Synthesis A10, Millipore)に10 gのグルコース (和光純薬工業)、10 gのイーストエキストラクト( Becton, Dickison and company )、0.2 gのMgCl2・6H2O (和光純薬工業)、0.10 gのCaCl2・2H2O (和光純薬工業)、0.10 gのNaCl (和光純薬工業)、0.02 gのFeCl2・4H2O (和光純薬工業)、0.50 gの(NH4)2SO4 (和光純薬工業)を加え、pHメーターを用いてpH 7.2に調整し、1Lまでメスアップして121℃で15分間オートクレーブした。 IB liquid medium: about 700 ml Milli-Q water (Synthesis A10, Millipore), 10 g glucose (Wako Pure Chemical Industries), 10 g yeast extract (Becton, Dickison and company), 0.2 g MgCl 2 · 6H 2 O (Wako Pure Chemical Industries), 0.10 g CaCl 2・ 2H 2 O (Wako Pure Chemical Industries), 0.10 g NaCl (Wako Pure Chemical Industries), 0.02 g FeCl 2・ 4H 2 O (Wako Pure Chemical Industries) ), 0.50 g of (NH 4 ) 2 SO 4 (Wako Pure Chemical Industries) was added, the pH was adjusted to 7.2 using a pH meter, the volume was increased to 1 L, and autoclaved at 121 ° C. for 15 minutes.
NP溶液:適当量のミリQ水に0.5 gの (NH4)2SO4、0.5 gのK2HPO4を加えて1Lまでメスアップし、121℃で15分間オートクレーブした。 NP solution: 0.5 g of (NH 4 ) 2 SO 4 and 0.5 g of K 2 HPO 4 were added to an appropriate amount of milli-Q water to make up to 1 L, and autoclaved at 121 ° C. for 15 minutes.
全ミネラル溶液:適当量のミリQ水に0.18 gのMgCl2・6H2O、0.10 gのCaCl2・2H2O、0.10 gのNaCl、0.02 gのFeCl2・4H2O、0.50 gの(NH4)2SO4 、0.50 gのK2HPO4を加えて1Lまでメスアップし、121℃で15分間オートクレーブした。 Total mineral solution: 0.18 g MgCl 2 · 6H 2 O, 0.10 g CaCl 2 · 2H 2 O, 0.10 g NaCl, 0.02 g FeCl 2 · 4H 2 O, 0.50 g ( NH 4 ) 2 SO 4 , 0.50 g of K 2 HPO 4 was added to make up to 1 L, and autoclaved at 121 ° C. for 15 minutes.
全ミネラル溶液に含まれる成分を個別に組み合わせた溶液を作製して。酢酸マグネシウム、乳酸マグネシウム、硝酸マグネシウム、硫酸マグネシウムについては、塩化マグネシウムと同濃度になるように調整し、適宜、(CH3COO)2・4H2O(和光純薬工業)、[CH3CH(OH)COO]2Mg・3H2O (和光純薬工業)、Mg(NO3)2・6H2O (和光純薬工業)、MgSO4 (和光純薬工業)を調整し培地に加えた。 Make a solution that combines the components contained in the total mineral solution individually. Magnesium acetate, magnesium lactate, magnesium nitrate, the magnesium sulfate was adjusted such that the magnesium chloride and the concentration, as appropriate, (CH 3 COO) 2 · 4H 2 O ( Wako Pure Chemical Industries), [CH 3 CH ( OH) COO] 2 Mg · 3H 2 O (Wako Pure Chemical Industries), Mg (NO 3 ) 2 · 6H 2 O (Wako Pure Chemical Industries), MgSO 4 (Wako Pure Chemical Industries) were prepared and added to the medium.
3.培養系の作製
まず、IB液体培地5 mlにPR4株を一白金耳摂取し、28 ℃、110 rpmで2〜3日培養した。この前培養液を、15 ml溶の遠心チューブに移し変え、4℃、10,000 rpmで10分間遠心分離した。その後、上清を捨て、5 mlの滅菌ミリQ水を加え、菌体をよく懸濁した後に、ボルテックスにて十分に攪拌した。
3. Preparation of culture system First, one platinum loop of PR4 strain was taken in 5 ml of IB liquid medium and cultured at 28 ° C. and 110 rpm for 2 to 3 days. This preculture was transferred to a 15 ml-dissolved centrifuge tube and centrifuged at 4 ° C. and 10,000 rpm for 10 minutes. Thereafter, the supernatant was discarded, 5 ml of sterilized milli-Q water was added, the cells were well suspended, and then sufficiently stirred by vortexing.
この懸濁液を再度4℃、10,000 rpmで10分間遠心し、上清を取り除いた。この操作を合計で6回行い菌体を洗浄した。次に、洗浄菌体を希釈し、菌体初期濃度が106cfu/mlになるように10 mlの各種培地に摂取した。最後に、アルカン類を終濃度5-10% (v/v)になるように摂取し、28℃、110 rpmで定常期になるまで培養した。 This suspension was centrifuged again at 4 ° C. and 10,000 rpm for 10 minutes, and the supernatant was removed. This operation was performed a total of 6 times to wash the cells. Next, the washed cells were diluted and ingested into 10 ml of various media so that the initial concentration of the cells was 10 6 cfu / ml. Finally, alkanes were ingested to a final concentration of 5-10% (v / v) and cultured at 28 ° C. and 110 rpm until the stationary phase was reached.
4.顕微鏡観察
得られた培養サンプルの有機層と水層が完全に分離した後、水層と有機層を別々に、あるいは、十分に懸濁して混合液をそれぞれ採取し、プレパラート(IWAKI)に滴下し、カバーガラス(IWAKI)を載せ、それぞれを水層、有機層、混合液として用意した。
4.Microscopic observation After the organic layer and the aqueous layer of the obtained culture sample are completely separated, the aqueous layer and the organic layer are separated separately or sufficiently suspended, and the mixed solutions are collected and prepared in a preparation (IWAKI). It was dropped and a cover glass (IWAKI) was placed, and each was prepared as an aqueous layer, an organic layer and a mixed solution.
システム生物顕微鏡(OLYMPUS BX50)のステージにサンプルを乗せ、スライドガラスにイマージョンオイルを一滴垂らし、対物レンズの倍率を100 倍にして観察した。各サンプルにつき、典型的な5視野を選択し、接続されている顕微鏡カメラ(OLYMPAS DP72)にて撮影し、画像処理ソフト(OLYMPAS DP2-BSW ver 2.1)にて解析した。 A sample was placed on the stage of a system biological microscope (OLYMPUS BX50), a drop of immersion oil was dropped on the slide glass, and the objective lens was magnified 100 times for observation. For each sample, five typical fields of view were selected, photographed with a connected microscope camera (OLYMPAS DP72), and analyzed with image processing software (OLYMPAS DP2-BSW ver 2.1).
5.結果と考察
菌体が吸着するアルカンの代表としてn-ドデカン(C12)、転移する代表としてプリスタン(C19)を用い、これらを含む二層培養系の各種培地成分を、個別または組み合わせて細胞の局在性が変化する条件の探索を試みた。IB培地の各主成分をイーストエキストラクト、グルコース、無機塩類に大別しそれぞれを個別に検討した。
5. Results and Discussion Using n-dodecane (C12) as a representative alkane adsorbed by cells and pristane (C19) as a representative for metastasis, cells can be combined with various medium components of these two-layer culture systems individually or in combination. Attempts were made to search for conditions that change the localization of the. The main components of IB medium were roughly divided into yeast extract, glucose, and inorganic salts, and each was examined individually.
5-1.イーストエキストラクト濃度の検討
イーストエキストラクトの濃度について検討を行った。IB液体培地中のイーストエキストラクトの終濃度が1.0、0.1、0.08、0.06、0.04、0.03、0.02、0.01%、0.001% (w/v)になるように培地を調製しC12またはC19を終濃度5%(v/v)にあるように添加した二層培養系を作製して、PR4株の生育および細胞の局在性に変化が出るか否かを検討した(図1)。
5-1. Examination of yeast extract concentration The concentration of yeast extract was examined. Prepare the medium so that the final concentration of yeast extract in IB liquid medium is 1.0, 0.1, 0.08, 0.06, 0.04, 0.03, 0.02, 0.01%, 0.001% (w / v). A bilayer culture system added at 5% (v / v) was prepared to examine whether or not the growth of PR4 strain and cell localization changed (FIG. 1).
コントロールとして生育させたC12またはC19を含むIB培地ではこれまでと同様の結果を示した。イーストエキストラクトが、1%から0.03%までの間では、培養液に白濁がみられたが0.02%以下の濃度では、白濁は見られなかった。 The IB medium containing C12 or C19 grown as a control showed the same results as before. When the yeast extract was between 1% and 0.03%, white turbidity was observed in the culture solution, but no white turbidity was observed at a concentration of 0.02% or less.
位相差顕微鏡で細胞の局在性を観察した結果、ドデカンを添加した0.1%から0.02% イーストエキストラクト溶液濃度の条件では、Rh-PR4の細胞が油滴の表面に吸着している様子が確認され、また、プリスタンを添加した場合にもRh-PR4細胞が油滴に転移している様子が確認された。以上の結果は、コントロールと同様の傾向であったことから、両者共に0.02%以上の条件では、細胞の局在性、即ち、細胞が炭化水素の油滴表面に吸着するか、それに転移するかの区別に影響は無いと判断した。 As a result of observing the localization of the cells with a phase contrast microscope, it was confirmed that the Rh-PR4 cells were adsorbed on the surface of the oil droplets under the condition of 0.1% to 0.02% yeast extract solution with dodecane added. In addition, it was confirmed that Rh-PR4 cells were transferred to the oil droplets when pristane was added. The above results were similar to those in the control, and in both cases, when the condition was 0.02% or more, cell localization, that is, whether the cells adsorbed to the surface of the hydrocarbon oil droplets or transferred to it. It was judged that there was no effect on the distinction.
一方で、0.02%以下の条件では、菌体を観察することはできなかった。このことから、PR4株が生育に必要なイーストエキストラクト濃度の限界値は0.02%であると考えられた。 On the other hand, microbial cells could not be observed under the condition of 0.02% or less. From this, it was considered that the limit value of yeast extract concentration necessary for growth of PR4 strain was 0.02%.
5-2.グルコース濃度の検討
続いてグルコースについて検討を行った。イーストエキストラクトを終濃度1%、グルコースの終濃度を1.0、0.1、0.08、0.06、0.04、0.02、0.01、0.001、0%になるように調整し、C12またはC19を添加した二層培養系を作製して、PR4株の生育および細胞の局在性に変化が出るか否かを検討した(図2)。その結果、培養の様子、顕微鏡観察ともに全てコントロールと同様の傾向が確認された。
5-2. Examination of glucose concentration Subsequently, glucose was examined. Adjust the yeast extract so that the final concentration is 1%, the final concentration of glucose is 1.0, 0.1, 0.08, 0.06, 0.04, 0.02, 0.01, 0.001, 0%, and add a C12 or C19 added bilayer culture system. It was prepared and examined whether changes in the growth and cell localization of the PR4 strain occurred (FIG. 2). As a result, the same tendency as the control was confirmed both in the culture state and the microscopic observation.
次に、イーストエキストラクトが添加されていない条件を設定し、これにグルコースを上述した条件で添加し、検討した。その結果、全ての条件で細胞の増殖を確認する事はできなかった。このことから、同菌の供試した二層培養環境下での生育には、グルコースは影響しないもものの、イーストエキストラクトが増殖に必須であることが示唆された。 Next, the conditions in which the yeast extract was not added were set, and glucose was added to the conditions mentioned above and examined. As a result, cell proliferation could not be confirmed under all conditions. This suggests that yeast extract is essential for growth, although glucose does not affect the growth in the two-layer culture environment tested by the same bacterium.
5-3.グルコース無添加時のイーストエキストラクト濃度の検討
前述のようにグルコースがPR4株の生育への影響がないことが分かったため、グルコースを添加しない条件でのイーストエキストラクト濃度の下限を検討した(図3)。その結果グルコースを添加した条件の場合と同様に、生育下限濃度が0.02%でそれ以下の条件では生育が確認できなかった。
5-3. Examination of the concentration of yeast extract without addition of glucose As described above, it was found that glucose has no effect on the growth of PR4 strain, so the lower limit of yeast extract concentration under the condition of no addition of glucose was examined. (Fig. 3). As a result, as in the case where glucose was added, the growth lower limit concentration was 0.02%, and growth could not be confirmed under these conditions.
以上の結果、PR4株の生育に必要な成分はイーストエキストラクトで、その最低濃度は0.02%であることが明らかとなった。この時、供試した1.0、0.1、0.08、0.06、0.04、0.02%までの全ての条件で、PR4株は、C19添加の場合には転移型、C12添加の場合には吸着型を示しながら生育したことから、イーストエキストラクトおよびグルコースは、同菌の細胞の局在性に影響を与えないと判断された。 As a result, it was revealed that the component necessary for growth of PR4 strain was yeast extract, and its minimum concentration was 0.02%. At this time, under all conditions up to 1.0, 0.1, 0.08, 0.06, 0.04, and 0.02%, the PR4 strain grew while showing a transfer type when C19 was added and an adsorbed type when C12 was added. Therefore, it was determined that yeast extract and glucose do not affect the localization of cells of the same fungus.
5-4.無機塩類の検討
無機塩類について検討を行った。IB培地中に添加されている全無機塩類のみで調整した培地を作製し、これにC12またはC19を添加し、これまでと同様の条件で培養し、観察した(図4)。
5-4. Examination of inorganic salts Inorganic salts were examined. A medium prepared only with all the inorganic salts added to the IB medium was prepared, and C12 or C19 was added thereto, and cultured and observed under the same conditions as before (FIG. 4).
その結果、K2HPO4及び(NH4) 2SO4が含まれない全ての条件ではPR4株の生育が確認できなかったが、K2HPO4及び(NH4) 2SO4だけを含む条件ではC19、C12共に生育が確認された。
C19を添加した場合には、これまで同様、細胞が転移している様子が確認されたが、興味深いことにC12を添加した場合にも細胞が油滴の中に転移して存在している様子が確認された。
Conditions As a result, in all the conditions that do not contain K 2 HPO 4 and (NH 4) 2 SO 4 containing although growth of PR4 strain can not be confirmed, K 2 HPO 4 and (NH 4) only 2 SO 4 In C19 and C12, growth was confirmed.
When C19 was added, it was confirmed that the cells had been transferred as before, but interestingly, when C12 was added, the cells were transferred and existed in the oil droplets. Was confirmed.
一方で、全無機塩類を添加した場合には、PR4株は、C12に転移することなく、吸着して存在することが分かっていることから、使用した無機塩類の中に上記条件での転移を阻害している成分があると予想し、続いて、その成分を検討した。 On the other hand, when all inorganic salts are added, the PR4 strain is known to be adsorbed and not transferred to C12. We anticipated that there was an inhibitory component, and then examined that component.
アルカンとしてC12、無機塩類としてK2HPO4及び(NH4)2SO4を基本とした培地に、各種無機塩をIB培地と同濃度になるようにそれぞれ添加して、PR4株のアルカンに対する局在性を確認したところ、MgCl2を添加した場合、PR4株は油滴へ転移することなく、吸着にして存在しているに過ぎないことが確認された(図5)。以上のことから、MgCl2を添加することで同菌のアルカンに対する局在性を制御できることが分かった。 Various mineral salts were added to the medium based on C12 as alkane and K 2 HPO 4 and (NH 4 ) 2 SO 4 as inorganic salts at the same concentration as IB medium, respectively. When the presence was confirmed, it was confirmed that when MgCl 2 was added, the PR4 strain was only adsorbed and not transferred to the oil droplets (FIG. 5). From the above, it was found that the localization of the bacterium to alkane can be controlled by adding MgCl 2 .
5-5.マグネシウム塩の濃度の検討
MgCl2がPR4株の炭化水素に対する局在性を変化させることに関与することが分かったので、さらに、MgCl2濃度が、細菌の局在性に及ぼす影響を検討した。IB培地のMgCl2濃度が885 mMであることから、K2HPO4及び(NH4) 2SO4の濃度を一定にした培地に、段階的に希釈したマグネシウム塩の濃度を順次低下させた培地を作製し、同菌の細胞の炭化水素に対する局在性を調べた(図6)。
5-5.Concentration of magnesium salt
Since MgCl 2 was found to be involved in changing the localization of PR4 strains to hydrocarbons, the effect of MgCl 2 concentration on bacterial localization was further investigated. Since the MgCl 2 concentration of the IB medium is 885 mM, the medium in which the concentration of magnesium salt diluted stepwise is sequentially reduced to a medium in which the concentrations of K 2 HPO 4 and (NH 4 ) 2 SO 4 are constant. And the localization of the cells of the same bacteria to hydrocarbons was examined (FIG. 6).
細胞の局在性を明快に転移型、吸着型のいずれかに区別できなかったので、顕微鏡写真を、吸着、一部に転移を含む吸着、一部に吸着を含む転移、転移の4つのパターンに分け、マグネシウム塩の濃度による推移に合わせて、4つのパターンの割合を検討した。 Since the cell localization could not be clearly distinguished as either metastatic or adsorbed, the micrographs were divided into four patterns: adsorption, partial adsorption, partial adsorption, and transition. The ratio of the four patterns was examined according to the transition according to the magnesium salt concentration.
その結果、コントロールのIB培地と同濃度の条件でも一部に転移している菌体を確認したが、MgCl2濃度の減少と共に吸着型の菌体の割合が少なくなり、全ての写真が転移型になったのは、塩化マグネシウムの濃度が88.5 nMであった。 As a result, cells that had partially transferred even under the same concentration conditions as the control IB medium were confirmed, but as the MgCl 2 concentration decreased, the proportion of adsorbed cells decreased, and all photographs were transferred. The concentration of magnesium chloride was 88.5 nM.
一方、MgCl2無添加時でも一部吸着している菌体も確認されたが、多くの菌体がC12中に転移していることが確認された。 On the other hand, although some cells were adsorbed even when MgCl 2 was not added, it was confirmed that many cells were transferred into C12.
以上の結果、MgCl2濃度を減少させていくことにより、その局在性は転移型から吸着型へ変化する方向に向かい、その濃度が8.9 mMの付近で転移型と吸着型の割合が逆転し、それ以下の濃度では転移型の菌体の割合が多くなることが示唆された。 As a result, by decreasing the MgCl 2 concentration, the localization tends to change from the transition type to the adsorption type, and the ratio of the transition type to the adsorption type is reversed when the concentration is around 8.9 mM. It was suggested that the concentration of metastatic cells increased at lower concentrations.
また、既述の現象が塩化マグネシウムに特有な現象かどうかを検討するため、上述したK2HPO4及び(NH4)2SO4のみを含む培地に、硫酸マグネシウム、硝酸マグネシウム、酢酸マグネシウム、乳酸マグネシウムをIB倍地中の塩化マグネシウムと同濃度になるように添加し、C12存在下で局在性を検討した。その結果、硫酸マグネシウム、硝酸マグネシウムを添加した条件でも、塩化マグネシウムと同様に細胞はC12粒子表面に吸着して存在した。 In addition, in order to examine whether the phenomenon described above is a phenomenon peculiar to magnesium chloride, the above-mentioned medium containing only K 2 HPO 4 and (NH 4 ) 2 SO 4 is added with magnesium sulfate, magnesium nitrate, magnesium acetate, lactic acid. Magnesium was added to the same concentration as magnesium chloride in the IB medium, and localization was examined in the presence of C12. As a result, even when magnesium sulfate and magnesium nitrate were added, the cells were adsorbed on the surface of the C12 particles like magnesium chloride.
したがって、硫酸マグネシウム、硝酸マグネシウム等塩化マグネシウム塩以外のマグネシウム塩の濃度を制限することにより、ロドコッカス属の細菌の炭化水素に対する局在性を調整できることが分かった。 Therefore, it was found that the localization of Rhodococcus bacteria to hydrocarbons can be adjusted by limiting the concentration of magnesium salts other than magnesium chloride such as magnesium sulfate and magnesium nitrate.
Claims (5)
前記親油性溶媒は、炭素数13以下の炭化水素であり、
前記培地として、(NH 4 ) 2 SO 4 とK 2 HPO 4 とを含むNP溶液を用い、
前記無機塩として、マグネシウム塩を無添加または88.5nM以下に調整する親油性溶媒処理方法。 A form in which Rhodococcus bacteria are added to a medium containing a lipophilic solvent, the concentration of the inorganic salt in the medium is adjusted for the localization of Rhodococcus bacteria in the medium, and the Rhodococcus bacteria are adsorbed to the lipophilic solvent And the ratio of the form transferred to the lipophilic solvent, metabolizing Rhodococcus bacteria and decomposing the lipophilic solvent ,
The lipophilic solvent is a hydrocarbon having 13 or less carbon atoms,
As the medium, an NP solution containing (NH 4 ) 2 SO 4 and K 2 HPO 4 is used,
A lipophilic solvent treatment method in which a magnesium salt is not added as the inorganic salt or is adjusted to 88.5 nM or less .
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