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JP5880447B2 - Method for transporting microbial cells - Google Patents
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JP5880447B2 - Method for transporting microbial cells - Google Patents

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JP5880447B2
JP5880447B2 JP2012552761A JP2012552761A JP5880447B2 JP 5880447 B2 JP5880447 B2 JP 5880447B2 JP 2012552761 A JP2012552761 A JP 2012552761A JP 2012552761 A JP2012552761 A JP 2012552761A JP 5880447 B2 JP5880447 B2 JP 5880447B2
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nitrile hydratase
microbial cells
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竹内 雅人
雅人 竹内
文昭 渡辺
文昭 渡辺
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Mitsubishi Rayon Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/04Preserving or maintaining viable microorganisms
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/96Stabilising an enzyme by forming an adduct or a composition; Forming enzyme conjugates
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/78Hydrolases (3) acting on carbon to nitrogen bonds other than peptide bonds (3.5)
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/88Lyases (4.)
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    • C12YENZYMES
    • C12Y305/00Hydrolases acting on carbon-nitrogen bonds, other than peptide bonds (3.5)
    • C12Y305/05Hydrolases acting on carbon-nitrogen bonds, other than peptide bonds (3.5) in nitriles (3.5.5)
    • C12Y305/05001Nitrilase (3.5.5.1)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12YENZYMES
    • C12Y402/00Carbon-oxygen lyases (4.2)
    • C12Y402/01Hydro-lyases (4.2.1)
    • C12Y402/01084Nitrile hydratase (4.2.1.84)

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Description

本発明は、ニトリルヒドラターゼ活性を有する微生物菌体を密閉容器に充填し輸送する際に、密閉容器内部の気相部を全容積の20%以下とすることにより、ニトリルヒドラターゼ活性を安定に保持したまま輸送する方法に関する。   The present invention stably stabilizes the nitrile hydratase activity by filling the sealed microbial cell having nitrile hydratase activity into a sealed container and transporting it to 20% or less of the total volume of the gas phase inside the sealed container. The present invention relates to a method of transporting while holding.

微生物の産生する酵素は、化学変換反応の触媒として多くの場面で使用されている。とりわけ、ニトリル基の水和又は加水分解能を有するニトリルヒドラターゼ、ニトリラーゼ等を利用することにより、化学工業上重要なアミド、カルボン酸、α-ヒドロキシカルボン酸等を安価に製造することが可能になる。更に、光学特異的水和又は光学特異的加水分解能を持つ上記酵素を利用することにより、医薬、農薬の製造原料として重要な光学活性カルボン酸、アミノ酸、α-ヒドロキシカルボン酸等の製造も可能になる。   Enzymes produced by microorganisms are used in many situations as catalysts for chemical conversion reactions. In particular, by using nitrile hydratase, nitrilase, etc., which have nitrile group hydration or hydrolytic ability, it becomes possible to produce amides, carboxylic acids, α-hydroxycarboxylic acids and the like important in the chemical industry at low cost. . Furthermore, by using the above-mentioned enzyme having optical specific hydration or optical specific hydrolyzing ability, it is possible to produce optically active carboxylic acids, amino acids, α-hydroxycarboxylic acids and the like that are important as raw materials for pharmaceuticals and agricultural chemicals. Become.

微生物酵素を触媒とする化学変換反応においては、培養及び集菌した微生物菌体の酵素の活性を使用時まで安定に維持しておく必要がある。すなわち、保管または輸送時に雑菌が混入して、腐敗し、あるいは溶菌することで、微生物酵素の触媒能が失われたり、低下したりしないように酵素の活性を維持しなければならない。そこで一般的には、安定剤、代謝阻害剤、高濃度塩類の存在下で保存することにより微生物菌体保存時の微生物酵素の失活や腐敗、溶菌を抑制し、化学変換反応に使用している。上記安定剤等を添加しない場合には、凍結や冷蔵、或いは通期撹拌により酵素の活性を維持しながら保管または輸送する。   In a chemical conversion reaction using a microbial enzyme as a catalyst, it is necessary to stably maintain the enzyme activity of cultured and collected microbial cells until use. That is, the activity of the enzyme must be maintained so that the microbial enzyme's catalytic ability is not lost or deteriorated by contamination or lysis or lysis during storage or transportation. Therefore, in general, by storing in the presence of stabilizers, metabolic inhibitors and high-concentration salts, inactivation, decay, and lysis of microbial enzymes during microbial cell storage are suppressed, and used for chemical conversion reactions. Yes. When the stabilizer is not added, it is stored or transported while maintaining the activity of the enzyme by freezing, refrigeration, or full-time stirring.

特許文献1(特開2004-305066号公報)には、ニトリル類、アミド類、カルボン酸類等の安定剤の添加による微生物菌体の保存方法が開示され、特許文献2(特開2005-295815号公報)には、アジ化化合物等の代謝阻害剤の添加による微生物菌体の保存方法が開示され、特許文献3(特開2001-149065号公報)には、微生物菌体の培養液成分を懸濁液に添加することによる微生物菌体の保存方法が開示されている。また、特許文献4(特許第3163224号)には高濃度の無機塩類の添加による保存方法が開示されている。更に、凍結により保存する方法については、特許文献5(特開2003-219870号公報)が知られており、通気撹拌により保存する方法については、特許文献6(特開2003-144144号公報)が知られている。   Patent Document 1 (Japanese Patent Laid-Open No. 2004-305066) discloses a method for preserving microbial cells by adding stabilizers such as nitriles, amides, and carboxylic acids, and Patent Document 2 (Japanese Patent Laid-Open No. 2005-295815). Discloses a method for preserving microbial cells by adding a metabolic inhibitor such as an azide compound, and Patent Literature 3 (Japanese Patent Application Laid-Open No. 2001-149065) discloses a culture solution component of microbial cells. A method for preserving microbial cells by adding to a suspension is disclosed. Patent Document 4 (Patent No. 3163224) discloses a storage method by adding high-concentration inorganic salts. Furthermore, Patent Document 5 (Japanese Patent Laid-Open No. 2003-21870) is known as a method of storing by freezing, and Patent Document 6 (Japanese Patent Laid-Open No. 2003-144144) is known as a method of storing by aeration stirring. Are known.

特開2004-305066号公報JP 2004-305066 A 特開2005-295815号公報JP 2005-295815 A 特開2001-149065号公報Japanese Patent Laid-Open No. 2001-149065 特許第3163224号Japanese Patent No. 3163224 特開2003-219870号公報JP 2003-21870 A 特開2003-144144号公報JP 2003-144144 A

これまでに知られている保存方法のうち、安定剤等の添加剤を使用する方法は、後の工程で添加剤等を分離する必要があるため、製品の品質に影響を与える恐れがあり、更に製造方法が煩雑になる。菌体を凍結させる方法で保存された微生物菌体の懸濁液は、凍結、融解操作が煩雑であるなど、その取り扱い性に問題があり、またその操作に伴って酵素活性が失われたり、低下したりする恐れがある。また冷蔵による保存では、雑菌の増殖防止と菌体細胞の安定化の観点から好ましいが、低温を保つ設備や電力が必要になり、冷却コスト面での負担が大きい。微生物菌体を高濃度の無機塩類水溶液中に保存する方法では、使用時に菌体を十分に洗浄する必要があり、添加する無機塩類や廃水処理にコストが掛かるというデメリットがある。通気撹拌等により微生物菌体の酵素活性がある程度維持されることも報告されているが、酵素によりその効果は一様ではなく、また通気及び撹拌に動力を必要としコスト面での負担も大きい。そこで、従来技術に加えて、さらに安定的はニトリルヒドラターゼ活性を有した菌体の保存方法が望まれる。   Among the storage methods known so far, the method using an additive such as a stabilizer needs to separate the additive in a later step, which may affect the quality of the product, Furthermore, the manufacturing method becomes complicated. Suspension of microbial cells stored by the method of freezing microbial cells has problems in handling such as complicated freezing and thawing operations, and the enzyme activity is lost with the operation, There is a risk of lowering. In addition, storage by refrigeration is preferable from the viewpoint of preventing proliferation of various bacteria and stabilization of bacterial cells, but requires equipment and electric power to maintain a low temperature, and the burden on cooling cost is large. In the method of storing microbial cells in an aqueous solution of high-concentration inorganic salt, it is necessary to sufficiently wash the microbial cells at the time of use, and there is a demerit that costs are required for the treatment of added inorganic salts and waste water. Although it has been reported that the enzyme activity of the microbial cells is maintained to some extent by aeration stirring, etc., the effect is not uniform depending on the enzyme, and power is required for aeration and agitation, and the cost burden is large. Therefore, in addition to the prior art, a more stable method for preserving bacterial cells having nitrile hydratase activity is desired.

本発明者らは、培養、集菌して得られた微生物菌体の懸濁液を、安価でしかも安定的に輸送する条件について鋭意検討した結果、輸送に使用する容器内部の気相を20%以下とすることで安定的にニトリルヒドラターゼ活性を有した菌体の保存及び輸送ができることを見出し、本発明を完成するに至った。   As a result of intensive studies on conditions for transporting a suspension of microbial cells obtained by culturing and collecting microorganisms at low cost and stably, the gas phase inside the container used for transport is 20%. It has been found that the cells having nitrile hydratase activity can be stably stored and transported when the content is less than or equal to%, and the present invention has been completed.

すなわち、本発明は、ニトリルヒドラターゼ活性を有する微生物菌体を密閉可能な容器内に保存する方法であって、前記微生物菌体を含む懸濁液が充填された前記容器内の気相部を容器内部の全容積の2%以上20%以下とすることを特徴とする前記方法である。
また、本発明は、ニトリルヒドラターゼ活性を有する微生物菌体を密閉可能な容器を用いて輸送する方法であって、前記微生物菌体を含む懸濁液が充填された前記容器内の気相部を容器内部の全容積の2%以上20%以下とすることを特徴とする前記方法である。
本発明の方法において、前記容器内の気相部の割合は、5%以上20%以下とすることが好ましい。また、前記保存又は輸送温度は、例えば氷点〜35℃の温度である。さらに、前記菌体懸濁液の分散媒は、有機酸水溶液であり、有機酸としては例えばアクリル酸が挙げられる。
That is, the present invention is a method for storing microbial cells having nitrile hydratase activity in a sealable container, wherein a gas phase portion in the container filled with a suspension containing the microbial cells is provided. It is the said method characterized by setting it as 2% or more and 20% or less of the total volume inside a container.
The present invention also relates to a method for transporting microbial cells having nitrile hydratase activity using a sealable container, wherein the gas phase portion in the container filled with a suspension containing the microbial cells. Is 2% to 20% of the total volume inside the container.
In the method of the present invention, the proportion of the gas phase part in the container is preferably 5% or more and 20% or less. The storage or transport temperature is, for example, a temperature of freezing point to 35 ° C. Furthermore, the dispersion medium of the cell suspension is an organic acid aqueous solution, and examples of the organic acid include acrylic acid.

本発明によれば、容器内部の気相部を2%以上20%以下となるように菌体懸濁液を充填することにより、多量の菌体を、室温下、無撹拌でもニトリルヒドラターゼ等の酵素活性を維持したまま保存及び輸送することが可能となる。更に、本発明によれば、従来の保存方法で必要とされてきた労力や冷却コストを大幅に削減することができ、工業的に満足し得る微生物菌体の保存方法が提供される。   According to the present invention, by filling the cell suspension so that the gas phase inside the container is 2% or more and 20% or less, nitrile hydratase or the like can be obtained even at room temperature without stirring. It can be stored and transported while maintaining its enzyme activity. Furthermore, according to the present invention, it is possible to greatly reduce the labor and cooling cost required in the conventional storage method, and to provide a method for storing microbial cells that can be industrially satisfied.

本発明は、ニトリルヒドラターゼ活性を有する微生物菌体を密閉可能な容器内に保存する方法、及び微生物菌体を密閉可能な容器を用いて輸送する方法に関する。本発明の方法は、前記微生物菌体を含む懸濁液を、容器内の気相部が容器内部の全容積の2%以上20%以下となるように充填するものである。
なお、本明細書において引用した文献、および公開公報、特許公報その他の特許文献は、参照として本明細書に組み込むものとする。また、2011年1月14日に出願し、本願優先権主張の基礎となる特願2011-005780号(JP2011-005780)の特許請求の範囲、明細書、図面および要約書の開示内容は、その全体が参照として本明細書に組み入れられる。
The present invention relates to a method for storing microbial cells having nitrile hydratase activity in a sealable container, and a method for transporting the microbial cells using a sealable container. In the method of the present invention, the suspension containing the microbial cells is filled so that the gas phase part in the container is 2% or more and 20% or less of the total volume in the container.
It should be noted that documents cited in the present specification, as well as published gazettes, patent gazettes, and other patent documents are incorporated herein by reference. In addition, the disclosure content of the claims, description, drawings and abstract of Japanese Patent Application No. 2011-005780 (JP2011-005780), which was filed on January 14, 2011 and is the basis for claiming priority of the present application, The entirety is incorporated herein by reference.

本発明においてニトリルヒドラターゼ活性を有する微生物菌体は、目的とする酵素触媒を生産し菌体内に蓄積又は菌体外に分泌する性質を有するものである。この微生物には自然界より単離された微生物及び遺伝子組換え微生物が含まれる。このような微生物の代表例としては、例えば、ニトリルヒドラターゼ活性を持つロドコッカス(Rhodococcus)属、ゴルドナ(Gordona)属、シュードモナス(Pseudomonas)属、シュードノカルディア(Pseudonocardia)属、ジオバチルス(Geobacillus)属に属する微生物菌体が挙げられる。更に、これらの微生物のニトリルヒドラターゼ遺伝子を導入した組換え微生物菌体が挙げられる。中でも工業的には、ロドコッカス属、ゴルドナ属並びにこれらの微生物のニトリルヒドラターゼ遺伝子を導入した組換え大腸菌及び組換えロドコッカス属細菌が好ましい。例えば、ロドコッカス属の微生物の具体例としては、特公平6-55148号公報に記載されるロドコッカス・ロドクロスJ-1株(Rhodococcus rhodochrous J-1)が挙げられる。当該株は、受託番号「FERM BP−1478」として、1987年9月18日
に独立行政法人産業技術総合研究所特許生物寄託センター(茨城県つくば市東1−1−1 中央第6(以下、本明細書において同様))に寄託されている。
In the present invention, the microbial cell having nitrile hydratase activity has the property of producing the target enzyme catalyst and accumulating it in the cell or secreting it outside the cell. These microorganisms include microorganisms isolated from nature and genetically modified microorganisms. Representative examples of such microorganisms include, for example, the genus Rhodococcus having nitrile hydratase activity, the genus Gordona, the genus Pseudomonas, the genus Pseudonocardia, and the genus Geobacillus. The microbial cell to which it belongs is mentioned. Furthermore, the recombinant microorganisms which introduce | transduced the nitrile hydratase gene of these microorganisms are mentioned. Among them, Rhodococcus genus, Gordona genus, and recombinant Escherichia coli and recombinant Rhodococcus bacteria into which nitrile hydratase genes of these microorganisms are introduced are preferable from an industrial viewpoint. For example, specific examples of microorganisms belonging to the genus Rhodococcus include Rhodococcus rhodochrous J-1 described in JP-B-6-55148. This strain was registered under the accession number “FERM BP-1478” on September 18, 1987 at the National Institute of Advanced Industrial Science and Technology, Patent Biological Depositary Center (1-1-1 Higashi 1-1-1 Tsukuba City, Ibaraki) The same in the description))).

ニトリルヒドラターゼとは、ニトリル化合物を加水分解して、対応するアミド化合物を生成する能力を持つ酵素をいうものである。ニトリルヒドラーゼをコードする核酸及びその配列の例としては、前記特許文献2に記載されるものが挙げられる。このような核酸は、通常の分子生物学的手法によって、微生物細胞内に導入可能である(これらの分子学的手法については、以下を参照:Sambrook, Fritsch and Maniatis, ”Molecular Cloning: A Laboratory Manual” 2nd Edition (1989), Cold Spring Harbor Laboratory Press)。   Nitrile hydratase refers to an enzyme having the ability to hydrolyze a nitrile compound to produce a corresponding amide compound. Examples of nucleic acids encoding nitrile hydrase and sequences thereof include those described in Patent Document 2. Such nucleic acids can be introduced into microbial cells by conventional molecular biology techniques (see Sambrook, Fritsch and Maniatis, “Molecular Cloning: A Laboratory Manual ”2nd Edition (1989), Cold Spring Harbor Laboratory Press).

本発明において、「密閉可能な容器」とは、輸送及び/又は保存に供するために微生物懸濁液を充填した後に密閉できる容器である。輸送時に容器内外で内容物の移動が行われない容器であれば、如何なる形態のものでも構わないが、工業的目的に供するためには、ドラム缶、コンテナ、タンクローリー車等が使われる。本容器の容量は、特に限定されないが、工業的目的に供するためには、200Lのものが好ましい。容器の材質も特に限定されないが、工業的目的に供するためには、ポリエチレン、ポリプロピレンなどプラスチック容器や、鉄・ステンレスなど金属製の容器が好ましい。以下、本発明において使用する容器を「密閉容器」という。   In the present invention, a “sealable container” is a container that can be sealed after being filled with a microbial suspension for transport and / or storage. Any container may be used as long as the contents are not moved inside and outside the container during transportation. For industrial purposes, a drum can, a container, a tank truck, and the like are used. The capacity of the container is not particularly limited, but 200 L is preferable for industrial purposes. The material of the container is not particularly limited, but for industrial purposes, a plastic container such as polyethylene or polypropylene, or a metal container such as iron or stainless steel is preferable. Hereinafter, the container used in the present invention is referred to as a “sealed container”.

本発明において、容器内部の気相部の割合は2%以上20%以下とする。「2%以上20%以下」とは、密閉容器を静置した状態で該容器中の菌体液の存在していない気相部の容積の割合が、全容積の2%以上20%以下であることを指す。本気相部のガス組成は特に限定されないが、工業的な理由から空気が入ることが一般的である。また、気相部は、通常は容器内の上部である。   In the present invention, the proportion of the gas phase inside the container is 2% or more and 20% or less. “2% or more and 20% or less” means that the ratio of the volume of the gas phase portion in which the bacterial cell liquid does not exist in the sealed container is 2% or more and 20% or less of the total volume. Refers to that. The gas composition of the gas phase portion is not particularly limited, but air is generally entered for industrial reasons. The gas phase part is usually the upper part in the container.

通常、密閉容器で液体を保存又は運搬する場合、状況に応じて液体の充填率を自由に設定するが、本発明においては、気相部が容器容積に対して20%以下である。但し、2%を下回ると、内容物の温度変化による膨張・収縮が起こる際、容器の変形を引き起こすおそれがある。従って、輸送時の密閉容器内部の気相部は、容器容積に対して2〜20%、3〜20%、4〜20%、5〜20%などとすることができ、より好ましくは3〜15%、さらに好ましくは4〜10%である。   Usually, when storing or transporting a liquid in an airtight container, the filling rate of the liquid is freely set according to the situation, but in the present invention, the gas phase part is 20% or less with respect to the container volume. However, if it is less than 2%, the container may be deformed when the contents are expanded or contracted due to a temperature change. Therefore, the gas phase inside the sealed container at the time of transportation can be 2 to 20%, 3 to 20%, 4 to 20%, 5 to 20%, etc., more preferably 3 to 20%. 15%, more preferably 4 to 10%.

本発明において、「保存」とは、菌体懸濁液を密閉容器内に充填した後に密閉し、静置しておくことをいう。また、輸送後に実際に使用されるまでに静置しておくことも「保存」に含まれる。保存期間は、懸濁液を充填してから輸送開始までの時間(保存1)、及び輸送終了から現場での使用開始までの時間(保存2)である。例えば保存1の場合は1時間〜180日であり、保存2の場合は1時間〜180日であるが、これらの期間に限定されるものではない。また、本発明において、「輸送」とは、密閉容器を用いて菌体懸濁液を移動することを意味する。一般的には、トラックやフォークリフト、タンクローリー、船に密閉容器を積載して移動する。   In the present invention, “preservation” means that the bacterial cell suspension is sealed in a sealed container and then allowed to stand. In addition, “preservation” includes leaving it still before it is actually used after transportation. The storage period is the time from the filling of the suspension to the start of transportation (storage 1) and the time from the end of transportation to the start of use at the site (storage 2). For example, in the case of storage 1, it is 1 hour to 180 days, and in the case of storage 2, it is 1 hour to 180 days, but it is not limited to these periods. In the present invention, “transport” means moving the cell suspension using a sealed container. Generally, trucks, forklifts, tank trucks, and ships are loaded with sealed containers and moved.

保存中及び輸送中の温度に関しては、菌体及び酵素の腐敗・分解を抑制するため低温であることがより好ましい。具体的には氷点〜35℃、好ましくは氷点〜30℃、より好ましくは氷点〜20℃、さらに好ましくは氷点〜10℃で行われる。ここで、「氷点」とは、菌体懸濁液の固体状態と液体状態の平衡温度を意味し、懸濁液の組成や保存容器内の圧力によって変化する温度である。   Regarding the temperature during storage and transportation, it is more preferable that the temperature is low in order to suppress the decay and decomposition of bacterial cells and enzymes. Specifically, it is carried out at a freezing point to 35 ° C, preferably a freezing point to 30 ° C, more preferably a freezing point to 20 ° C, and even more preferably a freezing point to 10 ° C. Here, “freezing point” means the equilibrium temperature between the solid state and the liquid state of the bacterial cell suspension, and is a temperature that varies depending on the composition of the suspension and the pressure in the storage container.

本発明に於いては、前記保存期間の後にニトリルヒドラターゼ活性が輸送開始前の90%以上、好ましくは95%以上、より好ましくは、98%以上、更に好ましくは、99%以上、最も好ましくは100%残存する。ニトリルヒドラターゼ活性の残存率は、当該技術分野で公知のいずれかの方法により測定できるが、例えば、保存開始前と保存後の基質(例えば、アクリロニトリル)に対するアクリルアミド生成反応速度を比較すること等により測定することが可能である。   In the present invention, after the storage period, the nitrile hydratase activity is 90% or more, preferably 95% or more, more preferably 98% or more, more preferably 99% or more, most preferably before the start of transportation. 100% remains. The residual ratio of nitrile hydratase activity can be measured by any method known in the art. For example, by comparing the reaction rate of acrylamide formation with respect to a substrate (for example, acrylonitrile) before and after storage, etc. It is possible to measure.

本発明において、懸濁液の分散媒とは、保存対象となる微生物菌体の懸濁に使用する溶液を意味する。該分散媒は、好ましくは、有機酸水溶液である。当該有機酸水溶液の有機酸の濃度は任意であるが、低過ぎると酵素活性の低下を招き、一方で、高過ぎると後の工程でこれを除去する際に作業が煩雑になるため、10〜100mmol/Lであることが好ましい。   In the present invention, the suspension dispersion medium means a solution used for suspending microbial cells to be stored. The dispersion medium is preferably an organic acid aqueous solution. The concentration of the organic acid in the aqueous organic acid solution is arbitrary, but if it is too low, the enzyme activity is reduced. On the other hand, if it is too high, the operation becomes complicated when removing it in a later step. It is preferable that it is 100 mmol / L.

本発明に於いて浸漬液の組成は、酵素活性を阻害しない有機酸水溶液であれば特に限定されない。有機酸としては、例えば、アクリル酸、ギ酸、酢酸、プロピオン酸、酪酸、シュウ酸、カルボン酸が挙げられ、中でもアクリルアミドの品質を維持する点で、アクリル酸が好ましい。   In the present invention, the composition of the immersion liquid is not particularly limited as long as it is an organic acid aqueous solution that does not inhibit enzyme activity. Examples of the organic acid include acrylic acid, formic acid, acetic acid, propionic acid, butyric acid, oxalic acid, and carboxylic acid. Among them, acrylic acid is preferable in terms of maintaining the quality of acrylamide.

本発明の懸濁液の調製では、ニトリルヒドラターゼ活性を有する微生物菌体は、当該技術分野で公知のいずれの濃縮方法で濃縮してもよいが、好ましくは、膜分離又は遠心分離によって濃縮される。濃縮を膜分離で行う場合、0.02〜0.45μmの孔径を有する膜を用いることが好ましい。このような膜は、市販されており、例えば、中空糸膜モジュール(クラレ社、細孔径0.05μm、表面積39000m)等が挙げられる。また、濃縮を遠心分離で行う場合、分離板型連続遠心分離機を用いることが好ましい。In the preparation of the suspension of the present invention, the microbial cells having nitrile hydratase activity may be concentrated by any concentration method known in the art, but are preferably concentrated by membrane separation or centrifugation. The When the concentration is performed by membrane separation, it is preferable to use a membrane having a pore size of 0.02 to 0.45 μm. Such a membrane is commercially available, and examples thereof include a hollow fiber membrane module (Kuraray Co., Ltd., pore diameter 0.05 μm, surface area 39000 m 2 ). Moreover, when concentrating by centrifugation, it is preferable to use a separation plate type continuous centrifuge.

以下、実施例により本発明の実施方法を更に詳細に説明するが、これらの実施例は、本発明の例示を目的とするものであり、本発明を限定するものではない。以下の実施例及び比較例に於ける%表示は特に記載のない限り、質量%である。   EXAMPLES Hereinafter, although the Example demonstrates the implementation method of this invention further in detail, these Examples aim at the illustration of this invention, and do not limit this invention. In the following examples and comparative examples,% display is mass% unless otherwise specified.

実施例1および2、比較例1
培養
ニトリルヒドラターゼ活性を有するロドコッカス・ロドクロスJ−1株(Rhodococcus rhodochrous J-1:FERM BP-1478)をグルコース2質量%、尿素1質量%、ペプトン0.5質量質量%、酵母エキス0.3%、塩化コバルト0.05質量%を含む培地(pH7.0)により好気的に培養した。
Examples 1 and 2 and Comparative Example 1
Culture Rhodococcus rhodochrous J-1 strain (FERM BP-1478) having nitrile hydratase activity is 2% by weight glucose, 1% by weight urea, 0.5% by weight peptone, 0.3% yeast extract. And aerobic culture in a medium (pH 7.0) containing 0.05% by mass of cobalt chloride.

保存用菌体懸濁液の調製
培養後の微生物菌体を遠心分離(12000rpm、20分)により回収後、0.1%アクリル酸ナトリウム水溶液(pH7.0)で洗浄した。洗浄した菌体に上記水溶液を添加し菌体懸濁液(乾燥菌体換算10質量%)を得た。
Preparation of microbial cell suspension for storage The cultured microbial cells were collected by centrifugation (12000 rpm, 20 minutes) and then washed with a 0.1% aqueous sodium acrylate solution (pH 7.0). The aqueous solution was added to the washed cells to obtain a cell suspension (10% by mass in terms of dry cells).

菌体懸濁液の保存
上記の方法で調製した菌体懸濁液115mL(実施例1)および70mL(比較例1)を総容積120mLのポリエチレン製容器に入れて密封し、輸送のモデルとして30℃、120rpmで3週間振盪した。また、上記の方法で調製した菌体懸濁液190L(実施例2)を容積200Lのポリエチレン製ドラムに入れて密封し、室温で3カ月間静置した。
Storage of bacterial cell suspension 115 mL (Example 1) and 70 mL (Comparative Example 1) of the bacterial cell suspension prepared by the above method were put in a polyethylene container having a total volume of 120 mL, sealed, and 30 as a transport model. The mixture was shaken at 120 ° C. for 3 weeks. Further, 190 L of the bacterial cell suspension (Example 2) prepared by the above method was placed in a 200 L polyethylene drum, sealed, and allowed to stand at room temperature for 3 months.

ニトリルヒドラターゼ活性の測定
ニトリルヒドラターゼ活性は、上記の方法で調製した直後の菌体懸濁液と、調製後3週間振盪または静置したものを用いて、これらの懸濁液に含まれる菌体によるアクリルアミド生成反応速度から算出した。基質であるアクリロニトリルの水溶液を菌体懸濁液に添加することで反応を開始し、10℃で10分間振盪した後、菌体の濾過分離とリン酸添加により反応を停止させ、ガスクロマトグラフィ(GC-14B、島津製作所)で分析した。分析条件は、Porapack PS(ウォーターズ社)を充填した1mガラスカラムを用い、カラム温度210℃、検出器は230℃のFIDを使用した。以下、0日に於ける反応速度を1とした相対反応速度を表1に示す。
Measurement of nitrile hydratase activity The nitrile hydratase activity was determined by using the cell suspension immediately after preparation by the above method and the one contained in these suspensions after shaking or standing for 3 weeks after preparation. It calculated from the acrylamide production | generation reaction rate by a body. The reaction is started by adding an aqueous solution of acrylonitrile as a substrate to the cell suspension. After shaking at 10 ° C. for 10 minutes, the reaction is stopped by filtration separation of the cells and addition of phosphoric acid, and gas chromatography (GC -14B, Shimadzu Corporation). As analysis conditions, a 1 m glass column packed with Porapak PS (Waters) was used, and a FID having a column temperature of 210 ° C. and a detector of 230 ° C. was used. The relative reaction rates with the reaction rate on day 0 as 1 are shown in Table 1 below.

実施例3、比較例2
ロドコッカス ロドクロウス M8株由来ニトリルヒドラターゼを有する形質転換体の作製
(1)ロドコッカス ロドクロウス M8株(以下、M8株という。)からの染色体DNA調製
M8株(SU1731814)は、ロシア菌株センターIBFM(VKPM S-926)から入手することができる。
M8株を100mLのMYK(0.5% ポリペプトン、0.3% バクトイーストエキス、0.3%バクトモルトエキス、0.2%K2HPO4、0.2% KH2PO4)培地(pH7.0)中、30℃にて72時間振盪培養した。培養液を遠心分離し、集菌した菌体をSaline-EDTA溶液(0.1M EDTA、0.15M NaCl(pH8.0))4mLに懸濁した。懸濁液にリゾチーム8mgを加えて37℃で1〜2時間振盪した後、−20℃で凍結した。
次に、当該懸濁液に10mLのTris-SDS液(1%SDS、0.1M NaCl、0.1M Tris-HCl(pH9.0))を穏やかに振盪しながら加えた。さらに、当該懸濁液にプロテイナーゼK(メルク社)(終濃度0.1mg)を加え37℃で1時間振盪した。次に、等量のTE飽和フェノールを加え攪拌後(TE:10mM Tris-HCl、1mM EDTA(pH8.0))遠心した。上層を採取し、2倍量のエタノールを加えて、ガラス棒でDNAを巻きとった。その後、これを順次90%、80%、70%のエタノールで遠心分離しフェノールを取り除いた。
次に、DNAを3mLのTE緩衝液に溶解させ、リボヌクレアーゼA溶液(100℃、15分間の加熱処理済)を10μg/mLになるよう加え37℃で30分間振盪した。さらに、プロテイナーゼK(メルク社)を加え37℃で30分間振盪した。これに等量のTE飽和フェノールを加えて遠心分離後、上層と下層に分離した。
上層をさらに等量のTE飽和フェノールを加えて遠心分離後、上層と下層に分離した。この操作を再度繰り返した。その後、上層に同量のクロロホルム(4%イソアミルアルコール含有)を加えて遠心分離し、上層を回収した。次いで、上層に2倍量のエタノールを加えガラス棒でDNAを巻きとって回収し、染色体DNAを得た。
Example 3 and Comparative Example 2
Production of transformants having nitrile hydratase derived from Rhodococcus rhodochrous M8 (1) Preparation of chromosomal DNA from Rhodococcus rhodochrous M8 (hereinafter referred to as M8) M8 (SU1731814) 926).
The M8 strain was cultured with shaking in 100 mL of MYK (0.5% polypeptone, 0.3% bactoeast extract, 0.3% bactomalt extract, 0.2% K2HPO4, 0.2% KH2PO4) medium (pH 7.0) at 30 ° C. for 72 hours. The culture broth was centrifuged, and the collected cells were suspended in 4 mL of Saline-EDTA solution (0.1 M EDTA, 0.15 M NaCl (pH 8.0)). 8 mg of lysozyme was added to the suspension, shaken at 37 ° C. for 1-2 hours, and then frozen at −20 ° C.
Next, 10 mL of Tris-SDS solution (1% SDS, 0.1 M NaCl, 0.1 M Tris-HCl (pH 9.0)) was added to the suspension with gentle shaking. Furthermore, proteinase K (Merck) (final concentration 0.1 mg) was added to the suspension and shaken at 37 ° C. for 1 hour. Next, an equal amount of TE saturated phenol was added and stirred (TE: 10 mM Tris-HCl, 1 mM EDTA (pH 8.0)) and centrifuged. The upper layer was collected, twice the amount of ethanol was added, and the DNA was wound with a glass rod. Thereafter, this was centrifuged sequentially with 90%, 80%, and 70% ethanol to remove phenol.
Next, DNA was dissolved in 3 mL of TE buffer, ribonuclease A solution (100 ° C., heat-treated for 15 minutes) was added to 10 μg / mL, and the mixture was shaken at 37 ° C. for 30 minutes. Further, proteinase K (Merck) was added and shaken at 37 ° C. for 30 minutes. An equal amount of TE-saturated phenol was added thereto, and after centrifugation, the mixture was separated into an upper layer and a lower layer.
The upper layer was further centrifuged with an equal amount of TE saturated phenol, and then separated into an upper layer and a lower layer. This operation was repeated again. Thereafter, the same amount of chloroform (containing 4% isoamyl alcohol) was added to the upper layer and centrifuged to recover the upper layer. Next, twice the amount of ethanol was added to the upper layer, and the DNA was wound with a glass rod and collected to obtain chromosomal DNA.

(2)PCRを用いたM8株染色体DNAからのニトリルヒドラターゼ遺伝子の調製
M8株由来ニトリルヒドラターゼは非特許文献(Veiko,V.P.et al, Cloning,nucleotide sequence of nitrile hydratase gene from Rhodococcus rhodochrous M8, Biotekhnologiia (Mosc.) 5, 3-5 (1995))に記載されており、βサブユニット、αサブユニット、アクチベーターの塩基配列及びアミノ酸配列をそれぞれ配列番号1及び2、配列番号3及び4、並びに配列番号5及び6に示す。配列情報に基づいて、配列表の配列番号7及び8記載のプライマーを合成し、(1)にて調製した染色体DNAを鋳型としてPCRを行った。

<PCR反応溶液組成>
鋳型DNA(染色体DNA) 200ng
PrimeSTAR Max Premix(宝酒造社製) 25μl
プライマーM8-1 10pmol
プライマーM8-2 10pmol
<プライマー>
M8-1: GGTCTAGAATGGATGGTATCCACGACACAGGC(配列番号7)
M8-2:cccctgcaggtcagtcgatgatggccatcgattc (配列番号8)
<反応条件>
(98℃ 10秒、55℃ 5秒、72℃で30秒)×30サイクル
PCR終了後、反応液5μlを0.7%アガロースゲル(同仁化学社製アガロースI使用;アガロース濃度0.7重量%)電気泳動に供し、1.6kbの増幅断片の検出を行った。反応終了液をWizard SV Gel and PCR Clean−Up Syste(プロメガ株式会社)を用いて精製した。
回収したPCR産物はLigation Kit(宝酒造)を用いてベクター(pUC118/HincII部位)に連結し、反応液により大腸菌JM109のコンピテントセルを形質転換した。得られた形質転換体コロニーより数クローンをLB-Amp培地1.5mLに接種し、37℃で12時間振盪培養した。培養後、この培養物を遠心分離により集菌した。QIAprep Spin Miniprep Kit (アマシャムバイオサイエンス社)を用いることにより、集菌した菌体からプラスミドDNAを抽出した。得られたプラスミドDNAに対し、シークエンシングキットとオートシークエンサーCEQ 8000
(ベックマンコールター社)を用いて、ニトリルヒドラターゼの塩基配列を確認した。
次に、得られたプラスミドDNAを制限酵素XbaIとSse8387Iで切断後、0.7%アガロースゲルにより電気泳動を行い、ニトリルヒドラターゼ遺伝子断片(1.6kb)を回収し、プラスミドpSJ042のXbaI-Sse8387Iサイトに導入した。
得られたプラスミドをpSJ-N01Aと命名した。
尚、pSJ042はロドコッカス菌においてJ1株ニトリルヒドラターゼを発現するプラスミドとして特開2008−154552号公報に示す方法で作製されたものであり、pSJ042の作製に使用したpSJ023は形質転換体ATCC12674/pSJ023(FERM BP-6232)として独立行政法人産業技術総合研究所 特許生物寄託センター(茨城県つくば市東1丁目1番地1 中央第6)に平成9年3月4日付けで寄託されている。
(2) Preparation of nitrile hydratase gene from chromosomal DNA of M8 strain using PCR Non-patent literature (Veiko, VP et al, Cloning, nucleotide sequence of nitrile hydratase gene from Rhodococcus rhodochrous M8, Biotekhnologiia ( Mosc.) 5, 3-5 (1995)), and the base sequence and amino acid sequence of β subunit, α subunit, and activator are shown in SEQ ID NOs: 1 and 2, SEQ ID NOs: 3 and 4, and The numbers 5 and 6 are shown. Based on the sequence information, primers described in SEQ ID NOs: 7 and 8 in the sequence listing were synthesized, and PCR was performed using the chromosomal DNA prepared in (1) as a template.

<PCR reaction solution composition>
Template DNA (chromosomal DNA) 200ng
PrimeSTAR Max Premix (Takara Shuzo) 25μl
Primer M8-1 10pmol
Primer M8-2 10pmol
<Primer>
M8-1: GGTCTAGAATGGATGGTATCCACGACACAGGC (SEQ ID NO: 7)
M8-2: cccctgcaggtcagtcgatgatggccatcgattc (SEQ ID NO: 8)
<Reaction conditions>
(98 ℃ 10 seconds, 55 ℃ 5 seconds, 72 ℃ 30 seconds) x 30 cycles
After completion of the PCR, 5 μl of the reaction solution was subjected to 0.7% agarose gel (using Agarose I manufactured by Dojin Chemical Co., Ltd .; agarose concentration 0.7 wt%) to detect a 1.6 kb amplified fragment. The reaction completion solution was purified using Wizard SV Gel and PCR Clean-Up System (Promega Corporation).
The collected PCR product was ligated to a vector (pUC118 / HincII site) using Ligation Kit (Takara Shuzo), and a competent cell of E. coli JM109 was transformed with the reaction solution. Several clones from the obtained transformant colonies were inoculated into 1.5 mL of LB-Amp medium and cultured with shaking at 37 ° C. for 12 hours. After culture, the culture was collected by centrifugation. Plasmid DNA was extracted from the collected cells by using QIAprep Spin Miniprep Kit (Amersham Bioscience). Sequencing kit and auto sequencer CEQ 8000
The base sequence of nitrile hydratase was confirmed using (Beckman Coulter).
Next, the obtained plasmid DNA was cleaved with restriction enzymes XbaI and Sse8387I, and then electrophoresed on a 0.7% agarose gel to recover the nitrile hydratase gene fragment (1.6 kb) and introduced into the XbaI-Sse8387I site of plasmid pSJ042. did.
The obtained plasmid was designated as pSJ-N01A.
PSJ042 was prepared as a plasmid expressing J1 strain nitrile hydratase in Rhodococcus by the method shown in Japanese Patent Application Laid-Open No. 2008-154552, and pSJ023 used for the preparation of pSJ042 is a transformant ATCC12674 / pSJ023 ( FERM BP-6232) was deposited on March 4, 1997 at the National Institute of Advanced Industrial Science and Technology, Patent Biological Depositary Center (1st, 1st East, 1st Street, Tsukuba, Ibaraki).

(3)コンピテントセルの作製
ロドコッカス・ロドクロウスATCC 12674株(以下、ATCC 12674株)をMYK培地で対数増殖期前期まで培養し、細胞を遠心分離器により集菌し、氷冷した滅菌水にて3回洗浄し、滅菌水に懸濁し、コンピテントセルを作製した。
(3) Production of competent cells Rhodococcus rhodochrous ATCC 12674 strain (hereinafter referred to as ATCC 12674 strain) was cultured in MYK medium until the early logarithmic growth phase, and the cells were collected using a centrifuge and then in ice-cold sterile water. The cells were washed 3 times and suspended in sterilized water to produce competent cells.

(4)M8株由来ニトリルヒドラターゼを有する形質転換体の作製
得られたプラスミドpSJ-N01A0.1μgとATCC12674株のコンピテントセルの菌体懸濁液各20μlとを混合し、各々氷冷した。キュベットに各混合液を入れ、遺伝子導入装置 Gene Pulser(BIO RAD)により20 KV/cm、200 OHMSで電気パルス処理を行った。電気パルス処理液を氷冷下10分静置し、37℃で10分間ヒートショックを行った。その後、キュベットにMYK培地500μlを加え、30 ℃、5時間静置した後、50μg/mLカナマイシン入りMYK寒天培地に塗布し、30℃、3日間培養した。
得られた形質転換体コロニーに含まれるプラスミドDNAを確認し、この組換え菌をM8株由来ニトリルヒドラターゼを有するロドコッカス属組換え菌(ATCC12674/pSJ-N01A)とした。
(4) Preparation of Transformant Containing M8 Strain-Derived Nitrile Hydratase The plasmid pSJ-N01A (0.1 μg) obtained was mixed with 20 μl each of a suspension of competent cells of the ATCC12674 strain, and each was ice-cooled. Each liquid mixture was put into a cuvette and subjected to electric pulse treatment at 20 KV / cm and 200 OHMS using a gene introduction apparatus Gene Pulser (BIO RAD). The electric pulse treatment solution was allowed to stand for 10 minutes under ice cooling, and heat shock was performed at 37 ° C. for 10 minutes. Thereafter, 500 μl of MYK medium was added to the cuvette, allowed to stand at 30 ° C. for 5 hours, applied to MYK agar medium containing 50 μg / mL kanamycin, and cultured at 30 ° C. for 3 days.
The plasmid DNA contained in the obtained transformant colony was confirmed, and this recombinant bacterium was named Rhodococcus genus recombinant bacterium (ATCC12674 / pSJ-N01A) having nitrile hydratase derived from M8 strain.

培養
得られた組み換え菌をグルコース2質量%、尿素1質量%、ペプトン0.5質量質量%、酵母エキス0.3%、塩化コバルト0.05質量%を含む培地(pH7.0)により好気的に培養した。
Culturing The obtained recombinant bacteria was aerobic in a medium (pH 7.0) containing 2% by mass of glucose, 1% by mass of urea, 0.5% by mass of peptone, 0.3% of yeast extract and 0.05% by mass of cobalt chloride. Cultured.

保存用菌体懸濁液の調製
培養後の微生物菌体を遠心分離(12000rpm、20分)により回収後、0.1%アクリル酸ナトリウム水溶液(pH7.0)で洗浄した。洗浄した菌体に上記水溶液を添加し菌体懸濁液(乾燥菌体換算10質量%)を得た。
Preparation of microbial cell suspension for storage The cultured microbial cells were collected by centrifugation (12000 rpm, 20 minutes) and then washed with a 0.1% aqueous sodium acrylate solution (pH 7.0). The aqueous solution was added to the washed cells to obtain a cell suspension (10% by mass in terms of dry cells).

菌体懸濁液の保存
上記の方法で調製した菌体懸濁液100mL(実施例3)および80mL(比較例2)を総容積120mLのポリエチレン製容器に入れて密封し、30℃、120rpmで3週間振盪した。
Storage of the cell suspension 100 mL (Example 3) and 80 mL (Comparative Example 2) of the cell suspension prepared by the above method were put in a polyethylene container having a total volume of 120 mL and sealed, and at 30 ° C. and 120 rpm. Shake for 3 weeks.

ニトリルヒドラターゼ活性の測定
ニトリルヒドラターゼ活性は、上記の方法で調製した直後の菌体懸濁液と、調製後7日間および21日間振盪したものを用いて、実施例1と同様の方法で測定した。以下、0日に於ける反応速度を1とした相対反応速度を表2に示す。
Measurement of nitrile hydratase activity The nitrile hydratase activity was measured in the same manner as in Example 1 using the cell suspension immediately after preparation by the above method and the suspension after 7 days and 21 days after preparation. did. The relative reaction rates with the reaction rate on day 0 as 1 are shown in Table 2 below.

実施例4、比較例3
培養
ニトリルヒドラターゼ活性を有するシュードモナス・マージナリスDSM16275株(Pseudomonas marginalis DSM16275)をグリセロール0.2質量%、クエン酸0.05質量%、酵母エキス0.15%、リン酸二水素カリウム0.3質量%、リン酸水素二カリウム0.7質量%、硫酸鉄0.0004質量%、硫酸マンガン0.01質量%、メチル尿素1.25質量%、塩酸コバルト0.001質量%を含む培地(pH7.0)により好気的に培養した。
Example 4, Comparative Example 3
Culture Pseudomonas marginalis DSM16275 (Pseudomonas marginalis DSM16275) having nitrile hydratase activity 0.2% by mass of glycerol, 0.05% by mass of citric acid, 0.15% of yeast extract, 0.3% by mass of potassium dihydrogen phosphate , A medium containing 0.7% by mass of dipotassium hydrogen phosphate, 0.0004% by mass of iron sulfate, 0.01% by mass of manganese sulfate, 1.25% by mass of methylurea, 0.001% by mass of cobalt hydrochloride (pH 7.0) ) Was aerobically cultured.

保存用菌体懸濁液の調製
培養後の微生物菌体を遠心分離(12000rpm、20分)により回収後、0.1%アクリル酸ナトリウム水溶液(pH7.0)で洗浄した。洗浄した菌体に上記水溶液を添加し菌体懸濁液(乾燥菌体換算10質量%)を得た。
Preparation of microbial cell suspension for storage The cultured microbial cells were collected by centrifugation (12000 rpm, 20 minutes) and then washed with a 0.1% aqueous sodium acrylate solution (pH 7.0). The aqueous solution was added to the washed cells to obtain a cell suspension (10% by mass in terms of dry cells).

上記の方法で調製した菌体懸濁液100mL(実施例4)および80mL(比較例3)を総容積120mLのポリエチレン製容器に入れて密封し、30℃、120rpmで1週間振盪した。   100 mL (Example 4) and 80 mL (Comparative Example 3) of the cell suspension prepared by the above method were put in a polyethylene container having a total volume of 120 mL, sealed, and shaken at 30 ° C. and 120 rpm for 1 week.

ニトリルヒドラターゼ活性の測定
ニトリルヒドラターゼ活性は、上記の方法で調製した直後の菌体懸濁液と、調製後7日間振盪したものを用いて、実施例1と同様の方法で測定した。以下、0日に於ける反応速度を1とした相対反応速度を表3に示す。
Measurement of nitrile hydratase activity The nitrile hydratase activity was measured in the same manner as in Example 1 using the cell suspension immediately after preparation by the above method and the suspension after 7 days of preparation. The relative reaction rates with the reaction rate on day 0 as 1 are shown in Table 3 below.

上記実施例1、2、3及び4の結果から、本発明の輸送方法を用いてニトリルヒドラターゼ活性を有する微生物菌体を輸送した場合には、微生物菌体がニトリルヒドラターゼ活性を保存前と同程度に維持した状態で保存されることが示される。   From the results of Examples 1, 2, 3 and 4 above, when a microbial cell having nitrile hydratase activity was transported using the transport method of the present invention, the microbial cell exhibited nitrile hydratase activity before storage. It is shown that it is stored in a state maintained at the same level.

本発明により、工業的に満足し得る微生物菌体の保存方法が提供される。本発明によれば、多量の菌体を、室温下、無撹拌でもニトリルヒドラターゼ等の酵素活性を維持したまま保存及び輸送することが可能となり、従来の保存方法で必要とされてきた労力や冷却コストを大幅に削減することができるため、本発明の方法は極めて有用である。   The present invention provides a method for preserving microbial cells that is industrially satisfactory. According to the present invention, a large amount of cells can be stored and transported at room temperature even without agitation while maintaining an enzyme activity such as nitrile hydratase. The method of the present invention is extremely useful because the cooling cost can be greatly reduced.

ロドコッカス・ロドクロスJ-1株(Rhodococcus rhodochrous J-1):受託番号「FERM BP−1478」として、1987年9月18日に独立行政法人産業技術総合研究所特許生物寄託センター(茨城県つくば市東1−1−1 中央第6)に寄託されている。
シュードモナス・マージナリスDSM16275株(Pseudomonas marginalis DSM16275):受託番号「DSM16275」として、2004年3月4日にドイチェ ザンムルンク フォン ミクロオルガニスメン ウント ツェルクル トゥレン ゲーエムベーハー(DSMZ)に寄託されている。
Rhodococcus rhodochrous J-1: Accession number “FERM BP-1478” on September 18, 1987, Patent Biodeposition Center, National Institute of Advanced Industrial Science and Technology (1st East, Tsukuba City, Ibaraki Prefecture) -1-1 Deposited at the center 6).
Pseudomonas marginalis DSM16275 (Pseudomonas marginalis DSM16275): Deposited to Deutsche Zammlung von Microorganismen und Zerkl Turren Gaembecher (DSMZ) on March 4, 2004 as the deposit number “DSM16275”.

配列番号7:合成DNA
配列番号8:合成DNA
Sequence number 7: Synthetic DNA
Sequence number 8: Synthetic DNA

Claims (3)

ニトリルヒドラターゼ活性を有する微生物菌体を密閉可能な容器内に保存する方法であって、
前記微生物菌体およびアクリル酸を含む懸濁液が充填された前記容器内の気相部を容器内部の全容積の2%以上20%以下とし、氷点〜35℃の温度で保存することを特徴とする前記方法。
A method for storing microbial cells having nitrile hydratase activity in a sealable container,
The gas phase portion in the container filled with the suspension containing the microbial cells and acrylic acid is 2% to 20% of the total volume inside the container, and is stored at a temperature of freezing point to 35 ° C. Said method.
ニトリルヒドラターゼ活性を有する微生物菌体を密閉可能な容器を用いて輸送する方法であって、
前記微生物菌体およびアクリル酸を含む懸濁液が充填された前記容器内の気相部を容器内部の全容積の2%以上20%以下とし、氷点〜35℃の温度で輸送することを特徴とする前記方法。
A method of transporting microbial cells having nitrile hydratase activity using a sealable container,
The gas phase part in the container filled with the suspension containing the microbial cells and acrylic acid is 2% to 20% of the total volume inside the container, and is transported at a temperature of freezing point to 35 ° C. Said method.
前記容器内の気相部の割合が5%以上20%以下である請求項1又は2に記載の方法。
The method according to claim 1 or 2, wherein a ratio of a gas phase portion in the container is 5% or more and 20% or less.
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