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JP2004275111A - Method for producing sporangia - Google Patents

Method for producing sporangia Download PDF

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Publication number
JP2004275111A
JP2004275111A JP2003072713A JP2003072713A JP2004275111A JP 2004275111 A JP2004275111 A JP 2004275111A JP 2003072713 A JP2003072713 A JP 2003072713A JP 2003072713 A JP2003072713 A JP 2003072713A JP 2004275111 A JP2004275111 A JP 2004275111A
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Japan
Prior art keywords
adsorbent
culture
sporangia
culture solution
bacillus
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JP2003072713A
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JP4438298B2 (en
Inventor
Masatoshi Kimura
雅敏 木村
Hideji Nishibashi
秀治 西橋
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DIC Corp
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Dainippon Ink and Chemicals Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a sporangium of a fungus belonging to Bacillus popilliae including a spore and a parasporal body in which the sporangium is efficiently cultured and the sporangium not containing an absorbent can readily be recovered, and to provide a production apparatus used for the production method. <P>SOLUTION: This method for producing the sporangium of the fungus belonging to Bacillus popilliae including the spore and the parasporal body comprises culturing Bacillus popilliae in a liquid culture medium containing the absorbent and a culture liquid and producing the sporangium including the spore and the parasporal body. In the production method, the absorbent is contained in a container through which the absorbent is not passed but the culture liquid is passed, and the absorbent is brought into contact with the culture liquid. The apparatus for producing the sporangium is equipped with a culturing tank containing the culture liquid and the container through which the absorbent is not passed, but the culture liquid is passed. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造方法、および該製造方法に用いられる胞子嚢の製造装置に関する。
【0002】
【従来の技術】
コガネムシ科昆虫の幼虫は、芝や農園芸作物や樹木等の広範囲な植物の根を食餌し、それらに多大の被害を与える。これらの幼虫は地中に棲息するため、地上から散布する化学農薬が効きにくく、且つその棲息場所が特定しにくいことから、十分な殺虫効果を得る為には、広範囲に多量の殺虫性農薬を散布して地中に浸透させる必要があった。さらに、その結果、環境汚染を引き起こすおそれもあり、事実上その防除、駆除は殆ど困難であった。
【0003】
一方、バチルス・ポピリエに属する菌は、これらコガネムシ科昆虫の幼虫を寄生宿主とし、通常胞子嚢の形態で経口的に感染、血リンパ中で大量に増殖し、やがて乳化病を引き起こして最終的に死に至らしめることが知られている。そこで、化学農薬が効きにくいコガネムシ科昆虫の駆除に、バチルス・ポピリエに属する菌を利用しようとする試みが古くから行われてきた。この方法は、化学農薬に替わる生物学的防除方法として有望であると考えられる。
【0004】
バチルス・ポピリエに属する菌の培養方法としては、寄生宿主であるコガネムシ科の生きた幼虫を用いて菌を増殖させ胞子嚢を製造する方法が従来から知られていた。
すなわち、バチルス・ポピリエに属する菌の胞子嚢をコガネムシ科昆虫の幼虫の存在する飼育培土に散布して、バチルス・ポピリエに属する菌の胞子嚢を経口的にコガネムシ科昆虫の幼虫に摂取させるか、又は体液中に注射により注入した後、幼虫を3週間〜4週間飼育し、該幼虫体内でバチルス・ポピリエを増殖させ、その後、幼虫に孔を開けるか切開して体液を採取し、得られた体液を遠心分離又は濾過することにより、幼虫体内で増やした胞子嚢を得る方法である。
しかしながら、この方法では、コガネムシ科昆虫の幼虫を大量に飼育する必要があり、結果的に胞子嚢を多量に、短時間に、且つ経済的に得ることは困難であった。この為、コガネムシ科昆虫の幼虫を用いない人工培地を用いての培養方法に関する多くの研究が行われてきた。
【0005】
ところで、バチルス・ポピリエの人工培地を用いた培養方法に関する従来の文献では、胞子嚢と胞子とが、明確な区別なく用いられている場合が多く、文献中の胞子という言葉が胞子のみを意味するのか、胞子は内包するがパラスポラルボディは含まない胞子嚢を意味するのか、あるいは胞子とパラスポラルボディとを内包する胞子嚢であるのかが不明である場合が多い。
これらに対して、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢が、優れた防除効果を有するという報告がなされている(特許文献1参照。)。従って、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢のより効率的な製造方法が望まれている。
【0006】
コガネムシ科昆虫の幼虫を用いない人工培地での培養方法としては、固体培養及び液体培養がある。しかし、固体培養による胞子嚢の生産は効率的であるとは言えず、液体培養による胞子嚢の生産が必要である。
液体培養で胞子嚢を得る場合には、生育阻害物質、過酸化物等を除去するための吸着剤として、活性炭を培地中に添加して液体培養で胞子嚢を得た培養例がある(例えば非特許文献1及び特許文献1乃至3参照。)。これらのうち、胞子とパラスポラルボディとを内包する胞子嚢を製造した例は、特許文献1乃至3に記載されている場合のみである。
【0007】
これらの方法はいずれも、培地中に活性炭を添加しているが、以下の点で大きな問題がある。
まず、粉末状の活性炭を使用した場合には、培養液中に胞子嚢と粉末状活性炭が混在してしまい、さらに、胞子嚢と粉末活性炭は粒径及び重量が似通っているため、遠心分離、ろ過等の通常の手段によって胞子嚢と粉末活性炭とを分離することが困難である。このような場合には、胞子嚢のみを得ることが難しく、活性炭を含んだ形で胞子嚢を回収せざるを得ない。また、例えば、特許文献3に記載の方法で製造された活性炭を含んだ胞子嚢は、胞子嚢の重量に対して2.3〜23倍の活性炭を含んでおり、活性炭等の吸着材を含む胞子嚢は、乾燥あるいは製品化の際の濃度調整、充填等の工程において、また、製剤化した際においても容量が大幅に増すこと、特に活性炭などを用いた場合には飛散しやすく作業者が吸引したり粉塵爆発を誘発する等の危険性が高く、取り扱いが面倒になるといった問題があった。また、最終製品に着色があり外観に劣るという問題もあった。
【0008】
一方、粒状の活性炭を培養槽内に単に添加した場合は、胞子嚢と該活性炭の分離工程を要するだけでなく、培養の際に活性炭が下部に沈降してしまうために吸着効率が低下して阻害物を十分に除去することができなくなる。通常の培養方法においては培養装置内を攪拌するので、攪拌翼の回転数を上げるといった方法で粒状活性炭を分散させる方法等も考えられるが、バチルス・ポピリエの培養においては攪拌回転数が高いと十分な量の胞子嚢が得られない。
【0009】
【非特許文献1】
ハイネス(W.C.Haynes)他,ジャーナル・オブ・バクテリオロジー(Journal of Bacteriology),(米国),1966年6月,91巻,6号,p.2270−2274.
【特許文献1】
特開2002−291467号公報
【特許文献2】
特開2002−291468号公報
【特許文献3】
特開2002−355030号公報
【0010】
【発明が解決しようとする課題】
本発明が解決しようとする課題は、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢を効率的に培養し、吸着剤を含まない胞子嚢を容易に回収することができる胞子嚢の製造方法、および該製造方法に用いられる製造装置を提供することにある。
【0011】
【課題を解決するための手段】
本発明者らは、上記の課題を解決すべく鋭意検討した結果、吸着剤は通過させないが培養液は通過させる容器内に吸着剤を包含して、吸着剤を培養液と接触させることにより、上記課題を解決することを見出し、本発明を完成するに至った。
すなわち、本発明は、吸着剤と培養液とを含む液体培地でバチルス・ポピリエを培養し、胞子とパラスポラルボディとを内包する胞子嚢を製造する方法であって、該吸着剤が、吸着剤は通過させないが培養液は通過させる容器内に包含され、かつ培養液と接触している胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造方法である。
また、本発明は、前記製造方法に用いられる胞子嚢の製造装置であって、培養液を包含する培養槽と、吸着剤は通過させないが培養液は通過させる容器とを備える胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造装置である。
【0012】
【発明の実施の形態】
以下に本発明を詳細に説明する。
本発明の胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造方法は、吸着剤と培養液とを含む液体培地でバチルス・ポピリエを培養し、胞子とパラスポラルボディとを内包する胞子嚢を製造する方法であって、該吸着剤が、該吸着剤は通過させないが培養液は通過させる容器内に包含され、かつ培養液と接触していることを特徴とするものである。
【0013】
本発明において胞子嚢とは、胞子とパラスポラルボディ(又は副胞子小体)と呼ばれる小体とを胞子嚢壁が内包しているものであり、バチルス・ポピリエに属する菌が産生する。
【0014】
本発明で用いられるバチルス・ポピリエに属する菌(以下、単に「バチルス・ポピリエの菌」ということがある。)とは、バチルス属ポピリエ種(Bacillus popilliae)に属する菌である。バチルス族ポピリエ種の細菌学的性質は、バージェイズ・マニュアル・オブ・デターミネイティブ・バクテリオロジー(Bergeys’Manual of Determinative Bacteriology)によれば、形態的性質は長さが1.3〜5.2μm、幅が0.5〜0.8μmのグラム陰性桿菌、生育温度は20〜35℃で、胞子嚢の中にパラスポラルボディを持っている。
バチルス属ポピリエ種に属する菌としては、バチルス・ポピリエ・セマダラ株(Bacillus popilliae var. popilliae Semadara)(FERM P−16818)、バチルス・ポピリエ・マメ株(Bacillus popilliae var. popilliae Mame)(FERM P−17661)、バチルス・ポピリエ・ヒメ株(Bacillus popilliae var. popilliae Hime)(FERM P−17660)、バチルス・ポピリエ・サクラ株(Bacillus popilliae var. popilliae Sakura)(FERM P−17662)、バチルス・ポピリエ・デュトキ株(Bacillus popilliae var. popilliae DIC−2001)(FERM P−18250)、バチルス・ポピリエ・デュトキ株(Bacillus popilliae Dutky, American Type Culture Collection No. 14706)等が挙げられる。
【0015】
近年、これまでの菌株も含め「バチルス属ポピリエ種」は、「パエニバチルス属ポピリエ種(Paenibacillus popilliae)」に再分類されるべきとの学説上の見解(Bertil Pettersson et al., 1999年, Int. J. Syst. Bacteriol., 49巻, 531−540頁)も示されており、現段階では両者の取り扱いが明確化していない。よって、本発明においては、「バチルス属ポピリエ種に属する菌」とは「パエニバチルス属ポピリエ種に属する菌」をも包含するものとする。
【0016】
本発明に用いられる吸着剤は、バチルス・ポピリエに属する菌の生育を阻害する物質の除去を目的として用いられるものである。該吸着剤としては、例えば、活性炭および合成吸着剤を挙げることができる。いずれも、微細物質を吸着する多孔質体であり、粒子内部にまで発達した細孔構造により水溶液中の阻害物質を効率良く吸着しうる物質であることが重要である。
【0017】
本発明に用いられる活性炭の形状は、粉末状、粒状、シート状等が挙げられ、特に制限はないが、粒子が飛散せず扱いやすいことから、特に粒状の活性炭が好ましい。
また、本発明に用いられる合成吸着剤とは、微細物質を吸着する多孔質重合体を意味し、例えば、粒子状に成型された架橋性多孔質重合体である。具体的には、三菱化学株式会社製のSEPABEADS SP825、SEPABEADS SP850、DIAION HP20、DIAION HP21などが挙げられる。
【0018】
これらの吸着剤は、吸着剤は通過させないが培養液は通過させる容器(以下、「吸着剤内包容器」という。)に保持される必要があることから、平均粒径が、0.3mm〜10mmであることが好ましく、さらに2.0mm〜6.0mmであることが好ましい。
平均粒径が0.3mmより小さい場合は、吸着剤内包容器につまり等が発生し、容器の通液性が著しく損なわれ、阻害物質の吸着効率が著しく低下してしまうため好ましくない。一方、平均粒径が10mmを超えると、通液性は良好であるが、阻害物質の吸着に必要な表面積が低下するために吸着剤の使用量が増え、結果として吸着剤内包容器が大きくなり効率的とは言えない。
【0019】
吸着剤の使用量はその吸着力によって異なるため特に限定されないが、培養液中の阻害物を充分に除去できることが必要である。また、吸着剤は充分に殺菌され他の微生物に汚染されていないことが必要であり、予め充分に殺菌された吸着剤を使用してもよいし、吸着剤内包容器に包含されて培地と接触した状態で培地と共に殺菌してから使用してもよい。
【0020】
本発明の胞子嚢の製造方法において、バチルス・ポピリエの菌の培養条件は、胞子嚢を得るための従来公知の培養条件に従って行えばよく、特に限定されないが、バチルス・ポピリエの菌の増殖に適した温度及びpHに適宜調整することが必要である。例えば、バチルス・ポピリエ・セマダラ株では培養温度25〜30℃が好ましく、pHは7〜8であることが好ましい。pHの調整は通常用いられる塩酸、硫酸などの酸あるいは水酸化ナトリウム、水酸化カリウム、アンモニア等のアルカリが使用できる。
【0021】
本発明に用いる培養液は、バチルス・ポピリエの胞子とパラスポラルボディとを内包する胞子嚢を製造する際に用いられる公知慣用の液体培地を用いることができ、例えば、窒素源や炭素源を蒸留水等の水に添加したものが用いられる。窒素源としては、通常、微生物の培養に用いられるペプトン、肉エキス、魚肉エキス、ラクトアルブミン水解物又は酵母エキス等の有機性窒素源が挙げられ、これらの添加により培地中にタンパク質、アミノ酸、ビタミン類等を補給する。それ以外の窒素源として、アンモニア、硝酸及びそれらの塩等の無機窒素源が挙げられる。本発明に用いる窒素源の添加濃度は胞子嚢を製造することができる範囲であれば特に限定されるものではないが、培養液に対して5質量%以下であることが好ましく、より優れた菌の増殖促進効果を呈することから0.2〜4質量%の範囲とすることが好ましい。
上記窒素源中には各種アミノ酸が含まれているが、より効果的に胞子嚢を製造するために特定のアミノ酸を添加することもできる。添加するアミノ酸としてはグルタミン酸が好ましく、さらにプロリンが特に好ましく、いずれか単独またはその両方を添加することができる。本発明の培地は、グルタミン酸を添加することによりグルタミン酸を培地に対して0.2〜4質量%含むものであることが好ましく、さらにプロリンを添加することによりプロリンを培地に対して0.1〜0.7質量%含むものであることがより好ましい。また、本発明の培地は、培地中の全アミノ酸に対するグルタミン酸の割合が35〜90質量%となるように調製することが好ましく、プロリンが10〜65質量%となるように添加することがより好ましい。ただし、ここでいう「全アミノ酸」とは、通常、窒素源に含まれていることが知られている、アラニン、アルギニン、アスパラギン酸、グルタミン酸、グリシン、イソロイシン、ロイシン、リジン、メチオニン、フェニルアラニン、プロリン、セリン、トレオニン、ヒスチジン、チロシン、又はバリンからなる16種類の遊離型アミノ酸をいう。全アミノ酸、すなわち、上述の16種類の遊離型アミノ酸の合計量は、ペプトンや酵母エキス等に含まれる全ての遊離型アミノ酸量を概ね示すものとして用いられるものである。
【0022】
さらに、炭素源としては、通常の微生物の培養に用いられる炭素源が挙げられ、例えば、トレハロース、シュークロース等の糖類、廃糖蜜、デンプン分解物、チーズホエー等の農産廃棄物が挙げられる。これらの炭素源の添加濃度は、本発明の効果を達成する範囲であれば特に限定されないが、より優れた菌の増殖促進効果を呈することから培養液に対して0.001〜5質量%が好ましい。ただし、胞子とパラスポラルボディとを内包する胞子嚢を形成させるためには、グルコースの存在は好ましくなく、培地に含まれるグルコース濃度は培養液に対して0.01質量%以下にすることが好ましい。
【0023】
本発明に用いる培養液には、必要に応じてリン酸二水素カリウム、リン酸水素二カリウム等のリン酸塩又はそのナトリウム塩等の無機塩が添加されていても良い。該無機塩の添加濃度は、本発明の効果を達成する範囲であれば特に制限されないが、培養液に対して1質量%以下が好ましい。
【0024】
本発明に用いる培養液には、更に上記成分に加えてピルビン酸及びその生理学的に許容される塩を添加することによりさらに優れた菌の増殖及び胞子嚢化率を示す。ピルビン酸の生理学的に許容される塩としては、ピルビン酸ナトリウム、ピルビン酸カリウム等があげられる。ピルビン酸又はその生理学的に許容される塩の添加濃度は培養液に対して0.05〜0.5質量%であり、より優れた菌の増殖及び胞子嚢化率を呈するため好ましくは培養液に対して0.1〜0.3質量%である。添加されるピルビン酸及びその塩は、培地成分と共に殺菌しても、又は培地成分と分けて殺菌して培養開始時に添加しても良い。
【0025】
上記培養条件に好適に用いられる培養の方法としては、回分培養、連続培養、半回分培養、流加培養等を挙げることができる。培養時間は、培養方法、培養温度、培養pH、接種菌体量等によって異なるが、回分培養の場合で7〜10日である。
【0026】
本発明の胞子嚢の製造方法では、吸着剤を吸着剤内包容器に収納し、培養液を、吸着剤内包容器内を通過させて吸着剤に接触させるため、従来の方法のように吸着剤を培養槽中に分散させるために回転速度を上げて撹拌を行う必要がなく、培養液中に高濃度で胞子とパラスポラルボディとを内包するバチルス・ポピリエの菌の胞子嚢を得ることができる。
また、上述の方法で得た胞子嚢を培養液から分離して回収する場合には、一般的に行われる遠心分離、ろ過等の容易な方法で行えばよい。
【0027】
本発明の製造方法により得られた胞子嚢は、胞子とパラスポラルボディとを含み、各種コガネムシ科昆虫に殺虫性を有し防除効果を示す。このため該胞子嚢はコガネムシ科昆虫を防除する目的で防除剤として用いられ、芝、農園芸用作物又は樹木等に施用することができる。
【0028】
コガネムシ科昆虫としては、ドウガネブイブイ(Anomala cuprea)、セマダラコガネ(Blitopertha orientalis)、マメコガネ(Popillia japonica)、ウスチャコガネ(Phyllopertha diversa)、チャイロコガネ(Adoretus tenuimaculatus)、ヒメコガネ(Anomala rufocuprea)等が挙げられる。本発明の防除剤はこれらに対して、いずれも優れた殺虫性、防除効果を示し、中でも比較的大型なコガネムシであるドウガネブイブイやセマダラコガネの幼虫に対して優れた殺虫性を有し、優れた防除効果を示す。
【0029】
次に、本発明の胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造装置は、前記製造方法に用いられる胞子嚢の製造装置であって、培養液を包含する培養槽と、吸着剤は通過させないが培養液は通過させる容器(吸着剤内包容器)とを備えることを特徴とする。
上述の吸着剤は、吸着剤内包容器内に収納され、培養液と接触する。吸着剤内包容器に備えられる吸着剤は通過させないが培養液は通過させる部分の構造としては、吸着剤の平均粒径より小さい直径の細孔を有する構造、及び網目構造等が挙げられる。このような網目構造の網目間隔または細孔の孔径等を吸着剤の平均粒径より小さくすることにより、吸着剤は吸着剤内包容器内に留まり、培養液中に流出することなく培養を行うことができる。
【0030】
上記のような培養槽と吸着剤内包容器とを備えた培養装置の好ましい例としては、例えば、吸着剤内包容器を、培養槽内部に設置した装置及び培養槽外部に設置した装置が挙げられる。この場合、吸着剤は通過させないが培養液は通過させる部分の構造によって、吸着剤内包容器の一部または全部が構成されている。
吸着剤内包容器を培養槽内部に設置する場合、吸着剤は通過させないが培養液は通過させる部分の構造の少なくとも一部が培養液の液面より下に位置するよう該吸着剤内包容器を培養槽内部に固定して、所定の培養を行うことが好ましい。すなわち培養槽内部において通気、攪拌等を行うことにより、培養液が吸着剤内包容器内を循環し、吸着剤と接触して生育阻害物質が除去され、効率的に胞子嚢を得ることができる。上述したように該吸着剤内包容器を固定しないと、培養中に発生した気泡により該容器が取り込まれ、気泡とともに液面から浮き出て培養液と接触せず十分な生育阻害物質除去能を発揮しない場合がある。
【0031】
吸着剤内包容器を培養槽外部に設置する場合、培養槽外に吸着剤内包容器を設置して、培養液を通液させることができる配管等を用いて培養槽と接続することが好ましい。そして、吸着剤内包容器の、配管等を接続して培養液を導入及び導出を行う部分の構造を、上述のような吸着剤は通過させないが培養液は通過させる構造にする。さらに、循環ポンプを接続することにより、培養液は培養槽から配管等を経て吸着剤内包容器内を循環し、吸着剤と接触して生育阻害物質が除去され、効率的に胞子嚢を得ることができる。
【0032】
上記の製造方法により取得した胞子嚢は、コガネムシ科昆虫の防除剤として、胞子嚢を懸濁させた液のまま用いてもよく、あるいは乾燥して粉末にして用いても良い。また乾燥した後、水あるいは緩衝液の懸濁液として使用しても良い。更にこれらの胞子嚢は農薬に用いられる公知慣用の賦形剤、担体、栄養剤等の各種任意成分と共に通常の微生物農薬の製造方法に従って、粉剤、粒剤、水和剤、乳剤、液剤、フロアブル、塗布剤等に製剤化しても良い。また本発明の胞子嚢と他の微生物製剤を混合して使用することも可能である。
【0033】
上記任意成分としては、固体担体として、カリオンクレー、ベントナイト、モンモリロナイト、珪藻土、酸性白土、タルク類、パーライト、バーミキュライト等の鉱物質微粉末、硫酸アンモニウム、尿素、塩化アンモニウム、硝酸アンモニウム等の無機塩、フスマ、キチン、多糖類、米糠、小麦粉等の有機物微粉末等を、また、補助剤として、カゼイン、ゼラチン、アラビアガム、アルギン酸、糖類、合成高分子(ポリビニルアルコール、ポリアクリル酸類等)、ベントナイト等の固着剤や分散剤、その他の成分として、プロピレングリコール、エチレングリコール等の凍結防止剤、キサンタンガム等の天然多糖類、ポリアクリル酸類等の増粘剤を挙げることができる。
【0034】
上記防除剤に含まれる胞子嚢の含有重量は、コガネムシ科昆虫に対して防除効果を呈する範囲であれば特に限定されないが、0.0001〜100%が好ましい。
施用の方法としては、剤型等の使用形態、作物等によって適宜選択され、例えば、地上液剤散布、地上固形散布、空中液剤散布、空中固形散布、施設内施用、土壌混和施用、土壌潅注施用等の方法を挙げることができる。
【0035】
また、他の薬剤、すなわち殺虫剤、殺線虫剤、殺ダニ剤、除草剤、殺菌剤、植物生長調節剤、肥料、又は土壌改良資材(泥炭、腐植酸資材、ポリビニルアルコール系資材等)等と混合して施用、あるいは混合せずに交互施用、または同時施用することも可能である。
【0036】
上記防除剤の施用量は、コガネムシ科昆虫の種類、適用植物の種類、剤型等によって異なるため一概には規定できないが、例えば、地上散布する場合、胞子嚢の施用量が、1010〜1015個/a、好ましくは1011〜1014個/a程度となるようにすればよい。
【0037】
【実施例】
以下本発明の実施例を説明するが、本発明の範囲はこれらの実施例に限定されるものではない。
図1は、本発明の胞子嚢の製造方法に好適に用いられる製造装置の一実施例の断面模式図を示したものである。
図1に示すように、この培養装置10は、培養槽1の内部に、2本の吸着剤内包容器3と撹拌翼2とが設置されて概略構成されている。
【0038】
培養槽1としては、従来公知のものを用いることができ、特に限定されない。培養槽1の容量も特に限定されず、培養するバチルス・ポピリエの菌の量によって決定すればよい。
撹拌翼2としては、好ましくはステンレス製の撹拌翼が用いられるが、その素材は限定されない。
【0039】
吸着剤内包容器3は、ステンレス製の円筒形容器で、培養液と接する容器下部はメッシュの網目構造4とされている。
吸着剤内包容器3の素材は任意であるが、培養中及び殺菌の際に加熱することから耐熱性を有する素材が好ましく、例えばステンレス、アルミニウム、銅、チタンなどの金属製のものや、ガラス、セラミックス等の無機材料などが好ましい。吸着剤内包容器3の外形も特に限定されず、円筒形、直方体形等のいずれであってもよいが、例えば、本実施例のように円筒形であることが好ましい。なお、この吸着剤内包容器3は、1本設置されていてもよいし、複数本設置されていてもよい。
【0040】
本実施例では、吸着剤内包容器3の吸着剤は通過させないが培養液は通過させる構造としては、網目構造4が採用されている。この他にも、細孔等の構造を採用でき、特に限定されない。この網目間隔または細孔の直径は、内包する吸着剤の平均粒径より小さければよく、限定されない。このような細孔または網目構造等は、容器全体に設けられていてもよいし、一部に設けられていてもよい。ただし、より広い容器表面に設けられている方が、培養液が容器内を循環する効率が上昇し、菌の生育阻害物質をより効率的に除去することができるため好ましい。
本実施例の製造装置を用いると、培養槽内部において通気、攪拌等を行うことにより、培養液は吸着剤内包容器内を循環し、吸着剤と接触して生育阻害物質が除去され、効率的に胞子嚢を得ることができる。
【0041】
次に、第二実施例として、図2に本発明の胞子嚢の製造方法に好適に用いられる製造装置の一例の断面模式図を示す。
本実施例にかかる胞子嚢の製造装置20においては、吸着剤内包容器3が培養槽1の外部に設置され、かつ培養液を通液させることができる配管等を用いて培養槽と接続されており、配管の途中に循環ポンプ5が設置されている。また、吸着剤内包容器3の、配管等を接続して培養液を導入及び導出を行う部分の構造は、網目状フィルター4とされている。上記以外は、上述の製造装置10と同様に構成されている。
【0042】
本実施例においても、上記第一実施例の場合と同様に、吸着剤内包容器3の素材、外形は限定されない。例えば、本実施例においては、ガラス製の円筒形容器が採用されている。なお、この吸着剤内包容器3は、1個設置されていてもよいし、複数個設置されていてもよい。複数個設置される場合は、直列に接続してもよいし、並列に接続してもよい。循環ポンプ5は、通常用いられるものを使用できる。
本実施例の製造装置20を用いると、循環ポンプ5を用いることにより、培養液は培養槽1から配管等を経て吸着剤内包容器3内を循環し、吸着剤と接触して生育阻害物質が除去され、効率的に胞子嚢を得ることができる。
【0043】
以下、本発明のさらに具体的な実施例を説明する。
(実施例1)
図1に示す培養装置10を用いて胞子嚢の製造を行った。
本実施例では、この培養装置10において、丸菱バイオエンジ株式会社社製の全容量5Lの培養槽(1)「MDL−5L」を使用して、吸着剤内包容器(3)を培養槽(1)内部に2本取り付けた。吸着剤内包容器(3)は内径2.0cmのステンレス製の円筒形で、培養液と接する容器下部は0.5mmの網目間隔であるメッシュの網目構造(4)とした。また、培養槽(1)には、撹拌翼(2)を取り付けた。
各吸着剤内包容器(3)内に、粒径3.35mm〜4.75mmの関東化学社製の粒状活性炭を30gずつ、合計60gを添加した。
【0044】
培地成分として、蒸留水3Lに、日本製薬社製ペプトン「ポリペプトンS」0.75質量%、和光純薬社製ラクトアルブミン水分物0.8質量%、オクソイド社製イースト0.75質量%、和光純薬社製トレハロース0.5質量%、和光純薬社製グルタミン酸ナトリウム0.64質量%、和光純薬社製プロリン0.5質量%、和光純薬社製ピルビン酸ナトリウム0.05質量%、および日本油脂社製消泡剤「ディスホームCA−123」0.33g/lを添加して溶解させた後、培養槽(1)に入れた。
次いで、上記の吸着剤内包容器(3)が設置された培養槽(1)を121℃、20分のオートクレーブ殺菌を行なった後、バチルス・ポピリエ・セマダラ株の胞子嚢を無菌的に接種し培養を開始した。培養中は培養温度を30℃、pHを7.6、攪拌回転数を100回転/分、通気量を0.8vvmに制御した。
7日間の培養を行ったところ、培養液中に7.0×10個(胞子嚢)/mlの濃度で、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢が得られた。培養終了後に得られた培養液には活性炭が含まれておらず、8000回転/分、10分の遠心分離により、容易に胞子嚢が回収された。
【0045】
(実施例2)
本実施例では、吸着剤として、三菱化学株式会社製イオン交換樹脂「SEPABEADS SP825」を使用して培養を行った。実施例1と同様の培養装置10を用いたが、吸着剤内包容器(3)下部の網目構造(4)の網目間隔は250μmとし、吸着剤の添加量は各吸着剤内包容器(3)に15gずつ、計30gを添加した。培地量、培地成分、培養条件は実施例1と同様である。
7日間の培養を行ったところ、培養液中に7.3×10個(胞子嚢)/mlの濃度で、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢が得られた。培養終了後に得られた培養液にはイオン交換樹脂が含まれておらず、8000回転/分、10分の遠心分離により、容易に胞子嚢が回収された。
【0046】
(実施例3)
図2に示した培養装置20を用いて、胞子嚢の製造を行った。
本実施例では、この培養装置20において、丸善バイオエンジ株式会社製全容量5Lの培養槽(1)「MDL−5L」を使用して、吸着剤内包容器(3)を培養槽外部に1本取り付けた。吸着剤内包容器(3)は内径4cmのガラス製の円筒形で、容器の出入り口は網目間隔が0.5mmの網目状フィルター(4)を付け、培養槽(1)と配管により接続した。さらに、配管の途中に循環ポンプ(5)を設置した。また、培養槽(1)には、撹拌翼(2)を取り付けた。
吸着剤内包容器(3)内に、実施例1と同様にして粒状活性炭を60g添加した。培地量、培地成分は実施例1と同様である。
【0047】
培養槽(1)及び活性炭を含有させた吸着剤内包容器(3)を121℃、20分のオートクレーブ殺菌を行なった後、バチルス・ポピリエ・セマダラ株の胞子嚢を無菌的に接種し培養を開始した。培養中はポンプ(5)を運転して培養液を循環させ、吸着剤内包容器(3)内の活性炭と接触させた。培養温度を30℃、pHを7.6、攪拌回転数を100回転/分、通気量を0.8vvmに制御した。
7日間の培養を行ったところ、培養液中に6.9×10個(胞子嚢)/mlの濃度で胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢が得られた。回収した培養液には活性炭が含まれておらず、8000回転/分、10分の遠心分離により、容易に胞子嚢が回収された。
【0048】
(比較例1)
本比較例においては、吸着剤として粉末活性炭を使用し、吸着剤内包容器を用いずに培養を行った。
液体培地中に、平均粒径20μmの関東化学社製粉末活性炭9gを添加して、実施例1と同様の培地量、培地成分、培養条件でバチルス・ポピリエの培養を行った。
7日間の培養を行ったところ、培養液中に7.1×10個(胞子嚢)/mlの濃度で胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢が得られた。回収した培養液には活性炭が含まれており、遠心分離では、胞子嚢と活性炭は分離することができなかった。
【0049】
(比較例2)
本比較例においては、吸着剤として粒状活性炭を使用し、吸着剤内包容器を用いずに培養を行った。
液体培地中に、粒径3.35mm〜4.75mmの関東化学社製粒状活性炭60gを添加して、実施例1と同様の培地量、培地成分、培養条件でバチルス・ポピリエの培養を行った。ただし、撹拌翼の回転数は、粒状活性炭が充分混合できるように500回転/分とした。
7日間の培養を行ったところ、培養液中に1.3×10個(胞子嚢)/mlの濃度で胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢が得られた。回収した培養液は、ろ過分離により活性炭と胞子嚢が分離できたが、得られた総胞子数は少なかった。
【0050】
【発明の効果】
本発明により、胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢を効率的に培養し、吸着剤を含まない培養液から容易に胞子嚢を回収することができる胞子嚢の製造方法、及び該製造方法に用いられる製造装置を提供することができる。また、該胞子嚢を有効成分とするコガネムシ科昆虫の防除剤、及び該胞子嚢を用いたコガネムシ科昆虫の防除方法を提供することができる。
【図面の簡単な説明】
【図1】吸着剤を包含した容器を培養槽内に設置した例である。
【図2】吸着剤を包含した容器を培養槽外に設置した例である。
【符号の説明】
10,20 培養装置
1 培養槽
2 攪拌翼
3 吸着剤の包含容器
4 網目構造部
5 循環ポンプ
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for producing a sporangium of a bacterium belonging to the genus Bacillus popier that contains a spore and a parasporal body, and an apparatus for producing a sporangium used in the production method.
[0002]
[Prior art]
Scarabaeidae larvae feed on and damage the roots of a wide range of plants, such as turf, agricultural and horticultural crops and trees. Since these larvae live in the ground, chemical pesticides sprayed from the ground are difficult to work, and their habitats are difficult to identify, so in order to obtain a sufficient insecticidal effect, a large amount of pesticides must be used in a wide range. It had to be sprayed and penetrated into the ground. Furthermore, as a result, there is a possibility that environmental pollution may be caused.
[0003]
On the other hand, bacteria belonging to Bacillus popiliae use these larvae of Scarabaeidae as parasitic hosts, and usually infect them orally in the form of sporangia, proliferate in large quantities in hemolymph, eventually cause emulsification disease, It is known to cause death. For this reason, attempts to utilize bacteria belonging to Bacillus popiliae for controlling insects of the order Scarabaeidae, for which chemical pesticides are difficult to work, have been made for a long time. This method is considered to be a promising alternative to chemical pesticides as a biological control method.
[0004]
As a method for cultivating a bacterium belonging to Bacillus popiliae, a method for producing a sporangia by growing the bacterium using a live larva of a scarab beetle, which is a parasitic host, has been conventionally known.
That is, the sporangium of the bacterium belonging to Bacillus popirie is sprayed on the breeding medium in which the larva of Scarabaeid insects are present, or the sporangium of the bacterium belonging to Bacillus popirie is orally ingested by the larva of Scarabaeid insect, Alternatively, after injection into body fluids by injection, larvae are bred for 3 to 4 weeks, Bacillus populiae is grown in the larvae, and then larvae are pierced or incised to collect bodily fluids. This is a method of obtaining sporangia increased in the larva by centrifuging or filtering the body fluid.
However, according to this method, it is necessary to breed a large number of larvae of Scarabaeidae, and as a result, it has been difficult to obtain a large number of sporangia in a short time and economically. For this reason, many studies have been conducted on a culture method using an artificial medium that does not use larvae of Scarabaeidae.
[0005]
By the way, in the conventional literature on a culture method using an artificial medium of Bacillus popirie, sporangia and spores are often used without distinction, and the term spore in the literature means only spores In many cases, it is unclear whether the term refers to a sporangium containing spores but not a parasporal body, or a sporangium containing spores and a parasporal body.
On the other hand, it has been reported that a spore sac of a bacterium belonging to Bacillus popillier, which contains a spore and a parasporal body, has an excellent control effect (see Patent Document 1). Therefore, there is a demand for a more efficient method for producing a sporangia of a bacterium belonging to Bacillus popiliae that contains a spore and a parasporal body.
[0006]
As a culture method using an artificial medium without using the larva of a beetle, there are a solid culture and a liquid culture. However, the production of sporangia by solid culture is not efficient, and the production of sporangia by liquid culture is necessary.
When a sporangia is obtained by liquid culture, there is a culture example in which activated carbon is added to a medium as an adsorbent for removing a growth inhibitor, a peroxide, etc., and a sporangium is obtained by liquid culture (for example, See Non-Patent Document 1 and Patent Documents 1 to 3.) Among these, examples of producing a sporangia containing a spore and a parasporal body are only those described in Patent Documents 1 to 3.
[0007]
All of these methods add activated carbon to the medium, but have major problems in the following points.
First, when powdered activated carbon is used, sporangia and powdered activated carbon are mixed in the culture solution.Furthermore, sporangium and powdered activated carbon are similar in particle size and weight, so centrifugation, It is difficult to separate sporangia from powdered activated carbon by ordinary means such as filtration. In such a case, it is difficult to obtain only the sporangium, and the sporangium must be collected in a form containing activated carbon. In addition, for example, a sporangia containing activated carbon produced by the method described in Patent Document 3 contains 2.3 to 23 times activated carbon with respect to the weight of the sporangia, and contains an adsorbent such as activated carbon. Spore sac is greatly increased in volume during the process of concentration adjustment, filling, etc. during drying or commercialization, and also when formulated, especially when using activated carbon, etc. There is a high risk of inhaling or inducing a dust explosion, and there is a problem that handling is troublesome. There was also a problem that the final product was colored and had poor appearance.
[0008]
On the other hand, when granular activated carbon is simply added to the culture tank, not only is a separation step between the sporangia and the activated carbon necessary, but also the adsorption efficiency is reduced due to the activated carbon settling down at the time of culture. Inhibitors cannot be removed sufficiently. In the usual culturing method, the inside of the culturing device is stirred, so that a method of dispersing the granular activated carbon by increasing the number of rotations of the stirring blades can be considered. A large amount of sporangia cannot be obtained.
[0009]
[Non-patent document 1]
WC Haynes et al., Journal of Bacteriology, (USA), June 1966, Vol. 91, No. 6, p. 2270-2274.
[Patent Document 1]
JP 2002-291467 A
[Patent Document 2]
JP-A-2002-291468
[Patent Document 3]
JP-A-2002-355030
[0010]
[Problems to be solved by the invention]
The problem to be solved by the present invention is to efficiently culture a sporangium of a bacterium belonging to Bacillus popiriae containing a spore and a parasporal body, and to easily collect a sporangium containing no adsorbent. It is an object of the present invention to provide a method for producing a sporangia capable of being produced and a production apparatus used for the method.
[0011]
[Means for Solving the Problems]
The present inventors have conducted intensive studies to solve the above-described problems, and as a result of including the adsorbent in a container through which the adsorbent is not allowed to pass but the culture solution is allowed to pass, by bringing the adsorbent into contact with the culture solution, The inventors have found that the above-mentioned problems can be solved, and have completed the present invention.
That is, the present invention is a method for producing a sporangia containing spores and a parasporal body by culturing Bacillus popirie in a liquid medium containing an adsorbent and a culture solution, wherein the adsorbent is adsorbed. This is a method for producing a sporangia of a bacterium belonging to Bacillus popiliae, which contains a spore in contact with the culture solution and a parasporal body, wherein the spores are contained in a container through which the agent does not pass but the culture solution does.
The present invention also relates to an apparatus for producing a sporangia used in the production method, wherein the spores and the parasporal spores each include a culture tank containing a culture solution, and a container that does not allow the adsorbent to pass but allows the culture solution to pass. This is an apparatus for producing a sporangia of a bacterium belonging to Bacillus popiliae that contains a body.
[0012]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described in detail.
The method of the present invention for producing a sporangia of a bacterium belonging to Bacillus popillier which contains a spore and a parasporal body comprises culturing Bacillus popilier in a liquid medium containing an adsorbent and a culture solution, and then forming the spore and the parasporial. A method for producing a sporangia containing a body, wherein the adsorbent is contained in a container through which the adsorbent does not pass but a culture solution does pass, and is in contact with the culture solution. Is what you do.
[0013]
In the present invention, a sporangia is a sporangia in which a spore and a body called a parasporal body (or parasporium) are included in a sporangia sac wall, and is produced by a bacterium belonging to Bacillus populiae.
[0014]
The bacterium belonging to Bacillus popilliae used in the present invention (hereinafter, may be simply referred to as "bacillus of Bacillus popilliae") is a bacterium belonging to Bacillus popilliae. According to the Bergeys 'Manual of Determinative Bacteriology, the bacteriological properties of the Bacillus spp. Species are 1.3-5.2 μm in length, according to the Bergeys' Manual of Determinative Bacteriology. A gram-negative bacillus with a width of 0.5 to 0.8 μm, a growth temperature of 20 to 35 ° C., and a parasporal body in the sporangia.
Examples of the bacteria belonging to the genus Bacillus popilliae include Bacillus popilliae var. ), A strain of Bacillus popilliae var. Popilliae Hime (FERM P-17660), a strain of Bacillus popilliae sakura (Bacillus popilliae var. (Bacillus popilliae var. Popilli) e DIC-2001) (FERM P-18250), Bacillus popilliae-Deyutoki strain (Bacillus popilliae Dutky, include the American Type Culture Collection No. 14706) and the like.
[0015]
In recent years, the theoretical opinion that "Bacillus spp., Including past strains" should be reclassified as "Paenibacillus popillia" (Bertil Pettersson et al., 1999, Int. J. Syst. Bacteriol., Vol. 49, pp. 531-540), and the handling of both is not clear at this stage. Therefore, in the present invention, “a bacterium belonging to Bacillus spp. Species” includes “a bacterium belonging to Paenibacillus spp. Species”.
[0016]
The adsorbent used in the present invention is used for the purpose of removing substances that inhibit the growth of bacteria belonging to Bacillus populiae. Examples of the adsorbent include activated carbon and a synthetic adsorbent. It is important that any of these is a porous material that adsorbs a fine substance and that can efficiently adsorb an inhibitor in an aqueous solution due to a pore structure developed to the inside of the particle.
[0017]
The shape of the activated carbon used in the present invention may be in the form of powder, granules, sheets, or the like, and is not particularly limited. However, granular activated carbon is particularly preferred because particles are not scattered and are easy to handle.
Further, the synthetic adsorbent used in the present invention means a porous polymer that adsorbs fine substances, and is, for example, a crosslinkable porous polymer formed into particles. Specific examples include SEPABEADS SP825, SEPABEADS SP850, DIAION HP20, and DIAION HP21 manufactured by Mitsubishi Chemical Corporation.
[0018]
Since these adsorbents need to be held in a container through which the adsorbent does not pass but through which the culture solution passes (hereinafter, referred to as an “adsorbent-containing container”), the average particle size is 0.3 mm to 10 mm. And more preferably 2.0 mm to 6.0 mm.
If the average particle size is smaller than 0.3 mm, clogging or the like will occur in the adsorbent-containing container, and the liquid permeability of the container will be significantly impaired, and the adsorption efficiency of the inhibitor will be significantly reduced, which is not preferable. On the other hand, when the average particle size exceeds 10 mm, the liquid permeability is good, but the amount of the adsorbent used increases because the surface area required for adsorption of the inhibitor decreases, and as a result, the adsorbent-containing container becomes large. It is not efficient.
[0019]
The amount of the adsorbent used depends on its adsorptive power and is not particularly limited. However, it is necessary that the inhibitor in the culture solution can be sufficiently removed. In addition, the adsorbent must be sufficiently sterilized and not contaminated by other microorganisms, and a pre-sterilized adsorbent may be used, or the adsorbent may be contained in an adsorbent-containing container and contacted with the culture medium. It may be used after being sterilized together with the medium in a state where it has been used.
[0020]
In the method for producing a sporangia of the present invention, the culture conditions of Bacillus populiae bacteria may be performed according to conventionally known culture conditions for obtaining sporangia, and are not particularly limited. It is necessary to adjust the temperature and pH appropriately. For example, in a Bacillus popirie semada strain, the culture temperature is preferably 25 to 30 ° C, and the pH is preferably 7 to 8. The pH can be adjusted with a commonly used acid such as hydrochloric acid or sulfuric acid or an alkali such as sodium hydroxide, potassium hydroxide or ammonia.
[0021]
The culture solution used in the present invention may be a known and commonly used liquid medium used for producing a sporangia containing Bacillus populiae spores and a parasporal body.For example, a nitrogen source or a carbon source may be used. What is added to water such as distilled water is used. Examples of the nitrogen source include organic nitrogen sources such as peptone, meat extract, fish meat extract, lactalbumin hydrolyzate or yeast extract, which are usually used for culturing microorganisms. Replenish the kind. Other nitrogen sources include inorganic nitrogen sources such as ammonia, nitric acid and their salts. The concentration of the nitrogen source used in the present invention is not particularly limited as long as the sporangia can be produced. However, the concentration is preferably 5% by mass or less based on the culture solution, and more excellent bacteria. Is preferably in the range of 0.2 to 4% by mass in order to exhibit the growth promoting effect.
Although various amino acids are contained in the nitrogen source, specific amino acids can also be added in order to produce sporangia more effectively. Glutamic acid is preferred as the amino acid to be added, and proline is particularly preferred. Either one or both can be added. The medium of the present invention preferably contains glutamic acid in an amount of 0.2 to 4% by mass of the medium by adding glutamic acid, and further adds proline to the medium in an amount of 0.1 to 0. More preferably, it contains 7% by mass. Further, the medium of the present invention is preferably prepared such that the ratio of glutamic acid to all amino acids in the medium is 35 to 90% by mass, and more preferably added so that proline is 10 to 65% by mass. . However, the term "all amino acids" as used herein generally means alanine, arginine, aspartic acid, glutamic acid, glycine, isoleucine, leucine, lysine, methionine, phenylalanine, proline, which are known to be contained in a nitrogen source. , Serine, threonine, histidine, tyrosine, or valine. The total amount of all amino acids, that is, the total amount of the 16 types of free amino acids described above is used as a general indicator of the amount of all free amino acids contained in peptone, yeast extract, and the like.
[0022]
Further, examples of the carbon source include carbon sources used for culturing ordinary microorganisms, and include, for example, saccharides such as trehalose and sucrose, molasses, starch decomposition products, and agricultural wastes such as cheese whey. The addition concentration of these carbon sources is not particularly limited as long as the effects of the present invention are achieved. preferable. However, in order to form a sporangia containing a spore and a parasporal body, the presence of glucose is not preferable, and the concentration of glucose contained in the medium should be 0.01% by mass or less based on the culture solution. preferable.
[0023]
The culture solution used in the present invention may optionally contain a phosphate such as potassium dihydrogen phosphate or dipotassium hydrogen phosphate or an inorganic salt such as a sodium salt thereof. The concentration of the inorganic salt is not particularly limited as long as the effect of the present invention is achieved, but is preferably 1% by mass or less based on the culture solution.
[0024]
By further adding pyruvic acid and a physiologically acceptable salt thereof to the culture solution used in the present invention in addition to the above-mentioned components, more excellent bacterial growth and sporangialization are exhibited. Physiologically acceptable salts of pyruvate include sodium pyruvate, potassium pyruvate and the like. The concentration of pyruvic acid or a physiologically acceptable salt thereof is 0.05 to 0.5% by mass based on the culture solution. 0.1 to 0.3% by mass. The added pyruvic acid and its salt may be sterilized together with the medium components, or may be sterilized separately from the medium components and added at the start of the culture.
[0025]
Examples of the culture method suitably used for the above culture conditions include batch culture, continuous culture, semi-batch culture, and fed-batch culture. The culturing time varies depending on the culturing method, culturing temperature, culturing pH, amount of inoculated cells and the like, but is 7 to 10 days in the case of batch culturing.
[0026]
In the method for producing a sporangia of the present invention, the adsorbent is stored in an adsorbent-containing container, and the culture solution is passed through the adsorbent-containing container and brought into contact with the adsorbent. There is no need to increase the rotation speed and stir to disperse in the culture tank, and it is possible to obtain a spore sac of Bacillus popiliae containing a spore and a parasporal body at a high concentration in the culture solution. .
When the sporangia obtained by the above-mentioned method is separated from the culture solution and collected, the method may be carried out by an easy method such as generally performed centrifugation and filtration.
[0027]
The sporangia obtained by the production method of the present invention contains spores and a parasporal body, has insecticidal properties against various Scarabaeidae insects, and has a controlling effect. Therefore, the sporangia is used as a controlling agent for controlling scarabidae insects, and can be applied to turf, agricultural and horticultural crops, trees, and the like.
[0028]
The Scarabaeidae insects, cupreous chafer (Anomala cuprea), Semadarakogane (Blitopertha orientalis), Japanese beetle (Popillia japonica), Usuchakogane (Phyllopertha diversa), Chairokogane (Adoretus tenuimaculatus), rufocuprea (Anomala rufocuprea), and the like. The pesticidal agent of the present invention has an excellent insecticidal property against them, all of which show an excellent pesticidal effect, and have an excellent pesticidal property against larvae of Douganebuui and Semaedaragane, which are relatively large beetles. Show the effect.
[0029]
Next, an apparatus for producing a sporangium of a bacterium belonging to Bacillus popillier which contains a spore and a parasporal body of the present invention is an apparatus for producing a sporangium used in the production method, and includes a culture solution. It is characterized by comprising a culture tank and a container (adsorbent-containing container) that does not allow the adsorbent to pass but allows the culture solution to pass.
The above-mentioned adsorbent is accommodated in an adsorbent-containing container and comes into contact with the culture solution. Examples of the structure of a portion that does not allow the adsorbent provided in the adsorbent-containing container to pass but allows the culture solution to pass include a structure having pores having a diameter smaller than the average particle diameter of the adsorbent, a network structure, and the like. By making the mesh interval or pore diameter of such a network structure smaller than the average particle size of the adsorbent, the adsorbent stays in the adsorbent-encapsulated container and can be cultured without flowing out into the culture solution. Can be.
[0030]
Preferable examples of the culturing apparatus including the above-described culture tank and the adsorbent-containing container include, for example, a device in which the adsorbent-containing container is installed inside the culture tank and an apparatus in which the adsorbent-containing container is installed outside the culture tank. In this case, part or all of the adsorbent-containing container is constituted by the structure of the portion that does not allow the adsorbent to pass but allows the culture solution to pass.
When the adsorbent-containing container is placed inside the culture tank, the adsorbent-containing container is cultured so that at least a part of the structure of the portion through which the adsorbent does not pass but the culture solution does pass is located below the liquid level of the culture solution. It is preferable to perform predetermined culturing while being fixed inside the tank. That is, by performing aeration, agitation, or the like inside the culture tank, the culture solution circulates through the adsorbent-containing container, contacts the adsorbent, removes the growth-inhibiting substances, and can efficiently obtain sporangia. If the adsorbent-containing container is not fixed as described above, the container is taken in by the bubbles generated during the culturing, and floats out of the liquid surface together with the bubbles, does not come into contact with the culture solution, and does not exhibit sufficient growth inhibitor removing ability. There are cases.
[0031]
When the adsorbent-containing container is installed outside the culture tank, it is preferable to install the adsorbent-containing container outside the culture tank and connect the adsorbent-containing container to the culture tank using a pipe or the like through which the culture solution can pass. Then, the structure of the portion of the adsorbent-containing container that connects and connects the pipes and the like to introduce and discharge the culture solution has a structure that does not allow the adsorbent to pass but allows the culture solution to pass. Furthermore, by connecting a circulation pump, the culture solution circulates through the adsorbent-containing container from the culture tank via pipes and the like, comes into contact with the adsorbent, the growth inhibitor is removed, and the sporangia is efficiently obtained. Can be.
[0032]
The sporangia obtained by the above-mentioned production method may be used as a liquid in which the sporangia is suspended, or may be used after drying as a powder as a control agent for Scarabaeidae. After drying, it may be used as a suspension of water or a buffer solution. Further, these sporangia can be used together with known and commonly used excipients, carriers, nutrients, and other various components used in pesticides, in accordance with a general method for producing microbial pesticides, in the form of powders, granules, wettable powders, emulsions, solutions, flowables. It may be formulated into a coating agent or the like. It is also possible to use the sporangia of the present invention in combination with other microbial preparations.
[0033]
As the optional component, as a solid carrier, mineral powder such as carion clay, bentonite, montmorillonite, diatomaceous earth, acid clay, talc, perlite, vermiculite, etc., inorganic salts such as ammonium sulfate, urea, ammonium chloride, ammonium nitrate, bran, Organic fine powders such as chitin, polysaccharides, rice bran, flour, etc., and adjuvants such as casein, gelatin, gum arabic, alginic acid, sugars, synthetic polymers (polyvinyl alcohol, polyacrylic acids, etc.), bentonite, etc. Examples of agents, dispersants and other components include antifreezing agents such as propylene glycol and ethylene glycol, and thickeners such as natural polysaccharides such as xanthan gum and polyacrylic acids.
[0034]
The weight content of the sporangia contained in the above-mentioned control agent is not particularly limited as long as it is within the range of exhibiting a control effect on Scarabaeidae insects, but is preferably 0.0001 to 100%.
The method of application is appropriately selected depending on the form of use such as the dosage form, crops, etc., for example, above-ground liquid application, above-ground solid application, aerial liquid application, aerial solid application, in-plant application, soil admix application, soil irrigation application, etc. Can be mentioned.
[0035]
In addition, other drugs, such as insecticides, nematicides, acaricides, herbicides, fungicides, plant growth regulators, fertilizers, or soil improvement materials (peat, humic acid materials, polyvinyl alcohol-based materials, etc.), etc. It is also possible to mix and apply, or alternately without mixing or simultaneous application.
[0036]
The application rate of the above-mentioned control agent cannot be unconditionally defined because it varies depending on the type of scarabidae insect, the type of applied plant, the dosage form, and the like. 10 -10 Fifteen Pcs / a, preferably 10 11 -10 14 The number may be about one piece / a.
[0037]
【Example】
Hereinafter, examples of the present invention will be described, but the scope of the present invention is not limited to these examples.
FIG. 1 is a schematic cross-sectional view of one embodiment of a production apparatus suitably used in the method for producing a sporangia of the present invention.
As shown in FIG. 1, the culturing apparatus 10 has a schematic configuration in which two adsorbent-containing containers 3 and stirring blades 2 are installed inside a culturing tank 1.
[0038]
As the culture tank 1, a conventionally known one can be used, and it is not particularly limited. The capacity of the culture tank 1 is also not particularly limited, and may be determined depending on the amount of Bacillus populiae bacteria to be cultured.
As the stirring blade 2, a stainless steel stirring blade is preferably used, but the material is not limited.
[0039]
The adsorbent-containing container 3 is a cylindrical container made of stainless steel, and has a mesh network structure 4 at the lower part of the container in contact with the culture solution.
The material of the adsorbent-containing container 3 is arbitrary, but is preferably a material having heat resistance because it is heated during culturing and sterilization. Examples of the material include metals such as stainless steel, aluminum, copper, and titanium; Inorganic materials such as ceramics are preferred. The outer shape of the adsorbent-containing container 3 is not particularly limited, and may be any of a cylindrical shape, a rectangular parallelepiped shape, and the like. For example, it is preferably a cylindrical shape as in this embodiment. It should be noted that the adsorbent-containing container 3 may be provided alone or in plurals.
[0040]
In the present embodiment, a mesh structure 4 is adopted as a structure that does not allow the adsorbent of the adsorbent-containing container 3 to pass but allows the culture solution to pass. In addition, a structure such as a pore can be adopted, and there is no particular limitation. The mesh spacing or the diameter of the pores is not limited as long as it is smaller than the average particle size of the contained adsorbent. Such a pore or a network structure may be provided on the entire container or on a part thereof. However, it is preferable to be provided on a wider container surface because the efficiency of circulating the culture solution in the container is increased and the growth inhibitor of bacteria can be removed more efficiently.
By using the manufacturing apparatus of the present embodiment, the culture solution is circulated in the adsorbent-containing container by performing aeration, stirring, and the like inside the culture tank, and the growth inhibitor is removed by contact with the adsorbent. A sporangia can be obtained.
[0041]
Next, as a second embodiment, FIG. 2 shows a schematic cross-sectional view of an example of a production apparatus suitably used in the method for producing a sporangia of the present invention.
In the sporangia manufacturing apparatus 20 according to the present embodiment, the adsorbent-containing container 3 is installed outside the culture tank 1 and connected to the culture tank using a pipe or the like through which the culture solution can pass. The circulation pump 5 is installed in the middle of the pipe. Further, the structure of a portion of the adsorbent-containing container 3 for introducing and discharging the culture solution by connecting a pipe or the like is a mesh filter 4. Except for the above, the configuration is the same as that of the manufacturing apparatus 10 described above.
[0042]
In this embodiment, as in the case of the first embodiment, the material and outer shape of the adsorbent-containing container 3 are not limited. For example, in this embodiment, a glass cylindrical container is employed. In addition, this adsorbent-containing container 3 may be provided alone or in plurals. When a plurality are installed, they may be connected in series or in parallel. As the circulation pump 5, a commonly used pump can be used.
When the production apparatus 20 of the present embodiment is used, by using the circulation pump 5, the culture solution circulates through the adsorbent-containing container 3 from the culture tank 1 via a pipe or the like, and comes into contact with the adsorbent, whereby the growth inhibitory substance is removed. It is removed and sporangia can be obtained efficiently.
[0043]
Hereinafter, more specific examples of the present invention will be described.
(Example 1)
Spore sac was produced using the culture apparatus 10 shown in FIG.
In the present embodiment, in this culture apparatus 10, the adsorbent-containing container (3) is used in a culture tank (1) “MDL-5L” having a total volume of 5 L manufactured by Marubishi Bio-Engineering Co., Ltd. 1) Two were installed inside. The adsorbent-containing container (3) was a stainless-steel cylindrical shape having an inner diameter of 2.0 cm, and the lower portion of the container in contact with the culture solution had a mesh network structure (4) with a mesh interval of 0.5 mm. Further, a stirring blade (2) was attached to the culture tank (1).
30 g of granular activated carbon manufactured by Kanto Chemical Co., Ltd. having a particle size of 3.35 mm to 4.75 mm was added to each of the adsorbent-containing containers (3), for a total of 60 g.
[0044]
As a medium component, 3 L of distilled water, 0.75% by mass of peptone “Polypeptone S” manufactured by Nippon Pharmaceutical Co., 0.8% by mass of lactalbumin hydrate manufactured by Wako Pure Chemical Industries, 0.75% by mass of yeast manufactured by Oxoid Co., Ltd. 0.5% by mass of trehalose manufactured by Kako Pure Chemical Industries, 0.64% by mass of sodium glutamate manufactured by Wako Pure Chemical Industries, 0.5% by mass of proline manufactured by Wako Pure Chemical Industries, 0.05% by mass of sodium pyruvate manufactured by Wako Pure Chemical Industries, After adding and dissolving 0.33 g / l of an antifoaming agent “DISFORM CA-123” manufactured by NOF CORPORATION, it was put into the culture tank (1).
Next, the culture tank (1) in which the above-mentioned adsorbent-containing container (3) is installed is subjected to autoclave sterilization at 121 ° C. for 20 minutes, and then aseptically inoculated with a spore of the Bacillus popirie semadala strain and cultured. Started. During the culture, the culture temperature was controlled at 30 ° C., the pH was controlled at 7.6, the stirring speed was controlled at 100 rotations / minute, and the aeration rate was controlled at 0.8 vvm.
After culturing for 7 days, 7.0 × 10 8 A sporangia of a bacterium belonging to Bacillus popiliae containing a spore and a parasporal body was obtained at a concentration of individual (spore sac) / ml. The culture solution obtained after the completion of the culture did not contain activated carbon, and sporangia was easily collected by centrifugation at 8000 rpm for 10 minutes.
[0045]
(Example 2)
In this example, cultivation was performed using an ion exchange resin "SEPABEADS SP825" manufactured by Mitsubishi Chemical Corporation as an adsorbent. The same culture apparatus 10 as in Example 1 was used, except that the mesh interval of the network structure (4) below the adsorbent-containing container (3) was 250 μm, and the amount of adsorbent added was set to each adsorbent-containing container (3). A total of 30 g was added in 15 g portions. The amount of medium, medium components, and culture conditions are the same as in Example 1.
After culturing for 7 days, 7.3 × 10 8 A sporangia of a bacterium belonging to Bacillus popiliae containing a spore and a parasporal body was obtained at a concentration of individual (spore sac) / ml. The culture solution obtained after completion of the culture did not contain an ion exchange resin, and sporangia was easily collected by centrifugation at 8,000 rpm for 10 minutes.
[0046]
(Example 3)
Using the culture device 20 shown in FIG. 2, sporangia was produced.
In the present embodiment, in this culture apparatus 20, one adsorbent-containing container (3) is provided outside the culture tank using a 5 L total volume culture tank (1) “MDL-5L” manufactured by Maruzen Bioengineering Co., Ltd. Attached. The adsorbent-containing container (3) was a glass cylinder having an inner diameter of 4 cm, and the entrance and exit of the container were provided with a mesh filter (4) having a mesh interval of 0.5 mm, and connected to the culture tank (1) by piping. Further, a circulation pump (5) was installed in the middle of the pipe. Further, a stirring blade (2) was attached to the culture tank (1).
In the adsorbent-containing container (3), 60 g of granular activated carbon was added in the same manner as in Example 1. The amount of the medium and the components of the medium are the same as in Example 1.
[0047]
After autoclaving the culture tank (1) and the adsorbent-containing container (3) containing activated carbon at 121 ° C. for 20 minutes, the spores of Bacillus popirie semadala strain are aseptically inoculated and culture is started. did. During the culture, the pump (5) was operated to circulate the culture solution, and was brought into contact with the activated carbon in the adsorbent-containing container (3). The culture temperature was 30 ° C., the pH was 7.6, the stirring speed was 100 rpm, and the aeration rate was 0.8 vvm.
After culturing for 7 days, 6.9 × 10 8 A sporangia of a bacterium belonging to Bacillus popiliae containing a spore and a parasporal body was obtained at a concentration of individual (spore sac) / ml. The recovered culture solution did not contain activated carbon, and sporangia was easily recovered by centrifugation at 8,000 rpm for 10 minutes.
[0048]
(Comparative Example 1)
In this comparative example, powdered activated carbon was used as an adsorbent, and cultivation was performed without using an adsorbent-containing container.
9 g of powdered activated carbon manufactured by Kanto Chemical Co., Ltd. having an average particle diameter of 20 μm was added to the liquid medium, and Bacillus popiriae was cultured under the same amount of medium, medium components and culture conditions as in Example 1.
After culturing for 7 days, 7.1 × 10 8 A sporangia of a bacterium belonging to Bacillus popiliae containing a spore and a parasporal body was obtained at a concentration of individual (spore sac) / ml. The recovered culture solution contained activated carbon, and sporangia and activated carbon could not be separated by centrifugation.
[0049]
(Comparative Example 2)
In this comparative example, granular activated carbon was used as an adsorbent, and culturing was performed without using an adsorbent-containing container.
60 g of granular activated carbon manufactured by Kanto Chemical Co., Ltd. having a particle size of 3.35 mm to 4.75 mm was added to the liquid medium, and Bacillus popiriae was cultured under the same amount of medium, medium components, and culture conditions as in Example 1. . However, the rotation speed of the stirring blade was set to 500 rotations / minute so that the granular activated carbon could be sufficiently mixed.
After culturing for 7 days, 1.3 × 10 8 A sporangia of a bacterium belonging to Bacillus popiliae containing a spore and a parasporal body was obtained at a concentration of individual (spore sac) / ml. In the collected culture solution, activated carbon and sporangia could be separated by filtration, but the total number of spores obtained was small.
[0050]
【The invention's effect】
INDUSTRIAL APPLICABILITY According to the present invention, a sporangium capable of efficiently culturing a sporangium of a bacterium belonging to Bacillus popillier encapsulating a spore and a parasporal body and easily recovering the sporangia from an adsorbent-free culture solution And a manufacturing apparatus used in the manufacturing method. In addition, it is possible to provide a control agent for Scarabaeidae insects using the sporangia as an active ingredient, and a method for controlling Scarabaeidae insects using the sporangia.
[Brief description of the drawings]
FIG. 1 is an example in which a container containing an adsorbent is installed in a culture tank.
FIG. 2 is an example in which a container containing an adsorbent is installed outside a culture tank.
[Explanation of symbols]
10,20 Culture device
1 Culture tank
2 stirring blade
3 Containment container for adsorbent
4 Network structure
5 Circulation pump

Claims (5)

吸着剤と培養液とを含む液体培地でバチルス・ポピリエを培養し、胞子とパラスポラルボディとを内包する胞子嚢を製造する方法であって、該吸着剤が、吸着剤は通過させないが培養液は通過させる容器内に包含され、かつ培養液と接触していることを特徴とする胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造方法。A method for producing a sporangia containing a spore and a parasporal body by culturing Bacillus populiae in a liquid medium containing an adsorbent and a culture solution, wherein the adsorbent does not allow the adsorbent to pass therethrough but is cultured. A method for producing a sporangia of a bacterium belonging to the genus Bacillus popirie, which contains a spore and a parasporal body, wherein the spore is contained in a container through which the liquid passes and is in contact with the culture solution. 前記吸着剤が、平均粒径0.3mm〜10mmであり、かつ活性炭及び合成吸着剤からなる群から選ばれる一種以上である請求項1に記載の胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造方法。The Bacillus. Containing the spores and the parasporal body according to claim 1, wherein the adsorbent has an average particle diameter of 0.3 mm to 10 mm and is at least one selected from the group consisting of activated carbon and a synthetic adsorbent. A method for producing a sporangia of a bacterium belonging to Popiriae. 請求項1または2に記載の製造方法に用いられる胞子嚢の製造装置であって、培養液を包含する培養槽と、吸着剤は通過させないが培養液は通過させる容器とを備えることを特徴とする胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造装置。An apparatus for producing a sporangia used in the production method according to claim 1 or 2, comprising a culture tank containing a culture solution, and a container through which the adsorbent does not pass but the culture solution passes. For producing a sporangium of a bacterium belonging to the genus Bacillus popillier, which contains a spore and a parasporal body. 前記吸着剤は通過させないが培養液は通過させる容器が、前記培養槽の内部に設置されている請求項3に記載の胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造装置。4. A sporangium of a bacterium belonging to Bacillus popiliae that contains the spore and the parasporal body according to claim 3, wherein a container that does not allow the adsorbent to pass therethrough but allows the culture solution to pass therethrough is provided inside the culture tank. Manufacturing equipment. 前記吸着剤は通過させないが培養液は通過させる容器が、前記培養槽の外部に設置され、かつ該培養槽と接続されており、培養液が、培養槽内と吸着剤は通過させないが培養液は通過させる容器内とを循環する請求項3に記載の胞子とパラスポラルボディとを内包するバチルス・ポピリエに属する菌の胞子嚢の製造装置。A container that does not allow the adsorbent to pass therethrough but allows the culture solution to pass therethrough is installed outside the culture tank and is connected to the culture tank, and the culture solution does not allow the adsorbent to pass through the culture tank but the culture solution An apparatus for producing a spore sac of Bacillus popiliae, which contains the spores and the parasporal body according to claim 3, wherein the spores circulate in a container through which the spores pass.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007195542A (en) * 2005-12-27 2007-08-09 Kumiai Chem Ind Co Ltd Method for producing spore of bacterium belonging to the genus bacillus, suitable for the preparation of microorganism agrochemical
CN103436428A (en) * 2013-07-19 2013-12-11 浙江大学 Automatic sperm floating apparatus and use method thereof
JP2020110077A (en) * 2019-01-11 2020-07-27 オリンパス株式会社 Cell culture device
JP2022502363A (en) * 2018-09-20 2022-01-11 バイエル クロップサイエンス エルピーBayer Cropscience Lp How to control animal pests with Paenibacillus terae

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007195542A (en) * 2005-12-27 2007-08-09 Kumiai Chem Ind Co Ltd Method for producing spore of bacterium belonging to the genus bacillus, suitable for the preparation of microorganism agrochemical
CN103436428A (en) * 2013-07-19 2013-12-11 浙江大学 Automatic sperm floating apparatus and use method thereof
CN103436428B (en) * 2013-07-19 2015-02-11 浙江大学 Automatic sperm floating apparatus and use method thereof
JP2022502363A (en) * 2018-09-20 2022-01-11 バイエル クロップサイエンス エルピーBayer Cropscience Lp How to control animal pests with Paenibacillus terae
JP7535037B2 (en) 2018-09-20 2024-08-15 バイエル クロップサイエンス エルピー Method for controlling animal pests using Paenibacillus terrae
JP2020110077A (en) * 2019-01-11 2020-07-27 オリンパス株式会社 Cell culture device
JP7136706B2 (en) 2019-01-11 2022-09-13 株式会社エビデント Cell culture device

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