JP2005013228A - Method for producing phosphorylase - Google Patents

Method for producing phosphorylase Download PDF

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JP2005013228A
JP2005013228A JP2004166616A JP2004166616A JP2005013228A JP 2005013228 A JP2005013228 A JP 2005013228A JP 2004166616 A JP2004166616 A JP 2004166616A JP 2004166616 A JP2004166616 A JP 2004166616A JP 2005013228 A JP2005013228 A JP 2005013228A
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phosphorylase
producing
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leuconostoc
phosphate
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JP4504739B2 (en
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Kazuaki Igarashi
一暁 五十嵐
Shuichi Takizawa
修一 瀧澤
Norihiko Higaki
紀彦 檜垣
Jun Hitomi
潤 人見
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Kao Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a phosphorylase from a phosphorylase-producing bacterium with a high purity in a simple manner. <P>SOLUTION: This method for producing the phosphorylase comprises culturing the phosphorylase-producing bacterium in a culture medium having a concentration of phosphoric acids or their salt of ≥50 mM, and collecting the phosphorylase formed in the culture medium. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

ホスホリラーゼ生産菌からホスホリラーゼを製造する方法に関する。   The present invention relates to a method for producing phosphorylase from a phosphorylase-producing bacterium.

ホスホリラーゼは、無機リン酸の存在下で基質糖類の加リン酸分解を触媒する酵素である。基質の糖の種類によってマルトデキストリンホスホリラーゼ、スクロースホスホリラーゼ、マルトースホスホリラーゼ、セロビオースホスホリラーゼ、トレハロースホスホリラーゼなどが知られている。各種ホスホリラーゼ類は、反応基質である無機リン酸や糖類の定量用酵素試薬として、または反応の可逆性を利用してリン酸化糖を基質に各種配糖体の合成などに使用できる酵素として有用である。   Phosphorylase is an enzyme that catalyzes the phosphorolysis of substrate sugars in the presence of inorganic phosphate. Maltodextrin phosphorylase, sucrose phosphorylase, maltose phosphorylase, cellobiose phosphorylase, trehalose phosphorylase and the like are known depending on the type of sugar of the substrate. Various phosphorylases are useful as enzyme reagents for quantification of inorganic phosphate and saccharides as reaction substrates, or as enzymes that can be used for the synthesis of various glycosides using phosphorylated saccharide as a substrate by utilizing the reversibility of the reaction. is there.

ホスホリラーゼは、Leuconostoc属等の多くの微生物が菌体内あるいは細胞内酵素として保有していることが知られている。
ホスホリラーゼを上記の目的に使用するためには酵素調製物の純度をある程度高めることが望ましく、このような酵素調製物を得るためにはホスホリラーゼ生産菌を培養した後、菌体(細胞)回収、菌体洗浄、菌体破砕、酵素画分回収、精製等の複雑な工程が必要となる(例えば、特許文献1〜5参照)。またこの際、菌体破砕のために溶菌酵素やキレート剤などを添加する必要があるのに加えて菌体成分のほとんどが溶出するため、ホスホリラーゼ純度を上げるための精製工程の負荷が大きくなるのを避けることができない。
It is known that phosphorylase is possessed by many microorganisms such as Leuconostoc as intracellular or intracellular enzymes.
In order to use phosphorylase for the above-mentioned purposes, it is desirable to increase the purity of the enzyme preparation to some extent. In order to obtain such an enzyme preparation, after cultivating the phosphorylase-producing bacteria, Complicated processes such as body washing, cell disruption, enzyme fraction collection, and purification are required (see, for example, Patent Documents 1 to 5). At this time, in addition to the need to add a lytic enzyme, chelating agent, etc. for disrupting the cells, most of the cell components are eluted, increasing the load of the purification process to increase the phosphorylase purity. Cannot be avoided.

このような負荷を低減する方法としては、培地組成の最適化などにより菌体内のホスホリラーゼレベルを上げる方法(例えば、特許文献6〜7参照)、遺伝子組換え体を使用することによって目的ホスホリラーゼを高純度に生成させる方法(例えば、非特許文献1、特許文献3〜5参照)及び簡単な精製方法(例えば、特許文献8参照)などが知られているが、工程そのものを変更することはできず必ずしも満足できるものではない。
特開平1−91778号公報 特開平8−280382号公報 特開平10−14580号公報 特開平10−276785号公報 特開平10−327887号公報 特開平2−154686号公報 特開平3−4785号公報 特開2002−345458号公報 Kitaoら、J.Ferment.Bioeng.,73,179-184 (1992)
As a method for reducing such a load, a method for increasing the phosphorylase level in the microbial cells by, for example, optimizing the composition of the medium (see, for example, Patent Documents 6 to 7), or using the gene recombinant to increase the target phosphorylase level. A method for producing a pure substance (for example, see Non-Patent Document 1 and Patent Documents 3 to 5) and a simple purification method (for example, see Patent Document 8) are known, but the process itself cannot be changed. It is not always satisfactory.
Japanese Unexamined Patent Publication No. 1-91778 JP-A-8-280382 Japanese Patent Laid-Open No. 10-14580 Japanese Patent Laid-Open No. 10-276785 JP-A-10-327887 Japanese Patent Laid-Open No. 2-154686 Japanese Patent Laid-Open No. 3-4785 JP 2002-345458 A Kitao et al., J. Ferment. Bioeng., 73, 179-184 (1992)

本発明は、ホスホリラーゼ生産菌から効率よく簡便にホスホリラーゼを製造する方法を提供することに関する。   The present invention relates to providing a method for producing phosphorylase efficiently and simply from a phosphorylase-producing bacterium.

本発明者らは、ホスホリラーゼ生産菌からホスホリラーゼ画分を効率よく調製する方法について検討したところ、リン酸高濃度培地上でホスホリラーゼ生産菌を培養すると、培養上清中にホスホリラーゼが高収率で生産され、菌体内から酵素を回収する等の操作をすることなく、効率よくホスホリラーゼを製造できることを見出した。   The present inventors examined a method for efficiently preparing a phosphorylase fraction from a phosphorylase-producing bacterium. When a phosphorylase-producing bacterium was cultured on a high-phosphate medium, phosphorylase was produced in a high yield in the culture supernatant. The present inventors have found that phosphorylase can be produced efficiently without performing an operation such as collecting the enzyme from the microbial cells.

すなわち本発明は、リン酸類又はその塩の濃度が50mM以上である培地中でホスホリラーゼ生産菌を培養し、培地中に生成されたホスホリラーゼを採取することを特徴とするホスホリラーゼの製造法を提供するものである。   That is, the present invention provides a method for producing phosphorylase, comprising culturing a phosphorylase-producing bacterium in a medium having a concentration of phosphoric acid or a salt thereof of 50 mM or more and collecting the phosphorylase produced in the medium. It is.

また本発明は、リン酸類又はその塩の濃度が50mM以上であるホスホリラーゼ生産用培地を提供するものである。   Moreover, this invention provides the culture medium for phosphorylase production whose density | concentration of phosphoric acid or its salt is 50 mM or more.

本発明によればホスホリラーゼ生産菌を培養した後、培養上清の回収(細胞除去)、精製といった極めてシンプルな工程で効率よく簡便にホスホリラーゼを製造することができる。   According to the present invention, phosphorylase can be efficiently and easily produced by an extremely simple process of culturing a phosphorylase-producing bacterium and then collecting (purifying cells) and purifying the culture supernatant.

本発明において用いられるホスホリラーゼ生産菌としては、菌体内あるいは細胞内にホスホリラーゼを有する菌であり、一定濃度のリン酸類またはその塩の存在下、培養上清中にホスホリラーゼを産生するものであればよいが、例えばEscherichia属、Bacillus属、Klebsiella属、Streptococcus属、Corynebacterium属、Thermus属、Thermococcus属、Thermotoga属、Leuconostoc属、Pseudomonas属、Clostridium属、Acetobacter属、Pullularia属、Agrobacterium属、Synecoccus属、Aspergillus属、Monilia属、Sclerotinea属、Chlamydomonas属、Lactobacillus属、Neiserria属、Enterococcus属、Lactococcus属、Plesiomonas属、Catellatospora属、Kineosporia属、Micrococcus属、Arthrobacter属、Brevibacterium属、Flavobacterium属、Seratia属、Streptomyces属、Xanthomonas属、Thermoanaerobium属、Rhizopus属、Chaetomium属、Acreomonium属、Byssochilamys属、Cercospora属、Glomerella属、Humicola属、Myceliophthora属、Rhizomucor属、Rosellinia属、Sclerotinia属、Sporidiobolus属、Sterigmatomyces属、Thermoascus属、Thielavia属、Tyromyces属、Erwinia属、Ruminococcus属、Cellvibrio属に属する細菌が挙げられる。
尚、斯かるホスホリラーゼ生産菌は、天然又はUV照射や化学変異剤例えばN-methyl-N'-nitro-N-nitrosoguanidine(MNNG)やethylmethane sulfonate(EMS)(C. Guhrie & G. R. Fink, Methods in Enzymology vol. 194, pp273-281 Academic Press Inc.)等の処理を施すことによって、ホスホリラーゼ産生能が向上した変異株であってもよい。
The phosphorylase-producing bacterium used in the present invention is a bacterium having phosphorylase in the microbial cells or cells, and any bacterium that produces phosphorylase in the culture supernatant in the presence of a certain concentration of phosphates or salts thereof. Is, for example, Escherichia, Bacillus, Klebsiella, Streptococcus, Corynebacterium, Thermus, Thermococcus, Thermotoga, Leuconostoc, Pseudomonas, Clostridium, Acetobacter, Pullularia, Agrobacterium, Synecoccus, , Monilia, Sclerotinea, Chlamydomonas, Lactobacillus, Neiserria, Enterococcus, Lactococcus, Plesiomonas, Catellatospora, Kineosporia, Micrococcus, Arthrobacter, Brevibacterium, Flamobacterium, Anthro Genus, Thermoanaerobium, Rhizopus, Chaetomium, Acreomonium, Byssochilamys, Cercospora, Glomerella, Examples include bacteria belonging to the genus Humicola, Myceliophthora, Rhizomucor, Rosellinia, Sclerotinia, Sporidiobolus, Sterigmatomyces, Thermoascus, Thielavia, Tyromyces, Erwinia, Ruminococcus, and Cellvibrio.
In addition, such phosphorylase-producing bacteria can be obtained by natural or UV irradiation, chemical mutagens such as N-methyl-N'-nitro-N-nitrosoguanidine (MNNG) and ethylmethane sulfonate (EMS) (C. Guhrie & GR Fink, Methods in Enzymology). vol. 194, pp 273-281 Academic Press Inc.) and the like, and may be a mutant having improved phosphorylase production ability.

このうち、Leuconostoc属、Corynebacterium属の細菌が好ましく、Leuconostoc属ではLeuconostoc mesenteroidesLeuconostoc lactisLeuconostoc fallaxLeuconostoc citreumLeuconostoc carnosumLeuconostoc argetinumLeuconostoc pseudomesenteroides、Corynebacterium属ではCorynebacterium glutamicumCorynebacterium callunaeCorynebacterium hoagiiCorynebacterium vitaeruminisCorynebacterium pilosumがより好ましく、中でもLeuconostoc mesenteroidesLeuconostoc mesenteroides KSM-SP1(FERM P-19737)及びLeuconostoc mesenteroides KSM-SP78(FERM AP-20037(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、平成16年4月28日受領))、Corynebacterium vitaeruminisCorynebacterium glutamicum KSM-MP669(FERM AP-20036(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、平成16年4月28日受領))が特に好ましい。 Among, Leuconostoc genus, bacteria are preferred genus Corynebacterium, Leuconostoc is Leuconostoc genus mesenteroides, Leuconostoc lactis, Leuconostoc fallax, Leuconostoc citreum, Leuconostoc carnosum, Leuconostoc argetinum, Leuconostoc pseudomesenteroides, the genus Corynebacterium Corynebacterium glutamicum, Corynebacterium callunae, Corynebacterium hoagii , Corynebacterium Vitaeruminis and Corynebacterium pilosum are more preferable. Among them, Leuconostoc mesenteroides , Leuconostoc mesenteroides KSM-SP1 (FERM P-19737) and Leuconostoc mesenteroides KSM-SP78 (FERM AP-20037 (National Institute of Advanced Industrial Science and Technology, Patent Organism Depositary, 2004) Corynebacterium vitaeruminis , Corynebacterium glutamicum KSM-MP669 (FERM AP-20036 (Incorporated Administrative Agency, National Institute of Advanced Industrial Science and Technology, Patent Biological Deposit Center, received on April 28, 2004))) is particularly preferable.

ホスホリラーゼの製造は、上記ホスホリラーゼ生産菌を、リン酸類又はその塩の濃度が50mM以上である培地(ホスホリラーゼ生産用培地)中で培養することにより行われる。   The phosphorylase is produced by culturing the phosphorylase-producing bacterium in a medium (phosphorylase production medium) in which the concentration of phosphoric acid or a salt thereof is 50 mM or more.

培地に添加されるリン酸類又はその塩としては、例えばリン酸、メタリン酸、トリポリリン酸、ポリリン酸、二リン酸、ポリメタリン酸及びこれらの塩が挙げられ、塩としてはナトリウム塩、カリウム塩が好ましい。特に好ましいリン酸類の塩としては、例えばリン酸一カリウム、リン酸二カリウム、リン酸一ナトリウム、リン酸二ナトリウム等が挙げられ、リン酸類とその塩又は数種のリン酸類の塩を混合して用いることが更に好ましい。   Examples of the phosphoric acids or salts thereof added to the medium include phosphoric acid, metaphosphoric acid, tripolyphosphoric acid, polyphosphoric acid, diphosphoric acid, polymetaphosphoric acid, and salts thereof, and the salt is preferably a sodium salt or a potassium salt. . Examples of particularly preferable salts of phosphoric acids include monopotassium phosphate, dipotassium phosphate, monosodium phosphate, disodium phosphate, and the like. A mixture of phosphoric acid and its salt or several phosphoric acid salts is mixed. And more preferably used.

培地中のリン酸類又はその塩の濃度は、一般的には効果の点から50mM以上であることが必要であるが、好ましくは50mM〜1.5M、より好ましくは50mM〜1M、特に100mM〜1Mの範囲が好ましい。また、Leuconostoc属の細菌においては、400mM〜1.2Mが好ましく、Corynebacterium属では100mM〜600mMが好ましい。   The concentration of phosphoric acid or a salt thereof in the medium is generally required to be 50 mM or more from the viewpoint of effect, but is preferably 50 mM to 1.5 M, more preferably 50 mM to 1 M, particularly 100 mM to 1 M. The range of is preferable. Moreover, 400 mM to 1.2 M is preferable for bacteria of the genus Leuconostoc, and 100 mM to 600 mM is preferable for the genus Corynebacterium.

本発明において用いられる培地は、ホスホリラーゼ生産菌が生育できるものであればよく、上記のリン酸及びその塩の他に、炭素源、窒素源、金属ミネラル類、ビタミン類等を含有する液体培地等が使用できる。   The medium used in the present invention may be any medium as long as it can grow a phosphorylase-producing bacterium, and in addition to the phosphoric acid and its salt, a liquid medium containing a carbon source, a nitrogen source, metal minerals, vitamins and the like Can be used.

培地に添加される糖としては、単糖、二糖、オリゴ糖、多糖が挙げられ、これら2種以上を混合して用いても良い。   Examples of the sugar added to the medium include monosaccharides, disaccharides, oligosaccharides, and polysaccharides. Two or more of these may be used in combination.

糖質以外の炭素源としては、例えば酢酸塩等の有機酸塩が挙げられ、窒素源としては、例えばアンモニア、塩化アンモニウム、硫酸アンモニウム、硝酸アンモニウム、炭酸アンモニウム、リン酸アンモニウム、酢酸アンモニウム等の無機及び有機アンモニウム塩、尿素、ペプトン、肉エキス、酵母エキス、カゼイン加水分解物等の窒素含有有機物、グリシン、グルタミン酸、アラニン、メチオニン等のアミノ酸等が挙げられ、金属ミネラル類としては、例えば塩化ナトリウム、硫酸第一鉄、硫酸マグネシウム、硫酸マンガン、硫酸亜鉛、炭酸カルシウム等が挙げられ、これらを単独で又は必要に応じ混合して用いればよい。   Examples of carbon sources other than carbohydrates include organic acid salts such as acetates, and examples of nitrogen sources include inorganic and organic substances such as ammonia, ammonium chloride, ammonium sulfate, ammonium nitrate, ammonium carbonate, ammonium phosphate, and ammonium acetate. Ammonium salts, urea, peptone, meat extract, yeast extract, nitrogen-containing organic substances such as casein hydrolyzate, amino acids such as glycine, glutamic acid, alanine, methionine, etc., and metal minerals include, for example, sodium chloride, sulfuric acid Examples thereof include ferrous iron, magnesium sulfate, manganese sulfate, zinc sulfate, calcium carbonate, and the like. These may be used alone or in combination as necessary.

培養方法は、微生物が十分に生育できる条件となるようpH及び温度を適宜調整して行われる。また、培養手段は、振とう培養、嫌気培養、静置培養、醗酵槽による培養の他、休止菌体反応及び固定化菌体反応も用いることができる。   The culture method is performed by appropriately adjusting the pH and temperature so that the microorganisms can sufficiently grow. In addition to shaking culture, anaerobic culture, stationary culture, and culture using a fermentor, the culture means can also use resting cell reaction and immobilized cell reaction.

斯くして、リン酸高濃度培地中でホスホリラーゼ生産菌を培養すると、培養上清中にホスホリラーゼが高収率で生産蓄積され、これを採取すれば目的のホスホリラーゼを容易に得ることができる。   Thus, when a phosphorylase-producing bacterium is cultured in a high-phosphate medium, the phosphorylase is produced and accumulated in a high yield in the culture supernatant, and the target phosphorylase can be easily obtained by collecting this.

培地中からホスホリラーゼを採取する方法は、公知の方法に従って行えば良く、例えば、菌体を分離除去し、限外ろ過、塩析、イオン交換、疎水クロマトグラフィー、ゲルろ過、乾燥などを組合わせることによって行うことができる。固定化酵素を作製する際にも菌体外へ産生させることにより煩雑な操作をすることなく可能である。   The method for collecting phosphorylase from the medium may be performed according to a known method, for example, by separating and removing cells and combining ultrafiltration, salting out, ion exchange, hydrophobic chromatography, gel filtration, drying, and the like. Can be done by. Even when the immobilized enzyme is produced, it can be produced outside the cells without complicated operations.

尚、得られたホスホリラーゼの活性測定は、一般的なホスホリラーゼ活性測定法を使用できる。例えば、Weinhausel(Enzyme Microb. Technol., 17, 140-146(1995))の方法が挙げられる。 In addition, the activity measurement of the obtained phosphorylase can use the general phosphorylase activity measuring method. An example is the method of Weinhausel (Enzyme Microb. Technol., 17 , 140-146 (1995)).

本発明によれば、直接菌体外にホスホリラーゼを生産させることが可能であり、菌体破砕など煩雑な操作がなく酵素を得ることが可能である。さらに、低分子化合物であるリン酸類を培地に添加するだけなので、精製工程への負荷も大きく低減され、ホスホリラーゼ高純度品の調製も容易である。   According to the present invention, phosphorylase can be produced directly outside the bacterial cells, and the enzyme can be obtained without complicated operations such as disrupting the bacterial cells. Furthermore, since phosphoric acids, which are low-molecular compounds, are only added to the medium, the load on the purification process is greatly reduced, and the preparation of high-purity phosphorylase is easy.

また、培養液に直接二糖、オリゴ糖、多糖及びリン酸類又はその塩などの基質を加えることによって、特別な操作なく糖リン酸を生産させることが可能である。さらに、アグリコンとなる化合物及び糖リン酸を培養液と直接作用させることによって、特別な操作なく配糖体を得ることも可能である。   In addition, by adding a substrate such as disaccharide, oligosaccharide, polysaccharide and phosphoric acid or a salt thereof directly to the culture solution, sugar phosphate can be produced without any special operation. Furthermore, it is also possible to obtain a glycoside without any special operation by allowing a compound that becomes an aglycone and sugar phosphate to directly act on the culture solution.

実施例1 ロイコノストック属細菌によるホスホリラーゼの生産 Example 1 Production of phosphorylase by bacteria belonging to the genus Leuconostoc

Leuconostoc mesenteroides JCM9693、Leuconostoc carnosum JCM9695、Leuconostoc argentinum JCM11052、Leuconostoc pseudomesenteroides JCM11045、及びLeuconostoc mesenteroides JCM9693株をMNNG処理(C. Guhrie & G. R. Fink, Methods in Enzymology vol. 194, pp273-281 Academic Press Inc.)することにより得られたホスホリラーゼ高生産変異株Leuconostoc mesenteroides KSM-SP1(FERM P-19737)及びLeuconostoc mesenteroides KSM-SP78(FERM AP-20037)を、MR寒天培地(Oxoid社製)に塗末し、嫌気条件で30℃にて培養した。本菌の一白金耳を液体培地(1% 酵母エキス(Difco社製)、1% ポリペプトン(日本製薬製)、0.04% 硫酸マグネシウム七水和物、0.02% 塩化マンガン四水和物、0.0002% 硫酸第二鉄四水和物、400、800,1000 mMのリン酸緩衝液、5%、10%、15%のシュークロース)に接種し、30℃で2日間静置培養を行った。遠心分離により菌体を除去した培養液上清のシュークロースホスホリラーゼ活性を測定した。 Leuconostoc mesenteroides JCM9693, Leuconostoc carnosum JCM9695, Leuconostoc argentinum JCM11052, Leuconostoc pseudomesenteroides JCM11045, and Leuconostoc mesenteroides JCM9693 strains are treated with MNNG (C. Guhrie & GR Fink, Methods in Enzymology Inc. 281) the resulting phosphorylase highly productive mutants Leuconostoc mesenteroides KSM-SP1 (FERM P -19737) and Leuconostoc mesenteroides KSM-SP78 (FERM AP -20037), and Nurimatsu the MR agar medium (Oxoid Ltd.), 30 in anaerobic conditions Incubated at 0 ° C. One platinum loop of this bacterium in liquid medium (1% yeast extract (Difco), 1% polypeptone (Nihon Pharmaceutical), 0.04% magnesium sulfate heptahydrate, 0.02% manganese chloride tetrahydrate, 0.0002% sulfuric acid Ferric tetrahydrate, 400, 800, 1000 mM phosphate buffer, 5%, 10%, 15% sucrose) and static culture at 30 ° C. for 2 days. The sucrose phosphorylase activity of the culture supernatant after removing the cells by centrifugation was measured.

上清のシュークロースホスホリラーゼ活性は、Weinhausel(Enzyme Microb. Technol., 17, 140-146(1995))の方法を一部改変し行った。96穴マイクロプレート上で適宜希釈した培養上清サンプル20μLに酵素反応液(200 mM リン酸カリウム緩衝液(pH7.0)、90 mM シュークロース、100 mM Tris-酢酸緩衝液(pH6.8)、2 mM EDTA、10 mM 硫酸マグネシウム、2 mM NAD、10μMグルコース−1,6−二リン酸、1.2unit/mlホスホグルコムターゼ(ウサギ筋肉由来、ロシュダイアグノスティック社製)、1.2 unit/ml グルコース−6−リン酸脱水素酵素(Leuconostoc mesenteroides由来、ロシュダイアグノスティック社製))を180μL加え、37℃で340 nmのG1P生成に起因する吸光度上昇を測定した。酵素単位1ユニット(U)は、1分間に1μmolのグルコース−1−リン酸(G1P)を生成する量とした。結果を表1に示す。 The sucrose phosphorylase activity in the supernatant was partially modified by the method of Weinhausel (Enzyme Microb. Technol., 17 , 140-146 (1995)). Enzyme reaction solution (200 mM potassium phosphate buffer (pH 7.0), 90 mM sucrose, 100 mM Tris-acetate buffer (pH 6.8), 20 μL of culture supernatant sample diluted appropriately on 96-well microplate, 2 mM EDTA, 10 mM magnesium sulfate, 2 mM NAD, 10 μM glucose-1,6-diphosphate, 1.2 unit / ml phosphoglucomutase (from rabbit muscle, manufactured by Roche Diagnostics), 1.2 unit / ml glucose 180 μL of 6-phosphate dehydrogenase (from Leuconostoc mesenteroides , manufactured by Roche Diagnostics) was added, and the increase in absorbance due to G1P generation at 340 nm was measured at 37 ° C. One unit (U) of the enzyme unit was an amount that produced 1 μmol of glucose-1-phosphate (G1P) per minute. The results are shown in Table 1.

Figure 2005013228
Figure 2005013228

表1より、培地中のリン酸濃度を高くすることにより、菌体外に生産されるホスホリラーゼの量が上昇することが確認された。   From Table 1, it was confirmed that the amount of phosphorylase produced outside the cells increased by increasing the phosphate concentration in the medium.

実施例2 コリネバクテリウム属細菌によるホスホリラーゼの生産
Corynebacterium vitaeruminis JCM1323、Corynebacterium callunae IFO15359、Corynebacterium glutamicum JCM1321及びCorynebacterium glutamicum JCM1321をMNNG処理することにより得られたホスホリラーゼ高生産変異株Corynebacterium glutamicum KSM-MP669(FERM AP-20036)を、SCD寒天培地(日本製薬株式会社)に塗末し30℃にて培養した。本菌の一白金耳を液体培地(0.67%のYeast Nitrogen Base(Difco社)、50, 100,200 mMのリン酸緩衝液(pH7)、15%のデキストリン(sigma社 potato由来))に接種し、30℃で6日間振とう培養を行った。遠心分離により菌体を除去した培養液上清のマルトデキストリンホスホリラーゼ活性を測定した。
Example 2 Production of phosphorylase by Corynebacterium
Corynebacterium vitaeruminis JCM1323, Corynebacterium callunae IFO15359, Corynebacterium glutamicum JCM1321 and Corynebacterium phosphorylase high-producing mutant strains obtained by the glutamicum JCM1321 to MNNG treatment Corynebacterium glutamicum KSM-MP669 the (FERM AP-20036), SCD agar medium (Nippon Pharmaceutical Co., Ltd. ) And cultured at 30 ° C. One platinum loop of this bacterium is inoculated into a liquid medium (0.67% Yeast Nitrogen Base (Difco), 50, 100, 200 mM phosphate buffer (pH 7), 15% dextrin (derived from sigma potato)), 30 Shaking culture was performed at 0 ° C. for 6 days. The maltodextrin phosphorylase activity of the culture supernatant after removing the cells by centrifugation was measured.

上清のマルトデキストリンホスホリラーゼ活性は、Weinhausel(Enzyme Microb. Technol., 17, 140-146(1995))の方法を一部改変し行った。96穴マイクロプレート上で適宜希釈した培養上清サンプル20μLに酵素反応液(200 mM リン酸カリウム緩衝液(pH7.0)、2% デキストリン、100 mM Tris-酢酸緩衝液(pH6.8)、2 mM EDTA、10 mM 硫酸マグネシウム、2 mM NAD、10μMグルコース−1,6−二リン酸、1.2unit/mlホスホグルコムターゼ(ウサギ筋肉由来、ロシュダイアグノスティック社製)、1.2 unit/ml グルコース−6−リン酸脱水素酵素(Leuconostoc mesenteroides由来、ロシュダイアグノスティック社製))を180μL加え、37℃で340 nmのG1P生成に起因する吸光度上昇を測定した。酵素単位1ユニット(U)は、1分間に1μmolのグルコース−1−リン酸(G1P)を生成する量とした。結果を表2に示す。 The maltodextrin phosphorylase activity in the supernatant was obtained by partially modifying the method of Weinhausel (Enzyme Microb. Technol., 17 , 140-146 (1995)). Enzyme reaction solution (200 mM potassium phosphate buffer (pH 7.0), 2% dextrin, 100 mM Tris-acetate buffer (pH 6.8), 2 mM EDTA, 10 mM magnesium sulfate, 2 mM NAD, 10 μM glucose-1,6-diphosphate, 1.2 unit / ml phosphoglucomutase (from rabbit muscle, manufactured by Roche Diagnostics), 1.2 unit / ml glucose-6 -Phosphate dehydrogenase (from Leuconostoc mesenteroides , manufactured by Roche Diagnostics) was added in an amount of 180 μL, and the increase in absorbance due to G1P production at 340 nm was measured at 37 ° C. One unit (U) of the enzyme unit was an amount that produced 1 μmol of glucose-1-phosphate (G1P) per minute. The results are shown in Table 2.

Figure 2005013228
Figure 2005013228

表2より、培地中のリン酸濃度を高くすることにより、菌体外に生産されるホスホリラーゼの量が上昇することが確認された。   From Table 2, it was confirmed that the amount of phosphorylase produced outside the cells increased by increasing the phosphate concentration in the medium.

Claims (3)

リン酸類又はその塩の濃度が50mM以上である培地中でホスホリラーゼ生産菌を培養し、培地中に生成されたホスホリラーゼを採取することを特徴とするホスホリラーゼの製造法。   A method for producing phosphorylase, comprising culturing a phosphorylase-producing bacterium in a medium having a concentration of phosphoric acid or a salt thereof of 50 mM or more and collecting the phosphorylase produced in the medium. ホスホリラーゼ生産菌がLeuconostoc属又はCorynebacterium属の細菌である請求項1記載のホスホリラーゼの製造法。   The method for producing phosphorylase according to claim 1, wherein the phosphorylase-producing bacterium is a bacterium of the genus Leuconostoc or Corynebacterium. リン酸類又はその塩の濃度が50mM以上であるホスホリラーゼ生産用培地。   A medium for producing phosphorylase, wherein the concentration of phosphoric acid or a salt thereof is 50 mM or more.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2547593A1 (en) * 1983-06-15 1984-12-21 Beghin Say Sa Process for the production of sucrose phosphorylase, sucrose phosphorylase obtained by the process and application to the synthesis of glucose-1-phosphoric acid and its salts
JPH034785A (en) * 1989-05-30 1991-01-10 Kikkoman Corp Production of sucrose phosphorylase
JPH1189566A (en) * 1997-09-18 1999-04-06 Nippon Shokuhin Kako Co Ltd Production of disaccharide phosphorylase
JP2000004670A (en) * 1998-06-25 2000-01-11 Chisso Corp Granular phosphoric acid medium and material for fertilizing seedling raising vessel using the same
JP2003079337A (en) * 2001-09-07 2003-03-18 Kao Corp Mineral taste improver

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2547593A1 (en) * 1983-06-15 1984-12-21 Beghin Say Sa Process for the production of sucrose phosphorylase, sucrose phosphorylase obtained by the process and application to the synthesis of glucose-1-phosphoric acid and its salts
JPH034785A (en) * 1989-05-30 1991-01-10 Kikkoman Corp Production of sucrose phosphorylase
JPH1189566A (en) * 1997-09-18 1999-04-06 Nippon Shokuhin Kako Co Ltd Production of disaccharide phosphorylase
JP2000004670A (en) * 1998-06-25 2000-01-11 Chisso Corp Granular phosphoric acid medium and material for fertilizing seedling raising vessel using the same
JP2003079337A (en) * 2001-09-07 2003-03-18 Kao Corp Mineral taste improver

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