JP2009039074A5 - - Google Patents

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JP2009039074A5
JP2009039074A5 JP2007209936A JP2007209936A JP2009039074A5 JP 2009039074 A5 JP2009039074 A5 JP 2009039074A5 JP 2007209936 A JP2007209936 A JP 2007209936A JP 2007209936 A JP2007209936 A JP 2007209936A JP 2009039074 A5 JP2009039074 A5 JP 2009039074A5
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protein
producing
continuous fermentation
porous membrane
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JP2007209936A
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JP2009039074A (en
JP5141133B2 (en
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本発明の連続発酵によるタンパク質の製造方法の好ましい態様によれば、前記のタンパク質は酵素であり、その酵素は好ましくはデンプンまたはセルロースの糖化酵素、プロテアーゼあるいはリパーゼであり、より好ましくはα−アミラーゼあるいはグルコアミラーゼである。 According to a preferred embodiment of the method for producing a protein by continuous fermentation of the present invention, the protein is an enzyme, which is preferably a starch or cellulose saccharifying enzyme, a protease or a lipase, more preferably an α-amylase or Glucoamylase.

Claims (9)

タンパク質の分泌生産能力を有する微生物の発酵培養液を分離膜で濾過し、濾液から生産物であるタンパク質を回収するとともに未濾過液を前記の発酵培養液に保持または還流し、かつ、その微生物の発酵原料を前記の発酵培養液に追加する連続発酵によりタンパク質製造する方法であって、前記の分離膜として平均細孔径が0.01μm以上1μm未満の細孔を有する多孔性膜を用い、その膜間差圧を0.1から20kPaの範囲にして濾過処理することを特徴とする連続発酵によるタンパク質の製造方法。 The fermentation broth of a microorganism having the ability to produce proteins is filtered through a separation membrane, the protein as a product is recovered from the filtrate, and the unfiltered liquid is retained or refluxed in the fermentation broth, and A method for producing a protein by continuous fermentation in which a fermentation raw material is added to the fermentation broth, wherein a porous membrane having pores having an average pore diameter of 0.01 μm or more and less than 1 μm is used as the separation membrane, A method for producing a protein by continuous fermentation, characterized by performing filtration treatment with a transmembrane pressure difference in the range of 0.1 to 20 kPa. 多孔性膜の純水透過係数が、2×10−9/m/s/pa以上6×10−7/m/s/pa以下である請求項1記載の連続発酵によるタンパク質の製造方法。 The pure water permeability coefficient of the porous membrane is 2 × 10 −9 m 3 / m 2 / s / pa or more and 6 × 10 −7 m 3 / m 2 / s / pa or less. A method for producing a protein. 多孔性膜の平均細孔径が0.01μm以上0.2μm未満であり、かつ、該平均細孔径の標準偏差が0.1μm以下である請求項1または2記載の連続発酵によるタンパク質の製造方法。   The method for producing a protein by continuous fermentation according to claim 1 or 2, wherein the porous membrane has an average pore size of 0.01 µm or more and less than 0.2 µm, and a standard deviation of the average pore size is 0.1 µm or less. 多孔性膜の膜表面粗さが0.1μm以下である請求項1から3のいずれかに記載の連続発酵によるタンパク質の製造方法。   The method for producing a protein by continuous fermentation according to any one of claims 1 to 3, wherein the membrane surface roughness of the porous membrane is 0.1 µm or less. 多孔性膜が多孔性樹脂層を含む多孔性膜である請求項1から4のいずれかに記載の連続発酵によるタンパク質の製造方法。   The method for producing a protein by continuous fermentation according to any one of claims 1 to 4, wherein the porous membrane is a porous membrane including a porous resin layer. 多孔性膜の素材がポリフッ化ビニリデン系樹脂である請求項1から5のいずれかに記載の連続発酵によるタンパク質の製造方法。   The method for producing a protein by continuous fermentation according to any one of claims 1 to 5, wherein the material of the porous membrane is a polyvinylidene fluoride resin. タンパク質が酵素である請求項1からのいずれかに記載の連続発酵によるタンパク質の製造方法。 The method for producing a protein by continuous fermentation according to any one of claims 1 to 6 , wherein the protein is an enzyme. 酵素がデンプンまたはセルロースの糖化酵素、プロテアーゼあるいはリパーゼである請求項7記載の連続発酵によるタンパク質の製造方法。The method for producing a protein by continuous fermentation according to claim 7, wherein the enzyme is starch or cellulose saccharifying enzyme, protease or lipase. 酵素がα−アミラーゼ、またはグルコアミラーゼである請求項記載の連続発酵によるタンパク質の製造方法。
The method for producing a protein by continuous fermentation according to claim 7 , wherein the enzyme is α-amylase or glucoamylase.
JP2007209936A 2007-08-10 2007-08-10 Protein production method by continuous fermentation Expired - Fee Related JP5141133B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007209936A JP5141133B2 (en) 2007-08-10 2007-08-10 Protein production method by continuous fermentation

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Application Number Priority Date Filing Date Title
JP2007209936A JP5141133B2 (en) 2007-08-10 2007-08-10 Protein production method by continuous fermentation

Publications (3)

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JP2009039074A JP2009039074A (en) 2009-02-26
JP2009039074A5 true JP2009039074A5 (en) 2010-09-16
JP5141133B2 JP5141133B2 (en) 2013-02-13

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Publication number Priority date Publication date Assignee Title
JP5659466B2 (en) * 2009-08-07 2015-01-28 東レ株式会社 Method and apparatus for producing chemicals by continuous culture

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0260404B1 (en) * 1986-08-21 1995-05-31 VAN DEN BERG, Robert Amylolytic enzymes producing microorganisms constructed by recombinant DNA technology and their use for fermentation processes
JPS63248396A (en) * 1987-04-06 1988-10-14 Nok Corp Production of dihydrooxoisophorone
JPH09173077A (en) * 1995-07-20 1997-07-08 Tadayuki Imanaka Ultrathermoresistant acidic alpha-amylase and dna fragment containing gene for producing the alpha-amylase
JPH10323543A (en) * 1997-05-22 1998-12-08 Arakawa Chem Ind Co Ltd Method for separating product in microbial reaction
JPH11113587A (en) * 1997-10-14 1999-04-27 Ube Ind Ltd Production of alcohol by alcoholic fermentation and apparatus therefor
WO2002064240A1 (en) * 2001-02-16 2002-08-22 Toray Industries, Inc. Separating film, separating film element, separating film module, sewage and waste water treatment device, and separating film manufacturing method
JP2003053164A (en) * 2001-08-20 2003-02-25 Kuraray Co Ltd Removing method of pathogenic protozoa and separating membrane used therein
JP3896101B2 (en) * 2003-07-11 2007-03-22 ダイセル化学工業株式会社 Car wash wastewater treatment equipment
JP2005111326A (en) * 2003-10-06 2005-04-28 Toray Ind Inc Liquid separation membrane and its use
JP5082496B2 (en) * 2006-02-24 2012-11-28 東レ株式会社 Process for producing chemicals by continuous fermentation and continuous fermentation apparatus

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