JP2009065970A5 - - Google Patents

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JP2009065970A5
JP2009065970A5 JP2008211685A JP2008211685A JP2009065970A5 JP 2009065970 A5 JP2009065970 A5 JP 2009065970A5 JP 2008211685 A JP2008211685 A JP 2008211685A JP 2008211685 A JP2008211685 A JP 2008211685A JP 2009065970 A5 JP2009065970 A5 JP 2009065970A5
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producing
fermentation
chemical product
porous membrane
fermentation broth
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JP2008211685A
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JP2009065970A (en
JP5287029B2 (en
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Claims (8)

微生物もしくは培養細胞の発酵培養液を分離膜で濾過し、濾液から生産物を回収すると共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、発酵原料を前記の発酵培養液に追加する連続発酵による化学品の製造方法であって、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て発酵培養液を濾過処理すると共に、前記の発酵培養液から微生物もしくは培養細胞を含む発酵培養液の一部を系外に抜き出すことを特徴とする連続発酵による化学品の製造方法。   The fermentation broth of microorganisms or cultured cells is filtered through a separation membrane, the product is recovered from the filtrate, the unfiltered liquid is retained or refluxed in the fermentation broth, and the fermentation raw material is added to the fermentation broth A method for producing a chemical product by continuous fermentation, wherein the fermentation broth is filtered using a porous membrane having pores having an average pore diameter of 0.01 μm or more and less than 1 μm as the separation membrane, A method for producing a chemical product by continuous fermentation, wherein a part of a fermentation broth containing microorganisms or cultured cells is extracted from the fermentation broth. 濾過処理を、膜間差圧を0.1から20kPaの範囲にして行うことを特徴とする請求項1記載の連続発酵による化学品の製造方法。   The method for producing a chemical product by continuous fermentation according to claim 1, wherein the filtration treatment is performed 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以下であることを特徴とする請求項1から2のいずれかに記載の連続発酵による化学品の製造方法。 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. 3. A method for producing a chemical product by continuous fermentation according to any one of items 1 to 2. 多孔性膜の平均細孔径が、0.01μm以上0.2μm未満の範囲内にあり、かつ、該平均細孔径の標準偏差が0.1μm以下であることを特徴とする請求項1から3のいずれかに記載の連続発酵による化学品の製造方法。   The average pore diameter of the porous membrane is in the range of 0.01 µm or more and less than 0.2 µm, and the standard deviation of the average pore diameter is 0.1 µm or less. The manufacturing method of the chemical by continuous fermentation in any one. 多孔性膜の膜表面粗さが0.1μm以下の多孔性膜であることを特徴とする請求項1から4のいずれかに記載の連続発酵による化学品の製造方法。   The method for producing a chemical product by continuous fermentation according to any one of claims 1 to 4, wherein the porous membrane has a membrane surface roughness of 0.1 µm or less. 多孔性膜が多孔質樹脂層を含む多孔性膜である請求項1から5のいずれかに記載の連続発酵による化学品の製造方法。   The method for producing a chemical product by continuous fermentation according to any one of claims 1 to 5, wherein the porous membrane is a porous membrane including a porous resin layer. 多孔性膜の膜素材がポリフッ化ビニリデンを含むことを特徴とする請求項1から6のいずれかに記載の連続発酵による化学品の製造方法。   The method for producing a chemical product by continuous fermentation according to any one of claims 1 to 6, wherein the membrane material of the porous membrane contains polyvinylidene fluoride. 系外に抜き出された微生物もしくは培養細胞を含む発酵培養液の体積と実質的に等しい量の液体を、発酵培養液に添加することを特徴とする請求項1から7のいずれかに記載の連続発酵による化学品の製造方法。   The liquid of an amount substantially equal to the volume of the fermentation broth containing microorganisms or cultured cells extracted out of the system is added to the fermentation broth. A method for producing chemicals by continuous fermentation.
JP2008211685A 2007-08-22 2008-08-20 Process for producing chemicals by continuous fermentation Expired - Fee Related JP5287029B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008211685A JP5287029B2 (en) 2007-08-22 2008-08-20 Process for producing chemicals by continuous fermentation

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2007216266 2007-08-22
JP2007216266 2007-08-22
JP2008211685A JP5287029B2 (en) 2007-08-22 2008-08-20 Process for producing chemicals by continuous fermentation

Publications (3)

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JP2009065970A JP2009065970A (en) 2009-04-02
JP2009065970A5 true JP2009065970A5 (en) 2011-09-29
JP5287029B2 JP5287029B2 (en) 2013-09-11

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JP2008211685A Expired - Fee Related JP5287029B2 (en) 2007-08-22 2008-08-20 Process for producing chemicals by continuous fermentation

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Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AP2011006029A0 (en) * 2009-05-20 2011-12-31 Xyleco Inc Processing biomass.
US8636402B2 (en) 2009-05-20 2014-01-28 Xyleco, Inc. Processing biomass
US20130323805A1 (en) * 2010-09-14 2013-12-05 Toray Industries, Inc. Production method for chemicals by continuous fermentation
JP6303984B2 (en) 2014-10-31 2018-04-04 トヨタ自動車株式会社 Method for producing ethanol by continuous culture and continuous culture apparatus
WO2020129342A1 (en) * 2018-12-18 2020-06-25 積水化学工業株式会社 Organic substance generation system
CN112481315B (en) * 2019-09-11 2023-05-12 吉林中粮生化有限公司 Method for preparing citric acid by continuous liquid-changing fermentation

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0734749B2 (en) * 1988-02-03 1995-04-19 日本碍子株式会社 Method for producing erythritol
CA2432046C (en) * 2001-02-16 2011-04-05 Toray Industries, Inc. Separation membrane, separation membrane element, separation membrane module, sewage treatment apparatus, and method for making the separation membrane
JP4436635B2 (en) * 2003-08-27 2010-03-24 有限会社新世紀発酵研究所 Method for producing useful substance using useful substance producing bacteria producing bacteriocin

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