JP2007252367A5 - - Google Patents

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JP2007252367A5
JP2007252367A5 JP2007040518A JP2007040518A JP2007252367A5 JP 2007252367 A5 JP2007252367 A5 JP 2007252367A5 JP 2007040518 A JP2007040518 A JP 2007040518A JP 2007040518 A JP2007040518 A JP 2007040518A JP 2007252367 A5 JP2007252367 A5 JP 2007252367A5
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fermentation
membrane
producing
continuous fermentation
chemical product
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JP5082496B2 (en
JP2007252367A (en
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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、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 by continuous fermentation, wherein a porous membrane having pores with an average pore diameter of 0.01 μm or more and less than 1 μm is used as the separation membrane, and the transmembrane pressure difference is 0.1 to 20 kPa. A method for producing a chemical product by continuous fermentation, characterized by subjecting to filtration in the range described above. 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. The manufacturing method of the chemical product by continuous fermentation of description. 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または2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. A method for producing chemicals by continuous fermentation. 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 method for producing a chemical product by continuous fermentation according to any one of claims 1 to 3, 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 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 membrane material of the porous membrane contains polyvinylidene fluoride. 微生物または培養細胞の発酵培養液および発酵原料が、糖類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 fermentation broth of the microorganism or cultured cell and the fermentation raw material contain saccharides. 化学品が有機酸またはアルコールであ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 method for producing a chemical product by continuous fermentation according to any one of claims 1 to 7, wherein the chemical product is an organic acid or an alcohol. 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装置であって、微生物もしくは培養細胞を発酵培養させるための発酵反応槽と、該発酵反応槽に発酵培養液循環手段を介して接続され内部に分離膜を備えた発酵培養液を濾過するための膜分離槽と、分離膜の膜間差圧を0.1から20kPaの範囲に制御する手段からなり、該分離膜が平均細孔径0.01μm以上1μm未満の多孔性膜であることを特徴とする連続発酵装置。   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 An apparatus for producing a chemical product by continuous fermentation, comprising a fermentation reaction vessel for fermenting and culturing microorganisms or cultured cells, and a separation membrane inside the fermentation reaction vessel connected via a fermentation culture fluid circulation means A membrane separation tank for filtering the fermentation broth and a means for controlling the transmembrane differential pressure of the separation membrane in the range of 0.1 to 20 kPa. A continuous fermentation apparatus characterized by being a membrane. 分離膜の膜間差圧を、水頭差制御装置による発酵培養液と多孔性膜処理水の液位差で制
御することを特徴とする請求項記載の連続発酵装置。
The transmembrane pressure of the separation membrane, a continuous fermentation apparatus according to claim 9, wherein the controller controls the liquid level difference of the fermentation broth and the porous membrane treated water by the water head difference control device.
分離膜の膜間差圧を、加圧ポンプまたは/および吸引ポンプで制御することを特徴とす
る請求項または10記載の連続発酵装置。
The continuous fermentation apparatus according to claim 9 or 10 , wherein the transmembrane pressure difference of the separation membrane is controlled by a pressurizing pump or / and a suction pump.
分離膜の膜間差圧を、気体または液体の圧力で制御することを特徴とする請求項から11のいずれかに記載の連続発酵装置。 Continuous fermentation apparatus according to any one of the transmembrane pressure of the separation membrane, the claim 9, characterized in that controlled by the pressure of the gas or liquid 11. 発酵培養液循環手段が、循環ポンプであることを特徴とする請求項12のいずれかに記載の連続発酵装置。 The continuous fermentation apparatus according to any one of claims 9 to 12 , wherein the fermentation culture medium circulation means is a circulation pump.
JP2007040518A 2006-02-24 2007-02-21 Process for producing chemicals by continuous fermentation and continuous fermentation apparatus Active JP5082496B2 (en)

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JP6815307B2 (en) * 2017-11-09 2021-01-20 株式会社村田製作所 Filtration filter for nucleated cells and filtration method using it
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