TY - JOUR
T1 - Membrane-assisted extractive butanol fermentation by Clostridium saccharoperbutylacetonicum N1-4 with 1-dodecanol as the extractant
AU - Tanaka, Shigemitsu
AU - Tashiro, Yukihiro
AU - Kobayashi, Genta
AU - Ikegami, Toru
AU - Negishi, Hideyuki
AU - Sakaki, Keiji
N1 - Funding Information:
This research was supported by a research grant form the New Energy and Industrial Technology Development Organization (NEDO) .
PY - 2012/7
Y1 - 2012/7
N2 - A polytetrafluoroethylene (PTFE) membrane was used in membrane-assisted extractive (MAE) fermentation of acetone-butanol-ethanol (ABE) by Clostridium saccharoperbutylacetonicum N1-4. The growth inhibition effects of 1-dodecanol, which has a high partition coefficient for butanol, can be prevented by employing 1-dodecanol as an extractant when using a PTFE membrane. Compared to conventional fermentation, MAE-ABE fermentation with 1-dodecanol decreased butanol inhibition and increased glucose consumption from 59.4 to 86.0g/L, and total butanol production increased from 16.0 to 20.1g/L. The maximum butanol production rate increased from 0.817 to 0.979g/L/h. The butanol productivity per membrane area was remarkably high with this system, i.e., 78.6g/L/h/m 2. Therefore, it is expected that this MAE fermentation system can achieve footprint downsizing.
AB - A polytetrafluoroethylene (PTFE) membrane was used in membrane-assisted extractive (MAE) fermentation of acetone-butanol-ethanol (ABE) by Clostridium saccharoperbutylacetonicum N1-4. The growth inhibition effects of 1-dodecanol, which has a high partition coefficient for butanol, can be prevented by employing 1-dodecanol as an extractant when using a PTFE membrane. Compared to conventional fermentation, MAE-ABE fermentation with 1-dodecanol decreased butanol inhibition and increased glucose consumption from 59.4 to 86.0g/L, and total butanol production increased from 16.0 to 20.1g/L. The maximum butanol production rate increased from 0.817 to 0.979g/L/h. The butanol productivity per membrane area was remarkably high with this system, i.e., 78.6g/L/h/m 2. Therefore, it is expected that this MAE fermentation system can achieve footprint downsizing.
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U2 - 10.1016/j.biortech.2012.03.096
DO - 10.1016/j.biortech.2012.03.096
M3 - Article
C2 - 22575842
AN - SCOPUS:84861663665
VL - 116
SP - 448
EP - 452
JO - Bioresource Technology
JF - Bioresource Technology
SN - 0960-8524
ER -