TY - JOUR
T1 - Non-carbon loss long-term continuous lactic acid production from mixed sugars using thermophilic Enterococcus faecium QU 50
AU - Abdel-Rahman, Mohamed Ali
AU - Tan, Jiaming
AU - Tashiro, Yukihiro
AU - Zendo, Takeshi
AU - Sakai, Kenji
AU - Sonomoto, Kenji
N1 - Funding Information:
This study has been supported by the Kyushu University, Japan to Mohamed Ali Abdel‐Rahman under the International Exchange Agreement Promotional Program between Kyushu University and Al‐Azhar University, Egypt.
Funding Information:
This study has been supported by the Kyushu University, Japan to Mohamed Ali Abdel-Rahman under the International Exchange Agreement Promotional Program between Kyushu University and Al-Azhar University, Egypt.
Publisher Copyright:
© 2020 Wiley Periodicals, Inc.
PY - 2020/6/1
Y1 - 2020/6/1
N2 - In this study, a non-sterile (open) continuous fermentation (OCF) process with no-carbon loss was developed to improve lactic acid (LA) productivity and operational stability from the co-utilization of lignocellulose-derived sugars by thermophilic Enterococcus faecium QU 50. The effects of different sugar mixtures on LA production were firstly investigated in conventional OCF at 50°C, pH 6.5 and a dilution rate of 0.20 hr−1. The xylose consumption ratio was greatly lower than that of glucose in fermentations with glucose/xylose mixtures, indicating apparent carbon catabolite repression (CCR). However, CCR could be efficiently eliminated by feeding solutions containing the cellobiose/xylose mixture. In OCF at a dilution rate ca. 0.10 hr−1, strain QU 50 produced 42.6 g L−1 of l-LA with a yield of 0.912 g g−1-consumed sugars, LA yield of 0.655 g g−1 based on mixed sugar-loaded, and a productivity of 4.31 g L−1 hr−1 from simulated energy cane hydrolyzate. In OCF with high cell density by cell recycling, simultaneous and complete co-utilization of sugars was achieved with stable LA production at 60.1 ± 3.25 g L−1 with LA yield of 0.944 g g−1-consumed sugar and LA productivity of 6.49 ± 0.357 g L−1 hr−1. Besides this, a dramatic increase in LA yield of 0.927 g g−1 based on mixed sugar-loaded with prolonged operational stability for at least 500 hr (>20 days) was established. This robust system demonstrates an initial green step with a no-carbon loss under energy-saving toward the feasibility of sustainable LA production from lignocellulosic sugars.
AB - In this study, a non-sterile (open) continuous fermentation (OCF) process with no-carbon loss was developed to improve lactic acid (LA) productivity and operational stability from the co-utilization of lignocellulose-derived sugars by thermophilic Enterococcus faecium QU 50. The effects of different sugar mixtures on LA production were firstly investigated in conventional OCF at 50°C, pH 6.5 and a dilution rate of 0.20 hr−1. The xylose consumption ratio was greatly lower than that of glucose in fermentations with glucose/xylose mixtures, indicating apparent carbon catabolite repression (CCR). However, CCR could be efficiently eliminated by feeding solutions containing the cellobiose/xylose mixture. In OCF at a dilution rate ca. 0.10 hr−1, strain QU 50 produced 42.6 g L−1 of l-LA with a yield of 0.912 g g−1-consumed sugars, LA yield of 0.655 g g−1 based on mixed sugar-loaded, and a productivity of 4.31 g L−1 hr−1 from simulated energy cane hydrolyzate. In OCF with high cell density by cell recycling, simultaneous and complete co-utilization of sugars was achieved with stable LA production at 60.1 ± 3.25 g L−1 with LA yield of 0.944 g g−1-consumed sugar and LA productivity of 6.49 ± 0.357 g L−1 hr−1. Besides this, a dramatic increase in LA yield of 0.927 g g−1 based on mixed sugar-loaded with prolonged operational stability for at least 500 hr (>20 days) was established. This robust system demonstrates an initial green step with a no-carbon loss under energy-saving toward the feasibility of sustainable LA production from lignocellulosic sugars.
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U2 - 10.1002/bit.27313
DO - 10.1002/bit.27313
M3 - Article
C2 - 32086810
AN - SCOPUS:85082318360
SN - 0006-3592
VL - 117
SP - 1673
EP - 1683
JO - Biotechnology and Bioengineering
JF - Biotechnology and Bioengineering
IS - 6
ER -