TY - JOUR
T1 - Economic process to co-produce poly(ε-L-lysine) and poly(L-diaminopropionic acid) by a pH and dissolved oxygen control strategy
AU - Xu, Zhaoxian
AU - Feng, Xiaohai
AU - Sun, Zhuzhen
AU - Cao, Changhong
AU - Li, Sha
AU - Xu, Zheng
AU - Xu, Zongqi
AU - Bo, Fangfang
AU - Xu, Hong
N1 - Publisher Copyright:
© 2015.
PY - 2015/7/1
Y1 - 2015/7/1
N2 - This study tended to apply biorefinery of indigenous microbes to the fermentation of target-product generation through a novel control strategy. A novel strategy for co-producing two valuable homopoly(amino acid)s, poly(ε-l-lysine) (ε-PL) and poly(l-diaminopropionic acid) (PDAP), was developed by controlling pH and dissolved oxygen concentrations in Streptomyces albulus PD-1 fermentation. The production of ε-PL and PDAP got 29.4 and 9.6g L-1, respectively, via fed-batch cultivation in a 5L bioreactor. What is more, the highest production yield (21.8%) of similar production systems was achieved by using this novel strategy. To consider the economic-feasibility, large-scale production in a 1t fermentor was also implemented, which would increase the gross profit of 54,243.5 USD from one fed-batch bioprocess. This type of fermentation, which produces multiple commercial products from a unified process is attractive, because it will improve the utilization rate of raw materials, enhance production value and enrich product variety.
AB - This study tended to apply biorefinery of indigenous microbes to the fermentation of target-product generation through a novel control strategy. A novel strategy for co-producing two valuable homopoly(amino acid)s, poly(ε-l-lysine) (ε-PL) and poly(l-diaminopropionic acid) (PDAP), was developed by controlling pH and dissolved oxygen concentrations in Streptomyces albulus PD-1 fermentation. The production of ε-PL and PDAP got 29.4 and 9.6g L-1, respectively, via fed-batch cultivation in a 5L bioreactor. What is more, the highest production yield (21.8%) of similar production systems was achieved by using this novel strategy. To consider the economic-feasibility, large-scale production in a 1t fermentor was also implemented, which would increase the gross profit of 54,243.5 USD from one fed-batch bioprocess. This type of fermentation, which produces multiple commercial products from a unified process is attractive, because it will improve the utilization rate of raw materials, enhance production value and enrich product variety.
KW - Co-production
KW - Dissolved oxygen
KW - PH
KW - Poly(L-diaminopropionic acid)
KW - Poly(ε-L-lysine)
UR - http://www.scopus.com/inward/record.url?scp=84936936543&partnerID=8YFLogxK
U2 - 10.1016/j.biortech.2015.03.101
DO - 10.1016/j.biortech.2015.03.101
M3 - 文章
C2 - 25841184
AN - SCOPUS:84936936543
SN - 0960-8524
VL - 187
SP - 70
EP - 76
JO - Bioresource Technology
JF - Bioresource Technology
ER -