TY - JOUR
T1 - Kinetic analysis and pH-shift control strategy for propionic acid production with propionibacterium freudenreichii CCTCC M207015
AU - Feng, Xiaohai
AU - Xu, Hong
AU - Yao, Jun
AU - Li, Sha
AU - Zhu, Hongyang
AU - Ouyang, Pingkai
PY - 2010
Y1 - 2010
N2 - The production of propionic acid by Propionibacterium freudenreichii CCTCC M207015 was investigated in a 7.5-l stirred-tank fermentor. Batch fermentations by P. freudenreichii CCTCC M207015 at various pH values ranging from 5.5 to 7.0 were studied. Based on the analysis of the time course of specific cell growth rate (μx) and specific propionic acid formation rate (μp), a two-stage pH-shift control strategy was proposed. At first 48 h, pH was controlled at 6.5 to obtain the maximal μx, subsequently pH 6.0 was used to maintain high μp to enhance the production of propionic acid. By applying this pH-shift control strategy in propionic acid fermentation, the maximal propionic acid and glucose conversion efficiency had a significant improvement and reached 19.21 g/l and 48.03%, respectively, compared with those of constant pH operation (14.58 g/l and 36.45%). Fed-batch fermentation with pH-shift control strategy was also applied to produce propionic acid; the maximal propionic acid yield and glucose conversion efficiency reached 25.23 g/l and 47.76%, respectively.
AB - The production of propionic acid by Propionibacterium freudenreichii CCTCC M207015 was investigated in a 7.5-l stirred-tank fermentor. Batch fermentations by P. freudenreichii CCTCC M207015 at various pH values ranging from 5.5 to 7.0 were studied. Based on the analysis of the time course of specific cell growth rate (μx) and specific propionic acid formation rate (μp), a two-stage pH-shift control strategy was proposed. At first 48 h, pH was controlled at 6.5 to obtain the maximal μx, subsequently pH 6.0 was used to maintain high μp to enhance the production of propionic acid. By applying this pH-shift control strategy in propionic acid fermentation, the maximal propionic acid and glucose conversion efficiency had a significant improvement and reached 19.21 g/l and 48.03%, respectively, compared with those of constant pH operation (14.58 g/l and 36.45%). Fed-batch fermentation with pH-shift control strategy was also applied to produce propionic acid; the maximal propionic acid yield and glucose conversion efficiency reached 25.23 g/l and 47.76%, respectively.
KW - Fed-batch fermentation
KW - Kinetic analysis
KW - PH-Shift Control Strategy
KW - Propionibacterium freudenreichii CCTCC M207015
KW - Propionic acid
UR - http://www.scopus.com/inward/record.url?scp=77949295180&partnerID=8YFLogxK
U2 - 10.1007/s12010-008-8300-6
DO - 10.1007/s12010-008-8300-6
M3 - 文章
C2 - 18626579
AN - SCOPUS:77949295180
SN - 0273-2289
VL - 160
SP - 343
EP - 349
JO - Applied Biochemistry and Biotechnology
JF - Applied Biochemistry and Biotechnology
IS - 2
ER -