MODELLING AND PARAMETER IDENTIFICATION OF BATCH FERMENTATION PROCESS

Author(s):  
A. Nakrachi ◽  
R. Laurent
2013 ◽  
Vol 06 (06) ◽  
pp. 1350044
Author(s):  
YAN WANG ◽  
XIAOHONG LI ◽  
ENMIN FENG ◽  
ZHILONG XIU

Based on 1,3-propanediol production from batch fermentation of glycerol by Klebsiella pneumoniae, a multistage dynamic system and its parameter identification are discussed in this paper. The batch fermentation process is divided into three stages exhibiting different dynamic behaviors and characteristics, from which a corresponding nonlinear multistage dynamic system is built. We then propose a parameter identification optimization model whose objective function is the average relative error. The model is solved by particle swarm optimization weighted by inertia, and the result shows that the relative error of our proposed model is 2–10% smaller than those of existing models.


2021 ◽  
Vol 26 (2) ◽  
pp. 2464-2470
Author(s):  
ANCA-IRINA GALACTION ◽  
◽  
ALEXANDRA CRISTINA BLAGA ◽  
ALEXANDRA TUCALIUC ◽  
LENUŢA KLOETZER ◽  
...  

The previous studies on ergosterol production by Saccharomyces cerevisiae in presence of n-dodecane as oxygen-vector have been continued by mathematical modelling the fermentation process. In this purpose, the most efficient fermentation regime has been considered, namely fed-batch fermentation, and was based on the influences of hydrocarbon volumetric fraction, biomass concentration, and aeration rate on the ergosterol content inside the yeast cells. The model describing the fermentation process has been established by means of the statistical analysis, using a factorial experiment of second order. The considered variables control the ergosterol production in a 94.4% extent, the biomass concentration exhibiting the most important influence.


2008 ◽  
Vol 8 (12) ◽  
pp. 2272-2278 ◽  
Author(s):  
Kouame Kan Benjamin ◽  
Assidjo N. Emmanue ◽  
Akaki David ◽  
Yao K. Benjamin

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