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Table 3 State variables initial values and simulation setup parameters

From: A novel process-based model of microbial growth: self-inhibition in Saccharomyces cerevisiae aerobic fed-batch cultures

Symbol Description Unit LBG H 1022a CBS 8066b CEN.PK113-7Dc CEN.PK2-1Cd
G 0 Glucose initial value g 9 0 20 20
E 0 Ethanol initial value g 0.1 0 0 0
P 0 Glycolysis products initial value g 5 × 10−5 5 × 10−5 5 × 10−5 5 × 10−5
C M0 Carbon metabolites initial value g 0.1 7 0.023 0.022
I 0 Inhibitor initial value g 0 0 0 0
R 0 Reserve compounds initial value g 0 0 0 0
D 0 Dead cells initial value g 0 0 0 0
t 0 Time of simulation start h 3 0 0 0
t F Time of feeding start h 3.2 17 15
t END Time of simulation end h 21 13 49 31; 40; 48
c F Glucose concentration in feeding solution g l−1 100 500 500
M F Cell mass at beginning of feeding g 3.66 3.66 4.52; 4.14; 4.14
μ Feeding rate h−1 0.3 0.16 0.1; 0.16; 0.2
y R Maximum biomass yield on glucose 0.1 0.5 0.5
  1. avon Meyenburg [53]; Fig. 2.
  2. bPham et al. [12]; Fig. 3.
  3. cFigure 4.
  4. dFigures 5, 6 and 7.