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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.