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Table 1 Start data of the unknown state variables in the model

From: A non-linear model of hydrogen production by Caldicellulosiruptor saccharolyticus for diauxic-like consumption of lignocellulosic sugar mixtures

State variable

Description

Case 1

Glucose fermentation

Case 2

Xylose fermentation

Case 3

Sugar mix fermentation

Case 4

Wheat straw hydrolysate fermentation

Unit

Glu

Glucose concentration

0.40

0.28

0.26

cmol/L

Xyl

Xylose concentration

0.36

0.10

0.11

cmol/L

Ara

Arabinose concentration

0.012

0.014

cmol/L

X (Biomass)

Biomass concentration

0.0013

0.00071

0.0016

0.0058

cmol/L

Ac

Acetate concentration

0.0012

0

0.0039

0.021

cmol/L

H2,aq

H2 concentration (liquid phase)

0

0

0

0

M

CO2,aq

CO2 concentration (liquid phase)

0

0

0

0

cmol/L

CO2,sol

Concentration of all CO2 ionic species (HCO3− and CO 23 −)

0

0

0

0

cmol/L

H2,g

H2 concentration (gas phase)

0

0

0

0

M

CO2,g

CO2 concentration (gas phase)

0

0

0

0

cmol/L

E2

Enzyme concentration

1e−7

1e−7

cmol/L