Fig. 5From: Metabolic modeling of synthesis gas fermentation in bubble column reactorsEffect of the CO gas–liquid mass transfer coefficient k m,C on steady-state concentrations in the exiting liquid and gas streams. The H2 and CO2 mass transfer coefficients were set to be 2.5k m,C and k m,C , respectively. The dashed lines indicate the nominal k m,C value used in the other simulationsBack to article page