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. 2019 Aug 21;7:195. doi: 10.3389/fbioe.2019.00195
a Specific interfacial area [m–1]
c* Maximum solubility in water at equilibrium [mol L–1]
cDO Temperature corrected actual oxygen concentration [mol L–1]
cL* Maximum solubility of oxygen in the broth under prevailing gas-phase composition, temperature, and pressure [mol L–1]
cM* Maximum oxygen solubility in media [mol L–1]
cO2 Actual oxygen concentration in the broth [mol L–1]
D Tank diameter m
di Impeller diameter m
DO Dissolved oxygen [%]
Gin/out Gas flow rate at real conditions in/out of bioreactor [mL min–1]
H Tank height m
kL Mass transfer coefficient [m s–1]
kLa Volumetric oxygen mass transfer coefficient [s–1]
MAPE Mean absolute percentage error [%]
N stirrer speed [s–1 or rpm]
OTR Oxygen transfer rate [mol L–1 d–1]
OUR Oxygen uptake rate [mol L–1 d–1]
pO2 Partial pressure of oxygen [Pa]
Q Gas flow rate [m3 s–1]
qO2 Specific oxygen uptake rate [mol cell–1 day–1]
R Gas constant [J mol–1 K–1]
T Temperature [°C];[K]
TCC Total cell concentration [cells mL–1]
τP Response time [s]
vs Superficial gas velocity [m s–1]
VCC Viable cell concentration [cells mL–1]
VL Volume of the liquid in vessel [m3]
xtarget target value
xi value of sample
n number of samples
X Biomass concentration [g L–1]
yCO2 Molar fraction of CO2 [%]