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 | [%] |