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Abbreviations
- ĀP :
-
mean interfacial area between dispersed ans continuous phase per unit volume of dispersion, cm−1
- ā:
-
mean surface area occupied per cell on oil droplet, cm2
- Di :
-
agitator diameter, cm
- dC :
-
Sauter mean diameter of cells, cm
- dP :
-
Sauter mean diameter of oil droplets, cm
- dPO :
-
Sauter mean diameter of oil droplets in oil-basal salt solution, cm
- d* :
-
dP · dd 1
- d *o :
-
dPO · dd 1
- H:
-
liquid depth in fermentor vessel, cm
- KS :
-
saturation constant for growth kinetic model, g · l−1 in Eq. (1), g · g−1 in Eq. (12)
- kLα:
-
volumetric oxygen transfer coefficient for liquid phase, h−1
- N:
-
agitation speed, rps or rpm
- NWe :
-
Weber number=N2 · D 3i · ρ aq · σ −1
- nP :
-
number of oil droplets per unit volume (cm−3) of dispersion,
- Pg :
-
agitator power consumption in gassed fermentor, hp
- QO2 :
-
oxygen uptake rate, (mole O2) · (g cell)−1 · h−1
- Q′O2 :
-
(oxygen uptake rate) — (endogenous respiration rate), (mole O2) · (g cell)−1 · h−1
- S:
-
concentration of oil in medium, g · l−1
- S*:
-
concentration of accommodated oil in medium, g · l−1
- T:
-
diameter of reactor, cm
- t:
-
growth time, h
- V:
-
working volume of reactor, m3
- X:
-
cell concentration, g · l−1
- μ:
-
specific growth rate, h−1
- μ max :
-
maximum specific growth rate, h−1
- ρ:
-
density of continuous phase, g · cm−3
- ρ aq :
-
density of aqueous phase, g · cm−3
- ρ o :
-
density of oil phase, g · cm−3
- σ:
-
interfacial tension, dyne · cm−1
- φ:
-
volume fraction of oil in medium
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© 1978 Springer-Verlag
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Miura, Y. (1978). Mechanism of liquid hydrocarbon uptake by microorganisms and growth kinetics. In: Advances in Biochemical Engineering, Volume 9. Advances in Biochemical Engineering, vol 9. Springer, Berlin, Heidelberg. https://doi.org/10.1007/BFb0048090
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DOI: https://doi.org/10.1007/BFb0048090
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