Abstract
A simple mathematical model for the interaction of mass transport with biochemical reaction in solid state fermentations (SSF) in static tray type bioreactors under isothermal conditions has been developed. The analysis has enabled scientific explanations to a number of practical observations, through the concept of critical substrate bed thickness. The model will be most useful in the prediction of the concentration gradients as also in efficient design of these bioreactors.
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Abbreviations
- C g/cm3 :
-
Oxygen concentration in the bed
- C g g/cm3 :
-
Atmospheric oxygen concentration
- C * :
-
Dimensionless oxygen concentration, C/C g
- D e cm2/h:
-
Effective diffusivity
- H cm:
-
Bed thickness or height
- H c cm:
-
Critical bed thickness or height
- H m cm:
-
Maximum height of zone of zero oxygen concentration
- p i mg/(g · h):
-
Productivity (Eq. 13)
- R g/(cm3 · h):
-
Biochemical reaction rate
- t h:
-
Fermentation time
- t * :
-
Dimensionless time, D e t/H2
- X mg/cm3 :
-
Biomass concentration
- X max mg/cm3 :
-
Maximum biomass concentration
- y :
-
Dimensionless thickness or height, (y = z/H)
- y′ cm:
-
Thickness of zone of zero oxygen concentration (Eq. 12)
- Y \(\frac{{{\text{g biomass}}}}{{{\text{g oxygen}}}}\) :
-
Yield coefficient
- z cm:
-
Bed thickness or height along tray axis
- ɛ:
-
Bed void fraction
- μmax h−1 :
-
Specific growth rate
- φ :
-
Thiele modulus \(\sqrt {\frac{{H^2 R}}{{D_e C_g Y}}} \)
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Raghava Rao, K.S.M.S., Gowthaman, M.K., Ghildyal, N.P. et al. A mathematical model for solid state fermentation in tray bioreactors. Bioprocess Engineering 8, 255–262 (1993). https://doi.org/10.1007/BF00369838
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DOI: https://doi.org/10.1007/BF00369838