Abstract
Four systems comprising of an ethanol fermentation integrated with microfiltration and/or pervaporation, and a conventional continuous culture, were compared with respect to the performance of the fermentation and economics. The processes are compared on the basis of the same kinetic model. It is found that cell retention by microfiltration leads to lower production costs, compared to a conventional continuous culture. Pervaporation becomes profitable at a high selectivity of ethanol/water separation and low membrane prices.
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Abbreviations
- A m2 :
-
area
- C kg m−3 :
-
concentration
- C s0 kg m−3 :
-
feed substrate concentration, i.e. substrate conversion
- C′ pp kg m−3 :
-
concentration of ethanol in pervaporate in configuration V
- d m:
-
diameter
- D h−1 :
-
dilution rate
- F kg h−1 :
-
flow rate
- F prod kg h−1 :
-
capacity of the plant
- f :
-
fraction of ethanol removed from recirculation stream
- J m3 m−2 h−1 :
-
membrane flux
- m s kg kg−1 h−1 :
-
maintenance coefficient
- Q PV kJ h−1 :
-
heat required for pervaporation
- r kg m−3 h−1 :
-
production or consumption rate
- S :
-
selectivity
- T °C:
-
temperature
- U Wm−2 °C−1 :
-
overall heat transfer coefficient
- V m3 :
-
volume
- x :
-
mass fraction
- Y sp kg kg−1 :
-
yield of product on substrate
- Y sx kg kg−1 :
-
yield of biomass on substrate
- μ h−1 :
-
specific growth rate
- ϱ kg m−3 :
-
density
- ac :
-
acetic acid
- c :
-
recirculation stream
- C.B.:
-
cell bleed
- cond (C):
-
condensor
- dist :
-
distillation column
- F :
-
feed
- HE :
-
heat exchanger
- in (0):
-
inlet
- m :
-
medium (filtrate)
- M.B.:
-
medium bleed
- max:
-
maximal
- MF :
-
microfiltration
- p :
-
product
- pp :
-
product in pervaporate
- PV :
-
pervaporation
- R.F. :
-
recirculation flow
- s :
-
substrate
- VP :
-
vacuum pump
- x :
-
biomass
- w :
-
water
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Groot, W.J., Kraayenbrink, M.R., van der Lans, R.G.J.M. et al. Ethanol production in an integrated fermentation/membrane system. Process simulations and economics. Bioprocess Engineering 8, 189–201 (1993). https://doi.org/10.1007/BF00369829
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DOI: https://doi.org/10.1007/BF00369829