Abstract
The production of lactic acid from glucose has been demonstrated using a CSTR (continuous stirred-tank reactor) with cell recycle. Studies were conducted withLactobacillus delbrueckii at a fermentation temperature of 42°C and a pH of 6.25. A cell density of 140 g dry weight/L and a volumetric productivity of 150 g/L.h, with complete glucose consumption, were obtained. It was not possible to obtain a lactic acid concentration above 60 g/L because of product inhibition. A cell purge was not necessary to maintain high viability bacteria culture or to obtain a steady state. At steady state the net cell growth appeared to be negligible. The specific glucose consumption for cell maintenance was 0.33 g glucose/g cells-h.
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Abbreviations
- B :
-
Bleed blow/reactor volume (h-1)
- D :
-
Dilution rate (h-1)
- k D :
-
Specific death rate (h-1)
- L :
-
Lactic acid concentration (g/L)
- m :
-
Maintenance coefficient (g/g.h)
- So :
-
Initial glucose concentration (g/L)
- S :
-
Final glucose concentration (g/L)
- t :
-
Time (h)
- μ:
-
Specific growth rate (h-1)
- X :
-
Biomass concentration (g/L)
- Y L/S :
-
Lactic acid yield (g lactic acid produced/g glucose consumed)
- YX/S :
-
Biomass yield (g cells produced/g glucose consumed)
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Ohleyer, E., Blanch, H.W. & Wilke, C.R. Continuous production of lactic acid in a cell recycle reactor. Appl Biochem Biotechnol 11, 317–332 (1985). https://doi.org/10.1007/BF02798444
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DOI: https://doi.org/10.1007/BF02798444
Index Entries
- Lactic acid, production fromLactobacillus delbrueckii
- continuous fermentation, production of lactic acid by
- cross-flow filtration, in continuous lactic acid production
- lactic acid inhibition, during continuous production
- cell concentration during continuous lactic acid production
- broth viscosity, during continuous lactic acid production
- cell recycle, during continuous lactic acid production
- Lactobacillus delbrueckii, continuous production of lactic acid from
- recycle reactor, continuous production of lactic acid in