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Mathematical modeling of production of microbial lipids

Part I: Kinetics of biomass growth

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Abstract

As a part of the investigations on the microbial lipid production using the yeast Rhodotorula gracilis, CFR-1, kinetics of the biomass synthesis has been studied using shake flask experiments. Using a medium containing a carbon to nitrogen ratio of 70∶1, the rates of biomass production were followed at different initial substrate concentrations in the range of 20–100 kg/m3. A logistic model was found to be reasonably adequate to describe the kinetics of the growth of biomass; the maximum specific growth rate of 0.105 h−1 was applicable for substrate concentrations less than 60 kg/m3, which gave reasonable agreement between predicted and actual biomass concentration values.

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Abbreviations

S 0, X 0 kg/m3 :

Initial concentrations of sugar, non lipid biomass respectively

X, X(t) kg/m3 :

Concentrations of non lipid biomass at any time t

dX/dt kg/(m3 · h):

Rate of biomass growth

μ h−1 :

Specific growth rate

μ max h−1 :

Maximum specific growth rate

K s mol/dm3 :

Monods constant

X max kg/m3 :

Maximum biomass reached in a run

References

  1. Woodbine, M.: Microbial fat: Microorganisms as potential fat producers. Prog. Ind. Microbiol. 1 (1959) 179–245

    Google Scholar 

  2. Sattur, A. P.; Karanth, N. G.: Production of Microbial lipids — A review. J Microbial Biotechnol. 3 (1988) 51–63

    Google Scholar 

  3. Ratledge, C.: Microbial oils and fats: An assessment of their commercial potential. Prog. Ind. Microbiol. 16 (1984) 119–245

    Google Scholar 

  4. Brown, D. B.; and Hsu, K.: Kinetic modeling of lipid accumulation in Candida curvata R. Proc. 12 Ann. Biochem. Engg. Symp. Kansas State University (1982) 1–7

  5. Brown, D. B. Ph. D. Thesis, Iowa State University (1984)

  6. Ykema, A.; Verbree, E. C.; Van Versevald, H. W.; Smit, H.: Mathematical modelling of lipid production by oleaginous yeast in continuous cultures. Antonie van Leeuewenhoek. 52 (1986) 491–506

    Google Scholar 

  7. Weiss, R. M.; Ollis, D. F.: Extracellular microbial polysaccharide. I. Substrate, biomass and product kinetic equations for batch xanthan gum fermentation. Biotechnol. Bioeng. 22 (1980) 859–873

    Google Scholar 

  8. Constantinides, A.; Spencer, J. L.; Gaden, Jr., E. L.: Optimisation of batch fermentation processes. I. Development of mathematical models for batch penicillin fermentations. Biotechnol. Bioengg. 12 (1970) 803–830

    Google Scholar 

  9. Edwards, V. H.; Wilke, C. R.: Mathematical representation of batch culture data. Biotechnol. Bioengg. 10 (1968) 205–232

    Google Scholar 

  10. Kono, T.: Kinetics of microbial cell growth. Biotechnol. Bioengg. 10 (1968) 105–131

    Google Scholar 

  11. Kono, T.; Asai, T.: Kinetics of fermentation processes. Biotechnol. Bioeng. 11 (1969) 294–320

    Google Scholar 

  12. Miller, G. L.: Use of dinitrosalicylic acid reagent for the determination of reducing sugars. Anal. Chem. 31 (1959) 426–428

    Google Scholar 

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Karanth, N.G., Sattur, A.P. Mathematical modeling of production of microbial lipids. Bioprocess Engineering 6, 227–234 (1991). https://doi.org/10.1007/BF00369716

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  • DOI: https://doi.org/10.1007/BF00369716

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