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The effects of fermentation conditions on yeast cell debris particle size distribution during high pressure homogenisation

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Abstract

Experiments were performed to characterize the particle size distribution of bakers' yeast cells during high pressure homogenisation. Results were obtained for mechanically agitated batch and continuously grown cultures under a range of operating conditions. It was found that the dependency of cell debris size distribution on the number of passes through the homogeniser and the homogeniser pressure was independent of the cell properties and culture conditions, but for a fixed pressure and number of passes the extent of disruption was strongly affected by the operating conditions in the fermenter. The entire cell debris size distributions were successfully simulated using the mean and variance of the distributions and a previously published model equation which related these parameters to the operating pressure and number of passes through the homogeniser.

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Abbreviations

k :

breakage coefficient in Eq. 1

d :

cell diameter

d 50 :

median diameter of homogenate size distribution

d 50 :

dimensionless d 50 defined as \(\frac{{d_{50_{N = 0} } - d_{50} }}{{d_{50_{N = 0} } }}\)

D :

dilution rate

F(d NP):

cumulative undersize distribution (volume basis)

N :

number of passes

P :

total pressure

P threshold :

threshold pressure

ΔP :

(P-P threshold)

w :

Boltzmann parameter, Eq. 4

w :

dimensionless standard deviation defined as \(w^ \star = \frac{{w_{N = 0} - w}}{{w_{N = 0} }}\)

α :

exponent in Eq. 1

β :

exponent in Eq. 1

References

  1. Hetherington, P. J.; Follows, M.; Dunnill, P.; Lilly, M. D.: 1971, Release of protein from Baker's yeast (Saccharomyces cerevisiae) by disruption in an industrial homogeniser, Trans. Instn Chem. Engrs, 49, 142–148

    Google Scholar 

  2. Lilly, M. D.: 1979, Production of intracellular microbial enzymes. Appl. Biochemistry and Bioengineering, 2, 1–269

    Google Scholar 

  3. Engler, C. R.: 1985, Disruption of microbial cells, in Comprehensive Biotechnology, Vol. 2, Moo-Young, M. and Cooney, C. L., (Eds), Chap. 20, Pergamon, Oxford, 305–324

    Google Scholar 

  4. Ayazi Shamlou, P.; Siddiqi, S. F.; Titchener-Hooker, N.: A Physical model of high pressure disruption of bakers' yeast cells, Chem. Engng Sci., 50, pp 1383–1391, 1995

    Google Scholar 

  5. Siddiqi, S.F.; Titchener-Hooker, N.: Simulation of changes occurring in the size distribution of cell debris during homogenisation, IChemE Anual Research Event, 1, 55–56, 1994

    Google Scholar 

  6. Middelberg, A.P.J.; O'Neill, B.K.; Bogle, I.D.L.: 1992a. A new model for the distribution of Escherichia coli by high pressure homogenisation, Part I. Model development and verification, Trans. IChemE., 70, Part C (Dec.), 205–212

    Google Scholar 

  7. Middelberg, A.P.J.; O'Neill, B.K.; Bogle, I.D.L.; Gully, N.J.; Rogers, A.H.; Thomas, C.J.: 1992b, A new model for the distribution of Escherichia coli by high pressure homogenisation, Part II. A correlation for the effective cell strength, Trans. IChem E., 70, Part C (Dec.) 212–218

    Google Scholar 

  8. Siddiqi, S.F.; Titchener-Hooker, N.J.; Ayazi Shamlou P: The operating conditions on the generation of cell debris in high-pressure homogenisation of baker's yeast, Biotech. Bioengng, (submitted)

  9. Gregory, M.; Bulmer, M.; Thornhill, N.F.; Titchener-Hooker, N.: Enzyme contents of bakers' yeast grown in continuous culture: Data for novel process design, to be submitted to Bioprocess Engng

  10. Dehghani, M.; Bulmer, M.; Gregory, M.; Thornhill, N.F.; Ison, A.P.: Correlation of intracellular enzyme activities with CO2 exit gas profiles in batch are repeated batch cultures of S. cerevisiae, J. Biotechnology (submitted)

  11. Fiechter, A.; Kappeli, O.; Meussdoerffer, F.: “Batch and continuous”culture, in The Yeasts, Rose, A.H. and Harrison, J.S. (Eds), Vol. 2. 2nd Ed., Ch. 5, p 108, Academic Press, Lon., 1987

    Google Scholar 

  12. Ayazi Shamlou, P.; Stavrinides, S.; Titchener-Hooker, N.; Hoare, M.: Growth-independent breakage frequency of protein precipitates in turbulently agitated bioreactors, Chem Engng Sci., 49, 2647–2656, 1994

    Google Scholar 

  13. Virkar, P.D.; Hoare, M.; Chan, M.Y.Y.; Dunnill, P.: Kinetics of the acid precipitation of soya protein in a continuous-flow tubular reactor. Biotech. Bioengng., XXIV, 871–887, 1982

    Google Scholar 

  14. Karuhn, R.F.; Berg, R.M.; The electrical sensing zone technique for particle size measurement, Particle Data Labs Ltd., Elmhurst, IL, 1982

    Google Scholar 

  15. Keshavarz-Moore, E.; Hoare, M.; Dunnill, P.: 1990, Disruption of Baker's yeast in a high pressure homogeniser: New evidence on mechanisms, Enzyme Microb. Technol., 12, 764–770

    Google Scholar 

  16. Keshavarz-Moore, E.; Hoare, M.; Dunnill, P.: 1987 Biochemical engineering aspects of cell disruption, in Separations for Biotechnology, Verral, M.S. and Hudson, M.J. (Eds.), Chap. 3, Ellis Horwood, Chichester, 62–79

    Google Scholar 

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UCL is the Biotechnology and Biological Sciences Research Council's Interdisciplinary Research Centre for Biochemical Engineering and the Council's support to the participating UCL departments is gratefully acknowledged. The provision of continuous fermentation material from Dr. M. Gregory, Process System Engineering IRC, is gratefully acknowledged.

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Siddiqi, S.F., Bulmer, M., Ayazi Shamlou, P. et al. The effects of fermentation conditions on yeast cell debris particle size distribution during high pressure homogenisation. Bioprocess Engineering 14, 1–8 (1995). https://doi.org/10.1007/BF00369846

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