Summary
The capability of the continuous tower fermenter to accumulate and retain high cell densities (70–90 g dry wt/1) when using naturally flocculant yeasts is demonstrated with semi-defined glucose feed at concentrations of 120–200 g/1 and high hydraulic loadings. Conversion and ethanol productivity data are given as a function of throughput and feed glucose concentration.
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References
Cysewski, G.R. and Wilke, C.R. (1976) Biotechnol. & Bioeng., 18, 1297.
Denny, S.C.T. (1976) J. Inst. Brew., 82, 255.
Greenshields, R.N. and Smith, E.L. (1971) The Chem. Engr.249, 182
Greenshields, R.N. and Smith, E.L. (1974) Process Biochem., 9 (3) 11.
Klopper, W.J. et al. (1965) Proc. 10th Eur. Brew. Conv., Stockholm.
Royston, M.G. (1966) Process Biochem., 1 (4) 215.
Smith, J.B. (1977) The Brewer, 63, 50.
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Prince, I.G., Barford, J.P. Continuous tower fermentation for power ethanol production. Biotechnol Lett 4, 263–268 (1982). https://doi.org/10.1007/BF00132398
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DOI: https://doi.org/10.1007/BF00132398