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1969
DOI: 10.1002/j.2050-0416.1969.tb03211.x
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Biological and Biochemical Aspects of Tower Fermentation*

Abstract: Biological and biochemical aspects of continuous fermentation in a Tower fermentor operated on a commercial scale are described with particular reference to the rate of utilization of α‐amino nitrogen and carbohydrate. Under stable conditions, well defined gradients exist in the Tower fermentor and a fully fermented beer, indistinguishable from the conventional batch beer, is produced. Breakdown of these gradients leads to unstable conditions with a resultant increase in effluent gravity. Yeast growth in the T… Show more

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Cited by 41 publications
(7 citation statements)
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“…The observations during laboratory scale experiments reported approximately 50% mutated cells after nine months of continuous cultivation with a deleterious effect on beer flavour 92 . Conversely, no mutation of the yeast was observed in other industrial scale continuous beer fermenters operating over several months 2,6 . Given that there was no clear evidence of mutation in continuous fermentation systems, it can be speculated that mutations are either strain specific and/or the majority of the mutations do not provide any advantage.…”
Section: Mutation Of Yeast In Continuous Culturesmentioning
confidence: 88%
See 1 more Smart Citation
“…The observations during laboratory scale experiments reported approximately 50% mutated cells after nine months of continuous cultivation with a deleterious effect on beer flavour 92 . Conversely, no mutation of the yeast was observed in other industrial scale continuous beer fermenters operating over several months 2,6 . Given that there was no clear evidence of mutation in continuous fermentation systems, it can be speculated that mutations are either strain specific and/or the majority of the mutations do not provide any advantage.…”
Section: Mutation Of Yeast In Continuous Culturesmentioning
confidence: 88%
“…The main fermentation has encountered problems of different origin such as engineering (carrier choice, reactor design, production inflexibility), microbial (upstream hygiene, long-term process asepticity), physiological (immobilization induced metabolic shifts, yeast mutation, aging) and economic (carrier cost, costs for skilled supervision) 2,45,59,92,112,113,120 . It is clear, that some of the problems were met in one system, but not in others.…”
Section: Introductionmentioning
confidence: 99%
“…The bioreactor had a high-aspect-ratio (beer depth divided by the inner diameter) of around 8:1, which is based on the APV tower fermentor that was used to produce lager and ale beer in the 1960s [30,31,38,39]. The inlet tube had an inner radius of 1 mm and a length of 18 mm; the outlet tube had an inner radius of 2 mm and a length of 25 mm; both contained barbs to facilitate the attachment of the silicone tubing.…”
Section: Mini Tower Fermentor Design and Constructionmentioning
confidence: 99%
“…Diacetyl concentrations can be decreased by increased fermentation/maturation temperature ('diacetyl rest'), a technique used in brewing, which accelerates the conversion of α-acetolactate to acetoin in green beer (34) or by using commercial enzymes that perform the same conversion (1). Accordingly, in the commercial, continuous Tower process, effluent beers had diacetyl concentration which was from 56 to 1350% higher than comparable batch beers, although the diacetyl concentration in both beers decreased to similar values after 14 days in cask (69). In maturation processes using immobilised yeast cells, it is common for a heat treatment (80°C) to be used, with α-acetolactate converted outside the yeast cell to diacetyl followed by diacetyl reduction to acetoin by immobilised yeast.…”
Section: Immobilisation and The Production Of Flavour Compoundsmentioning
confidence: 93%