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1.
Electron. j. biotechnol ; Electron. j. biotechnol;48: 46-52, nov. 2020. graf, tab
Article de Anglais | LILACS | ID: biblio-1254708

RÉSUMÉ

BACKGROUND: Fructose and single cell protein are important products for the food market. Abundant amounts of low-grade dates worldwide are annually wasted. In this study, highly concentrated fructose syrups and single cell protein were obtained through selective fermentation of date extracts by Saccharomyces cerevisiae. RESULTS: The effect of air flow (0.1, 0.5, 0.75, 1, 1.25 and 1.5 vvm) and pH (4.5, 4.8, 5, 5.3 and 5.6) was investigated. Higher air flow led to lower fructose yield. The optimum cell mass production of 10 g/L was achieved at air flow of 1.25 vvm with the fructose yield of 91%. Similar cell mass production was obtained in the range pH of 5.0­5.6, while less cell mass was obtained at pH less than 5. Controlling the pH at 4.5, 5.0 and 5.3 failed to improve the production of cell mass which were 5.6, 5.9 and 5.4 g/L respectively; however, better fructose yield was obtained. CONCLUSIONS: Extension of the modified Gompertz enabled excellent predictions of the cell mass, fructose production and fructose fraction. The proposed model was also successfully validated against data from literatures. Thus, the model will be useful for wide application of biological processes.


Sujet(s)
Saccharomyces cerevisiae/physiologie , Phoeniceae , Fructose/biosynthèse , Aérobiose , Concepts mathématiques , Fermentation , Ordures ménagères , Concentration en ions d'hydrogène
2.
Electron. j. biotechnol ; Electron. j. biotechnol;34: 1-8, july. 2018. tab, graf
Article de Anglais | LILACS | ID: biblio-1026812

RÉSUMÉ

Background: Ethanol and fructose are two important industrial products that enjoy many uses. In this contribution, their production via selective fermentation of date extract using Saccharomyces cerevisiae was studied. Scaling up the process for possible commercialization was investigated in three fermentors with working volume ratio of 1:40:400. Results: Higher ethanol concentration was obtained in the larger fermentor due to conversion of fructose. Fructose yields in the 0.5-L, 7.5-L and 80-L fermentors were 99, 92 and 90%, respectively. Good fitting was obtained with the modified Monod kinetics; however, a better fit of cell mass was obtained with the modified Ghose­Tyagi model which accounts for ethanol inhibition. Conclusions: The modified Gompertz model was expanded to facilitate prediction of products' formation and fructose fractions in all three fermentors. Such expansion will be beneficial in industrial applications.


Sujet(s)
Saccharomyces cerevisiae/métabolisme , Éthanol/synthèse chimique , Fructose/biosynthèse , Levures , Cinétique , Bioréacteurs , Fermentation
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