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• W3114601236 endingPage "93" @default.
• W3114601236 startingPage "93" @default.
• W3114601236 abstract "High energy demand, competitive fuel prices and the need for environmentally friendly processes have led to the constant development of the alcohol industry. Pervaporation is seen as a separation process, with low energy consumption, which has a high potential for application in the fermentation and dehydration of ethanol. This work presents the experimental ethanol recovery by pervaporation and the semi-empirical model of partial fluxes. Total permeate fluxes between 15.6–68.6 mol m−2 h−1 (289–1565 g m−2 h−1), separation factor between 3.4–6.4 and ethanol molar fraction between 16–171 mM (4–35 wt%) were obtained using ethanol feed concentrations between 4–37 mM (1–9 wt%), temperature between 34–50 ∘C and commercial polydimethylsiloxane (PDMS) membrane. From the experimental data a semi-empirical model describing the behavior of partial-permeate fluxes was developed considering the effect of both the temperature and the composition of the feed, and the behavior of the apparent activation energy. Therefore, the model obtained shows a modified Arrhenius-type behavior that calculates with high precision the partial-permeate fluxes. Furthermore, the versatility of the model was demonstrated in process such as ethanol recovery and both ethanol and butanol dehydration." @default.
• W3114601236 created "2021-01-05" @default.
• W3114601236 creator A5040143816 @default.
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• W3114601236 creator A5089124662 @default.
• W3114601236 date "2020-12-29" @default.
• W3114601236 modified "2023-10-14" @default.
• W3114601236 title "Separation and Semi-Empiric Modeling of Ethanol–Water Solutions by Pervaporation Using PDMS Membrane" @default.
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• W3114601236 doi "https://doi.org/10.3390/polym13010093" @default.
• W3114601236 hasPubMedCentralId "https://www.ncbi.nlm.nih.gov/pmc/articles/7795344" @default.
• W3114601236 hasPubMedId "https://pubmed.ncbi.nlm.nih.gov/33383641" @default.
• W3114601236 hasPublicationYear "2020" @default.
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