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(Referência obtida automaticamente do Web of Science, por meio da informação sobre o financiamento pela FAPESP e o número do processo correspondente, incluída na publicação pelos autores.)

Separation and Semi-Empiric Modeling of Ethanol-Water Solutions by Pervaporation Using PDMS Membrane

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Autor(es):
Bermudez Jaimes, John Hervin [1] ; Torres Alvarez, Mario Eusebio [1] ; Bannwart de Moraes, Elenise [1] ; Wolf Maciel, Maria Regina [1] ; Maciel Filho, Rubens [1]
Número total de Autores: 5
Afiliação do(s) autor(es):
[1] Univ Estadual Campinas, Sch Chem Engn, Separat Proc Dev Lab, Albert Einstein 500, BR-13083582 Campinas - Brazil
Número total de Afiliações: 1
Tipo de documento: Artigo Científico
Fonte: POLYMERS; v. 13, n. 1 JAN 2021.
Citações Web of Science: 0
Resumo

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 degrees 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. (AU)

Processo FAPESP: 15/20630-4 - Desenvolvimento integrado de biorrefinaria e planta de bioetanol de cana-de-açúcar com emissão zero de CO2: rotas para converter recursos renováveis em bioprodutos e bioeletricidade
Beneficiário:Rubens Maciel Filho
Modalidade de apoio: Auxílio à Pesquisa - Temático