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|Type:||Artigo de periódico|
|Title:||Bioethanol production optimization: A thermodynamic analysis|
|Abstract:||In this work, the phase equilibrium of binary mixtures for bioethanol production by continuous extractive process was studied. The process is composed of four interlinked units: fermentor, centrifuge, cell treatment unit, and flash vessel (ethanol-congener separation unit). A proposal for modeling the vapor-liquid equilibrium in binary mixtures found in the flash vessel has been considered. This approach uses the Predictive Soave-Redlich-Kwong equation of state, with original and modified molecular parameters. The congeners considered were acetic acid, acetaldehyde, furfural, methanol, and 1-pentanol. The results show that the introduction of new molecular parameters r and q in the UNIFAC model gives more accurate predictions for the concentration of the congener in the gas phase for binary and ternary systems.|
|Editor:||Humana Press Inc|
|Citation:||Applied Biochemistry And Biotechnology. Humana Press Inc, v. 148, n. 41699, n. 141, n. 149, 2008.|
|Appears in Collections:||Unicamp - Artigos e Outros Documentos|
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