Finding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production

dc.creatorDurruty, Gisela N.
dc.creatorDiaz, M. Soledad
dc.creatorHoch, Patricia
dc.date2014-09
dc.date2014
dc.date2014-10-28T15:07:32Z
dc.identifierhttp://sedici.unlp.edu.ar/handle/10915/41998
dc.identifierhttp://43jaiio.sadio.org.ar/proceedings/SII/16_Durruty%20et%20al..pdf
dc.identifierissn:2313-9102
dc.descriptionA model for a reactive distillation column for ETBE production was devel-oped using both a rigorous thermodynamic model (UNIFAC) and hydraulic constrains. The thermodynamic model included an activity coefficient approach for the liquid phase, UNIFAC, and ideal gas approximation for the vapor phase. The binary interaction parameters of UNIFAC were improved to better predict the equilibrium in the column. The binary interaction parameters were estimat-ed using experimental data taken from literature.
dc.descriptionSociedad Argentina de Informática e Investigación Operativa (SADIO)
dc.formatapplication/pdf
dc.format185-195
dc.languageen
dc.rightshttp://creativecommons.org/licenses/by/3.0/
dc.rightsCreative Commons Attribution 3.0 Unported (CC BY 3.0)
dc.subjectCiencias Informáticas
dc.subjectreactive distillation
dc.subjectETBE
dc.subjectthermodynamics
dc.titleFinding rigorous thermodynamic model parameters for the simulation of a reactive distillation column: case of ETBE production
dc.typeObjeto de conferencia
dc.typeObjeto de conferencia


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