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

A 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....

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Autores principales: Durruty, Gisela N., Diaz, M. Soledad, Hoch, Patricia
Formato: Objeto de conferencia
Lenguaje:Inglés
Publicado: 2014
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Acceso en línea:http://sedici.unlp.edu.ar/handle/10915/41998
http://43jaiio.sadio.org.ar/proceedings/SII/16_Durruty%20et%20al..pdf
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