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....
Guardado en:
| Autores principales: | Durruty, Gisela N., Diaz, M. Soledad, Hoch, Patricia |
|---|---|
| Formato: | Objeto de conferencia |
| Lenguaje: | Inglés |
| Publicado: |
2014
|
| Materias: | |
| Acceso en línea: | http://sedici.unlp.edu.ar/handle/10915/41998 http://43jaiio.sadio.org.ar/proceedings/SII/16_Durruty%20et%20al..pdf |
| Aporte de: |
Ejemplares similares
-
Batch distillation : simulation, optimal design, and control /
por: Diwekar, Urmila
Publicado: (2012) -
Distillers grains production, properties, and utilization /
Publicado: (2011) - ETB Centro multifuncional, Sappada
-
Advanced distillation technologies design, control and applications /
por: Kiss, Anton Alexandru
Publicado: (2013) -
Distillation control, optimization, and tuning fundamentals and strategies /
por: Robbins, Lanny
Publicado: (2011)