Artículo

Optimal design of supercritical fluid processes

Espinosa, Susana Noemi; Díaz, María SoledadIcon ; Brignole, Esteban AlbertoIcon
Fecha de publicación: 07/2000
Editorial: Pergamon-Elsevier Science Ltd
Revista: Computers and Chemical Engineering
ISSN: 0098-1354
Idioma: Inglés
Tipo de recurso: Artículo publicado

Resumen

Optimal schemes and operating conditions are analyzed for the deterpenation of citrus peel oils with supercritical carbon dioxide. The problem is formulated as a mathematical programming model using the group contribution equation of state (GC-EOS) for rigorous phase equilibria predictions. Both thermodynamic predictions and simulation results are found to be in agreement with experimental studies. Optimization results give insight to improve current experimental values of product recovery and purity.

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https://www.sciencedirect.com/science/article/pii/S0098135400003367
http://dx.doi.org/10.1016/S0098-1354(00)00336-7
info:eu-repo/semantics/restrictedAccess Excepto donde se diga explícitamente, este item se publica bajo la siguiente descripción: Creative Commons Attribution-NonCommercial-ShareAlike 2.5 Unported (CC BY-NC-SA 2.5)
Citación: Espinosa, Susana Noemi; Díaz, María Soledad; Brignole, Esteban Alberto; Optimal design of supercritical fluid processes; Pergamon-Elsevier Science Ltd; Computers and Chemical Engineering; 24; 2-7; 7-2000; 1301-1307
URI: http://hdl.handle.net/11336/37690
 

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