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
Clasificación temática:

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.
Palabras clave: Deterpenation , Essential Oils , Process Optimization , Supercritical Fluid Extraction
 
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Licencia
info:eu-repo/semantics/openAccess 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)
Identificadores
URI: http://hdl.handle.net/11336/37690
URL: https://www.sciencedirect.com/science/article/pii/S0098135400003367
DOI: http://dx.doi.org/10.1016/S0098-1354(00)00336-7
Colecciones
Articulos(PLAPIQUI)
Articulos de PLANTA PILOTO DE INGENIERIA QUIMICA (I)
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
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