Thermodynamic analysis of supercritical carbon dioxide extraction of terpenes from cold-pressed orange oil
作者： Robert J. Braddock , Feral Temelli , John P. O'Connell , Chin S. Chen
DOI: 10.1021/IE00100A019
关键词: Phase equilibrium 、 Analytical chemistry 、 Organic chemistry 、 Terpene 、 Flow system 、 Supercritical carbon dioxide 、 Activity coefficient 、 Chemistry 、 Orange oil 、 Fugacity
摘要: Extraction of terpene hydrocarbons was studied using a dynamic flow system. Phase equilibrium data are presented for temperatures from 40 to 70°C and pressures 8.3 12.4 MPa. The have been correlated with simple model vapor fugacity coefficients the group contribution state unsymmetric convention activity
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