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J. C. de la Fuente and S. B. Bottini, “High-Pressure Phase Equilibria and Thermodynamic Modelling for the Binary Systems CO2+Lemon Oil and C2H6+Lemon Oil,” Fluid Phase Equilibria, Vol. 175, No. 1-2, 2000, pp. 45-52.
http://dx.doi.org/10.1016/S0378-3812(00)00454-4

has been cited by the following article:

• TITLE: Supercritical Equilibrium Data of the Systems Carbon Dioxide—Linalool and Carbon Dioxide—Orange Essential Oil

  AUTHORS: Claudio Capparucci, Sara Frattari, Fausto Gironi

  KEYWORDS: Supercritical; Extraction; Carbon Dioxide; Orange Essential Oil; Linalool; Phase Equilibrium

  JOURNAL NAME: American Journal of Analytical Chemistry, Vol.4 No.12, December 16, 2013

  ABSTRACT: In this paper experimental equilibrium data on the system supercritical CO2-orange essential oil and the system supercritical CO2-linalool are reported at 323.15 K and 343.15 K, for pressures in the ranges of 7.6-13.5 MPa. The behavior of the system supercritical CO2-orange essential oil was represented by means of thermodynamic model, based on Peng-Robinson equation of state. To this aim the orange essential oil was represented by a mixture of limonene, linalool and β-caryophyllene, selected to represent the classes of monoterpenes, oxygenated terpenes and sesquiterpenes respectively. The model uses only regression parameters calculated from binary sub-systems, CO2-limonene and CO2-β-caryophyllene (taken from literature) and CO2-linalool (calculated from the fitting of original data reported in the present work) thus being predictive with respect to the multicomponent mixture.