Phase equilibrium measurements for the system clove (Eugenia caryophyllus) oil plus CO2

被引:38
作者
Souza, AT
Corazza, ML
Cardozo, L
Guirardello, R
Meireles, MAA
机构
[1] Univ Estadual Campinas, Coll Food Engn, LASEFI, DEA FEA, BR-13083970 Campinas, SP, Brazil
[2] Univ Estadual Campinas, Coll Chem Engn, DPQ, FEQ, BR-13081970 Campinas, SP, Brazil
[3] Univ Estadual Maringa, Dept Chem Engn, BR-87020900 Maringa, Parana, Brazil
关键词
D O I
10.1021/je034190f
中图分类号
O414.1 [热力学];
学科分类号
摘要
Phase equilibria data for the system formed by clove oil + CO2 were measured at pressures from 58.3 to 108.1 bar and temperatures of 303.2, 313.2, and 328.2 K. The phase equilibrium experiments (cloud points) were performed using a high-pressure variable-volume view cell. The phase transitions were visually recorded as bubble or dew points. The clove oil used in the present work was extracted with carbon dioxide at 150 bar and 298.2 K, and it consisted of a mixture of the following mass fractions: eugenol (75.5%), beta-caryophyllene (12.1%), eugenol acetate (11.0%), and alpha-humulene (1.40%). Liquid-liquid-vapor equilibria were observed at 303.2 and 308.2 K, and liquid-vapor equilibria were observed at 313.2, 318.2, and 328.2 K. The phase equilibria data were modeled assuming the system to be a pseudobinary system. The Peng-Robinson equation of state with the quadratic mixing rule was used. The experimental data were fitted using the simulated annealing minimization method. Two different procedures were employed: (i) the phase stability was calculated using the Helmholtz free energy and the interval analysis, and (ii) the phase equilibrium was calculated using the Gibbs free energy, which was solved with the simulated annealing method. The model described quantitatively the experimental data.
引用
收藏
页码:352 / 356
页数:5
相关论文
共 21 条
[1]  
Adams R. P., 2001, IDENTIFICATION ESSEN
[2]   GIBBS ENERGY ANALYSIS OF PHASE-EQUILIBRIA [J].
BAKER, LE ;
PIERCE, AC ;
LUKS, KD .
SOCIETY OF PETROLEUM ENGINEERS JOURNAL, 1982, 22 (05) :731-742
[3]   Vapor-liquid equilibria at elevated pressures of binary mixtures of carbon dioxide with methyl salicylate, eugenol, and diethyl phthalate [J].
Cheng, KW ;
Kuo, SJ ;
Tang, M ;
Chen, YP .
JOURNAL OF SUPERCRITICAL FLUIDS, 2000, 18 (02) :87-99
[4]   High pressure phase equilibria of the related substances in the limonene oxidation in supercritical CO2 [J].
Corazza, ML ;
Filho, LC ;
Antunes, OAC ;
Dariva, C .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2003, 48 (02) :354-358
[5]   Reliable computation of phase stability using interval analysis: Cubic equation of state models [J].
Hua, JZ ;
Brennecke, JF ;
Stadtherr, MA .
COMPUTERS & CHEMICAL ENGINEERING, 1998, 22 (09) :1207-1214
[6]   INTBIS, A PORTABLE INTERVAL NEWTON BISECTION PACKAGE [J].
KEARFOTT, RB ;
NOVOA, M .
ACM TRANSACTIONS ON MATHEMATICAL SOFTWARE, 1990, 16 (02) :152-157
[7]   ALGORITHM-737 - INTLIB - A PORTABLE FORTRAN-77 INTERVAL STANDARD-FUNCTION LIBRARY [J].
KEARFOTT, RB ;
DAWANDE, M ;
DU, K ;
HU, C .
ACM TRANSACTIONS ON MATHEMATICAL SOFTWARE, 1994, 20 (04) :447-459
[8]  
McHugh MA., 1994, SUPERCRITICAL FLUID, V2nd
[9]   THE ISOTHERMAL FLASH PROBLEM .1. STABILITY [J].
MICHELSEN, ML .
FLUID PHASE EQUILIBRIA, 1982, 9 (01) :1-19
[10]   THE ISOTHERMAL FLASH PROBLEM .2. PHASE-SPLIT CALCULATION [J].
MICHELSEN, ML .
FLUID PHASE EQUILIBRIA, 1982, 9 (01) :21-40