TY - JOUR
T1 - Experimental determination and correlation of phase equilibria for the ethane + 1-propanol and propane + 1-propanol systems
AU - Jiménez-Gallegos, Rodrigo
AU - Galicia-Luna, Luis A.
AU - Bouchot, Christian
AU - Camacho-Camacho, Luis E.
AU - Elizalde-Solis, Octavio
PY - 2006/9
Y1 - 2006/9
N2 - In this work, isothermal vapor-liquid equilibrium (VLE) for the ethane + 1-propanol and propane + 1-propanol systems were measured in an apparatus based on the static-analytic method. VLE data and the critical point for the ethane + 1-propanol system were measured at (317.59, 324.51, and 348.68) K. Upper critical end point, lower critical end point, and liquid-liquid-vapor locus were also obtained. For the propane + 1-propanol system, equilibrium measurements were performed at (318.30, 324.31, and 348.93) K. Experimental VLE data were correlated with the Peng-Robinson equation of state using the classical and the Wong-Sandier mixing rules. A better representation of the phase behavior was obtained using the Wong-Sandier mixing rule.
AB - In this work, isothermal vapor-liquid equilibrium (VLE) for the ethane + 1-propanol and propane + 1-propanol systems were measured in an apparatus based on the static-analytic method. VLE data and the critical point for the ethane + 1-propanol system were measured at (317.59, 324.51, and 348.68) K. Upper critical end point, lower critical end point, and liquid-liquid-vapor locus were also obtained. For the propane + 1-propanol system, equilibrium measurements were performed at (318.30, 324.31, and 348.93) K. Experimental VLE data were correlated with the Peng-Robinson equation of state using the classical and the Wong-Sandier mixing rules. A better representation of the phase behavior was obtained using the Wong-Sandier mixing rule.
UR - http://www.scopus.com/inward/record.url?scp=33749871229&partnerID=8YFLogxK
U2 - 10.1021/je060112r
DO - 10.1021/je060112r
M3 - Artículo
SN - 0021-9568
VL - 51
SP - 1629
EP - 1633
JO - Journal of Chemical and Engineering Data
JF - Journal of Chemical and Engineering Data
IS - 5
ER -