TY - JOUR
T1 - Vapor-liquid equilibrium measurements for the ternary systems of CO 2 + n-hexane + n-decane and CO2 + n-octane + n-decane
AU - Sánchez-García, Carmen
AU - Vázquez-Hernández, Karla E.
AU - Galicia-Luna, Luis A.
AU - Elizalde-Solis, Octavio
PY - 2011/11/2
Y1 - 2011/11/2
N2 - The experimental vapor-liquid equilibrium (VLE) data for two ternary systems containing CO2 + n-alkane + n-decane were measured using an online static-analytic apparatus with a movable ROLSI sampler. The studied CO2 + n-hexane + n-decane and CO2 + n-octane + n-decane systems were measured at temperatures of (312.89, 342.50, and 376.20) K and (313.59, 344.28, and 373.49) K, respectively. The Peng-Robinson equation of state was used to predict the VLE data of the ternary systems from the temperature-independent interaction parameters of the binary systems.
AB - The experimental vapor-liquid equilibrium (VLE) data for two ternary systems containing CO2 + n-alkane + n-decane were measured using an online static-analytic apparatus with a movable ROLSI sampler. The studied CO2 + n-hexane + n-decane and CO2 + n-octane + n-decane systems were measured at temperatures of (312.89, 342.50, and 376.20) K and (313.59, 344.28, and 373.49) K, respectively. The Peng-Robinson equation of state was used to predict the VLE data of the ternary systems from the temperature-independent interaction parameters of the binary systems.
UR - http://www.scopus.com/inward/record.url?scp=80055101012&partnerID=8YFLogxK
U2 - 10.1021/ie201516g
DO - 10.1021/ie201516g
M3 - Artículo
SN - 0888-5885
VL - 50
SP - 12254
EP - 12258
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 21
ER -