TY - JOUR
T1 - Experimental Study and Thermodynamic Modeling of Isothermal VLE Properties of the Binary CO2 + Pyridine Mixture at High Temperatures and High Pressures
AU - Khairutdinov, Vener
AU - Khabriev, Ilnar
AU - Yarullin, Lenar
AU - Gabitov, Il’giz R.
AU - Hernández, Ariel
AU - Abdulagatov, Ilmutdin M.
N1 - Publisher Copyright:
© 2025 American Chemical Society.
PY - 2025/7/10
Y1 - 2025/7/10
N2 - The phase equilibrium properties (isothermal VLE, PTxy behavior) of the CO2 and pyridine binary mixture were studied. The measurements were carried out using a high-temperature and high-pressure optical cell. The measurements were performed at three selected supercritical isotherms of 313.15, 333.15, and 353.15 K and at pressures of up to 12.35 MPa. The liquid-vapor critical curve properties (PC, TC, xC) of the CO2 + pyridine system have been estimated using the measured VLE data. Based on the derived critical curve data, the value of the physically meaningful and theoretically important Krichevskii parameter of the mixture was estimated. The derived value of the Krichevskii parameter, together with reference thermodynamic property data of the pure supercritical solvent (CO2), can be used to calculate all thermodynamic properties of the dilute mixture near the critical point of pure CO2. The new measured VLE data were successfully calculated with the Peng-Robinson, 1978 (E-PPR78) model of the equation of state (EoS). The EoS accurately predicts the critical curve behavior of the CO2 + pyridine mixture and determines its vapor-liquid equilibrium properties across the temperature range of (313.15 to 353.15) K.
AB - The phase equilibrium properties (isothermal VLE, PTxy behavior) of the CO2 and pyridine binary mixture were studied. The measurements were carried out using a high-temperature and high-pressure optical cell. The measurements were performed at three selected supercritical isotherms of 313.15, 333.15, and 353.15 K and at pressures of up to 12.35 MPa. The liquid-vapor critical curve properties (PC, TC, xC) of the CO2 + pyridine system have been estimated using the measured VLE data. Based on the derived critical curve data, the value of the physically meaningful and theoretically important Krichevskii parameter of the mixture was estimated. The derived value of the Krichevskii parameter, together with reference thermodynamic property data of the pure supercritical solvent (CO2), can be used to calculate all thermodynamic properties of the dilute mixture near the critical point of pure CO2. The new measured VLE data were successfully calculated with the Peng-Robinson, 1978 (E-PPR78) model of the equation of state (EoS). The EoS accurately predicts the critical curve behavior of the CO2 + pyridine mixture and determines its vapor-liquid equilibrium properties across the temperature range of (313.15 to 353.15) K.
UR - http://www.scopus.com/inward/record.url?scp=105008993040&partnerID=8YFLogxK
U2 - 10.1021/acs.jced.5c00189
DO - 10.1021/acs.jced.5c00189
M3 - Article
AN - SCOPUS:105008993040
SN - 0021-9568
VL - 70
SP - 2831
EP - 2847
JO - Journal of Chemical and Engineering Data
JF - Journal of Chemical and Engineering Data
IS - 7
ER -