Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Bubble point pressures of binary system of methanol and methyl propionate

Shariati, A.[Alireza], Florusse, L. J.[Louw J.], Kroon, M. C., Peters, C. J.[Cor J.]
Fluid Phase Equilib. 2016, 417, 166-170
ABSTRACT
In this work, bubble point pressures of the system of methanol + methyl propionate were measured for several isopleths within temperature and pressure ranges of 382 - 444 K and 0.437 - 2.285 MPa, respectively. The vapor pressures of pure methanol and methyl propionate were also measured. The two-suffix Margules equation was used to represent the nonidealities of the liquid phase and the virial equation of state was used to take into account the nonidealities of the vapor phase. The temperature-dependent parameter of the two-suffix Margules equation was determined using Barker's method. The results show that the model can successfully estimate the bubble points of this system with average errors less than 0.69%.
Compounds
# Formula Name
1 CH4O methanol
2 C4H8O2 methyl propanoate
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 55