Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Isobaric vapor-liquid equilibria of the binary system maleic anhydride and dimethyl phthalate at 2.67, 5.33 and 8.00 kPa

Liu, Z.[Zhihua], Xu, W.[Wei], Tian, Y.[Yiling], Li, H.[Hesong]
Fluid Phase Equilib. 2006, 247, 1-2, 54-58
ABSTRACT
Isobaric vapor-liquid equilibrium data for the binary system maleic anhydride + dimethyl phthalate at 2.67, 5.33 and 8.00 kPa were determined using the ebulliometric method. Saturated vapor pressures of pure dimethyl phthalate were also measured and Antoine constants were obtained. The experimental equilibrium temperatures, pressures and feed compositions were used to obtain NRTL parameters and equilibrium liquid and vapor compositions. Moreover, vapor-liquid equilibrium data for the binary system were predicted by use of the UNIFAC model. Predicted results were compared with those from the ebulliometric method, and good agreement was found.
Compounds
# Formula Name
1 C10H10O4 dimethyl 1,2-benzenedicarboxylate
2 C4H2O3 maleic anhydride
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
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 1
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:16
  • 12
  • POMD
  • 2
  • Normal melting temperature, K ; Crystal
  • Crystal
  • Liquid
  • Air at 1 atmosphere
  • VISOBS
  • 1
  • POMD
  • 2
  • 1
  • Boiling temperature at pressure P, K ; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:16
  • 27