Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

(r, VE, T) Measurements of the Ternary Mixture (Dibutyl Ether + 1-Heptanol + Heptane) at Temperatures up to 393.15 K and Pressures up to 140 MPa and Modeling Using the Peng-Robinson and PC-SAFT Equations of State

Abala, I.[Ilham], Alaoui, F. E. M.[Fatima Ezzahrae M'hamdi], Eddine, A. S.[Abdelaziz Sahib], Aguilar, F.[Fernando], Rujas, N. M.[Natalia Munoz], Montero, E.[Eduardo]
J. Chem. Eng. Data 2019, 64, 9, 3861-3873
ABSTRACT
New measurement density data (1360 points) for dibutyl ether (1) + 1-heptanol (2) + heptane (3), were measured at various temperatures T (298.15 to 393.15) K and at various pressures p (0.1 to 140) MPa, adopting an Anton-Paar Densimeter (DMA HPM). The excess molar volumes VE of the studied ternary system were derived from the measured density data. Subsequently, they are calculated with the Singh and Redlich-Kister equations. VE values were employed to write the different interactions imply in the mixture. The Peng-Robinson and the PC-SAFT equations of states (EoS) were performed for their potential to correlate and predict experimental density for ternary mixture. The PC-SAFT parameters of pure compounds that constituted the studied ternary mixture were regressed by using the measured data of density of each pure compounds.
Compounds
# Formula Name
1 C8H18O dibutyl ether
2 C7H16O heptan-1-ol
3 C7H16 heptane
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
  • 3
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Vibrating tube method
  • 1360