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

Geometric Structures of Associating Component Optimized toward Correlation and Prediction of Isobaric Vapor Liquid Equilibria for Binary and Ternary Mixtures of Ethanal, Ethanol, and Ethanoic Acid

Zhu, D.[Dechun], Gao, D.[Daming], Zhang, H.[Hui], Winter, B.[Bernhard], Lucking, P.[Peter], Sun, H.[Hong], Guan, H.[Hangmin], Chen, H.[Hong], Shi, J.[Jianjun]
J. Chem. Eng. Data 2013, 58, 1, 7-17
ABSTRACT
It has relatively been difficult to accurately correlate and predict vapor liquid equilibrium (VLE) data for the strongly associating system containing the carboxyl acid due to its monomer undergoing partial dimerization and even higher polymerization in the vapor and liquid phases. Herein, this paper reports that the formation state for the associating component mainly has been the existence of dimer in the vapor and liquid phases through the geometric structures of ethanoic acid investigated theoretically with density functional theory (DFT), and the VLE data for the associating ternary system ethanal + ethanol + ethanoic acid and the three constituent binary systems were measured using a recirculating still at 101.325 kPa. Marek s chemical theory was considered due to the associating species as the dimer existence in the both phases. The three experimental binary data sets were independently correlated using nonrandom two-liquid (NRTL), Wilson, and universal quasichemical activity coefficient (UNIQUAC) model, respectively, and the binary parameters were applied to predict the VLE data for ternary system without any additional adjustment. By comparison with the measured values, the ternary equilibrium values predicted agreed well with the measured values in this way. The thermodynamic consistency of the experimental VLE data was checked out by means of the Wisniak s L W test for the binary systems and the Wisniak Tamir s modification of McDermott Ellis test for the ternary system, respectively.
Compounds
# Formula Name
1 C2H6O ethanol
2 C2H4O ethanal
3 C2H4O2 acetic acid
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 1
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:6
  • 1
  • POMD
  • 2
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 1
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 1
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:6
  • 1
  • POMD
  • 3
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 1
  • POMD
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 1
  • POMD
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 1
  • POMD
  • 1
  • 2
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:6
  • 26
  • POMD
  • 1
  • 2
  • Mole fraction - 2 ; Gas
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • Chromatography
  • 27
  • POMD
  • 3
  • 2
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 30
  • POMD
  • 3
  • 2
  • Mole fraction - 2 ; Gas
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • Chromatography
  • 30
  • POMD
  • 1
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:6
  • 24
  • POMD
  • 1
  • 3
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • Chromatography
  • 24
  • POMD
  • 1
  • 3
  • 2
  • Mole fraction - 1 ; Liquid
  • Mole fraction - 1 ; Gas
  • Mole fraction - 2 ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Chromatography
  • Chromatography
  • Chromatography
  • 43