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

Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K

Liao, W.-C.[Wei-Chen], Lin, H. M.[Ho-Mu], Lee, M. J.[Ming-Jer]
J. Chem. Eng. Data 2011, 56, 4, 757-762
ABSTRACT
Excess molar enthalpies, HE, of binary mixtures of n-valeric anhydride or n-hexanoic anhydride with n-dodecane, n-tetradecane, or n-hexadecane were measured by an isothermal titration calorimeter at 298.15 K under atmospheric pressure. The experimental HE values are positive for all binary systems over the entire composition range. In these six investigated systems, the maximum values of HE exhibit at the composition ranging from 0.47 to 0.49 and 0.44 to 0.47 in the mole fraction of anhydrides for the mixtures containing n-valeric anhydride and n-hexanoic anhydride, respectively. The maximum values increase with increasing chain length of the alkanes for the mixtures containing a given anhydride. A Redlich-Kister equation correlated the experimental HE data to within the experimental uncertainty. The new enthalpy data were also correlated, respectively, with the Peng-Robinson (PR), the Patel-Teja (PT), and two versions of the cubic chain-of-rotators (CCOR) equations of state and the NRTL model as well. The CCOR equation of state with two binary interaction parameters yielded the best representation for the investigated systems.
Compounds
# Formula Name
1 C10H18O3 pentanoic anhydride
2 C12H22O3 caproic anhydride
3 C12H26 dodecane
4 C14H30 tetradecane
5 C16H34 hexadecane
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 4
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 5
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 3
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Calvet calorimetry
  • 64
  • POMD
  • 4
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Calvet calorimetry
  • 60
  • POMD
  • 5
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Calvet calorimetry
  • 56
  • POMD
  • 3
  • 2
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Calvet calorimetry
  • 68
  • POMD
  • 4
  • 2
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Calvet calorimetry
  • 72
  • POMD
  • 5
  • 2
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Calvet calorimetry
  • 67