Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

The heat of mixing and second virial cross coefficient of water + oxygen and water + nitrogen

Wormald, C. J.[Christopher J.]
J. Chem. Thermodyn. 2009, 41, 5, 689-694
ABSTRACT
A vapour phase flow mixing calorimeter has been used to measure the heat of mixing HE m of (0.5H2O + 0.5O2)(g) and (0.5H2O + 0.5N2)(g) at the pressure p = 0.101325 MPa and at temperatures from (373.15 to 493.15) K. The HE m measurements were analysed using an association model for water in which the non-specific part of the interaction energy was calculated from the Stockmayer potential with the parameters e/k = 233 K, r = 0.312 nm, and t* = 1.278. The specific part of the energy was calculated from an equilibrium constant for the association of two water molecules K298K = 0.36 MPa 1 together with an enthalpy of association DH = 16.85 kJ mol 1. The second virial coefficients of O2 and N2 were calculated from the Lennard-Jones potential. Cross coefficients B12 were calculated from a combining rule containing an adjustable parameter n which is known to be satisfactory for mixtures of (water + hydrogen, or nitrogen, or argon, or methane). For all these mixtures the combining rule gives n = 0.99, and this value gives a good fit to the new HE m measurements on (water + nitrogen). For (water + oxygen) it was necessary to reduce n from 0.99 to 0.83 to fit the measurements. The values of B12 for both mixtures are close to those obtained from measurements of the solubility of water in compressed oxygen or nitrogen, and confirm that B12 for water oxygen is less negative than that for water nitrogen. This is in accord with recent theoretical calculations of the potential surfaces for water oxygen and water nitrogen.
Compounds
# Formula Name
1 H2O water
2 O2 oxygen
3 N2 nitrogen
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
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Gas
  • Temperature, K; Gas
  • Mole fraction - 2; Gas
  • Pressure, kPa; Gas
  • Gas
  • Flow calorimetry
  • 13
  • POMD
  • 3
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Gas
  • Temperature, K; Gas
  • Mole fraction - 3; Gas
  • Pressure, kPa; Gas
  • Gas
  • Flow calorimetry
  • 13