Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Thermodynamic properties of aqueous solutions of pyridine and piperidine

Kul, I.[Ismail], Lieu, T.[Tam]
Fluid Phase Equilib. 2010, 290, 1-2, 95-102
ABSTRACT
This research was designed to examine the thermodynamic properties of aqueous solutions of pyridine and piperidine. The density, excess molar enthalpy of mixing, HE, and excess molar volume of mixing, vE, of piperidine water and pyridine water mixtures were studied at three temperatures, ranging from 294 K to 315 K. The HE and vE are negative for both mixtures, minimizing at a water mole fraction of about 0.55. The minimum HE for piperidine water mixtures is -2.23 kJ/mol which is compared with -1.63 kJ/mol for pyridine water mixtures. The minimum vE are about -1.7cm3/mol and -0.7cm3/mol for piperidine water and pyridine water mixtures, respectively. The thermal expansion coefficients alpha at 303 K, calculated from the density studies, exhibited significant positive deviations (about 20 %) from ideality for piperidine water mixtures. In contrast to this pyridine water alpha only exhibited small positive deviations from ideality of about 2 %. The results predict decreases in the absolute magnitude of vE with an increase in temperature which are 5.*10-3 cm3/K mol and 1.*10-3 cm3/K mol, for piperidine water and pyridine water mixtures, respectively. The results for vE for piperidine water mixtures agree with the very precise work of Afzal et al., J. Chem. Thermodyn. 40 (2008) 47 53. The data are interpreted in terms of the greater number of opportunities for hydrogen bonding interactions between the unlike molecules for the piperidine water mixtures.
Compounds
# Formula Name
1 C5H5N pyridine
2 C5H11N piperidine
3 H2O water
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
  • Pycnometric method
  • 15
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 15
  • POMD
  • 1
  • 3
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Constant Pressure Calorimeter
  • 21
  • POMD
  • 1
  • 3
  • Partial molar volume, m3/mol - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Derived analytically
  • 3
  • POMD
  • 1
  • 3
  • Partial molar volume, m3/mol - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Derived analytically
  • 3
  • POMD
  • 2
  • 3
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Constant Pressure Calorimeter
  • 20
  • POMD
  • 2
  • 3
  • Partial molar volume, m3/mol - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Derived analytically
  • 3
  • POMD
  • 2
  • 3
  • Partial molar volume, m3/mol - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Derived analytically
  • 3