Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K

Liang, K.-L.[Kai-Ling], Leron, R. B.[Rhoda B.], Li, M.-H.[Meng-Hui]
J. Chem. Thermodyn. 2016, 103, 51-58
ABSTRACT
A new set of values for the molar heat capacities of N-(2-aminoethyl)piperazine (AEP) and N,N,N'-trime thylethylenediamine (tMEDA) and their aqueous mixtures over the whole range of compositions are reported in the present work. Molar heat capacities of ternary mixtures of each polyamine with piperazine (PZ): (AEP + PZ + H2O) and (tMEDA + PZ + H2O) were also measured. Measurements were done over the temperature range T = (303.2 353.2) K and p = 101.3 kPa by the differential scanning calorimetry technique. Excess molar heat capacities of aqueous binary mixtures were correlated with composition and temperature using a Redlich Kister relation, which was then used to correlate molar heat capacities of the mixtures at different temperatures and compositions. The equation fit the results with the average absolute deviation (AAD) of 2.1% and 0.2% for the excess molar heat capacity and molar heat capacity, respectively. A modified Sohnel and Novotny' equation was applied to represent the composition and temperature dependence of the molar heat capacity of aqueous ternary mixtures at AAD between the correlated and the experimental data of about 0.1%. The correlations proposed here are of acceptable accuracy for application in process design and engineering.
Compounds
# Formula Name
1 C4H10N2 piperazine
2 C6H15N3 N-(.beta.-aminoethyl)piperazine)
3 C5H14N2 N,N,N'-trimethylethylenediamine
4 H2O water
5 C7H8 toluene
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
  • 2
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 11
  • POMD
  • 3
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 11
  • POMD
  • 4
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 11
  • POMD
  • 5
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 11
  • POMD
  • 2
  • 4
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 77
  • POMD
  • 3
  • 4
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 77
  • POMD
  • 1
  • 2
  • 4
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 2; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 44
  • POMD
  • 1
  • 3
  • 4
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 3; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Small sample (50 mg) DSC
  • 44