Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Experiment and correlation of osmotic coefficient for aqueous solution of carboxylic acids using NRTL nonrandom factor model

Pirouzi, A.[Ali], Nosrati, M.[Mohsen], Haghtalab, A.[Ali], Vasheghani-Farahani, E.[Ebrahim]
Fluid Phase Equilib. 2012, 327, 38-44
ABSTRACT
Using isopiestic method, osmotic data are measured at 298.15 K for carboxylic acid systems such as acetic, propionic, butyric, formic, malic, malonic and tartaric acids at a wide range of concentration that very rare data are available for these systems. The NRTL-NRF model of Haghtalab and Vera was already modified and applied for aqueous phosphoric acid solution [A. Haghtalab, M. Nosrati, Fluid Phase Equilib., 152, 1(1998) 43-55]. In this work the model is applied for calculation of osmotic coefficients of the other weak electrolyte systems such as carboxylic acids. Using a numerical version of Marquardt-Levenberg's optimization method, the interaction energy parameters of the NRTL-NRF model are calculated through minimization of the root mean square deviation between the calculated and experimental osmotic coefficient so that the corresponding equilibrium reaction of acid's dissociation is satisfied. Agreement of the calculated osmotic coefficient values with experimental data is very good over the whole range of concentration. In addition, molality of the undissociated electrolyte is simultaneously calculated during the process of the parameter optimization. Using the present model, the pH values for each aqueous carboxylic electrolyte solution are calculated so that the calculated results are in very good agreement with experiment.
Compounds
# Formula Name
1 CH2O2 formic acid
2 H2O water
3 C3H6O2 propanoic acid
4 C4H8O2 butanoic acid
5 C3H4O4 propanedioic acid
6 C4H6O5 hydroxybutanedioic acid
7 C4H6O6 2,3-dihydroxybutanedioic acid
8 C6H8O7 citric acid
9 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
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 16
  • POMD
  • 3
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 3; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 15
  • POMD
  • 4
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 4; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 15
  • POMD
  • 5
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 5; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 6
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 6; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 7
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 7; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 13
  • POMD
  • 8
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 8; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 18
  • POMD
  • 9
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 9; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • ISOPIE
  • 14