Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling

Wang, J.[Jian], Xu, A.[Anli], Xu, R.[Renji]
J. Chem. Thermodyn. 2017, 108, 45-58
ABSTRACT
By using the isothermal saturation method, the solid-liquid equilibrium of 2-nitro-p-phenylenediamine in pure organic solvents of methanol, ethanol, n-propanol, isopropanol, N-methyl-2-pyrrolidone, acetonitrile, ethyl acetate, toluene and 1,4-dioxane and liquid mixture of (N-methyl-2-pyrrolidone + methanol) was obtained experimentally at the temperatures ranging from (283.15 to 318.15) K under atmospheric pressure, and the solubility of 2-nitro-p-phenylenediamine in the selected solvents was determined by a high-performance liquid chromatography (HPLC). Within the studied temperature range, the 2-nitro-p-phenylenediamine solubility in mole fraction in these solvents increased with increasing temperature. The descending order of the mole fraction solubility in pure solvents was as follow: (N-methyl-2-pyrrolidone, 1,4-dioxane) greater than ethyl acetate greater than acetonitrile greater than methanol greater than ethanol greater than n-propanol greater than isopropanol greater than toluene, and for the (N-methyl-2-pyrrolidone + methanol) mixture with given initial composition, the mole fraction solubility of 2-nitro-p-phenylenediamine increased with increasing temperature and mass fraction of N-methyl-2-pyrrolidone. The values of solubility for 2-nitro-pphenylenediamine in pure solvent were correlated and calculated with the modified Apelblat equation, kh equation, Wilson model and NRTL model; and in the binary solvent mixture of (N-methyl-2- pyrrolidone + methanol), the Jouyban Acree model, modified Apelblat Jouyban Acree model and Sun model. For the pure solvents, the largest values of the relative average deviation (RAD) and root-meansquare deviation (RMSD) obtained by the four models were 1.17% and 6.80*10-4, respectively; and for (N-methyl-2-pyrrolidone + methanol) mixture, they were a larger, which were 3.59% and 19.12*10-4. In general, the selected thermodynamic models were all acceptable for describing the solubility behaviour of 2-nitro-p-phenylenediamine in the solvents. In addition, the mixing properties including the mixing Gibbs energy, mixing enthalpy, mixing entropy, activity coefficient at infinitesimal concentration (c1 1 ) and reduced excess enthalpy (HE;1 1 ) were calculated for 2-nitro-p-phenylenediamine in pure solvents. Knowledge of the solubility and thermodynamic studies is essential in optimizing the purification process of 2-nitro-p-phenylenediamine.
Compounds
# Formula Name
1 C6H7N3O2 2-nitro-1,4-benzenediamine
2 CH4O methanol
3 C2H6O ethanol
4 C3H8O propan-1-ol
5 C3H8O propan-2-ol
6 C2H3N acetonitrile
7 C5H9NO N-methylpyrrolidone
8 C7H8 toluene
9 C4H8O2 1,4-dioxane
10 C4H8O2 ethyl acetate
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
  • Normal melting temperature, K ; Crystal
  • Crystal
  • Liquid
  • Air at 1 atmosphere
  • DTA
  • 1
  • POMD
  • 1
  • Molar enthalpy of transition or fusion, kJ/mol ; Crystal
  • Crystal
  • Liquid
  • Air at 1 atmosphere
  • DSC
  • 1
  • POMD
  • 2
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 3
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 4
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 6
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 10
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 7
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 8
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 9
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 14
  • POMD
  • 5
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 15
  • POMD
  • 2
  • 7
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Solvent: Mass fraction - 7; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Chromatography
  • 165