Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method

Pascual, Gladys Kate, Donnellan, Philip, Glennon, Brian, Kamaraju, Vamsi Krishna, Jones, Roderick C.
J. Chem. Eng. Data 2017, 62, 10, 3193-3205
ABSTRACT
The solubility of 2-chloro-N-(4-methylphenyl)propanamide (S1) in ethyl acetate + hexane mixtures between the temperatures of 273.43 to 327.67 K, in toluene + hexane mixtures from 273.24 to 331.62 K, in acetone + hexane mixtures from 269.81 to 318.8 butanone + hexane mixtures between 267.10 and 322.92 were determined using the Polythermal method. In situ Focused Beam Reflectance Measurement (FBRM) was used to characterize the dissolution properties and to provide S1 s saturation temperature profile as a function of concentration. It was demonstrated that the solubility of S1 increases with increasing temperature at constant solvent composition. The experimental solubility data were correlated using Apelblat, eh and Phase Equilibria with NRTL (non-random two liquid) model equations, and the predicted solubility data obtained agree sufficiently with the experimental data based on the relative deviation (RD%) and average relative deviation (ARD%) values. The Apelblat and eh model equation provides a convenient operational model of engineering interest to calculate the solubility of S1 quickly and easily, although it does not take the solvent composition into account, therefore needing separate parameters for each different solvent compositions. Therefore, the Phase Equilibria with NRTL model equation is used to provide a more comprehensive model that illustrates the effect of solvent composition on the solubility more apparently. One general set of NRTL parameters has the capability of describing all solvent compositions. Additionally, the melting temperature, Tm and the molar fusion enthalpy, 'fusH, (394.83 K and 26.77 kJ.mol-1 respectively) of S1 were determined by Differential Scanning Calorimetry (DSC).
Compounds
# Formula Name
1 C10H12ClNO 2-chloro-N-(4-methylphenyl)propanamide
2 C4H8O2 ethyl acetate
3 C7H8 toluene
4 C3H6O acetone
5 C4H8O butanone
6 C6H14 hexane
7 C8H9NO2 N-acetyl-p-aminophenol
8 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
  • 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
  • 7
  • 8
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mole fraction - 7; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 7
  • VISOBS
  • 8
  • POMD
  • 1
  • 2
  • 6
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 40
  • POMD
  • 1
  • 3
  • 6
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Solvent: Mass fraction - 3; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 40
  • POMD
  • 1
  • 4
  • 6
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Solvent: Mass fraction - 4; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 40
  • POMD
  • 1
  • 5
  • 6
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Solvent: Mass fraction - 5; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 40
  • POMD
  • 1
  • 3
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 10
  • POMD
  • 1
  • 4
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 10
  • POMD
  • 1
  • 5
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • VISOBS
  • 10