Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine

Klauck, M.[Mandy], Silbermann, R.[Rico], Metasch, R.[Robert], Unger, S.[Sven], Schmelzer, J.[Jurgen]
Fluid Phase Equilib. 2012, 314, 169-179
ABSTRACT
The group interaction parameters for modified UNIFAC (Dortmund) of the newly defined amine group at cycloaliphatic hydrocarbon occurring for example in cyclohexylamine with six established groups were determined using binary data available from literature and new experimental data presented in this paper. The calculations of binary and ternary systems are compared to the predictions using the amine group at aliphatic hydrocarbon. The liquid-liquid and vapour-liquid equilibria of the quaternary system water + toluene + aniline + cyclohexylamine were determined at two temperatures, each, and predicted with mod. UNIFAC (Do) using the new group interaction parameters. Furthermore, the predictions for the ternary and quaternary systems with mod. UNIFAC (Do) are compared to the predictions with NRTL, UNIQUAC, and Elliott-Suresh-Donohue equation of state using binary interaction parameters.
Compounds
# Formula Name
1 C9H20 nonane
2 C6H12 cyclohexane
3 C7H14 methylcyclohexane
4 C8H16 ethylcyclohexane
5 C6H13N cyclohexylamine
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
  • 5
  • 1
  • Mole fraction - 1 ; Gas
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Density calibration data
  • 29
  • POMD
  • 5
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Density calibration data
  • 29
  • POMD
  • 3
  • 5
  • Activity coefficient - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Differential ebulliometry
  • 3
  • POMD
  • 3
  • 5
  • Activity coefficient - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Differential ebulliometry
  • 3
  • POMD
  • 3
  • 5
  • Mole fraction - 3 ; Gas
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 18
  • POMD
  • 3
  • 5
  • Mole fraction - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 18
  • POMD
  • 5
  • 2
  • Activity coefficient - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Differential ebulliometry
  • 2
  • POMD
  • 5
  • 2
  • Activity coefficient - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Differential ebulliometry
  • 2
  • POMD
  • 5
  • 4
  • Activity coefficient - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Differential ebulliometry
  • 3
  • POMD
  • 5
  • 4
  • Activity coefficient - 4 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Differential ebulliometry
  • 3