Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Equilibrium CO2 solubility and thermophysical properties of aqueous blends of 1-(2-aminoethyl) piperazine and N-methyldiethanolamine

Dey, A.[Anirban], Dash, S. K.[Sukanta K.], Mandal, B.[Bishnupada]
Fluid Phase Equilib. 2018, 463, 91-105
ABSTRACT
The present work reports new experimental CO2 solubility data of CO2 absorption in aqueous mixture of 1-(2-aminoethyl)piperazine (AEP) and N-methyldiethanolamine (MDEA) over the temperature and pressure range of (303.2 tov323.2) K and (3 to 300) kPa, respectively. The total mass fraction for AEP and MDEA was fixed to be yAEP + yMDEA -= 0.4 in the aqueous solution. In the experimental measurement, the samples with the five different composition of AEP: MDEA (yAEP : yMDEAP) have been considered as 0.05:0.35; 0.10:0.30; 0.15:0.25; 0.20:0.20 and 0.25:0.15 respectively. The experimental solubility data is modeled using modified Kent-Eisenberg (KE) equilibrium model. The equilibrium constants related to AEP deprotonation, and carbamate formation reactions are regressed as a function of CO2 partial pressure, amine concentration and temperature to fit the equilibrium CO2 solubility data. The model predicted VLE results from KE model are in good agreement with the experimental data within an average absolute deviation (AAD) of 5.94%. The solubility data is also correlated using Artificial Neural Network (ANN) approach. The predicted value from the feed forward neural network model, which involves Levenberg-Marquardt algorithm, shows very good agreement with the experimental data having mean square error (MSE) of 0.000413 and correlation coefficient (R2) of 0.997. Thermophysical properties such as density, viscosity and surface tension of aqueous (AEP + MDEA) have been also measured in the temperature range of (303.2 to 343.2) K. The density and viscosity data is modeled as a function of temperature and amine composition using Redlich-Kister and Grunberg-Nissan models, respectively. The model results of these temperature dependent physical properties are also in good agreement with the experimental data.
Compounds
# Formula Name
1 C6H15N3 N-(.beta.-aminoethyl)piperazine)
2 C5H13NO2 N-methyldiethanolamine
3 C4H11NO2 diethanolamine
4 CO2 carbon dioxide
5 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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 5
  • POMD
  • 1
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 5
  • POMD
  • 2
  • 5
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 12
  • POMD
  • 2
  • 5
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 12
  • POMD
  • 1
  • 2
  • 5
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Mass fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 25
  • POMD
  • 1
  • 2
  • 5
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Mass fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 25
  • POMD
  • 1
  • 2
  • 5
  • Surface tension liquid-gas, N/m ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Mass fraction - 2; Liquid
  • Liquid
  • Air at 1 atmosphere
  • Pendant drop shape
  • 25
  • POMD
  • 2
  • 5
  • 4
  • Mole fraction - 4 ; Liquid
  • Pressure, kPa - 4; Gas
  • Temperature, K; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 9
  • POMD
  • 3
  • 5
  • Surface tension liquid-gas, N/m ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 3; Liquid
  • Liquid
  • Air at 1 atmosphere
  • Pendant drop shape
  • 9