Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Solubility of CO2 in triglycerides using Monte Carlo simulations

Howlader, Md Shamim, Venkatesan, Shanmuga, Goel, Himanshu, Huda, Md Masrul, French, William Todd, Rai, Neeraj
Fluid Phase Equilib. 2018, 476, 39-47
ABSTRACT
The knowledge of solubility of different gases in triglycerides is required to design efficient cell disruption processes for biodiesel production from wet biomass. In this combined experimental and simulation study, we determine carbon dioxide solubility in long (C18) and short (C4) chain triglycerides, and provide microscopic picture of CO2 - triglyceride interaction. The solubility of CO2 in tributyrin (a small chain triglyceride) was determined using a pressure drop gas apparatus at P = 800 - 1700 kPa and T = 283.2 - 303.2 K. Gibbs ensemble Monte Carlo simulations with configurational biased Monte Carlo algorithm were used to compute the solubility of CO2 in both a long chain triglyceride (to mimic canola oil) and tributyrin at different pressures and temperatures. The transferable potentials for phase equilibria force field was used for modeling triglycerides and CO2. Predicted densities and viscosities of both canola oil and tributyrin were in good agreement with the experimental data.We find that the computed solubilities are in excellent agreement with the experimental results for both CO2 - canola oil and CO2 - tributyrin where the mean deviation were 2.85% and 9.51%, respectively. The structural analysis of liquid phase indicates that CO2 has slightly higher preference to bind with carbonyl group than the nonpolar segments.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C15H26O6 1,2,3-propanetriyl tributanoate
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
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Pressure drop gas apparatus
  • 29