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

Experimental Investigation of Isothermal Vapor-Liquid Equilibrium and Estimation of Excess Thermodynamic Properties (hE) of CHO2K-H2O from 278.15 to 423.15 K

Takalkar, Gorakshnath D., Bhosale, Rahul R., Mali, Nilesh A., Bhagwat, Sunil S.
J. Chem. Eng. Data 2019, 64, 4, 1488-1500
ABSTRACT
In this paper, vapor liquid equilibrium (VLE) of a binary mixture i.e., potassium formate - water (CHO2K-H2O) was measured experimentally using a dynamic moving type VLE setup in the temperature range of 313.15 to 393.15 K. Overall, large vapor pressure data points generated for the mole fraction of CHO2K from 0.023 to 0.461 and the solution temperature up to 423.15 K were used to correlate the local composition based activity coefficient model (NRTL model). The data obtained via thermodynamic model fitting shows good agreement with the experimental VLE data with overall average relative deviation (ARD) of 2.15% and root mean square deviation (RMSD) of 0.25%. The obtained results further indicate that the binary mixture exhibits a negative deviation from the Raoult's law, which is an important characteristic of the working fluid used for heat activated vapor absorption system (VAS). Therefore, the CHO2K-H2O mixture can be considered as an alternative working pair that will overcome the limitations allied to the crystallization and corrosion of the commercial working fluids mainly lithium bromide- water (LiBr-H2O). The fitted NRTL model was further utilized to determine the excess thermodynamic properties, solution enthalpy, solution entropy, and equilibrium P-T-x (Duhring) plot.
Compounds
# Formula Name
1 CHKO2 potassium formate
2 H2O water
3 BrLi lithium bromide
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
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 7
  • POMD
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 85
  • POMD
  • 3
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 3; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 7