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

Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems

Zhang, M.[Min], Zheng, D.[Danxing], Yang, W.[Wenzhi], Li, X.[Xiaoxiao]
J. Chem. Eng. Data 2014, 59, 11, 3912-3919
ABSTRACT
According to the structure feature of the absorption power cycle, three binary systems 1,1,1,3,3-pentafluoropropane (R245fa) + N,N-dimethylacetamide (DMAC), 1,1,1,3,3,3-hexafluoropropane (R236fa) + DMAC and R236fa + dimethyl ether diethylene glycol (DMEDEG) were identified as potential working fluids. The vapor liquid equilibrium (VLE) data of these three systems were measured over a temperature range of 293.15 K to 353.15 K and a pressure range of 20 MPa to 800 kPa. The five-parameter nonrandom two-liquid (NRTL) model was used to fit the experimental data. The average relative deviations in the pressure between the experimental and calculated data for R245fa + DMAC, R236fa + DMAC and R236fa + DMEDEG were 1.51 %, 1.61 % and 1.25 %, respectively, and the maximum relative deviations were 3.21 %, 3.52 % and 2.96 %, respectively. The calculated data were in good agreement with the experimental data. The three working fluids all displayed negative deviations from Raoult s law, and the deviations decreased in the following order: R236fa + DMEDEG greater than R236fa + DMAC greater than R245fa + DMAC.
Compounds
# Formula Name
1 C3H3F5 1,1,1,3,3-pentafluoropropane
2 C3H2F6 1,1,1,3,3,3-hexafluoropropane
3 C3H7NO dimethylformamide
4 C4H9NO N,N-dimethylethanamide
5 C6H14O3 2,5,8-trioxanonane
6 CH2F2 difluoromethane
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
  • 3
  • 6
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 6; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 8
  • POMD
  • 4
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 52
  • POMD
  • 4
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 56
  • POMD
  • 5
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 55