2,3,3,3-Tetrafluoroprop-1-ene (HFO1234yf) is recently recognized as a new generation refrigerant to replace R134a in automotive air-conditioning system and other refrigeration applications. The knowledge of phase equilibrium property for refrigerant with lubricant oil is therefore interested in these systems. A systematic research program on the phase equilibrium of HFO1234yf with lubricant oils has been carried out in our laboratory, and the purpose is to investigate the influence of the molecular structure of oils, pressure and temperature on the phase behavior of HFO1234yf and lubricant oil system. In this work, the measurements of phase equilibrium for HFO1234yf + pentaerythritol tetrahexanoate (PEC6), HFO1234yf + pentaerythritol tetraheptanoate (PEC7), and HFO1234yf + pentaerythritol tetraoctanoate (PEC8) between 293.15 K and 348.15 K were performed by means of isochoric saturation method. The experimental data were correlated using the PR EOS and HVOS mixing rule combined with Wilson excess free-energy model. The average relative deviations between experimental results and the calculated pressure by the model for HFO1234yf + PEC6, HFO1234yf + PEC7, and HFO1234yf + PEC8 system were 1.23%, 1.19%, and 1.39%, respectively. The maximum relative deviations were 4.04%, 4.34%, and 4.84%, respectively.
Compounds
#
Formula
Name
1
C3H2F4
2,3,3,3-tetrafluoro-1-propene
2
C29H52O8
pentaerythritol tetrahexanoate
3
C33H60O8
pentaerythritol tetraheptanoate
4
C37H68O8
pentaerythritol tetraoctanoate
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.