Predictive Molecular Simulation Studies on the Vapor–Liquid Equilibria of 10 Binary Mixtures Containing Different Hydrofluoroolefins

In this work, predictions from Gibbs Ensemble Monte Carlo simulations on the vapor liquid phase equilibria properties of 10 different binary mixtures of the components, carbon dioxide, 2,3,3,3-tetrafluoropropene (R-1234yf), cis-and trans-1,3,3,3-tetrafluoropropene [R-1234ze(Z/E)], cis- and trans-1,1,1,4,4,4-hexafluorobut-2-ene [R-1336mzz(Z/E)], and trans-1-chloro-3,3,3-trifluoroprop-1-ene [R-1233zd(E)], are presented. For seven of these mixtures, the simulation results represent the first information on their phase behavior, addressing gaps in the existing data on potential HFO-based refrigerant blends. The simulation results together with available experimental data were then used to derive parameters for the multifluid modeling of these mixtures. Different variants of the multifluid model, i.e., predictive mixing rules as well as different parametrizations of the adjustable parameters, are evaluated by assessing their performance in reproducing bubble and dew point lines, as well as saturated densities.

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Publication Details

Journal
Journal of Chemical & Engineering Data
Published
2024-11-05
DOI
https://doi.org/10.1021/acs.jced.4c00464
Citations
1
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
0.18

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article

Predictive Molecular Simulation Studies on the Vapor–Liquid Equilibria of 10 Binary Mixtures Containing Different Hydrofluoroolefins

G. Raabe
1 citations
Journal of Chemical & Engineering Data
Phase Equilibria and Thermodynamics
0.18
article

Predictive Molecular Simulation Studies on the Vapor–Liquid Equilibria of 10 Binary Mixtures Containing Different Hydrofluoroolefins

G. Raabe
article en
1 citations

Abstract

In this work, predictions from Gibbs Ensemble Monte Carlo simulations on the vapor liquid phase equilibria properties of 10 different binary mixtures of the components, carbon dioxide, 2,3,3,3-tetrafluoropropene (R-1234yf), cis-and trans-1,3,3,3-tetrafluoropropene [R-1234ze(Z/E)], cis- and trans-1,1,1,4,4,4-hexafluorobut-2-ene [R-1336mzz(Z/E)], and trans-1-chloro-3,3,3-trifluoroprop-1-ene [R-1233zd(E)], are presented. For seven of these mixtures, the simulation results represent the first information on their phase behavior, addressing gaps in the existing data on potential HFO-based refrigerant blends. The simulation results together with available experimental data were then used to derive parameters for the multifluid modeling of these mixtures. Different variants of the multifluid model, i.e., predictive mixing rules as well as different parametrizations of the adjustable parameters, are evaluated by assessing their performance in reproducing bubble and dew point lines, as well as saturated densities.

Journal of Chemical & Engineering DataVol. 69(11)
Technische Universität Braunschweig (DE)
Deutsche Forschungsgemeinschaft
Openalex Percentile: Top 51%
Phase Equilibria and Thermodynamics
0.18
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