Multifluid MixtureModels for the Binary Mixturesof Trifluoroethene (R-1123) with Difluoromethane (R-32), 2,3,3,3-Tetrafluoroprop-1-ene(R-1234yf), and Propane (R-290)

This work presents mixture models for the thermodynamic properties of the mixtures of R-1123 with R-32, R-1234yf, and R-290, which are potential refrigerants for next-generation air conditioning systems. The models are based on the multifluid approximation and employ accurate Helmholtz energy equations of state for the pure fluids. The mixing parameters of the models are determined by fitting experimental data for the (<i>p</i>, ρ, <i>T</i>) behavior and vapor–liquid equilibrium. The range of validity of the models is approximately temperatures from 273 to 400 K and pressures up to 7 MPa. Typical uncertainties (<i>k</i> = 2) in this range are 0.3% for liquid densities, 1.5% for vapor densities, and 1% for bubble-point pressures. The mixture models exhibit qualitatively correct behavior in the critical and extrapolated regions; this is demonstrated by plots of several thermodynamic properties over wide ranges of temperature and pressure.

Publication Details

Journal
Figshare
Published
2025-01-28
DOI
https://doi.org/10.1021/acsomega.4c09878.s001
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Multifluid MixtureModels for the Binary Mixturesof Trifluoroethene (R-1123) with Difluoromethane (R-32), 2,3,3,3-Tetrafluoroprop-1-ene(R-1234yf), and Propane (R-290)

Figshare
Phase Equilibria and Thermodynamics
article

Multifluid MixtureModels for the Binary Mixturesof Trifluoroethene (R-1123) with Difluoromethane (R-32), 2,3,3,3-Tetrafluoroprop-1-ene(R-1234yf), and Propane (R-290)

article en

Abstract

This work presents mixture models for the thermodynamic properties of the mixtures of R-1123 with R-32, R-1234yf, and R-290, which are potential refrigerants for next-generation air conditioning systems. The models are based on the multifluid approximation and employ accurate Helmholtz energy equations of state for the pure fluids. The mixing parameters of the models are determined by fitting experimental data for the (<i>p</i>, ρ, <i>T</i>) behavior and vapor–liquid equilibrium. The range of validity of the models is approximately temperatures from 273 to 400 K and pressures up to 7 MPa. Typical uncertainties (<i>k</i> = 2) in this range are 0.3% for liquid densities, 1.5% for vapor densities, and 1% for bubble-point pressures. The mixture models exhibit qualitatively correct behavior in the critical and extrapolated regions; this is demonstrated by plots of several thermodynamic properties over wide ranges of temperature and pressure.

Figshare
Affordable and clean energy
Openalex Percentile: Top 58%
Phase Equilibria and Thermodynamics
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.

Multifluid MixtureModels for the Binary Mixturesof Trifluoroethene (R-1123) with Difluoromethane (R-32), 2,3,3,3-Tetrafluoroprop-1-ene(R-1234yf), and Propane (R-290) · Figshare (2025) | TGRS Research Map | TGRS