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Predicting the Vle, Sle and Surface Tension of Refrigerant Systems Using a Saft-Based Activity Coefficient Model
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Outgoing claims: the papers this work cites, builds on, or argues with.
inferredcites →https://doi.org/10.1002/aic.15859openalex-extracted
Next generation of low global warming potential refrigerants: Thermodynamic properties molecular modeling
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Local compositions in thermodynamic excess functions for liquid mixtures
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Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems
inferredcites →https://doi.org/10.1007/s10765-009-0618-yopenalex-extracted
Solid–Liquid Equilibria for the CO2 + R143a and N2O + R143a Systems
inferredcites →https://doi.org/10.1007/s11814-010-0293-5openalex-extracted
High pressure isothermal vapor-liquid equilibria for the binary system of carbon dioxide (CO2)+1,1,1-trifluoroethane (R-143a)
inferredcites →https://doi.org/10.1016/0378-3812(78)85002-xopenalex-extracted
On the derivation and extension of the uniquac equation
inferredcites →https://doi.org/10.1016/j.apenergy.2013.01.081openalex-extracted
Numerical investigations on the performance of a single-stage auto-cascade refrigerator operating with two vapor–liquid separators and environmentally benign binary refrigerants
inferredcites →https://doi.org/10.1016/j.applthermaleng.2020.114898openalex-extracted
Performance evaluation of novel double internal auto-cascade two-stage compression system using refrigerant mixtures
inferredcites →https://doi.org/10.1016/j.enbuild.2023.112815openalex-extracted
Theoretical performance comparison for a regenerator-enhanced three-stage auto-cascade refrigeration system using different zeotropic mixed refrigerants
inferredcites →https://doi.org/10.1016/j.enconman.2014.04.076openalex-extracted
Exergy and energy analysis of three stage auto refrigerating cascade system using Zeotropic mixture for sustainable development
inferredcites →https://doi.org/10.1016/j.expthermflusci.2008.08.006openalex-extracted
A study on the cycle characteristics of an auto-cascade refrigeration system
inferredcites →https://doi.org/10.1016/j.fluid.2003.12.002openalex-extracted
Vapor–liquid equilibrium data for the carbon dioxide (CO2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa
inferredcites →https://doi.org/10.1016/j.fluid.2006.11.015openalex-extracted
Solid–liquid equilibria for the CO2+N2O, CO2+R32, and N2O+R32 systems
inferredcites →https://doi.org/10.1016/j.fluid.2007.07.029openalex-extracted
Vapor pressure measurements in the range 10−5Pa to 1Pa of four pentaerythritol esters
inferredcites →https://doi.org/10.1016/j.fluid.2013.06.019openalex-extracted
Solid–liquid equilibria measurements of the carbon dioxide+2,3,3,3-tetrafluoroprop-1-ene and carbon dioxide+trans-1,3,3,3-tetrafluoropropene mixtures
inferredcites →https://doi.org/10.1016/j.fluid.2014.12.030openalex-extracted
Solubility of trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) in pentaerythritol ester heptanoic acid (PEC7) and in pentaerythritol tetranonanoate (PEC9) between 283.15 K and 353.15 K
inferredcites →https://doi.org/10.1016/j.fluid.2016.01.013openalex-extracted
Surface tension and liquid viscosity measurement for binary mixtures of R134a with R1234yf and R1234ze(E)
inferredcites →https://doi.org/10.1016/j.ijrefrig.2004.06.014openalex-extracted
Blends of carbon dioxide and HFCs as working fluids for the low-temperature circuit in cascade refrigerating systems
inferredcites →https://doi.org/10.1016/j.ijrefrig.2008.01.013openalex-extracted
The next generation of refrigerants – Historical review, considerations, and outlook
inferredcites →https://doi.org/10.1016/j.ijrefrig.2016.05.017openalex-extracted
Prediction of thermodynamic properties of refrigerant fluids with a new three-parameter cubic equation of state
inferredcites →https://doi.org/10.1016/j.ijrefrig.2019.04.004openalex-extracted
Molecular modeling of the solubility of low global warming potential refrigerants in polyol ester lubricants
inferredcites →https://doi.org/10.1016/j.ijrefrig.2019.10.005openalex-extracted
Phase behavior of R1234yf and R600a in pentaerythritol tetranonanoate
inferredcites →https://doi.org/10.1016/j.ijrefrig.2020.02.029openalex-extracted
Phase equilibrium and liquid viscosity data for R-290/POE ISO 22 mixtures between 283 and 353 K
inferredcites →https://doi.org/10.1016/j.ijrefrig.2021.01.028openalex-extracted
Energy and exergy performance evaluation of a three-stage auto-cascade refrigeration system using low-GWP alternative refrigerants
inferredcites →https://doi.org/10.1016/j.ijrefrig.2021.01.033openalex-extracted
Investigation on solid-liquid equilibrium for trifluoromethane (R23) plus difluoromethane (R32) binary system
inferredcites →https://doi.org/10.1016/j.jct.2008.06.002openalex-extracted
(Vapor + liquid) equilibrium data for (carbon dioxide + 1,1-difluoroethane) system at temperatures from (258 to 343) K and pressures up to about 8 MPa
inferredcites →https://doi.org/10.1016/j.jct.2015.08.038openalex-extracted
Experimental investigations for the phase equilibrium of R1234yf and R1234ze(E) with two linear chained pentaerythritol esters
inferredcites →https://doi.org/10.1016/j.jct.2017.04.020openalex-extracted
Measurement and correlation for phase equilibrium of HFO1234yf with three pentaerythritol esters from 293.15 K to 348.15 K
inferredcites →https://doi.org/10.1016/j.molliq.2018.07.056openalex-extracted
On the anomalous composition dependence of viscosity and surface tension in refrigerant blends
inferredcites →https://doi.org/10.1016/j.molliq.2023.123211openalex-extracted
Predicting the phase equilibria of refrigerant gas hydrate systems in the presence of electrolytes using molecular theory
inferredcites →https://doi.org/10.1016/j.supflu.2017.09.006openalex-extracted
Transport properties of HFC and HFO based refrigerants using an excess entropy scaling approach
inferredcites →https://doi.org/10.1016/s0140-7007(96)00076-xopenalex-extracted
Refrigerant conversion of auto-refrigerating cascade (ARC) systems
inferredcites →https://doi.org/10.1016/s0140-7007(97)00044-3openalex-extracted
The surface tension of HFC refrigerants and mixtures
inferredcites →https://doi.org/10.1016/s0378-3812(97)00257-4openalex-extracted
Vapor–liquid equilibria for the pure, binary and ternary systems containing HFC32, HFC125 and HFC134a
inferredcites →https://doi.org/10.1021/acs.iecr.1c03800openalex-extracted
Activity Coefficients from an Equation of State: Novel Approach for Fast Phase Equilibrium Calculations
inferredcites →https://doi.org/10.1021/acs.iecr.2c02896openalex-extracted
Beyond Flory–Huggins: Activity Coefficients from Perturbation Theory for Polar, Polarizable, and Associating Solvents to Polymers
inferredcites →https://doi.org/10.1021/acs.iecr.9b06821openalex-extracted
Solubility and Diffusivity of Hydrofluoroolefin Refrigerants in a Polyol Ester Lubricant
inferredcites →https://doi.org/10.1021/acs.jced.0c00682openalex-extracted
Thermal Conductivity of Pure Fluids and Multicomponent Mixtures Using Residual Entropy Scaling with PC-SAFT—Application to Refrigerant Blends
inferredcites →https://doi.org/10.1021/acs.jced.5b00082openalex-extracted
Solubility Measurement and Correlation of Isobutane with Two Pentaerythritol Tetraalkyl Esters between (293.15 and 348.15) K
inferredcites →https://doi.org/10.1021/acs.jced.5b00798openalex-extracted
Surface Tension and Liquid Viscosity of R32+R1234yf and R32+R1234ze
inferredcites →https://doi.org/10.1021/acs.jced.7b00950openalex-extracted
Vapor–Liquid Equilibria for the Binary and Ternary Systems of Difluoromethane (R32), 1,1-Difluoroethane (R152a), and 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf)
inferredcites →https://doi.org/10.1021/cr60137a013openalex-extracted
On the Thermodynamics of Solutions. V. An Equation of State. Fugacities of Gaseous Solutions.
inferredcites →https://doi.org/10.1021/ie0003887openalex-extracted
Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules
inferredcites →https://doi.org/10.1021/je010075yopenalex-extracted
Vapor−Liquid Equilibrium (VLE) Data for the Carbon Dioxide (CO2) + 1,1,1,2-Tetrafluoroethane (R134a) System at Temperatures from 252.95 K to 292.95 K and Pressures up to 2 MPa
inferredcites →https://doi.org/10.1021/je050281wopenalex-extracted
Vapor−Liquid Equilibrium Measurements for the Ethane + Hexafluoroethane System over a Temperature Range from (199.64 to 242.93) K
inferredcites →https://doi.org/10.1021/je0601107openalex-extracted
Vapor−Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K
inferredcites →https://doi.org/10.1021/je0603067openalex-extracted
Solid−Liquid Equilibria for the CO2 + R125 and N2O + R125 Systems: A New Apparatus
inferredcites →https://doi.org/10.1021/je7000182openalex-extracted
Surface Tension of the Ternary System Water + Acetone + Toluene
inferredcites →https://doi.org/10.1021/je700384eopenalex-extracted
Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems
inferredcites →https://doi.org/10.1021/je800285kopenalex-extracted
Solid−Liquid Equilibria for the Carbon Dioxide + 1,1-Tetrafluoroethane and Nitrous Oxide + 1,1-Tetrafluoroethane Systems
inferredcites →https://doi.org/10.1021/je980180gopenalex-extracted
Phase Equilibria of Chlorofluorocarbon Alternative Refrigerant Mixtures
inferredcites →https://doi.org/10.1023/a:1021983502589openalex-extracted
Molar Heat Capacity at Constant Volume of 1,1-Difluoroethane (R152a) and 1,1,1-Trifluoroethane (R143a) from the Triple-Point Temperature to 345 K at Pressures to 35 MPa
inferredcites →https://doi.org/10.1039/c6cp08031fopenalex-extracted
The phase and interfacial properties of azeotropic refrigerants: the prediction of aneotropes from molecular theory
inferredcites →https://doi.org/10.1039/c9cp03231bopenalex-extracted
Interfacial anomaly in low global warming potential refrigerant blends as predicted by molecular dynamics simulations
inferredcites →https://doi.org/10.1063/1.1675048openalex-extracted
Equilibrium Thermodynamic Properties of the Mixture of Hard Spheres
inferredcites →https://doi.org/10.1063/1.1701689openalex-extracted
Perturbation Theory and Equation of State for Fluids. II. A Successful Theory of Liquids
inferredcites →https://doi.org/10.1080/00268979909482832openalex-extracted
Application of Wertheim's thermodynamic perturbation theory to dipolar hard sphere chains
inferredcites →https://doi.org/10.1098/rspa.1932.0040openalex-extracted
The thermodynamics of the surfaces of solutions
inferredcites →https://doi.org/10.26678/abcm.encit2022.cit22-0487openalex-extracted
Phase Equilibrium Data for R-290 + POE ISO 32 Mixtures between 283.15 and 343.15 K
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