1 |
Liquid viscosity of low-GWP refrigerant mixtures (R32+R1234yf) and (R125+R1234yf) Dang YG, Kamiaka T, Dang CB, Hihara E Journal of Chemical Thermodynamics, 89, 183, 2015 |
2 |
Prediction of isoenthalps, Joule-Thomson Coefficients and Joule-Thomson inversion curves of refrigerants by molecular simulation Figueroa-Gerstenmaier S, Lisal M, Nezbeda I, Smith WR, Trejos VM Fluid Phase Equilibria, 375, 143, 2014 |
3 |
Power-based performance comparison between carbon dioxide and R125 transcritical cycles for a low-grade heat source Baik YJ, Kim M, Chang KC, Kim SJ Applied Energy, 88(3), 892, 2011 |
4 |
Isothermal vapor-liquid equilibria for the pentafluoroethane plus propane and pentafluoroethane+1,1,1,2,3,3,3-heptafluoropropane systems Hou SX, Duan YY Fluid Phase Equilibria, 290(1-2), 121, 2010 |
5 |
Vapor-liquid equilibrium measurement and modeling for the difluoromethane plus pentafluoroethane plus propane ternary mixture Hou SX, Duan YY Fluid Phase Equilibria, 298(1), 106, 2010 |
6 |
Isothermal vapour plus liquid equilibrium measurements and correlation for the pentafluoroethane plus cyclopropane and the cyclopropane plus 1,1,1,2-tetrafluoroethane binary systems Fedele L, Bobbo S, Camporese R, Scattolini M Fluid Phase Equilibria, 251(1), 41, 2007 |
7 |
Vapour-liquid equilibrium measurements and correlation for the pentafluoroethane (R125)+n-butane (R600) system Fedele L, Bobbo S, Camporese R, Stryjek R Fluid Phase Equilibria, 227(2), 275, 2005 |
8 |
VLLE measurements and correlation for the pentafluoroethane (R125)+n-butane (R600) system Fedele L, Bobbo S, Camporese R, Stryjek R Fluid Phase Equilibria, 222, 283, 2004 |
9 |
Use of artificial neural networks for calculating derived thermodynamic quantities from volumetric property data Laugier S, Richon D Fluid Phase Equilibria, 210(2), 247, 2003 |
10 |
PVTx measurements for the R125+CO2 system by the Burnett method Di Nicola G, Giuliani G, Polonara F, Stryjek R Fluid Phase Equilibria, 199(1-2), 161, 2002 |