1 |
Flow boiling heat transfer, dry-out vapor quality and pressure drop of propane (R290): Experiments and assessment of predictive methods Lillo G, Mastrullo R, Mauro AW, Viscito L International Journal of Heat and Mass Transfer, 126, 1236, 2018 |
2 |
Measurements of isothermal (vapor plus liquid) equilibrium for the (propane + cis-1,3,3,3-tetrafluoropropene) system at temperatures from (253.150 to 293.150) K Gong MQ, Zhao YX, Dong XQ, Guo H, Shen J, Wu JF Journal of Chemical Thermodynamics, 98, 319, 2016 |
3 |
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 |
4 |
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 |
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Isothermal vapour plus liquid equilibrium measurements and correlation for the dimethyl ether+1,1,1,2,3,3,3-heptafluoropropane and the propane+1,1,1,2,3,3,3-heptafluoropropane systems Bobbo S, Fedele L, Scattolini M, Camporese R, Stryjek R Fluid Phase Equilibria, 224(1), 119, 2004 |
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Mutual solubility and VLLE correlation for the R32+R290 system Bobbo S, Fedele L, Camporese R, Scattolini M, Stryjek R Fluid Phase Equilibria, 212(1-2), 245, 2003 |
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Isothermal vapor-liquid equilibrium for the three binary systems 1,1,1,2,3,3-hexafluoropropane with dimethyl ether or propane, and 1,1,1,3,3,3-hexafluoropropane with dimethyl ether Bobbo S, Fedele L, Camporese R, Stryjek R Fluid Phase Equilibria, 174(1-2), 3, 2000 |
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(Vapour plus liquid) equilibrium measurement and correlation of the refrigerant (propane plus 1,1,1,3,3,3-hexafluoropropane) at T = (283.13, 303.19, and 323.26) K Bobbo S, Camporese R, Stryjek R Journal of Chemical Thermodynamics, 32(12), 1647, 2000 |