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Results: 1-9 |
Results: 9
Isothermal VLE measurements for the binary mixtures HFC-134a+HFC-245fa andHC-600a+HFC-245fa
Authors: Bobbo, S Fedele, L Scattolini, M Camporese, R
Citation: S. Bobbo et al., Isothermal VLE measurements for the binary mixtures HFC-134a+HFC-245fa andHC-600a+HFC-245fa, FLU PH EQUI, 185(1-2), 2001, pp. 255-264
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
Authors: Bobbo, S Fedele, L Camporese, R Stryjek, R
Citation: S. Bobbo et al., 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, FLU PH EQUI, 174(1-2), 2000, pp. 3-12
Vapor plus liquid equilibrium measurements and correlation of the binary refrigerant mixtures difluoromethane (HFC-32)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroethane (HFC-125)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) at 288.6, 303.2, and 318.2 K
Authors: Bobbo, S Fedele, L Scattolini, M Camporese, R
Citation: S. Bobbo et al., Vapor plus liquid equilibrium measurements and correlation of the binary refrigerant mixtures difluoromethane (HFC-32)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) and pentafluoroethane (HFC-125)+1,1,1,2,3,3-hexafluoropropane (HFC-236ea) at 288.6, 303.2, and 318.2 K, INT J THERM, 21(3), 2000, pp. 781-791
(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
Authors: Bobbo, S Camporese, R Stryjek, R
Citation: S. Bobbo et al., (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, J CHEM THER, 32(12), 2000, pp. 1647-1656
Vapor-liquid equilibrium for dimethyl ether and 2-methylpropane
Authors: Bobbo, S Camporese, R Stryjek, R Malanowski, SK
Citation: S. Bobbo et al., Vapor-liquid equilibrium for dimethyl ether and 2-methylpropane, J CHEM EN D, 45(5), 2000, pp. 829-832
Isothermal vapor-liquid equilibria for the binary system 1,1,1-trifluoroethane (R143a)+1,1,1,3,3,3-hexafluoropropane (R236fa) at 283.11, 298.16, and 313.21 K
Authors: Bobbo, S Camporese, R Zilio, C
Citation: S. Bobbo et al., Isothermal vapor-liquid equilibria for the binary system 1,1,1-trifluoroethane (R143a)+1,1,1,3,3,3-hexafluoropropane (R236fa) at 283.11, 298.16, and 313.21 K, J CHEM EN D, 45(2), 2000, pp. 276-279
High-pressure vapor-liquid equilibrium of binary systems with R236fa
Authors: Bobbo, S Camporese, R Stryjek, R
Citation: S. Bobbo et al., High-pressure vapor-liquid equilibrium of binary systems with R236fa, FLU PH EQUI, 161(2), 1999, pp. 305-313
Gas chromatographic measurements of activity coefficients at infinite dilution for refrigerants with a polyol ester oil as a stationary phase
Authors: Stryjek, R Bobbo, S Camporese, R Zilio, C
Citation: R. Stryjek et al., Gas chromatographic measurements of activity coefficients at infinite dilution for refrigerants with a polyol ester oil as a stationary phase, J CHEM EN D, 44(3), 1999, pp. 568-573
Vapor-liquid equilibria for difluoromethane (R32) plus and pentafluoroethane (R125) plus 1,1,1,3,3,3-hexafluoropropane (R236fa) at 303.2 and 323.3 K
Authors: Bobbo, S Camporese, R Stryjek, R
Citation: S. Bobbo et al., Vapor-liquid equilibria for difluoromethane (R32) plus and pentafluoroethane (R125) plus 1,1,1,3,3,3-hexafluoropropane (R236fa) at 303.2 and 323.3 K, J CHEM EN D, 44(2), 1999, pp. 349-352
Risultati: 1-9 |