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| 1 | 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 显示文摘 | Bobbo S Fedele L Camporese R | 2000 | Fluids Phase Equilibria2000，，： | 2 |
| 2 | Experimental evaluation of refrigerant mixtures as substitutes for CFC-12 and R502显示文摘 | Camporese R Bigolaro G Bobbo S | 1997 | International Journal of Refrig- eration1997，20，1： | 1 |
| 3 | Isothermal VLE measurements for the binary mixtures HFC134a + HFC236ea and HC600a + HFC236ea 显示文摘 | S Bobbo L Fedele M Scattolini | 2001 | Fluid Phase Equilibria2001，185，： | 1 |
| 4 | (P, p, T) behavior of 1,1,1,2,3,3,3 - heptafluoropropane (HFC - 227ea) at temperatures between 253 K and 403 K and pressures up to 20 MPa显示文摘 | Sealabrin G Bobbo S C houai A | 2002 | J Chem Eng Data2002，47，： | 1 |
| 5 | Isothermal VLE measurements for the binary mixtures HFC-134a + HFC-245fa and HC-600a +HFC-245{a 显示文摘 | Bobbo S Fedele L Scattolini M | 2001 | Fluid Phase Equilib2001，185，12： | 1 |
| 6 | Viscosity and thermal conductivity measurements of water based nanofluids containing titanium oxide nanoparticles 显示文摘 | FEDELE L COLLA L BOBBO S | 2012 | International Journal of Refrigeration Revue Internationale Du Froid2012，35，5： | 1 |
| 7 | 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 显示文摘 | Bobbo S Fedele L Scattolini M | 2004 | Fluid Phase Equilib2004，224，1： | 1 |
| 8 | 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 显示文摘 | Bobbo S Fedele L Camporese R | 2000 | Fluid Phase Equilib2000，174，： | 1 |
| 9 | Hydrogen- bonding of HFCs with dimethyl ether: evaluation by isothermal VLE measurements 显示文摘 | Bobbo S Fedele L Camporese R Stryjek R | 2002 | Fluid Phase Equilibria2002，199，12： | 1 |
| 10 | Isothermal vapour -- liquid equilibrium measurements and correlation for the dimethyl ether q- 1,1,1,2,3,3,3- heptafluoropropane and the propane nu 1, 1, 1,2, 3, 3, 3- heptafluoropropane systems 显示文摘 | Bobbo S Fedele L Scattolini M Camporese R Stryjek R | 2004 | Fluid Phase Equilibria2004，224，1： | 1 |
| 11 | Experiment evalu- ation of refrigerant mixtures as substitutes for CFCI2 and R502 显示文摘 | Camporese R Bigolaro G Bobbo S | 1997 | International Journal of Refrigeration1997，20，1： | 1 |
| 12 | A recirculation apparatus for vapor liquid equilibrium measurements of refrigerants:binary mixtures of R600a,R134a and R236fa显示文摘 | Bobbo S Stryjek R Elvassore N | 1998 | Fluid Phase Equilibria1998，，： | 1 |
| 13 | Isothermal VLE measurements for the binary mixtures HFC-134a+HFC-245fa and HC-600a+ HFC-245fa显示文摘 | Bobbo S Fedele L Scattolini M | 2001 | Fluid Phase Equilibria2001，185，： | 1 |
| 14 | High-pressurevapor-liquid equilibrium of binary systems with R236fa显示文摘 | Bobbo S Camporese R Stryjek R | 1999 | Fluid Phase Equilib1999，161，2： | 1 |
| 15 | (p,ρ,T) behavior of 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) at temperatures between 253 K and 403 K and pressures up to 20 MPa显示文摘 | Scalabrin G Bobbo S Chouai A | 2002 | J Chem Eng Data2002，47，2： | 1 |
| 16 | Isothermal VLE measurements for the binary mixtures HFC-134a+HFC-245fa and HFC-600a+HFC-245fa 显示文摘 | BOBBO S FEDELE L SCATTOLINI M | 2001 | Fluid Phase Equilibria2001，185，5： | 1 |
| 17 | Compressed Liquid Density Measurements for 1,1, !, 2,3,3,3-Hep- tafluoropropane (R227ea) 显示文摘 | Fedele L Pernechele F Bobbo S | 2007 | Journal of Chemical & Engineering Data2007，52，5： | 1 |
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