| 1 |
A new three-parameter corresponding states model for pure halocarbons viscosity prediction
Scalabrin G, Cristofoli G, Grigiante M
Chemical Engineering Communications, 189(12), 1705, 2002 |
| 2 |
A corresponding states thermodynamic model for pure and mixed refrigerants in terms of the Helmholtz energy
Scalabrin G, Piazza L, Cristofoli G
Fluid Phase Equilibria, 199(1-2), 79, 2002 |
| 3 |
A viscosity equation of state for R134a through a multi-layer feedforward neural network technique
Cristofoli G, Piazza L, Scalabrin G
Fluid Phase Equilibria, 199(1-2), 223, 2002 |
| 4 |
Viscosity equations of pure fluids in an innovative extended corresponding states framework I. Modelling techniques
Scalabrin G, Cristofoli G, Richon D
Fluid Phase Equilibria, 199(1-2), 265, 2002 |
| 5 |
Viscosity equations of pure fluids in an innovative extended corresponding states framework II. Application to four fluids
Scalabrin G, Cristofoli G, Richon D
Fluid Phase Equilibria, 199(1-2), 281, 2002 |
| 6 |
A corresponding states predictive viscosity model based on a new scaling parameter: application to hydrocarbons, halocarbons and mixtures
Scalabrin G, Cristofoli G, Grigiante M
International Journal of Energy Research, 26(1), 1, 2002 |
| 7 |
A corresponding states predictive model for the saturated liquid density of halogenated alkanes and of fluorinated propanes and ethers
Cristofoli G, Grigiante M, Scalabrin G
Fluid Phase Equilibria, 170(1), 23, 2000 |
| 8 |
Prediction of halocarbon mixture thermodynamics using an innovative g(E)-EoS mixing rule in a three-parameter CS framework
Scalabrin G, Cristofoli G, Grigiante M
Fluid Phase Equilibria, 174(1-2), 143, 2000 |
