H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase Equilib. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase EquilibFluid Phase Equilib. 2008;273 :page 92.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase Equilib. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase EquilibFluid Phase Equilib. 2008;273 :page 92.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase Equilib. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase EquilibFluid Phase Equilib. 2008;273 :page 92.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase Equilib. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase EquilibFluid Phase Equilib. 2008;273 :page 92.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase Equilib. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH, Richon D. Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase EquilibFluid Phase Equilib. 2008;273 :page 92.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH. Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa,. Fluid phase equilibriaFluid Phase Equilibria. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH. Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa,. Fluid phase equilibriaFluid Phase Equilibria. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH. Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa,. Fluid phase equilibriaFluid Phase Equilibria. 2008;268 :68-73.

H. Madani, Valtz A, C.Coquelet, D. Ramjugernath, MENIAI AH. Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa,. Fluid phase equilibriaFluid Phase Equilibria. 2008;268 :68-73.

MADANI H, Valtz A, Coquelet C, Meniai AH, Richon D. Vapor–liquid equilibrium data for the (hexafluoroethane+ 1, 1, 1, 2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa. Fluid Phase EquilibriaFluid Phase Equilibria. 2008;268 :68-73.

MADANI H, Valtz A, Coquelet C, Meniai AH, Richon D. Vapor–liquid equilibrium data for the (hexafluoroethane+ 1, 1, 1, 2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa. Fluid Phase EquilibriaFluid Phase Equilibria. 2008;268 :68-73.

MADANI H, Valtz A, Coquelet C, Meniai AH, Richon D. Vapor–liquid equilibrium data for the (hexafluoroethane+ 1, 1, 1, 2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa. Fluid Phase EquilibriaFluid Phase Equilibria. 2008;268 :68-73.

MADANI H, Valtz A, Coquelet C, Meniai AH, Richon D. Vapor–liquid equilibrium data for the (hexafluoroethane+ 1, 1, 1, 2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa. Fluid Phase EquilibriaFluid Phase Equilibria. 2008;268 :68-73.

MADANI H, Valtz A, Coquelet C, Meniai AH, Richon D. Vapor–liquid equilibrium data for the (hexafluoroethane+ 1, 1, 1, 2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa. Fluid Phase EquilibriaFluid Phase Equilibria. 2008;268 :68-73.

Slimen MH, Fakhfakh H, Gassara M, Kechaou S, Bahloul A, MHIRI MOHAMEDNABIL. Venous priapism: Treatment and prognosis based on a series of 26 cases. BASIC AND CLINICAL ANDROLOGYBASIC AND CLINICAL ANDROLOGY. 2008;18 :264-273.