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MADANI Hakim
Enseignant Chercheur
Département de Mécanique
Faculté de Technologie
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2014
Fedali. S, Madani. H, Bougriou. C
.
Modeling of the Thermodynamic Properties of the Mixtures: Prediction of the Position of Azeotropes for Binary Mixtures
. Fluid Phase Equilbria. 2014;379 :120-127.
azeotropes_sf.pdf
2013
Madani. H, Valtz. A, Coquelet. C
.
Isothermal vapor-liquid equilibrium data for the decafluorobutane (R3110) + 1,1,1,3,3-pentafluorobutane (R365mfc) system at temperatures from 333 to 441 K
. Fluid Phase Equilibria [Internet]. 2013;354 :109-113.
Publisher's Version
r3110_r365mfc.pdf
2012
Madani. H, C.Coquelet., Richon. D
.
Vapor-liquid equilibrium data concerning refrigerant systems (R116 + R143a)
. Energy Procedia. 2012;18 :21-34.
r116_r143a_ep.pdf
2011
Laugier. S, Madani. H, Meniai. AH, Richon. D
.
Data Consistency Tests Through the Use of Neural Networks and Virial Equation. Application of the Proposed Methodology to Critical Study of Density data
. Open Journal of Physical Chemistry. 2011;1 :61-69.
ojpc_hm.pdf
2010
Coquelet. C, Ramjugernath. D, Madani. H, Valtz. A, Naidoo. P, Meniai. AH
.
Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
. J. Chem. Eng. Data. 2010;55 :2093-2099.
hfp_denismetre.pdf
2009
Madani. H, Valtz. A, Coquelet. C, Meniai. AH, Richon. D
.
Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1-tetrafluoroethane) binary system at temperatures from 258 to 343 K and pressures up to 3.89 MPa
. International Journal of refrigeration. 2009;32 :1396-1402.
r116_r143a.pdf
2008
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 253 to 353 K and pressures up to 4.16 MPa
. Fluid Phase Equilbria. 2008;273 :92.
fpe2.pdf
Madani. H, Valtz. A, Coquelet. C, Meniai. AH, Richon. D
.
Vapor-liquid equilibrium data for the (Carbob dioxide+ 1,1-difluoroethane) system at temperatures from 258 to 343 K and pressures up to 8 MPa
. J. Chem. Thermodynamics. 2008;40 :1490-1494.
co2_r152a-main.pdf
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 253 to 353 K and pressures up to 4.16 MPa
. Fluid Phase Equilibria. 2008;268 :68-73.
r116_r134a.pdf
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Recent Publications
Implementation of PC-SAFT for Predicting Thermodynamic Properties of Pure Refrigerants and Vapor-Liquid Equilibria of Refrigerants Binary Mixtures.
Calculation of azeotropic properties for binary mixtures with the PC-SAFT equation of state
Influence of azeotropic binary mixtures on single-stage refrigeration system performance
Method for Prediction of Liquid- Vapor Critical Points in Binary Mixtures: Geometrical-Eos model
Performance analysis of ternary azeotropic mixtures in different vapor compression refrigeration cycles
Performance analysis of ejector refrigeration cycle with zeotropic mixtures
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