MAALEM Y, Zerfa A, M.MEHEMMAI, H. Madani, FEDALI S. Study of the performance of a refrigeration cycle without and with ejector using ternary azeotropic refrigerants. Journal of New Technology and Materials . 2022;12 (01) :25-31.

BENBIA L, Fedali S, Bougriou C, Madani. H. Influence of azeotropic binary mixtures on single-stage refrigeration system performance. High temperature High Pressure. 2022;54 (4) :319-339.

Maalem. Y, Tamene Y, H. Madani. Behavior of the thermo-physical properties andperformance evaluation of the refrigerants blends (Fluorocarbon/hydrocarbon) forcooling cycle. RDM. 2022;6 (1) :544-559.

GRINE H, Madani. H. Method for Prediction of Liquid- Vapor Critical Points in Binary Mixtures: Geometrical-Eos model. High temperature High Pressure. 2022;51 (1) :63-82.

Anoune. I, Mimoune. Z, Madani. H, Merzougui. A. New modified PC-SAFT pure component parameters for accurate VLE and critical phenomena description. Fluid Phase Equilibria. 2021;532 (112916).

Maalem. Y, Fedali. S, Madani. H, Tamene Y. Performance analysis of ternary azeotropic mixtures in different vapor compression refrigeration cycles. International Journal of refrigeration. 2020;119 :139-151.

Maalem Y, Zerfa A, Tamene Y, Fedali S, Madani. H. Prediction of thermodynamic properties of the ternary azeotropic mixtures. Fluid Phase Equilibria. 2020;517 (112613).

Grine H, Madani. H, Fedali. S. Critical behaviour of binary mixtures : calculation by the Heidemann-Khalil Method. High tempertaure High Pressure. 2019;48 :497-525.

Maalem. Y, Fedali. S, Madani. H. Modeling of thermodynamic properties of binary and ternary mixtures. Determination of phase digrams. J. Recueil de Mécanique. 2019;4 (1) :326-334.

Fedali. S, Madani. H, Bougriou. C. Prediction method of both azeotropic and critical points of the binary refrigerant mixtures. J. Appl. Eng. Sci. Technol. 2017;3 :37-41.

Fedali. S, Madani. H. Azeotropic points with relative volatility-prediction and calculation. Mathematical Modelling of Engineering Problems. 2017;4 :38-42.

Madani. H, Valtz. A, Zhang. F, Abbadi. J, Houriez. C, Paricaud. P, C.Coquelet. Isothermal vapor–liquid equilibrium data for the trifluoromethane (R23) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) system at temperatures from 254 to 348 K. Fluid Phase Equilibria. 2016;415 :158-165. r23_r1234yf.pdf

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

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

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

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

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

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

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