M.MEHEMMAI, Grine H, H. Madani, BOUGRIOU C. Performance analysis of ejector refrigeration cycle with zeotropic mixtures. International Journal of Thermofluid Science and Technology. 2023;10 (4) :1 - 17.

MAALEM Y, Tamene Y, H. Madani. Performances Investigation of the Eco-friendly Refrigerant R13I1 used as Working Fluid in the Ejector-Expansion Refrigeration Cycle. International Journal of Thermodynamics. 2023;26 (2) :25-35.

ABDOU C, H. Madani, HESSEINE A. Study of the performances of an ejector refrigeration cycle using CO₂ based mixtures in subcritical and transcritical mode. International Journal of Thermofluid Science and Technology. 2023;10 (3) :1-16.

Zerfa A, MAALEM Y, H. Madani, A.BEICHA. Modelling of the Isothermal Vapor-Liquid Equilibrium ofAlternative Refrigerants: Determination of Phase Diagrams(High-pressure/Low-pressure) and Optimized Binary InteractionParameters. Journal of Pakistan Institute of Chemical Engineers. 2023;51 (1) :39-58.

MAALEM Y, H. Madani, M.MEHEMMAI. Modélisation Mathématique et Simulation Numérique des Performances de Refroidissement de Différentes Unités de Réfrigération à Compression de Vapeur - Application de Nouveaux Fluides Frigorigènes. Revue des Sciences et Science de l'ingénieur. 2023;10 (01) :21 - 39.

Mimoune Z, Anoune. I, MADANI H. Implementation of PC-SAFT for Predicting Thermodynamic Properties of Pure Refrigerants and Vapor-Liquid Equilibria of Refrigerants Binary Mixtures. Fluid Phase Equilibria. 2023;573 (113868) :1 -24.

MAALEM Y, Tamene Y, H. Madani. Modeling of the Vapor-Liquid Equilibria Properties of Binary Mixtures for Refrigeration Machinery. International Journal of Thermodynamics. 2023 :1-12.

BENTAMA B, GRINE H, ANOUNE I, MADANI H, Bougriou C. Calculation of azeotropic properties for binary mixtures with the PC-SAFT equation of state. Fluid PhaseEquilibria. 2023;565 (113631).

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