21 results on '"Madani, Hakim"'
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2. Performances Investigation of the Eco-friendly Refrigerant R13I1 used as Working Fluid in the Ejector-Expansion Refrigeration Cycle
3. Modeling of the Vapor-Liquid Equilibria Properties of Binary Mixtures for Refrigeration Machinery
4. Calculation of azeotropic properties for binary mixtures with the PC-SAFT equation of state
5. Influence of azeotropic binary mixtures on single-stage refrigeration system performance
6. Method for prediction of liquid-vapor critical points in binary mixtures: geometrical-EOS model
7. New modified PC-SAFT pure component parameters for accurate VLE and critical phenomena description
8. Performance analysis of ternary azeotropic mixtures in different vapor compression refrigeration cycles
9. Prediction of thermodynamic properties of the ternary azeotropic mixtures
10. Critical behaviour of binary mixtures: Calculation by the Heidemann-Khalil method
11. Azeotropic points with relative volatility-prediction and calculation
12. 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
13. Modeling of the thermodynamic properties of the mixtures: Prediction of the position of azeotropes for binary mixtures
14. Isothermal vapor–liquid equilibrium data for the decafluorobutane (R3110)+1,1,1,3,3-pentafluorobutane (R365mfc) system at temperatures from 333K to 441K
15. Vapor-liquid Equilibrium Data Concerning Refrigerant Systems (R116 + R143a)
16. Data Consistency Tests through the Use of Neural Networks and Virial Equation. Application of the Proposed Methodology to Critical Study of Density Data
17. Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
18. Vapor–liquid equilibria of the (hexafluoroethane+1,1,1-trifluoroethane) binary system from 258 to 343K up to 3.89MPa
19. Erratum to “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 Equilib. 268 (2008) 68–73]
20. (Vapor+liquid) equilibrium data for (carbon dioxide+1,1-difluoroethane) system at temperatures from (258 to 343)K and pressures up to about 8MPa
21. Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
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