Drupal-Biblio17<style face="normal" font="default" size="100%">DESIGN AND ENERGY ANALYSIS OF A MODIFIED ECO-FRIENDLY COMBINED CYCLE FOR ENHANCED WASTE HEAT RECOVERY UTILIZATION</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performance indicators investigation oftwo configurations of combined power-cooling system activated by low-gradethermal energy: Improved design andcomparative analysis</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Introducing and investigation of novel energy systempowered by geothermal energy: Thermodynamic modelingand energy analysis</style>Drupal-Biblio17<style face="normal" font="default" size="100%">An influence study of nitrous oxide gas on performance behavior of transcritical single-stage cooling systems</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Enhancement of the capabilities of energy andexergy efficiencies of low cascade cooling process</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performance Investigation of an Automotive Hybrid Air-Conditioning System without and with an Internal Heat Exchanger (IHX) using R1234ze(E) as Substitute for R134a</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performance Characteristics Investigation of a Solar Rankine Cycle Powered Air Conditioning System for Residential Buildings using Low GWP Working Fluids</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Analysis of Thermodynamic Models for Liquid-Vapor Equilibrium: Evaluating Accuracy and Applicability</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Thermodynamic Efficiency Analysis of a Combined Power and Cooling (ORC-VCRC) System Using Cyclopentane (C5H10) as a Substitute for Conventional Hydrocarbons</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performances Study of Eco-friendly Binary Azeotropic Mixtures Used as Working Fluid in Three Refrigeration Cycles</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Calculation of Azeotropic Properties for Ternary Mixtures with the PC-SAFT Equation os State</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Energetic performance investigation of ejector air conditioning cycles using the environment friendly gas R161 (Fluoroethane) as substitue to the phase - out R22 (Chlorodifluoromethane) </style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performance analysis of ejector refrigeration cycle with zeotropic mixtures</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performances Investigation of the Eco-friendly Refrigerant R13I1 used as Working Fluid in the Ejector-Expansion Refrigeration Cycle</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Study of the performances of an ejector refrigeration cycle using CO<sub>2</sub> based mixtures in subcritical and transcritical mode</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Modelling of the Isothermal Vapor-Liquid Equilibrium ofAlternative Refrigerants: Determination of Phase Diagrams(High-pressure/Low-pressure) and Optimized Binary InteractionParameters</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Modélisation Mathématique et Simulation Numérique des Performances de Refroidissement de Différentes Unités de Réfrigération à Compression de Vapeur - Application de Nouveaux Fluides Frigorigènes</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Implementation of PC-SAFT for Predicting Thermodynamic Properties of Pure Refrigerants and Vapor-Liquid Equilibria of Refrigerants Binary Mixtures.</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Modeling of the Vapor-Liquid Equilibria Properties of Binary Mixtures for Refrigeration Machinery</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Calculation of azeotropic properties for binary mixtures with the PC-SAFT equation of state</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Study of the performance of a refrigeration cycle without and with ejector using ternary azeotropic refrigerants</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Influence of azeotropic binary mixtures on single-stage refrigeration system performance</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Behavior of the thermo-physical properties andperformance evaluation of the refrigerants blends (Fluorocarbon/hydrocarbon) forcooling cycle</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Method for Prediction of Liquid- Vapor Critical Points in Binary Mixtures: Geometrical-Eos model</style>Drupal-Biblio17<style face="normal" font="default" size="100%">New modified PC-SAFT pure component parameters for accurate VLE and critical phenomena description</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Performance analysis of ternary azeotropic mixtures in different vapor compression refrigeration cycles</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Prediction of thermodynamic properties of the ternary azeotropic mixtures</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Critical behaviour of binary mixtures : calculation by the Heidemann-Khalil Method</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Modeling of thermodynamic properties of binary and ternary mixtures. Determination of phase digrams</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Prediction method of both azeotropic and critical points of the binary refrigerant mixtures</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Azeotropic points with relative volatility-prediction and calculation</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Isothermal vapor&ndash;liquid equilibrium data for the trifluoromethane (R23) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) system at temperatures from 254 to 348 K</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Modeling of the Thermodynamic Properties of the Mixtures: Prediction of the Position of Azeotropes for Binary Mixtures</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Isothermal vapor-liquid equilibrium data for the decafluorobutane (R3110) + 1,1,1,3,3-pentafluorobutane (R365mfc) system at temperatures from 333 to 441 K</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Vapor-liquid equilibrium data concerning refrigerant systems (R116 + R143a)</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Data Consistency Tests Through the Use of Neural Networks and Virial Equation. Application of the Proposed Methodology to Critical Study of Density data</style>Drupal-Biblio17<style face="normal" font="default" size="100%">Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene</style>Drupal-Biblio17<style face="normal" font="default" size="100%">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</style>Drupal-Biblio17<style face="normal" font="default" size="100%">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</style>Drupal-Biblio17<style face="normal" font="default" size="100%">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</style>Drupal-Biblio17<style face="normal" font="default" size="100%">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</style>