Critical point and saturation pressure calculations for multicomponents systems, Soc. Petrol. Eng. J, 1978. ,
DOI : 10.2118/7478-pa
Gibbs Energy Analysis of Phase Equilibria, Society of Petroleum Engineers Journal, vol.22, issue.05 ,
DOI : 10.2118/9806-PA
Computer aided chemical thermodynamics of gases and liquids, Theory, Models, Programs, 1985. ,
The coexistence curve in liquid-liquid binary systems, Transactions of the Faraday Society, vol.52, pp.926-956, 1956. ,
DOI : 10.1039/tf9565200926
Institute for Physical Property Data, Data compilation of pure compound properties, 1985. ,
Liquid liquid Equilibrium, Inter Science, 1963. ,
CRITICAL SOLUTION TEMPERATURES, Copyright, ADVANCES IN CHEMISTRY SERIES, Am. Chem. Soc, vol.32, 1961. ,
DOI : 10.1021/ba-1961-0031.fw001
A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties, Industrial & Engineering Chemistry Research, vol.32, issue.1, pp.178-193, 1993. ,
DOI : 10.1021/ie00013a024
A Modified UNIFAC (Dortmund) Model. 3. Revision and Extension, ) Model. 3. Revision and Extension, pp.4876-4882, 1998. ,
DOI : 10.1021/ie980347z
The calculation of critical points, AIChE Journal, vol.26, issue.5, pp.769-779, 1980. ,
DOI : 10.1002/aic.690260510
Les méthodes de calcul sur ordinateurs appliquées au raffinage et à la pétrochimie, Collectif, Editions TECHNIP, 1969. ,
A modified UNIFAC group-contribution model for prediction of phase equilibria and heats of mixing, Industrial & Engineering Chemistry Research, vol.26, issue.11, pp.2274-2286, 1987. ,
DOI : 10.1021/ie00071a018
Measurement and Correlation of Mutual Solubilities for High-Viscosity Binary Systems:??? Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol, Journal of Chemical & Engineering Data, vol.48, issue.4, pp.1076-1080, 2003. ,
DOI : 10.1021/je034043h
The isothermal flash problem. Part I, Stability, Fluid phase equilibria, pp.1-19, 1982. ,
The isothermal flash problem. Part II, Phase-Split calculation, Fluid phase equilibria, pp.21-40, 1982. ,
Properties of gases and liquids, 2000. ,
Molecular thermodynamics of fluidphase equilibria, pp.260-261, 1968. ,
The properties of gases and liquids, -, 5 éme Edition, 2001. ,
Local compositions in thermodynamic excess functions for liquid mixtures, AIChE Journal, vol.14, issue.1, pp.135-144, 1968. ,
DOI : 10.1002/aic.690140124
Critical data of pure substances, Dechema, pp.3-921567, 1986. ,
Liquid Liquid Equilibrium Data Collection, Binary Systems, part 1 of Chemistry Data Series, 1979. ,
Application au génie chimique et à l'industrie pétrolière, 1997. ,
48 IV.1. Etat de référence, 50 IV.2. Calcul des propriétés des corps purs, p.51 ,
74 III.3. Coefficient de performance (COP), p.79 ,
84 a) Description et bilans 84 b) Construction de PONCHON, 86 c) Recherche des points limites de, p.91 ,
104 IV.2. Cycle avec récupération interne de chaleur 106 III.1. Representation du cycle simple sur les diagrammes température-composition (Tx ,y) et enthalpie-composition (H-x,y) 116 III.2. Representation du Cycle modifie sur les diagrammes température-composition (Tx ,y) et enthalpie-composition (H-x,y), IV.1. Cycle sans récupération interne, p.118 ,
118 III.3.2. Saut thermique interne maximal (?T i max ), III.3.1. Saut thermique interne (?T i ) ? Rendement thermique, p.120 ,
124 IV.2. Influence de la température de démixtion (T démix ) sur le saut tHermique interne maximal (?T i max ), p.126 ,
132 II.1.2. Capacité calorifique du gaz parfait (Cp gi ), p.136 ,
137 II.2. Variation des propriétés de corps purs pour le cycle modifié, p.140 ,
155 IV.2.1. Variation simultanée des enthalpies de vaporisation (Lv i ) et des paramètres Variation simultanée des paramètres d'interaction (b 12 , b 21 et ?) et Lv i et Cp li .... 156 IV.3. Influence de la variation simultanée des paramètres d'ELL et d'ELV sur les deux types de cycle, Chapitre III. Thermo Transformateur à Absorption-Démixtion : Principe et outil de simulation IV.2. Variations simultanée des paramètres de l'équilibre................. 161 III.2. SELECTION DES MELANGES à ETUDIER ................................................... 162 IV.1. Comparaison des performances maximales des deux types de cycle 164 IV.2. Performances du cycle modifié pour des conditions opératoires fixées, p.168 ,
231 II. Données d'équilibre liquide-liquide, p.231 ,
Thermo-transformateur à absorption?démixtion: Expérimentation et Optimisation ,
Performance simulation of an absorption heat transformer operating with partially miscible mixtures, Applied Energy, vol.72, issue.3-4, pp.583-597, 2002. ,
DOI : 10.1016/S0306-2619(02)00052-1
Experimental study of an innovative absorption heat transformer using partially miscible working mixtures, International Journal of Thermal Sciences, vol.42, issue.6, pp.631-638, 2003. ,
DOI : 10.1016/S1290-0729(03)00028-0
The coexistence curve in liquid-liquid binary systems, Transactions of the Faraday Society, vol.52, pp.926-956, 1956. ,
DOI : 10.1039/tf9565200926
Vapor-Liquid Equilibrium data collection, Chemistry data series, 1981. ,
Liquid Liquid Equilibrium Data Collection, Binary Systems, 1979. ,
A novel absorption-cycle heat-pump, pp.355-367, 1994. ,
DOI : 10.1016/0306-2619(94)90043-4
174 II.1. Description de l'installation 175 II.1.1. Colonne de rectification inverse, p.177 ,
179 II.2.1. Capteurs de température, p.179 ,
191 IV.1. Mode opératoire, Paramères 191 IV.2. Exploitation des enregistrements des mesures expérimentales, . ,
Exemple de résultats : représentation des différentes phases sur le diagramme d'équilibre de la puissance fournie à l'évaporateur sur le rendement thermique, 210 IV.5.3. Comparaison des performances expérimentales et simulées............................ 213 IV.5.4. Détermination du nombre d'étages théoriques de la colonne (NET), p.215 ,
Salt effects on liquid liquid equilibria in partially miscible systems water+2 butanone and water +ethyl acetate, Fluid Phase Equilibria, pp.271-283, 1999. ,
Salt Effects on Liquid???Liquid Equilibrium in Water + Ethanol + Alcohol + Salt Systems, Journal of Chemical & Engineering Data, vol.45, issue.6, pp.1055-1059, 2000. ,
DOI : 10.1021/je000029i
Phase equilibria of the water sodium chloride Trielethylamine system, Journal of Chemical and Engineering Data, vol.21, issue.3, 1976. ,
Influence of temperature on the liquid-liquid equilibrium of the water-n-butyl alcohol-sodium chloride system, Journal of Chemical & Engineering Data, vol.21, issue.3, pp.324-327, 1976. ,
DOI : 10.1021/je60070a008
Salting effect in partially miscible systems of n-butanol???water and butanone???water 1. Determination and correlation of liquid-liquid equilibrium data, Fluid Phase Equilibria, vol.103, issue.1, pp.143-153, 1995. ,
DOI : 10.1016/0378-3812(94)02615-8
Prediction of liquid???liquid equilibria for PEG 2000???sodium citrate based aqueous two-phase systems, Fluid Phase Equilibria, vol.244, issue.1, pp.52-61, 2006. ,
DOI : 10.1016/j.fluid.2006.03.008
Graphical Concepts To Orient the Minimum Reflux Ratio Calculation on Ternary Mixtures Distillation, Industrial & Engineering Chemistry Research, vol.39, issue.10, pp.3912-3919, 2000. ,
DOI : 10.1021/ie9907021
The influence of salts on the phase composition in aqueous two-phase: experiments and predictions, Fluid Phase Equilibria 187-188, pp.489-498, 2001. ,
Salt effect on liquid???liquid equilibrium of water+1-butanol+acetone system: experimental determination and thermodynamic modeling, Fluid Phase Equilibria, vol.187, issue.188, pp.187-188, 2001. ,
DOI : 10.1016/S0378-3812(01)00541-6
Liquid liquid equilibria of water/acetic acid/1-butanol system effects of sodium (potassium) chloride and correlations, Fluid Phase Equilibria, pp.243-257, 1999. ,
Coexistence curves of the binary mixture isobutyric acid???water with added ions (K+,Cl???), Chemical Physics Letters, pp.567-573, 2002. ,
DOI : 10.1016/S0009-2614(02)01107-7
Modeling phase equilibria and speciation in mixed-solvent electrolyte systems: II. Liquid???liquid equilibria and properties of associating electrolyte solutions, Journal of Molecular Liquids, vol.125, issue.1, pp.37-44, 2006. ,
DOI : 10.1016/j.molliq.2005.11.030
Liquid liquid equilibria of aqueous two-phase systems containing plyethylene glycol and sodium succinate or sodium formate, Computer Coupling of Phase Diagrams and Thermochemistry, pp.1-6, 2005. ,
Initialisation de T bulle : T bulle = ? T eb i . x i Initialisation de coefficients d ,
Initialisation de T bulle : T bulle = ? T eb i . x i Initialisation de coefficients d ,
258 PARTIE 2 : INFLUENCE, p.258 ,
Enjeux énergétiques et environnementaux des pompes à chaleur Figure 1 : Consommation mondiale d'énergie primaire en, 1971. ,