Добірка наукової літератури з теми "Equilibre Vapeur-Liquide"
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Статті в журналах з теми "Equilibre Vapeur-Liquide":
Michou-Saucet, Marie-Annie, Jacques Jose, and Christian Michou-Saucet. "Equilibre liquide-vapeur isotherme des systèmes hexamethylphosphorotriamide-benzène et hexamethylphosphorotriamide-toluène." Thermochimica Acta 158, no. 2 (March 1990): 247–57. http://dx.doi.org/10.1016/0040-6031(90)80072-7.
Michou-Saucet, Marie-Annie, Jacques Jose, and Christian Michou-Saucet. "Equilibre liquide-vapeur isotherme des systemes pyridine-n-hexane et pyridine-n-heptane." Thermochimica Acta 102 (June 1986): 271–79. http://dx.doi.org/10.1016/0040-6031(86)85335-7.
Belaribi, F. B., G. Belaribi-Boukais, A. Ait-Kaci, and J. Jose. "Equilibres liquide-vapeur isothermes de melanges binaires formes de composes heterocycliques tels que: Morpholine, tetrahydropyranne, piperidine et 1,4-dioxane." Journal of Thermal Analysis 44, no. 4 (April 1995): 911–27. http://dx.doi.org/10.1007/bf02547275.
Belaribi, F. B., A. Ait-Kaci, and J. Jose. "Equilibres liquide-vapeur isothermes de melanges binaires de la piperidine et de la N-methyl piperidine avec certains ethers." Journal of Thermal Analysis 44, no. 5 (May 1995): 1177–94. http://dx.doi.org/10.1007/bf02547548.
Belaribi, F. B., A. Ait-Kaci, and J. Jose. "Equilibres liquide-vapeur isothermes de melanges binaires de la piperidine et de la N-methyl piperidine avec certains ethers." Journal of Thermal Analysis 46, no. 1 (January 1996): 245–61. http://dx.doi.org/10.1007/bf01979965.
Дисертації з теми "Equilibre Vapeur-Liquide":
Ammar, Mohamed Naceur. "Modélisation d'opérations unitaires et méthodes numériques de calcul d'équilibre liquide-vapeur." ENMP, 1986. http://www.theses.fr/1986ENMP0002.
SOLASTIOUK, GALIVEL FRANCINE. "Equilibres liquide-vapeur des systemes propane-methanol et propane-methanol-dioxyde de carbone : mesures et representations." Paris, ENMP, 1988. http://www.theses.fr/1988ENMP0103.
Mokraoui, Salim. "Mesures et modélisation des solubilités mutuelles dans les systèmes aqueux hydrocarbures - alcanolamines." Phd thesis, École Nationale Supérieure des Mines de Paris, 2006. http://pastel.archives-ouvertes.fr/pastel-00002487.
Coquelet, Christophe. "Etude des fluides frigorigéniques : mesures et modélisations." Paris, ENMP, 2003. https://pastel.archives-ouvertes.fr/pastel-00000991.
Sadli, Mohammad. "Equilibre liquide-vapeur du potassium dans un four caloduc contrôle en pression : vers une référence secondaire de température entre 600 et 840c." Paris, CNAM, 1997. http://www.theses.fr/1997CNAM0301.
Riva, Mauro. "Procédés de purification du biométhane : étude thermodynamique des équilibres solide-liquide-vapeur de mélanges riches méthane." Thesis, Paris Sciences et Lettres (ComUE), 2016. http://www.theses.fr/2016PSLEM098.
In the field of non-fossil energy sources and exploitation of wasted energies, this PhD project aims to improve the availability of the alternative and renewable resource that is the upgraded biogas, also calledbiomethane. A particular type of biogas is here studied: landfill gas, produced in landfills from the anaerobic digestion of wastes. Depending on the final use, landfill gas need to be treated in order to remove impurities and increase the methane content (upgrading). Carbon dioxide (CO2 ), nitrogen (N2 ) and oxygen (O2 ) need thus to be separated from methane. Because upgrading process is fundamental for further applications of the landfill gas, suitable separationtechniques have to be studied. The objective of the thesis is the study and simulation of an optimized cryogenic technology applied to a landfill upgrading process. The base of the study is the knowledge of the thermodynamic behavior of mixtures constituted of methane and minor compositions of N2 , O2 andCO2 . At this purpose, thermodynamic model will be developed for determining the phase diagrams of methane with the other gases present in the landfill gas. Moreover, in order to validate and calibrate the thermodynamic models, phase equilibrium data involving a CO2 solid phase are needed: an extended bibliographic research on existing data is performed and original measurements are provided where data from literature are missing
Campestrini, Marco. "Étude thermodynamique des équilibres solide-liquide-vapeur : application à la cryogénie et aux unités de séparation de l’air." Thesis, Paris, ENMP, 2014. http://www.theses.fr/2014ENMP0035/document.
In the framework of the cryogenic air separation, impurities such as CO2 and N2O may solidify at the reboiler-condenser placed between the two distillation columns.The formed solid could provide an additional strength to the heat and material transfers, and increase the pressure drops in the distillation columns.Furthermore, the presence of a solid phase can promote the accumulation of light hydrocarbons which may form flammable mixtures with liquid oxygen.Therefore, the presence of solid phases must be controlled see avoided within the cryogenic air distillation process.The main issue of this thesis is to develop a suitable model for representing solid phases and their equilibrium with the liquid and vapor phases at the operating conditions of the process, and to obtain full phase diagrams which would improve the knowledge of phase equilibria and the control of the risks associated to the presence of solid phases
Messabeb, Hamdi. "Caractérisation thermodynamique des équilibres liquide-vapeur des systèmes CO2 – eaux salées dans des conditions de hautes températures et hautes pressions." Thesis, Pau, 2017. http://www.theses.fr/2017PAUU3013/document.
This work was supported by Total and ‘’Agence National de la recherche’’ as a part of SIGARRR project (Simulation of the impact of annex gases co-injected with CO2 during its geological storage on the Reservoir-Rocks Reactivity. The aim of the thesis was to obtain experimental CO2 solubility data in salty aqueous solutions of sodium chloride and calcium chloride at different molalities (1, 3 and 6 mol/kg) under high temperature (323K < T < 423K) and high pressure (5 MPa < P < 20 MPa).Following a bibliographical study on experimental methods used for the carbon dioxide solubility determination, three characterization methods were tested: Aqueous phase analysis by ion chromatography Solubility estimation from mass balance, amounts of CO2 and liquid initially loaded into the cell and experimental parameters (density of liquid phase, molar volume of gas phase, and total volume of the equilibrium cell…). A liquid sample trapping in sodium hydroxide solution followed by a titrationA sensitivity study was carried out on the Solubility estimation method from mass balance. This study identified the level of accuracy of autoclave volume measurement to obtain reliable and accurate solubility data high-pressure.A sampling protocol was developed to withdraw aqueous samples and trap them into soda solution at high pressure. Two titration procedures were set up; liquid samples of CO2-H2O and CO2-H2O-NaCl systems were analyzed by potentiometric titration and samples of CO2-H2O-CaCl2 system were analyzed by conductimetric titration. 84 solubility data were obtained during this study, which include 45 new experimental data. Experimental measurement were compared to the results of simulation performed with PHREEQC software using a ‘’Pitzer.dat’’ database.The salting out effect observed was evaluated for each system under all temperature and pressure conditions
Bassil, Georgio. "Gazéification de la biomasse : élimination des goudrons par lavage, étude expérimentale et modélisation." Thesis, Lyon 1, 2012. http://www.theses.fr/2012LYO10057/document.
Gasification of biomass is a promising thermochemical renewable energy resource. Among all biomass conversion processes, gasification by heat cogeneration / bio-SNG (Substitute Natural Gas) is the promising one. But still, one of the deadlocks to be raised is the reduction of the high level of tar present in the product gas. The objective of this work is to perform a data base which will be useful at the operation of tar removal from aqueous medium. The present work has mainly focused on the acquisition of bi and triphasic equilibrium data model molecules of tars - water - washing solvent. Such data are indeed essential for the development of the thermodynamic model for the modeling and the optimization of the washing process. Analyses of liquid phases in equilibrium have been performed by GC-FID or GC-MS. In some cases the concentration levels were particularly low (up to 10-10 mole fraction of anthracene in the aqueous phase). Reciprocal concentrations obtained and the partition coefficients which are deduced from the empirical correlation satisfy each of Hands and the Van't Hoff relationship. Liquid-liquid-vapor equilibrium of binary systems (water-extracting solvent) was studied with the static method. The concentrations of the phases in equilibrium were correlated by the NRTL and UNIQUAC models using the commercial software 'Thermodynamic Simulis'. The interaction parameters adjusted allow a good reproduction of experimental data
Kuswandi, M. "Procédés de séparation en milieu dispersé : régénération du triéthylène glycol par extraction de l'eau à l'aide d'un brouillard. Etude sur pilote et simulation. Séparation d'hydrocarbures par membranes liquides émulsionnées." Compiègne, 2000. http://www.theses.fr/2000COMP1275.