Literatura académica sobre el tema "Modélisation cinétique chimique"
Crea una cita precisa en los estilos APA, MLA, Chicago, Harvard y otros
Índice
Consulte las listas temáticas de artículos, libros, tesis, actas de conferencias y otras fuentes académicas sobre el tema "Modélisation cinétique chimique".
Junto a cada fuente en la lista de referencias hay un botón "Agregar a la bibliografía". Pulsa este botón, y generaremos automáticamente la referencia bibliográfica para la obra elegida en el estilo de cita que necesites: APA, MLA, Harvard, Vancouver, Chicago, etc.
También puede descargar el texto completo de la publicación académica en formato pdf y leer en línea su resumen siempre que esté disponible en los metadatos.
Artículos de revistas sobre el tema "Modélisation cinétique chimique"
Woolschlager, J. y B. E. Rittmann. "Que mesurent les tests de CODB et de COA ?" Revue des sciences de l'eau 8, n.º 3 (12 de abril de 2005): 371–85. http://dx.doi.org/10.7202/705229ar.
Texto completoVERDU, Jacques. "Vieillissement chimique : modélisation cinétique". [Archives] Plastiques et composites, agosto de 2015. http://dx.doi.org/10.51257/a-v1-am3153.
Texto completoCÔME, Guy-Marie. "Cinétique chimique générale - Modélisation mécanistique". Opérations unitaires. Génie de la réaction chimique, septiembre de 1995. http://dx.doi.org/10.51257/a-v2-j1110.
Texto completoEl Ouardi, Mokhtar. "Modélisation et analyse d’un milieu granulaire carbonaté à haute température". Journal of Renewable Energies 13, n.º 4 (25 de octubre de 2023). http://dx.doi.org/10.54966/jreen.v13i4.234.
Texto completoTesis sobre el tema "Modélisation cinétique chimique"
Jallais, Simon. "Etude expérimentale et modélisation de l'oxydation d'hydrocarbures légers". Poitiers, 2001. http://www.theses.fr/2001POIT2334.
Texto completoSabonnadière, Marc. "Etude et modélisation d'un laser chimique HF photo-initié". Aix-Marseille 1, 1999. http://www.theses.fr/1999AIX11020.
Texto completoCochegrue, Hélène. "Modélisation cinétique du reformage catalytique sur catalyseur Pt-Sn/Al2O3". Poitiers, 2001. http://www.theses.fr/2001POIT2262.
Texto completoBlanchin, Stéphane. "Modélisation cinétique de l'hydrodésazotation de la quinoléine et de ses intermédiaires de réaction". Poitiers, 2001. http://www.theses.fr/2001POIT2319.
Texto completoPelletier, David. "Modélisation de la cinétique chimique dans les plasmas inductifs application aux procédés". Thèse, Université de Sherbrooke, 2006. http://savoirs.usherbrooke.ca/handle/11143/1792.
Texto completoPelletier, David. "Modélisation de la cinétique chimique dans les plasmas inductifs : applications aux procédés". Grenoble INPG, 2006. https://hal.archives-ouvertes.fr/tel-01331569.
Texto completoThe chemical equilibrium (CE), often used as a first approximation in the modeling of thermal plasma processes, does not always make it possible to explain the experimental results, in particular in the vicinity of a wall or a surface placed under the plasma jet. A numericaf tool allowing the analysis of effects related to chemical kinetics in atmospheric ICP was developed under FLUEN© and applied on a process of silicon purification by plasma. The first results show that the assumption of CE is valid within plasma, but not in the interfacial zone between the plasma and the target where a broad variation with CE was predicted. Ln addition, an experimental validation of the numerical model was carried out by a spectroscopie study of an ICP torch, and general kinetics studies through the attack of a graphite target by an Ar-02 plasma
Pommier, Pierre-Lin. "Modélisation de l'interaction cinétique chimique - turbulence : application à la combustion homogène diesel". Paris 6, 2008. http://www.theses.fr/2008PA066354.
Texto completoThe objective of this thesis is to study the interaction between chemical kinetics and turbulence applied to homogeneous Diesel combustion (HCCI). Heterogeneities air-fuel mixture control the heat release rate and are directly linked to emissions during the engine cycle. The proposed model based on a particular method takes into account the heterogeneities of temperature and species present in the combustion chamber. Heterogeneities are modelled by random vectors (i. E. Particles) of species mass and temperature. The 0D model used describes two physical phenomena: the chemical kinetics and the mixture between the particles. The micro-mixing time is modelled by a k-ε turbulence model. Model against experimental data shows overall satisfactory agreement. However, this approach is very promising and can be linked to 3D approach, where this model can be implemented in each computational cell
Ristori, Alain. "Modélisation de la combustion du gazole : étude des aspects chimiques". Orléans, 2000. http://www.theses.fr/2000ORLE2057.
Texto completoRafalimanana, Célestin Alexis. "Contribution à la modélisation des cinétiques réactionnelles, à la simulation et à la conduite thermique des réacteurs de chimie fine". Toulouse, INPT, 1990. http://www.theses.fr/1990INPT039G.
Texto completoChamouleau, Françoise. "Étude et modélisation de la cinétique de synthèse enzymatique de palmitates de glucose et de fructose". Vandoeuvre-les-Nancy, INPL, 2002. http://www.theses.fr/2002INPL120N.
Texto completoThe aim of this work is to study the kinetics of sugar esters synthesis in the presence of glucose or fructose and palmitic acid. These syntheses were conducted at 60°C in 2-methyl-2-butanol. Immobilised lipase B of Candida antarctica was used as biocatalyst. The explored parameters in this study are: the origin of lipase, the nature of the support, the type of immobilisation, the quantity of water and the solubility and dissolution rate of sugars. These studies showed that these reactions are affected mainly by the quantity of water, the solubility and the dissolution rate of sugars. The control of water by the use of molecular sieves allowed to reach a conversion yield of fatty acid about 98% for two sugars. However the reactions in the presence of glucose are slower compared to these conducted with fructose. This behaviour is due to the low solubility of the glucose (14 mM). The obtained results were structured in the form of a Bi-Bi ping pong kinetics model. This model was validated in a broad domain of concentrations of substrates and enzymes. It was used thereafter as a tool to define the best conditions of these reactions