Littérature scientifique sur le sujet « Multichannel fixed bed reactor modelling »
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Articles de revues sur le sujet "Multichannel fixed bed reactor modelling"
Nosek, Radovan, Jozef Jandacka et Andrzej Szlek. « Boiler Modelling of Simple Combustion Processes ». International Journal of Energy Optimization and Engineering 1, no 3 (juillet 2012) : 96–119. http://dx.doi.org/10.4018/ijeoe.2012070105.
Texte intégralBell, N. H., et T. F. Edgar. « Modelling of a fixed-bed water-gas shift reactor ». Journal of Process Control 1, no 2 (mars 1991) : 59–67. http://dx.doi.org/10.1016/0959-1524(91)80002-2.
Texte intégralBell, N. H., et T. F. Edgar. « Modelling of a fixed-bed water-gas shift reactor ». Journal of Process Control 1, no 1 (janvier 1991) : 22–31. http://dx.doi.org/10.1016/0959-1524(91)87004-h.
Texte intégralDhaundiyal, Alok, Suraj B. Singh et Istvan Bacskai. « Mathematical Modelling of Pyrolysis of Hardwood (Acacia) ». Acta Technologica Agriculturae 23, no 4 (1 décembre 2020) : 176–82. http://dx.doi.org/10.2478/ata-2020-0028.
Texte intégralChing, C. B., et K. H. Chu. « Modelling of a fixed bed and a fluidized bed immobilized enzyme reactor ». Applied Microbiology and Biotechnology 29, no 4 (octobre 1988) : 316–22. http://dx.doi.org/10.1007/bf00265813.
Texte intégralDixon, Anthony G. « Fixed bed catalytic reactor modelling-the radial heat transfer problem ». Canadian Journal of Chemical Engineering 90, no 3 (28 décembre 2011) : 507–27. http://dx.doi.org/10.1002/cjce.21630.
Texte intégralDhaundiyal, Alok, et Suraj Bhan Singh. « Mathematical Modelling of Volatile Gas Using Lattice Boltzmann Method ». Environmental and Climate Technologies 24, no 1 (1 janvier 2020) : 483–500. http://dx.doi.org/10.2478/rtuect-2020-0030.
Texte intégralAcharya, D. R., et R. Hughes. « Modelling of butene-1 dehydrogenation in a fixed bed reactor - bed and pellet profiles ». Canadian Journal of Chemical Engineering 68, no 1 (février 1990) : 89–96. http://dx.doi.org/10.1002/cjce.5450680111.
Texte intégralZhapbasbayev, U. K., G. I. Ramazanova et O. B. Kenzhaliev. « Modelling of turbulent flow in a radial reactor with fixed bed ». Thermophysics and Aeromechanics 22, no 2 (mars 2015) : 229–43. http://dx.doi.org/10.1134/s0869864315020092.
Texte intégralCiambelli, P., A. Di Benedetto, R. Pirone et G. Russo. « Spontaneous isothermal oscillations in N2O catalytic decomposition : fixed-bed reactor modelling ». Chemical Engineering Science 54, no 20 (octobre 1999) : 4521–27. http://dx.doi.org/10.1016/s0009-2509(99)00162-1.
Texte intégralThèses sur le sujet "Multichannel fixed bed reactor modelling"
Hazard, Browning Barbara. « Dynamic Modelling of a Fixed Bed Reactor to Study the First Instants of Gas Phase Ethylene Polymerisation ». Thesis, Lyon 1, 2013. http://www.theses.fr/2013LYO10109/document.
Texte intégralThe behaviour of silica supported metallocene catalyst in the early moments of olefin polymerization is not well understood. The complexity, rapidity and high exothermicity of the reaction impede observation of the kinetics and morphological changes. The fixed bed reactor constructed by McKenna’s group is designed to study these first instants of gas phase olefin polymerisation. The purpose of the modelling work presented is to gain understanding and improve the set-up through better knowledge of the reactor conditions. After a literature survey, the existing set-up was reviewed and analysed. A reactor model was constructed and programmed with polymerisation kinetics represented by a simple relation. The model was validated for individual experiments under optimised conditions. Use of the reactor as a calorimeter was evaluated and a state observer for the polymerisation rate was tested. The model was also used to show that very high temperatures are possible in the reactor bed and to simulate effects of changes to reactor construction and operating conditions. The reactor pressurisation profile is non negligible for experiments of shorter duration. New kinetics based on this were incorporated into the model: these were able to represent series of experiments and take account of the deactivation reaction. Contrary to results from longer duration experiments, our model finds initial deactivation does not appear to be controlled by temperature
Nugrahany, Febryana. « Modelling of Biomass Pyrolysis with Ex-situ Catalytic Upgrading for Bio-crude Production ». Thesis, KTH, Materialvetenskap, 2018. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-231489.
Texte intégralTry, Rasmey. « Étude expérimentale et modélisation dynamique d'un réacteur catalytique modulaire pour l'hydrogénation du CO2 en méthane ». Thesis, Lyon, 2018. http://www.theses.fr/2018LYSE1038/document.
Texte intégralThis work is within the Power-to-Gas framework, which aims to store the electrical energy surpluses from renewable energy in chemicals, here the methane. The intermittency of the electrical production requires the methanation system to have a certain level of flexibility with respect to temporal changes of operational conditions. In this context, the work carried out during this thesis is dedicated to the study of the dynamic behavior of a catalytic fixed-bed heat-exchanger methanation reactor. A reactor-exchanger highly equipped with thermocouples is designed and is used for the experimental study of the performances and the dynamics behavior of such a reactor. In particular, phenomena of thermal wave fronts, overshoot and inverse responses are found. The hydrodynamic and thermal parameters of the bed have been experimentally characterized. Modeling of the reactor-exchanger is also established and simulations of the reactor behavior are done. The experimental results are compared with the simulation results, allowing the precise analysis of the behaviors observed in the reactor
Phan, Duy Dũng. « Modelling and Evaluation of Fixed-Bed Photocatalytic Membrane Reactors ». Doctoral thesis, 2019. https://tud.qucosa.de/id/qucosa%3A36776.
Texte intégralZakari, A. Y., Yakubu M. John, B. O. Aderemi, Rajnikant Patel et Iqbal M. Mujtaba. « Modelling, simulation and sensitivity analysis of naphtha catalytic reforming reactions ». 2019. http://hdl.handle.net/10454/17587.
Texte intégralIn this paper, a model of catalytic naphtha reforming process of commercial catalytic reforming unit of Kaduna Refining & Petrochemical Company (KRPC) is adopted and simulated using the gPROMS software, an equation-oriented modelling software. The kinetic and thermodynamic parameters and properties were obtained from literature. The model was used to monitor the behaviour of the temperature and concentrations of parafins, naphthenes and aromatics with respect to the changing heights of the reactors. A comprehensive sensitivity analysis of the product quality (Aromatics) and product yield, reformate, lighter gases and hydrogen yields is performed by varying the operating conditions of the reaction and the following conclusions were made. It was found that the production of aromatics, hydrogen yield, lighter gases and coke on catalyst increase with increasing temperature of the reaction while the reformate yield decreases with the increasing temperature and vice versa. The aromatics, hydrogen yield, coke on catalyst and lighter gases decrease with increasing pressure while the reformate yield decreases with decreasing pressure and vice versa. Hydrogen-hydrocarbon ratio (HHR) affects the product quality slightly by increasing the reformate and hydrogen yield and decreasing the aromatics slightly as well decreasing the coke on catalyst.
Pereira, Sara Filipa Fagulha. « The thermal effects on the methanol-to-olefins reaction : A modelling and experimental approach ». Master's thesis, 2015. http://hdl.handle.net/10362/15798.
Texte intégralChapitres de livres sur le sujet "Multichannel fixed bed reactor modelling"
Elnashaie, S. S. E. H., et S. S. Elshishini. « The Overall Reactor Models ». Dans Modelling, Simulation and Optimization of Industrial Fixed Bed Catalytic Reactors, 261–397. London : Routledge, 2022. http://dx.doi.org/10.1201/9780203746769-7.
Texte intégralHenda, Redhouane. « Transient Runaway in a Fixed-Bed Catalytic Reactor ». Dans Modelling and Simulation. I-Tech Education and Publishing, 2008. http://dx.doi.org/10.5772/5985.
Texte intégralBo Hwang, Young, et D. Dochain. « DYNAMICAL MODELLING OF A BIOLOGICAL DETOXICATION PROCESS IN A FIXED BED REACTOR ». Dans Computer Applications in Biotechnology, 148–53. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042377-7.50029-5.
Texte intégralSilva, Jornandes Dias da, et Sérgio Mário Lins Galdino. « Mathematical Modelling for the Storage Process of Hydrogen in a Catalyst (ZSM-5)-Assisted Fixed Bed Reactor : Adsorption and Simulation ». Dans Engenharia química : princípios fundamentais. Editora Conhecimento Livre, 2022. http://dx.doi.org/10.37423/220606136.
Texte intégralActes de conférences sur le sujet "Multichannel fixed bed reactor modelling"
Dehestani, Davood, Hung Nguyen, Fahimeh Eftekhari, Jafar Madadnia, Steven Su et Ying Guo. « Comprehensive Mathematical Modeling and Dynamic Simulation of Fixed Bed Reactor with Finite Element Method ». Dans Modelling and Simulation. Calgary,AB,Canada : ACTAPRESS, 2011. http://dx.doi.org/10.2316/p.2011.735-077.
Texte intégralJamaleddine, Tarek J., et Ramsey M. Bunama. « CFD Modelling of the Dehydrogenation Reaction of Isobutane to Isobutylene in a Fixed Bed Reactor ». Dans ASME 2016 Heat Transfer Summer Conference collocated with the ASME 2016 Fluids Engineering Division Summer Meeting and the ASME 2016 14th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/ht2016-1071.
Texte intégralGopan, Gokul, Lalhmingsanga Hauchhum, Renjith Krishnan et Satyajit Pattanayak. « Pyrolysis and liquefaction of rice straw and computational modelling of fixed-bed reactor for heat distribution ». Dans Proceedings of the Mizoram Science Congress 2018 (MSC 2018) - Perspective and Trends in the Development of Science Education and Research. Paris, France : Atlantis Press, 2018. http://dx.doi.org/10.2991/msc-18.2018.5.
Texte intégral« Modelling of the rinsing of a Fixed Bed Reactor for Solid Phase Peptide Synthesis using COMSOL Multiphysics® ». Dans The 34th European Modeling & Simulation Symposium. CAL-TEK srl, 2022. http://dx.doi.org/10.46354/i3m.2022.emss.011.
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