Literatura académica sobre el tema "Multichannel fixed bed reactor modelling"
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Artículos de revistas sobre el tema "Multichannel fixed bed reactor modelling"
Nosek, Radovan, Jozef Jandacka y Andrzej Szlek. "Boiler Modelling of Simple Combustion Processes". International Journal of Energy Optimization and Engineering 1, n.º 3 (julio de 2012): 96–119. http://dx.doi.org/10.4018/ijeoe.2012070105.
Texto completoBell, N. H. y T. F. Edgar. "Modelling of a fixed-bed water-gas shift reactor". Journal of Process Control 1, n.º 2 (marzo de 1991): 59–67. http://dx.doi.org/10.1016/0959-1524(91)80002-2.
Texto completoBell, N. H. y T. F. Edgar. "Modelling of a fixed-bed water-gas shift reactor". Journal of Process Control 1, n.º 1 (enero de 1991): 22–31. http://dx.doi.org/10.1016/0959-1524(91)87004-h.
Texto completoDhaundiyal, Alok, Suraj B. Singh y Istvan Bacskai. "Mathematical Modelling of Pyrolysis of Hardwood (Acacia)". Acta Technologica Agriculturae 23, n.º 4 (1 de diciembre de 2020): 176–82. http://dx.doi.org/10.2478/ata-2020-0028.
Texto completoChing, C. B. y K. H. Chu. "Modelling of a fixed bed and a fluidized bed immobilized enzyme reactor". Applied Microbiology and Biotechnology 29, n.º 4 (octubre de 1988): 316–22. http://dx.doi.org/10.1007/bf00265813.
Texto completoDixon, Anthony G. "Fixed bed catalytic reactor modelling-the radial heat transfer problem". Canadian Journal of Chemical Engineering 90, n.º 3 (28 de diciembre de 2011): 507–27. http://dx.doi.org/10.1002/cjce.21630.
Texto completoDhaundiyal, Alok y Suraj Bhan Singh. "Mathematical Modelling of Volatile Gas Using Lattice Boltzmann Method". Environmental and Climate Technologies 24, n.º 1 (1 de enero de 2020): 483–500. http://dx.doi.org/10.2478/rtuect-2020-0030.
Texto completoAcharya, D. R. y R. Hughes. "Modelling of butene-1 dehydrogenation in a fixed bed reactor - bed and pellet profiles". Canadian Journal of Chemical Engineering 68, n.º 1 (febrero de 1990): 89–96. http://dx.doi.org/10.1002/cjce.5450680111.
Texto completoZhapbasbayev, U. K., G. I. Ramazanova y O. B. Kenzhaliev. "Modelling of turbulent flow in a radial reactor with fixed bed". Thermophysics and Aeromechanics 22, n.º 2 (marzo de 2015): 229–43. http://dx.doi.org/10.1134/s0869864315020092.
Texto completoCiambelli, P., A. Di Benedetto, R. Pirone y G. Russo. "Spontaneous isothermal oscillations in N2O catalytic decomposition: fixed-bed reactor modelling". Chemical Engineering Science 54, n.º 20 (octubre de 1999): 4521–27. http://dx.doi.org/10.1016/s0009-2509(99)00162-1.
Texto completoTesis sobre el tema "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.
Texto completoThe 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.
Texto completoTry, 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.
Texto completoThis 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.
Texto completoZakari, A. Y., Yakubu M. John, B. O. Aderemi, Rajnikant Patel y Iqbal M. Mujtaba. "Modelling, simulation and sensitivity analysis of naphtha catalytic reforming reactions". 2019. http://hdl.handle.net/10454/17587.
Texto completoIn 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.
Texto completoCapítulos de libros sobre el tema "Multichannel fixed bed reactor modelling"
Elnashaie, S. S. E. H. y S. S. Elshishini. "The Overall Reactor Models". En Modelling, Simulation and Optimization of Industrial Fixed Bed Catalytic Reactors, 261–397. London: Routledge, 2022. http://dx.doi.org/10.1201/9780203746769-7.
Texto completoHenda, Redhouane. "Transient Runaway in a Fixed-Bed Catalytic Reactor". En Modelling and Simulation. I-Tech Education and Publishing, 2008. http://dx.doi.org/10.5772/5985.
Texto completoBo Hwang, Young y D. Dochain. "DYNAMICAL MODELLING OF A BIOLOGICAL DETOXICATION PROCESS IN A FIXED BED REACTOR". En Computer Applications in Biotechnology, 148–53. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042377-7.50029-5.
Texto completoSilva, Jornandes Dias da y Sérgio Mário Lins Galdino. "Mathematical Modelling for the Storage Process of Hydrogen in a Catalyst (ZSM-5)-Assisted Fixed Bed Reactor: Adsorption and Simulation". En Engenharia química: princípios fundamentais. Editora Conhecimento Livre, 2022. http://dx.doi.org/10.37423/220606136.
Texto completoActas de conferencias sobre el tema "Multichannel fixed bed reactor modelling"
Dehestani, Davood, Hung Nguyen, Fahimeh Eftekhari, Jafar Madadnia, Steven Su y Ying Guo. "Comprehensive Mathematical Modeling and Dynamic Simulation of Fixed Bed Reactor with Finite Element Method". En Modelling and Simulation. Calgary,AB,Canada: ACTAPRESS, 2011. http://dx.doi.org/10.2316/p.2011.735-077.
Texto completoJamaleddine, Tarek J. y Ramsey M. Bunama. "CFD Modelling of the Dehydrogenation Reaction of Isobutane to Isobutylene in a Fixed Bed Reactor". En 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.
Texto completoGopan, Gokul, Lalhmingsanga Hauchhum, Renjith Krishnan y Satyajit Pattanayak. "Pyrolysis and liquefaction of rice straw and computational modelling of fixed-bed reactor for heat distribution". En 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.
Texto completo"Modelling of the rinsing of a Fixed Bed Reactor for Solid Phase Peptide Synthesis using COMSOL Multiphysics®". En The 34th European Modeling & Simulation Symposium. CAL-TEK srl, 2022. http://dx.doi.org/10.46354/i3m.2022.emss.011.
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