Добірка наукової літератури з теми "Multichannel fixed bed reactor modelling"
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Статті в журналах з теми "Multichannel fixed bed reactor modelling"
Nosek, Radovan, Jozef Jandacka, and Andrzej Szlek. "Boiler Modelling of Simple Combustion Processes." International Journal of Energy Optimization and Engineering 1, no. 3 (July 2012): 96–119. http://dx.doi.org/10.4018/ijeoe.2012070105.
Повний текст джерелаBell, N. H., and T. F. Edgar. "Modelling of a fixed-bed water-gas shift reactor." Journal of Process Control 1, no. 2 (March 1991): 59–67. http://dx.doi.org/10.1016/0959-1524(91)80002-2.
Повний текст джерелаBell, N. H., and T. F. Edgar. "Modelling of a fixed-bed water-gas shift reactor." Journal of Process Control 1, no. 1 (January 1991): 22–31. http://dx.doi.org/10.1016/0959-1524(91)87004-h.
Повний текст джерелаDhaundiyal, Alok, Suraj B. Singh, and Istvan Bacskai. "Mathematical Modelling of Pyrolysis of Hardwood (Acacia)." Acta Technologica Agriculturae 23, no. 4 (December 1, 2020): 176–82. http://dx.doi.org/10.2478/ata-2020-0028.
Повний текст джерелаChing, C. B., and K. H. Chu. "Modelling of a fixed bed and a fluidized bed immobilized enzyme reactor." Applied Microbiology and Biotechnology 29, no. 4 (October 1988): 316–22. http://dx.doi.org/10.1007/bf00265813.
Повний текст джерелаDixon, Anthony G. "Fixed bed catalytic reactor modelling-the radial heat transfer problem." Canadian Journal of Chemical Engineering 90, no. 3 (December 28, 2011): 507–27. http://dx.doi.org/10.1002/cjce.21630.
Повний текст джерелаDhaundiyal, Alok, and Suraj Bhan Singh. "Mathematical Modelling of Volatile Gas Using Lattice Boltzmann Method." Environmental and Climate Technologies 24, no. 1 (January 1, 2020): 483–500. http://dx.doi.org/10.2478/rtuect-2020-0030.
Повний текст джерелаAcharya, D. R., and R. Hughes. "Modelling of butene-1 dehydrogenation in a fixed bed reactor - bed and pellet profiles." Canadian Journal of Chemical Engineering 68, no. 1 (February 1990): 89–96. http://dx.doi.org/10.1002/cjce.5450680111.
Повний текст джерелаZhapbasbayev, U. K., G. I. Ramazanova, and O. B. Kenzhaliev. "Modelling of turbulent flow in a radial reactor with fixed bed." Thermophysics and Aeromechanics 22, no. 2 (March 2015): 229–43. http://dx.doi.org/10.1134/s0869864315020092.
Повний текст джерелаCiambelli, P., A. Di Benedetto, R. Pirone, and G. Russo. "Spontaneous isothermal oscillations in N2O catalytic decomposition: fixed-bed reactor modelling." Chemical Engineering Science 54, no. 20 (October 1999): 4521–27. http://dx.doi.org/10.1016/s0009-2509(99)00162-1.
Повний текст джерелаДисертації з теми "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.
Повний текст джерелаThe 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.
Повний текст джерелаTry, 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.
Повний текст джерелаThis 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.
Повний текст джерелаZakari, A. Y., Yakubu M. John, B. O. Aderemi, Rajnikant Patel, and Iqbal M. Mujtaba. "Modelling, simulation and sensitivity analysis of naphtha catalytic reforming reactions." 2019. http://hdl.handle.net/10454/17587.
Повний текст джерелаIn 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.
Повний текст джерелаЧастини книг з теми "Multichannel fixed bed reactor modelling"
Elnashaie, S. S. E. H., and S. S. Elshishini. "The Overall Reactor Models." In Modelling, Simulation and Optimization of Industrial Fixed Bed Catalytic Reactors, 261–397. London: Routledge, 2022. http://dx.doi.org/10.1201/9780203746769-7.
Повний текст джерелаHenda, Redhouane. "Transient Runaway in a Fixed-Bed Catalytic Reactor." In Modelling and Simulation. I-Tech Education and Publishing, 2008. http://dx.doi.org/10.5772/5985.
Повний текст джерелаBo Hwang, Young, and D. Dochain. "DYNAMICAL MODELLING OF A BIOLOGICAL DETOXICATION PROCESS IN A FIXED BED REACTOR." In Computer Applications in Biotechnology, 148–53. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042377-7.50029-5.
Повний текст джерелаSilva, Jornandes Dias da, and Sérgio Mário Lins Galdino. "Mathematical Modelling for the Storage Process of Hydrogen in a Catalyst (ZSM-5)-Assisted Fixed Bed Reactor: Adsorption and Simulation." In Engenharia química: princípios fundamentais. Editora Conhecimento Livre, 2022. http://dx.doi.org/10.37423/220606136.
Повний текст джерелаТези доповідей конференцій з теми "Multichannel fixed bed reactor modelling"
Dehestani, Davood, Hung Nguyen, Fahimeh Eftekhari, Jafar Madadnia, Steven Su, and Ying Guo. "Comprehensive Mathematical Modeling and Dynamic Simulation of Fixed Bed Reactor with Finite Element Method." In Modelling and Simulation. Calgary,AB,Canada: ACTAPRESS, 2011. http://dx.doi.org/10.2316/p.2011.735-077.
Повний текст джерелаJamaleddine, Tarek J., and Ramsey M. Bunama. "CFD Modelling of the Dehydrogenation Reaction of Isobutane to Isobutylene in a Fixed Bed Reactor." In 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.
Повний текст джерелаGopan, Gokul, Lalhmingsanga Hauchhum, Renjith Krishnan, and Satyajit Pattanayak. "Pyrolysis and liquefaction of rice straw and computational modelling of fixed-bed reactor for heat distribution." In 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.
Повний текст джерела"Modelling of the rinsing of a Fixed Bed Reactor for Solid Phase Peptide Synthesis using COMSOL Multiphysics®." In The 34th European Modeling & Simulation Symposium. CAL-TEK srl, 2022. http://dx.doi.org/10.46354/i3m.2022.emss.011.
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