Kinetics modeling for the mixed reforming of methane over Ni-CeO2/MgAl2O4 catalyst
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Cited by (28)
Effects of biogas feed distribution ratio on the reforming efficiency of a direct biogas reforming system for hydrogen production
2024, International Journal of Hydrogen EnergyCarbon dioxide abatement by integration of methane bi-reforming process with ammonia and urea synthesis
2021, Renewable and Sustainable Energy ReviewsCitation Excerpt :Since the kinetic model for ammonia synthesis was developed under conditions close to industrial practice, it was immediately employed in the simulations. The kinetic models chosen to represent the BRM process, however, were subject to a model validation by using experimental data from Jun et al. [24]. The selected kinetic models, however, were originated from laboratory-scale experimental data, in which catalyst particles are generally small and/or high linear velocity flows are used.
Methanol production from captured CO<inf>2</inf> using hydrogenation and reforming technologies- environmental and economic evaluation
2019, Journal of CO2 UtilizationCitation Excerpt :This procedure is also used for the tri-reforming process which is presented in the next section. In this research, a kinetic model for the combined reforming by a Ni-CeO2/MgAl2O4 catalyst [28,29] is employed to predict the results for the syngas synthesis from bi-reforming reactions. The kinetic equations of this model are given by Equations B.1 - B.10 while the kinetic parameters are presented in Table B1.
This work was supported by the Energy Efficiency & Resources Program of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) grant funded by the Korea Government Ministry of Knowledge Economy (No. 2006CCC11P011B-21-2-100) and Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education, Science and Technology (No. 2010-0003380).