Simulation of CO preferential oxidation (COPrOx) monolithic reactors

In this work, a COPrOx monolithic reactor with a CuO/CeO 2/Al2O3 catalytic washcoat was modelled to purify a H2 stream for a 2 kW PEM fuel cell. Preliminary simulations included isothermal monoliths operating between 423 and 463 K, and the optimization of linear axial temperature profiles. For a fix...

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Autor principal: Jeifetz, L.G
Otros Autores: Giunta, P.D, Mariño, F.J, Amadeo, Nora Elvira, Laborde, M.A
Formato: Capítulo de libro
Lenguaje:Inglés
Publicado: 2014
Acceso en línea:Registro en Scopus
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100 1 |a Jeifetz, L.G. 
245 1 0 |a Simulation of CO preferential oxidation (COPrOx) monolithic reactors 
260 |c 2014 
270 1 0 |m Jeifetz, L.G.; Department of Chemical Engineering, Laboratorio de Procesos Catalíticos, Universidad de Buenos Aires, Buenos Aires 1428, Argentina; email: lejeifetz@gmail.com 
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504 |a Semeniuk, H.M., (2011) CuO/CeO2/Al2O3 catalysts for the preferential oxidation of CO (COPrOx), , Eng. thesis, Engineering School, University of Buenos Aires 
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504 |a Jeifetz, L.G., Monolithic reactors modelling for its application to the preferential CO oxidation reaction (COPrOx), 2012. , Eng. thesis, Engineering School, University of Buenos Aires 
506 |2 openaire  |e Política editorial 
520 3 |a In this work, a COPrOx monolithic reactor with a CuO/CeO 2/Al2O3 catalytic washcoat was modelled to purify a H2 stream for a 2 kW PEM fuel cell. Preliminary simulations included isothermal monoliths operating between 423 and 463 K, and the optimization of linear axial temperature profiles. For a fixed total system size and a desired CO outlet molar fraction lower than 20 ppm, an isothermal temperature profile maximized the global selectivity towards CO oxidation. Then, different schemes of adiabatic monoliths with interstage cooling were modelled and evaluated. It was found that wide operating temperature ranges lower the necessary number of stages, but decrease the global selectivity and rise system sensitivity to inlet temperatures. A 1D heterogeneous model was used to simulate the monoliths. © 2014 by Walter de Gruyter Berlin / Boston 2014.  |l eng 
536 |a Detalles de la financiación: Agencia Nacional de Promoción Científica y Tecnológica 
536 |a Detalles de la financiación: Acknowledgements: To ANPCYT, CONICET and University of Buenos Aires for the financial support. 
593 |a Department of Chemical Engineering, Laboratorio de Procesos Catalíticos, Universidad de Buenos Aires, Buenos Aires 1428, Argentina 
690 1 0 |a COPROX 
690 1 0 |a HEAT EXCHANGE 
690 1 0 |a MODELLING 
690 1 0 |a MONOLITHIC REACTOR 
690 1 0 |a PEM FUEL CELL 
690 1 0 |a CO PREFERENTIAL OXIDATION 
690 1 0 |a CO-PROX 
690 1 0 |a HEAT EXCHANGE 
690 1 0 |a MONOLITHIC REACTOR 
690 1 0 |a PEM FUEL CELL 
690 1 0 |a MODELS 
700 1 |a Giunta, P.D. 
700 1 |a Mariño, F.J. 
700 1 |a Amadeo, Nora Elvira 
700 1 |a Laborde, M.A. 
773 0 |d 2014  |g v. 12  |k n. 1  |p Int. J. Chem. Reactor Eng.  |x 15426580  |t International Journal of Chemical Reactor Engineering 
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856 4 0 |u https://doi.org/10.1515/ijcre-2013-0071  |y DOI 
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