Egg-shell CuO/CeO2/Al2O3 catalysts for CO preferential oxidation

Catalytic systems based on copper and cerium supported on γ-Al2O3 have shown to be extremely effective for CO preferential oxidation. In order to selectively oxidize carbon monoxide, it is desired that only CO can access to the active sites. Since the effective diffusion of H2 is higher than that of...

Descripción completa

Guardado en:
Detalles Bibliográficos
Autor principal: Mariño, F.
Otros Autores: Iglesias, I., Baronetti, G., Alemany, L., Laborde, M.
Formato: Capítulo de libro
Lenguaje:Inglés
Publicado: Elsevier Ltd 2014
Materias:
Acceso en línea:Registro en Scopus
DOI
Handle
Registro en la Biblioteca Digital
Aporte de:Registro referencial: Solicitar el recurso aquí
LEADER 07880caa a22009137a 4500
001 PAPER-23784
003 AR-BaUEN
005 20230518205532.0
008 190411s2014 xx ||||fo|||| 00| 0 eng|d
024 7 |2 scopus  |a 2-s2.0-84951043387 
040 |a Scopus  |b spa  |c AR-BaUEN  |d AR-BaUEN 
030 |a IJHED 
100 1 |a Mariño, F. 
245 1 0 |a Egg-shell CuO/CeO2/Al2O3 catalysts for CO preferential oxidation 
260 |b Elsevier Ltd  |c 2014 
270 1 0 |m Mariño, F.; ITHES (CONICET/Universidad de Buenos Aires), Laboratorio de Procesos Catalíticos, Pabellón Industrias, Ciudad UniversitariaArgentina; email: fernando@di.fcen.uba.ar 
506 |2 openaire  |e Política editorial 
504 |a Dincer, I., Environmental and sustainability aspects of hydrogen and fuel cell systems (2007) Int J Energy Res, 31, pp. 29-55 
504 |a Turner, J., Sverdrup, G., Mann, M.K., Maness, P.C., Kroposki, B., Ghirardi, M., Renewable hydrogen production (2008) Int J Energy Res, 32, pp. 379-407 
504 |a Ghenciu, A.F., Review of fuel processing catalysts for hydrogen production in PEM fuel cell systems (2002) Curr Opin Solid State Mater Sci, 6, pp. 389-399 
504 |a U.S. Department of Energy, (2004) Fuel Cell Handbook, , 7th ed. EG&G Technical Services, Inc 
504 |a Yee, R.S.L., Rozendalb, R.A., Zhangc, K., Ladewiga, B.P., Cost effective cation exchange membranes: A review (2012) Chem Eng Res Des, 90, pp. 950-959 
504 |a Oh, S.H., Sinkevitch, R.M., Carbon monoxide removal from hydrogen-rich fuel cell feedstreams by selective catalytic oxidation (1993) J Catal, 142, pp. 254-262 
504 |a Avgouropoulos, G., Ioannides, T., Papadopoulou, C., Batista, J., Hocevar, S., Matralis, H.K., A comparative study of Pt/γ-Al2O3, Au/α-Fe2O3 and CuO-CeO2 catalysts for the selective oxidation of carbon monoxide in excess hydrogen (2002) Catal Today, 75, pp. 157-167 
504 |a Mishra, A., Prasad, R., A review on preferential oxidation of carbon monoxide in hydrogen rich gases (2011) Bull Chem React Eng Catal, 6, pp. 1-14 
504 |a Mariño, F., Descorme, C., Duprez, D., Supported base metal catalysts for the preferential oxidation of carbon monoxide in the presence of excess hydrogen (PROX) (2005) Appl Catal B Environ, 58, pp. 175-183 
504 |a Bion, N., Epron, F., Moreno, M., Mariño, F., Duprez, D., Preferential oxidation of carbon monoxide in the presence of hydrogen (PROX) over noble metals and transition metal oxides: Advantages and drawbacks (2008) Top Catal, 51, pp. 76-88 
504 |a Schönbrod, B., Mariño, F., Baronetti, G., Laborde, M., Catalytic performance of a copper-promoted CeO2 catalyst in the CO oxidation: Influence of the operating variables and kinetic study (2009) Int J Hydrogen Energy, 34, pp. 4021-4028 
504 |a Augustine, R.L., (1996) Heterogeneous Catalysis for the Synthetic Chemist, , Marcel Dekker, Inc 
504 |a Morbidelli, M., Gavriilidis, A., Varma, A., (2001) Catalyst Design: Optimal Distribution of Catalyst in Pellets, Reactors and Membranes, , Cambridge University Press 
504 |a Potemkin, D.I., Snytnikov, P.V., Belyaev, V.D., Sobyanin, V.A., Preferential CO oxidation over Cu/CeO2-x catalysts: Internal mass transport limitation (2011) Chem Eng J, 177, pp. 165-171 
504 |a Vayenas, C.G., Pavlou, S., Optimal catalyst distribution for selectivity maximization in pellets: Parallel and consecutive reactions (1987) Chem Eng Sci, 42, pp. 1655-1666 
504 |a Lekhal, A., Glasser, B.J., Khinast, J.G., Impact of drying on the catalyst profile in supported impregnation catalyst (2001) Chem Eng Sci, 56, pp. 4473-4487 
504 |a Kotter, M., Riekert, L., The influence of impregnation, drying and activation on the activity and distribution of CuO on α-alumina (1979) Stud Surf Sci Catal, 3, pp. 51-63 
504 |a Liu, X., Khinast, J.G., Glasser, B.J., Drying of supported catalysts for low melting point precursors: Impact of metal loading and drying methods on the metal distribution (2012) Chem Eng Sci, 79, pp. 187-199 
504 |a Liu, X., Khinast, J.G., Glasser, B.J., A parametric investigation of impregnation and drying of supported catalyst (2008) Chem Eng Sci, 63, pp. 4517-4530 
504 |a Mariño, F., Baronetti, G., Laborde, M., Bion, N., Le Valant, A., Epron, F., Optimized CuO-CeO2 catalysts for COPROX reaction (2008) Int J Hydrogen Energy, 33, pp. 1345-1353 
520 3 |a Catalytic systems based on copper and cerium supported on γ-Al2O3 have shown to be extremely effective for CO preferential oxidation. In order to selectively oxidize carbon monoxide, it is desired that only CO can access to the active sites. Since the effective diffusion of H2 is higher than that of CO, an egg-shell type distribution is preferred. With the objective of modifying the radial distribution of the active phases in the catalyst particle, the effect of four variables of the impregnation process is analyzed: metal loading, support-solution contact time, impregnation temperature and drying time. Radial profiles of Cu and Ce show that the egg-shell type distribution is favored by low metal loading, short contact and drying times and by high impregnation temperature. The effect of such variables is stronger on copper profile than on cerium profile. Catalytic performance on COPROX was enhanced by egg-shell type distribution. Copyright © 2015 Hydrogen Energy Publications, LLC.  |l eng 
536 |a Detalles de la financiación: Universidad de Buenos Aires 
536 |a Detalles de la financiación: Agencia Nacional de Promoción Científica y Tecnológica 
536 |a Detalles de la financiación: Consejo Nacional de Investigaciones Científicas y Técnicas 
536 |a Detalles de la financiación: The authors acknowledge to the University of Buenos Aires (UBA), ANPCyT and CONICET for their financial support. 
593 |a ITHES (CONICET/Universidad de Buenos Aires), Laboratorio de Procesos Catalíticos, Pabellón Industrias, Ciudad Universitaria, Buenos Aires, 1428, Argentina 
593 |a Departamento de Ingeniería Química, Facultad de Ciencias, Campus de Teatinos, Universidad de Málaga, Málaga, E-29071, Spain 
690 1 0 |a CERIUM 
690 1 0 |a COPPER 
690 1 0 |a COPROX 
690 1 0 |a HYDROGEN 
690 1 0 |a INTRAPARTICULAR PROFILES 
690 1 0 |a CARBON MONOXIDE 
690 1 0 |a CATALYSTS 
690 1 0 |a CATALYTIC OXIDATION 
690 1 0 |a COPPER 
690 1 0 |a HYDROGEN 
690 1 0 |a IMPREGNATION 
690 1 0 |a OXIDATION 
690 1 0 |a SHELLS (STRUCTURES) 
690 1 0 |a CATALYST PARTICLES 
690 1 0 |a CATALYTIC PERFORMANCE 
690 1 0 |a CO PREFERENTIAL OXIDATION 
690 1 0 |a CO-PROX 
690 1 0 |a EFFECTIVE DIFFUSION 
690 1 0 |a IMPREGNATION PROCESS 
690 1 0 |a INTRAPARTICULAR PROFILES 
690 1 0 |a RADIAL DISTRIBUTIONS 
690 1 0 |a CERIUM 
650 1 7 |2 spines  |a CARBON 
700 1 |a Iglesias, I. 
700 1 |a Baronetti, G. 
700 1 |a Alemany, L. 
700 1 |a Laborde, M. 
773 0 |d Elsevier Ltd, 2014  |g v. 40  |h pp. 11235-11241  |k n. 34  |p Int. J. Hydrogen Energy  |x 03603199  |w (AR-BaUEN)CENRE-5264  |t International Journal of Hydrogen Energy 
856 4 1 |u https://www.scopus.com/inward/record.uri?eid=2-s2.0-84951043387&doi=10.1016%2fj.ijhydene.2015.03.051&partnerID=40&md5=bbf54fa86b52cca8a353d73c9c58d426  |y Registro en Scopus 
856 4 0 |u https://doi.org/10.1016/j.ijhydene.2015.03.051  |y DOI 
856 4 0 |u https://hdl.handle.net/20.500.12110/paper_03603199_v40_n34_p11235_Marino  |y Handle 
856 4 0 |u https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_03603199_v40_n34_p11235_Marino  |y Registro en la Biblioteca Digital 
961 |a paper_03603199_v40_n34_p11235_Marino  |b paper  |c PE 
962 |a info:eu-repo/semantics/article  |a info:ar-repo/semantics/artículo  |b info:eu-repo/semantics/publishedVersion 
999 |c 84737