Bio-ethanol steam reforming on Ni/Al2O3 catalyst

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In this work, the ethanol steam reforming on Ni/γAl2O3 catalyst at temperatures between 573 and 773 K was studied and an overall reaction scheme as a function of temperature was proposed. It can be concluded that higher water/ethanol ratio (6:1) and higher temperature (773 K) promote hydrogen produc...

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Detalles Bibliográficos
Autor principal: Comas, J.
Otros Autores: Marino, F., Laborde, M., Amadeo, Nora Elvira
Formato: Capítulo de libro
Lenguaje:Inglés
Publicado: 2004
Acceso en línea:Registro en Scopus
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Aporte de:Registro referencial: Solicitar el recurso aquí
Biblioteca Central Dr. Luis F. Leloir (FCEN) de Universidad de Buenos Aires
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100 1 |a Comas, J. 
245 1 0 |a Bio-ethanol steam reforming on Ni/Al2O3 catalyst 
260 |c 2004 
270 1 0 |m Amadeo, N.; Lab. de Procesos Cataliticos, Depto. Ingenieria Química, Fac. de Ing. Pabellon de Industrias, Buenos Aires 1428, Argentina; email: norma@di.fcen.uba.ar 
504 |a Klouz, V., Fierro, V., Denton, P., Katz, H., Lisse, J.P., Bouvot-Mauduit, S., Mirodatos, C., (2002) J. Power Sour., 105, p. 26 
504 |a Peppley, B.A., Amhlett, J.C., Kearns, L.M., Mann, R.F., (1999) Appl. Catal. A, 179, p. 21 
504 |a Peppley, B.A., Amhlett, J.C., Kearns, L.M., Mann, R.F., (1999) Appl. Catal. A, 179, p. 31 
504 |a Lindstrom, B., Pettersson, L.J., (2001) Int. J. Hydrogen Energy, 26, p. 923 
504 |a Garća, E.Y., Laborde, M.A., (1991) Int. J. Hydrogen Energy, 16, p. 307 
504 |a Vasudeva, K., Mitra, N., Umansankar, P., Dhingra, S.C., (1996) Int. J. Hydrogen Energy, 2, p. 13 
504 |a Iwasa, N., Takezawa, N., (1991) Bull. Chem. Soc. Jpn., 64, p. 2619 
504 |a Cavallaro, S., Freni, S., (1996) Int. J. Hydrogen Energy, 216, p. 465 
504 |a Marino, F.J., Cerrella, E.G., Duhalde, S., Jobbagy, M., Laborde, M., (1998) Int. J. Hydrogen Energy, 2312, p. 1095 
504 |a Marino, F.J., Jobbagy, M., Baronetti, G., Laborde, M., (2000) Stud. Surf. Sci. Catal. C, 130, p. 2147 
504 |a Cavallaro, S., (2000) Energy Fuels, 14, pp. 1195-1199 
504 |a Freni, S., Mondello, N., Cavallaro, S., Cacciola, G., Parmon, V.N., Sobyanin, V.A., (2000) React. Kinet. Catal. Lett., 711, pp. 143-152 
504 |a Galvita, V.V., Semin, G.L., Belyaev, V.D., Semikolenov, V.A., Tsiakaras, P., Sobyanin, V.A., (2001) Appl. Catal. A, 220, pp. 123-127 
504 |a Liguras, D.K., Kondarides, D.I., Verykios, X.E., (2003) Appl. Catal. B, 43, pp. 345-354 
504 |a Aupretre, F., Descome, C., Duprez, D., (2002) Catal. Commun., 3, pp. 263-267 
504 |a Llorca, J., Homs, N., Sales, J., Ramirez de la Piscina, P., (2002) J. Catal., 209, pp. 306-317 
504 |a Descorme, C., Madier, Y., Duprez, D., Birchem, T., (2000) Stud. Surf. Sci. Catal., 130, p. 347 
504 |a Jiang, C.J., Trimm, D.L., Wainwright, M.S., Cant, N., (1993) Appl. Catal. A, 93, pp. 245-255 
504 |a Jiang, C.J., Trimm, D.L., Wainwright, M.S., Cant, N., (1993) Appl. Catal. A, 97, pp. 145-158 
504 |a Joensen, F., Rostrup-Nielsen, J.R., (2001) J. Power Sour., 4566, pp. 1-7 
504 |a Haga, F., Nakajima, T., Miya, H., Mishima, S., (1997) Catal. Lett., 48, p. 223 
504 |a Rostrup-Nielsen, J.R., Hojlund, N., (1985) Deactivation and Poisoning of Catalyst, p. 57. , J. Oudar, H. Wise (Eds.), Marcel Dekker, New York, Basel 
504 |a Ioannides, T., (2001) J. Power Sour., 92, pp. 17-25 
506 |2 openaire  |e Política editorial 
520 3 |a In this work, the ethanol steam reforming on Ni/γAl2O3 catalyst at temperatures between 573 and 773 K was studied and an overall reaction scheme as a function of temperature was proposed. It can be concluded that higher water/ethanol ratio (6:1) and higher temperature (773 K) promote hydrogen production (91% selectivity). Over Ni-based catalyst there would not be evidences that water gas shift reaction occurs. The presence of oxygen in the feed produces a favorable effect on carbon deposition; nevertheless the carbon monoxide production is not reduced. © 2003 Elsevier B.V. All rights reserved.  |l eng 
536 |a Detalles de la financiación: Universidad de Buenos Aires, IN041 
536 |a Detalles de la financiación: The authors wish to acknowledge the financial support received from Universidad de Buenos Aires (project IN041). 
593 |a Lab. de Procesos Cataliticos, Depto. Ingenieria Química, Fac. de Ing. Pabellon de Industrias, Buenos Aires 1428, Argentina 
690 1 0 |a ETHANOL REFORMING 
690 1 0 |a FUEL CELL 
690 1 0 |a HYDROGEN PRODUCTION 
690 1 0 |a NI-BASED CATALYST 
690 1 0 |a ALUMINA 
690 1 0 |a CARBON MONOXIDE 
690 1 0 |a DEPOSITION 
690 1 0 |a ETHANOL 
690 1 0 |a HIGH TEMPERATURE EFFECTS 
690 1 0 |a HYDROGEN 
690 1 0 |a NICKEL 
690 1 0 |a STEAM 
690 1 0 |a GAS SHIFT REACTIONS 
690 1 0 |a STEAM REFORMING 
690 1 0 |a CATALYSTS 
690 1 0 |a FUEL CELL 
700 1 |a Marino, F. 
700 1 |a Laborde, M. 
700 1 |a Amadeo, Nora Elvira 
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