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Abstract:

The interaction of Cu2+, Ni2+ and Al3+ ions during the impregnation step of K/γ-Al2O3 support was studied. Cu-Ni catalyst precursors ("just impregnated solids"), just reduced precursors (H2, 300°C), and calcined precursors in the range of 400-800°C were characterised by X-ray diffraction (XRD), temperature programmed reduction (TPR) and X-ray photoelectron spectroscopy (XPS) measurements. In addition, the catalytic behaviour of reduced precursors and calcined catalysts was analysed in the ethanol steam reforming reaction at 300°C and atmospheric pressure. XRD results of different precursors indicated that, after the impregnation step, copper is present in two different phases: a copper basic nitrate and a CuAl and/or CuNiAl hydrotalcite-type compound (HT). In the sample containing only nickel, this metal is present as a NiAl-HT compound. At constant copper content of 6 wt.%, the ratio between the copper phases depends on the nickel content. Adding nickel favours the formation of HT compounds. While calcination of Cu-Ni precursors in the range of 400-800°C produces a CuO segregated phase and/or a phase of copper called "surface spinel", nickel is always found as a nickel aluminate after the calcination treatment. The catalytic behaviour of the samples strongly depends on the conditions of the thermal treatments. Thus, the increase in the calcination temperature of the precursors produces a strong interaction between nickel and aluminium, decreasing nickel reducibility and selectivity to C1 compounds. On the other hand, the just reduced precursors showed to have the best catalytic performance for the ethanol steam reforming reaction at 300°C. © 2002 Elsevier Science B.V. All rights reserved.

Registro:

Documento: Artículo
Título:Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction
Autor:Mariño, F.; Baronetti, G.; Jobbagy, M.; Laborde, M.
Filiación:Depto. de Ingenieria Quimica (FI), Universidad de Buenos Aires, Ciudad Universitaria, 1428 Buenos Aires, Argentina
INQUIMAE, FCEyN, Universidad de Buenos Aires, Buenos Aires, Argentina
Palabras clave:Cu-Ni catalysts; CuNiAl hydrotalcite-type compounds; Ethanol steam reforming; Alumina; Calcination; Copper; Ethanol; Heat treatment; Impregnation; Nickel; Potassium; Steam; Temperature programmed desorption; X ray diffraction analysis; X ray photoelectron spectroscopy; Catalyst precursors; Steam reforming; Catalysts
Año:2002
Volumen:238
Número:1
Página de inicio:41
Página de fin:54
DOI: http://dx.doi.org/10.1016/S0926-860X(02)00113-8
Título revista:Applied Catalysis A: General
Título revista abreviado:Appl Catal A Gen
ISSN:0926860X
CODEN:ACAGE
Registro:https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_0926860X_v238_n1_p41_Marino

Referencias:

  • Mariño, F., Cerrella, E., Duhalde, S., Jobbagy, M., Laborde, M., (1998) Int. J. Hydrogen Energy, 23 (12), p. 1095
  • Mariño, F., Jobbagy, M., Baronetti, G., Laborde, M., (2000) Stud. Surf. Sci. Catal., 130, p. 2147
  • Mariño, F., Boveri, M., Baronetti, G., Laborde, M., (2001) Int. J. Hydrogen Energy, 7, p. 26
  • De Bokx, P., Wassenberg, W., Geus, J., (1987) J. Catal., 104, p. 86
  • Paulhiac, J.L., Clause, O., (1993) J. Am. Chem. Soc., 115, p. 11602
  • D'Espinose de la Caillerie, J., Kermarec, M., Clause, O., (1995) J. Am. Chem. Soc., 117, p. 11602
  • Lo Jacono, M., Cimino, A., Inversi, M., (1982) J. Catal., 76, p. 320
  • Sivaraj, Ch., Kantarao, P., (1988) Appl. Catal., 45, p. 103
  • Alejandre, A., Medina, F., Salagre, P., Fabregat, A., Suerias, J., (1998) Appl. Catal. B, 18, p. 307
  • Hierl, R., Knözinger, H., Urbach, H., (1981) J. Catal., 69, p. 475
  • Cavani, F., Trifiro, F., Vaccari, A., (1991) Catal. Today, 11, p. 173
  • Alejandre, A., Medina, F., Salagre, P., Correig, X., Sueiras, J., (1999) Chem. Mater., 11, p. 939
  • Rives, V., Kannan, S., (2000) J. Mater. Chem., 10, p. 489
  • Brindley, G.W., Kikkawa, S., (1979) Am. Mineral., 64, p. 836
  • Ross, J.R.H., Steel, M.C.F., Zeini-Isfahani, A., (1978) J. Catal., 52, p. 280
  • Clause, O., Rbours, B., Merlen, E., Trifiro, F., Vaccari, A., (1992) J. Catal., 133, p. 231
  • Tichit, D., Medina, F., Coq, B., Dutartre, R., (1997) Appl. Catal. A Gen., 159, p. 241

Citas:

---------- APA ----------
Mariño, F., Baronetti, G., Jobbagy, M. & Laborde, M. (2002) . Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction. Applied Catalysis A: General, 238(1), 41-54.
http://dx.doi.org/10.1016/S0926-860X(02)00113-8
---------- CHICAGO ----------
Mariño, F., Baronetti, G., Jobbagy, M., Laborde, M. "Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction" . Applied Catalysis A: General 238, no. 1 (2002) : 41-54.
http://dx.doi.org/10.1016/S0926-860X(02)00113-8
---------- MLA ----------
Mariño, F., Baronetti, G., Jobbagy, M., Laborde, M. "Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction" . Applied Catalysis A: General, vol. 238, no. 1, 2002, pp. 41-54.
http://dx.doi.org/10.1016/S0926-860X(02)00113-8
---------- VANCOUVER ----------
Mariño, F., Baronetti, G., Jobbagy, M., Laborde, M. Cu-Ni-K/γ-Al2O3 supported catalysts for ethanol steam reforming: Formation of hydrotalcite-type compounds as a result of metal-support interaction. Appl Catal A Gen. 2002;238(1):41-54.
http://dx.doi.org/10.1016/S0926-860X(02)00113-8