The steam reforming of ethanol was studied at 823 K on 10% Co/Al2O3 samples calcined at 973 K and reduced at different temperatures from 773 K to 1173 K. The catalysts were characterized by XPS, XRD, TPR, Raman and DRIFT spectroscopy. XRD results revealed that spinel structures are detectable after the thermal treatment of Co/Al2O3, which could be attributed mainly to Co3O4 formation. TPR and XPS measurements show that even the high temperature (1173 K) reduction is not sufficient to totally reduce Co to metallic state. The ethanol conversion at 823 K was relatively stable and it was higher than 90% in all cases, but the product distribution as a function of time on stream significantly depended on the reduction temperature. The selectivities of H-2, CO2, and CH4 formation decreased in time but those of ethylene, acetone and acetaldehyde increased. The changes became less pronounced when the reduction temperature increased, so the H-2, CO, and CO2 selectivities increased while that of ethylene decreased significantly as a function of reduction temperature. XPS measurements revealed a new low binding energy state in the Co 2p(3/2) region during the reaction when the samples were reduced at or below 973 K. This feature was assigned to the formation of a very thin Co layer. On the used catalysts reduced at or above 973 K structured carbon was detected. On the XP spectra several carbon species were identified at the beginning of the reaction. A new feature was also found at lower binding energy which became more and more dominant with the exception of Co/Al2O3 reduced at 1173 K. These species could be assigned as CoCx carbide-like structures rather than a structured carbon layer. It was found that the surface carbon formed in the reaction gradually influences the product distribution. The carbon which probably is built in the Co subsurface poisons the reactivity of the metal and the effect of the support comes in the forefront. The structured carbon layer formed on the Co/Al2O3 reduced at high temperature does not influence the hydrogen formation in the ethanol reforming. (C) 2017 Elsevier Inc. All rights reserved.
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UNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, ArgentinaUNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, Argentina
Quincoces, CE
Dicundo, S
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UNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, ArgentinaUNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, Argentina
Dicundo, S
Alvarez, AM
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UNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, ArgentinaUNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, Argentina
Alvarez, AM
González, MG
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UNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, ArgentinaUNLP, CONICET, Ctr Invest & Desarrollo Proc Catalitcos, RA-1900 La Plata, Argentina
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Univ Nacl La Plata, CONICET, Fac Ciencias Exactas, CINDECA, RA-1900 La Plata, Argentina
Univ Nacl La Plata, Fac Ingn, RA-1900 La Plata, ArgentinaUniv Nacl La Plata, CONICET, Fac Ciencias Exactas, CINDECA, RA-1900 La Plata, Argentina
Pompeo, Francisco
Gazzoli, Delia
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Univ Roma La Sapienza, Dipartimento Chim, I-00185 Rome, ItalyUniv Nacl La Plata, CONICET, Fac Ciencias Exactas, CINDECA, RA-1900 La Plata, Argentina
Gazzoli, Delia
Nichio, Nora N.
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Univ Nacl La Plata, CONICET, Fac Ciencias Exactas, CINDECA, RA-1900 La Plata, Argentina
Univ Nacl La Plata, Fac Ingn, RA-1900 La Plata, ArgentinaUniv Nacl La Plata, CONICET, Fac Ciencias Exactas, CINDECA, RA-1900 La Plata, Argentina