We have studied the reaction of ethanol and water over Ni− CeO 2-x (111) model surfaces to elucidate the mechanistic steps associated with the ethanol steam reforming (ESR) reaction. Our results provide insights about the importance of hydroxyl groups to the ESR reaction over Ni-based catalysts. Systematically, we have investigated the reaction of ethanol on Ni−CeO 2-x (111) at varying Ce 3+ concentrations (CeO 1.8−2.0 ) with absence/presence of water using a combination of soft X-ray photoelectron spectroscopy (sXPS) and temperature-programmed desorption (TPD). Consistent with previous reports, upon annealing, metallic Ni formed on reduced ceria while NiO was the main component on fully oxidized ceria. Ni 0 is the active phase leading to both the C− C and C−H cleavage of ethanol but is also responsible for carbon accumulation or coking. We have identified a Ni 3 C phase that formed prior to the formation of coke. At temperatures above 600 K, the lattice oxygen from ceria and the hydroxyl groups from water interact cooperatively in the removal of coke, likely through a strong metal−support interaction between nickel and ceria that facilitates oxygen transfer.
■ INTRODUCTIONThe steam reforming of ethanol, C 2 H 5 OH + 3H 2 O → 6H 2 + 2CO 2 , is of interest to the chemical industry and fuel cell applications as it provides an alternative route to obtain renewable hydrogen through ethanol (or bioethanol), which can be readily extracted from sources such as biomass. 1,2 Typically, it involves the use of metal/oxide catalysts (i.e., Pt, Rh or Pd supported on CeO x ), and the reaction occurs by a complex series of mechanistic steps which are strongly coupled to a combination of factors, including the structural, chemical and electronic properties of the catalyst. 2,3 It has been postulated that this process requires both the metal and oxide parts of the catalyst to work co-operatively, with the metal component contributing to the C−C and C−H bond scissions of ethanol, and the oxide support promoting the dehydrogenation (or dehydration) reaction as well as the dissociation of H 2 O. 2−6 Catalysts based on nickel have emerged as promising candidates for the ethanol steam reforming reaction and have been reported to exhibit activity and selectivity comparable to that of noble metals such as Rh and Pd. 7,8 However, the drawback of nickel based catalysts is the high propensity for the loss in selectivity (i.e., through methanation), and deactivation which occurs through metal sintering and coke formation. 2,3,8−11 In particular, for coke formation, it could occur through the following side reactions during the steam reforming processes:① Dehydrogenation of the hydrocarbon groups from ethanol: −CH x (ad) → C + xH(ad) ② Boudouard reaction: CO(ad) + CO(ad) → CO 2 (g) + C ③ Polymerization: nC 2 H 4 → polymer → C + nH 2 (g) 2,3 In principle, minimizing the coke deposition could be achieved by perturbing the electronic properties of the metal through interactions with the oxide support, 7,12 by controlling particle size, 13,14...