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Dry reforming of methane with isotopic gas mixture over Ni-based pyrochlore catalyst
Affiliation:1. Cain Department of Chemical Engineering, Louisiana State University, Baton Rouge, LA 70803, USA;2. National Energy Technology Laboratory, US Department of Energy, Morgantown, WV 26507, USA;1. Department of Applied Chemistry, National Chiao-Tung University, 1001 University Rd., Hsinchu, 30010, Taiwan;2. Center for Emergent Functional Matter Science, National Chiao-Tung University, Hsinchu, 30010, Taiwan;3. Graduate Degree Program of Science and Technology of Accelerator Light Source, National Chiao Tung University, Hsinchu, 30010, Taiwan;1. Department of Applied Chemistry, National Chiao Tung University, 1001 University Rd., Hsinchu 30010, Taiwan;2. Graduate Degree Program of Science and Technology of Accelerator Light Source, National Chiao-Tung University, Hsinchu 30010, Taiwan;1. Laboratorio de Procesos Catalíticos, Dpto. de Ingeniería Química, ITHES (UBA-CONICET), Universidad de Buenos Aires (UBA), Ciudad Autónoma de Buenos Aires, Argentina;2. Grupo de Procesos Catalíticos (PROCAT), Universidad de Málaga (UMA), Málaga, Spain;1. Department of Chemistry, Nanchang University, Nanchang 330031, PR China;2. Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, PR China;3. Jiangxi Golden Century Advance Materials Co. Ltd, Nanchang 330013, PR China;1. Department of Chemistry, Heterogeneous Catalysis Laboratory, University of Cyprus, 1 University Ave., University Campus, P.O. Box 20537, CY 1678, Nicosia, Cyprus;2. Department of Environmental Sciences and Engineering, National Institute of Chemistry, Hajdrihova 19, SI-1001 Ljubljana, Slovenia
Abstract:Dry reforming of methane was carried out using isotopic 13CO2 and C18O2 gases over a Ni-based pyrochlore catalyst that was synthesized using the modified Pechini method. In this method, 1 wt% Ni was doped into the La2Zr2O7 pyrochlore structure. The catalyst was characterized by H2-TPR, TPO, and XRD and tested for its methane reforming activity under CO2 dry-reforming reaction conditions.The results of repeated TPR/TPO cycles up to 950 °C showed that the consecutive TPR profiles were nearly identical, indicating that the catalyst was stable at high temperatures, and that the nickel oxidation/reduction processes were reversible. The dry-reforming experimental results using labelled 13CO2 gas showed the syngas production for this material proceeded through the activation of CH4 with O that came from breaking one of the Csingle bondO bonds of CO2 with the latter reaction (CO2 activation) likely occurring at oxygen vacancies at or near the Ni particle-pyrochlore interface. It was also found that only a small portion of the CO originated from CH4. A variation of the same experimental test, but using 12C18O2, revealed only 12C18O was formed and no 12C16O was detected, ruling out the possibility of reaction with the lattice oxygen in the catalyst structure with this material. Over this catalyst, the activated CH4 appeared to dissociate to elemental carbon on the catalyst surface, which was determined to be the source of carbon from a post reaction TPO of the catalyst that was exposed to the 13CO2single bond12CH4 mixture. No carbon deposition appeared to originate from 13CO2.
Keywords:Nickel  Dry-reforming mechanism  Pyrochlore  Syngas  Methane activation
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