Preparation and characterisation of γ-Al2O3 particles-supported Rh/Ce0.9Pr0.1O2 catalyst for N2O decomposition in the presence of O2, H2O and NOx
| Autor: | Agustín Bueno-López, S. Parres-Esclapez, María José Illán-Gómez, C. Salinas-Martínez de Lecea |
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| Rok vydání: | 2012 |
| Předmět: |
Inorganic chemistry
Analytical chemistry chemistry.chemical_element Management Monitoring Policy and Law Pollution Decomposition Nitrogen Industrial and Manufacturing Engineering Catalysis chemistry.chemical_compound General Energy Adsorption chemistry X-ray photoelectron spectroscopy Nitric acid Chemisorption NOx |
| Zdroj: | International Journal of Greenhouse Gas Control. 11:251-261 |
| ISSN: | 1750-5836 |
| DOI: | 10.1016/j.ijggc.2012.09.003 |
| Popis: | A supported catalyst composed by the active phase Rh/Ce0.9Pr0.1O2 loaded on γ-Al2O3 particles was prepared and characterised by SEM, TEM, XRD, Raman spectroscopy, N2 adsorption at −196 °C, H2-TPR and XPS. The catalytic decomposition of N2O was studied in simulated nitric acid plant streams (in the presence of O2, H2O and/or NOx) both in a fix-bed reactor and by in situ DRIFTS-MS experiments. The supported catalyst is able to decompose N2O from around 350–400 °C in the presence of O2, H2O and/or NOx, and this temperature would be enough to decompose N2O in a nitric acid production plant after the expansion turbine, avoiding the use of an additional energy input. Among O2, H2O and NOx, NOx is the strongest inhibitor and O2 the weakest. The inhibiting effect of O2 is attributed to its reversible chemisorption on catalyst active sites, while the effect of H2O and NOx is mainly related with their irreversible chemisorption. The inhibition of H2O is not as high as that of NOx because the product of H2O chemisorption (Ce–OH surface groups) is suitable for N2O chemisorption and decomposition, while the surface nitrogen species created upon NOx chemisorption are not. |
| Databáze: | OpenAIRE |
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