Abstract <p>Using the Pechini method, LaFe<sub>1 <i>– x</i></sub>Ni<sub><i>x</i></sub>O<sub>3</sub> (<i>x</i> = 0, 0.6, 1) perovskite-containing catalysts supported on a monolith corundum support were prepared and studied in the reaction of high-temperature decomposition of nitrous oxide. It is shown that the supported catalysts can be arranged in the following order by activity: LaFeO<sub>3</sub>/α-Al<sub>2</sub>O<sub>3</sub> &gt; LaFe<sub>0.4</sub>Ni<sub>0.6</sub>O<sub>3</sub>/α-Al<sub>2</sub>O<sub>3</sub> &gt; LaNiO<sub>3</sub>/α-Al<sub>2</sub>O<sub>3</sub>, which differs from the activity order of perovskites without a support. The change in the activity order is due to the interaction of the impregnating solution with the support, as a result of which an admixture of the nickel aluminate phase, inactive in this reaction, can be formed in nickel-containing catalysts. The LaFeO<sub>3</sub>/α-Al<sub>2</sub>O<sub>3</sub> catalyst with an active component content of ~5%, even with a fragment height of 20 mm (and a contact time of 0.06 s), provides a high (~84%) conversion of nitrous oxide, due to the possible presence of an impurity of the dispersed phase of active Fe<sub>2</sub>O<sub>3</sub> as well.</p>

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Honeycomb Supported LaFe1 – xNixO3 (x = 0, 0.6, 1) Perovskite Catalysts for High-Temperature N2O Decomposition

  • L. A. Isupova,
  • Yu. A. Ivanova,
  • A. N. Salanov

摘要

Abstract

Using the Pechini method, LaFe1 – xNixO3 (x = 0, 0.6, 1) perovskite-containing catalysts supported on a monolith corundum support were prepared and studied in the reaction of high-temperature decomposition of nitrous oxide. It is shown that the supported catalysts can be arranged in the following order by activity: LaFeO3/α-Al2O3 > LaFe0.4Ni0.6O3/α-Al2O3 > LaNiO3/α-Al2O3, which differs from the activity order of perovskites without a support. The change in the activity order is due to the interaction of the impregnating solution with the support, as a result of which an admixture of the nickel aluminate phase, inactive in this reaction, can be formed in nickel-containing catalysts. The LaFeO3/α-Al2O3 catalyst with an active component content of ~5%, even with a fragment height of 20 mm (and a contact time of 0.06 s), provides a high (~84%) conversion of nitrous oxide, due to the possible presence of an impurity of the dispersed phase of active Fe2O3 as well.