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Monolithic FeOx/Al2O3 catalysts for ammonia oxidation and nitrous oxide decomposition

(1.2–8.3)%FeO х /Al 2 O 3 monolith catalysts have been prepared by impregnating alumina with aqueous solutions of iron(III) nitrate and oxalate and have been tested in NH 3 oxidation and in the selective decomposition of N 2 O in mixtures resulting from ammonia oxidation over a Pt–Rh gauze pack unde...

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Published in:Kinetics and catalysis 2017, Vol.58 (2), p.167-178
Main Authors: Pinaeva, L. G., Dovlitova, L. S., Isupova, L. A.
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Language:English
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creator Pinaeva, L. G.
Dovlitova, L. S.
Isupova, L. A.
description (1.2–8.3)%FeO х /Al 2 O 3 monolith catalysts have been prepared by impregnating alumina with aqueous solutions of iron(III) nitrate and oxalate and have been tested in NH 3 oxidation and in the selective decomposition of N 2 O in mixtures resulting from ammonia oxidation over a Pt–Rh gauze pack under conditions of nitric acid synthesis (800–900°C). In the case of the support calcined at 1200°C, the catalyst is dominated by bulk Fe 2 O 3 particles localized on the Al 2 O 3 surface. The activity of these samples in both reactions decreases with a decreasing active component content, thus limiting the potential of Fe 2 (C 2 O 4 ) 3 · 5H 2 O, an environmentally friendlier but poorly soluble compound, as a substitute for Fe(NO 3 ) 3 · 9H 2 O. Decreasing the support calcination temperature to 1000°C or below leads to the formation of a highly defective Fe–Al–O solid solution in the (1.2–2.7)%FeO х /Al 2 O 3 catalysts. The surface layers of the solid solution are enriched with iron ions or stabilize ultrafine FeO х particles. The catalytic activity of these samples in both reactions is close to the activities measured for ~8%FeO х /Al 2 O 3 samples prepared using iron nitrate.
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Decreasing the support calcination temperature to 1000°C or below leads to the formation of a highly defective Fe–Al–O solid solution in the (1.2–2.7)%FeO х /Al 2 O 3 catalysts. The surface layers of the solid solution are enriched with iron ions or stabilize ultrafine FeO х particles. 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S.</creatorcontrib><creatorcontrib>Isupova, L. A.</creatorcontrib><title>Monolithic FeOx/Al2O3 catalysts for ammonia oxidation and nitrous oxide decomposition</title><title>Kinetics and catalysis</title><addtitle>Kinet Catal</addtitle><description>(1.2–8.3)%FeO х /Al 2 O 3 monolith catalysts have been prepared by impregnating alumina with aqueous solutions of iron(III) nitrate and oxalate and have been tested in NH 3 oxidation and in the selective decomposition of N 2 O in mixtures resulting from ammonia oxidation over a Pt–Rh gauze pack under conditions of nitric acid synthesis (800–900°C). In the case of the support calcined at 1200°C, the catalyst is dominated by bulk Fe 2 O 3 particles localized on the Al 2 O 3 surface. The activity of these samples in both reactions decreases with a decreasing active component content, thus limiting the potential of Fe 2 (C 2 O 4 ) 3 · 5H 2 O, an environmentally friendlier but poorly soluble compound, as a substitute for Fe(NO 3 ) 3 · 9H 2 O. 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The activity of these samples in both reactions decreases with a decreasing active component content, thus limiting the potential of Fe 2 (C 2 O 4 ) 3 · 5H 2 O, an environmentally friendlier but poorly soluble compound, as a substitute for Fe(NO 3 ) 3 · 9H 2 O. Decreasing the support calcination temperature to 1000°C or below leads to the formation of a highly defective Fe–Al–O solid solution in the (1.2–2.7)%FeO х /Al 2 O 3 catalysts. The surface layers of the solid solution are enriched with iron ions or stabilize ultrafine FeO х particles. The catalytic activity of these samples in both reactions is close to the activities measured for ~8%FeO х /Al 2 O 3 samples prepared using iron nitrate.</abstract><cop>Moscow</cop><pub>Pleiades Publishing</pub><doi>10.1134/S0023158417020100</doi><tpages>12</tpages></addata></record>
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title Monolithic FeOx/Al2O3 catalysts for ammonia oxidation and nitrous oxide decomposition
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