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Transition metal oxide catalysts as an alternative for the oxidation of nitrogen monoxide to nitrogen dioxide: kinetic modelling at high space velocity.

Authors :
Tecchio, Leonardo
Marín, Pablo
Díez, Fernando V
Ordóñez, Salvador
Source :
Journal of Chemical Technology & Biotechnology; Feb2016, Vol. 91 Issue 2, p359-366, 8p
Publication Year :
2016

Abstract

BACKGROUND The oxidation of NO to NO<subscript>2</subscript> is a key step in environmental pollution abatement techniques, such as 'fast- SCR' or diesel engine catalytic traps. In both cases, the conversion of an important fraction of NO into NO<subscript>2</subscript> is a key step. In this work, two commercially available transition metal oxide catalysts, CuMn and CuCr-based, are studied as an alternative to noble metal catalysts (a Pt/ Al<subscript>2</subscript>O<subscript>3</subscript> catalyst is used as reference catalyst). RESULTS Steady NO conversion is obtained after the first 1-2 h of operation. The experiments, carried out in an isothermal fixed-bed reactor operating at high space velocities (5.60 g<subscript>cat</subscript> min mol<superscript>-1</superscript>, GHSV<subscript>monolith</subscript><subscript>-eq.</subscript> = 83 000 h<superscript>-1</superscript>) with 500 ppm NO and 20% oxygen, showed that the optimum operating temperature is 380 °C for the CuMn catalyst, 430 °C for the CuCr catalyst and 366 °C for a 0.5% Pt/ Al<subscript>2</subscript>O<subscript>3</subscript> catalyst. CONCLUSIONS The CuMn catalyst performed very similarly to the 0.5% Pt/ Al<subscript>2</subscript>O<subscript>3</subscript> catalyst in the vicinity of 380 °C, being a good and cheaper alternative to noble metal catalysts. Kinetic measurements obtained under different conditions, e.g. 3.73-5.60 g<subscript>cat</subscript> min mol<superscript>-1</superscript> ( GHSV<subscript>monolith</subscript><subscript>-eq.</subscript> = 83 000-125 000 h<superscript>-1</superscript>), 300-900 ppm NO, 1-20% oxygen concentration and 330-480 °C, have been found to fit a mechanistic kinetic model based on the reaction between gas nitrogen oxide and adsorbed oxygen. © 2014 Society of Chemical Industry [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
02682575
Volume :
91
Issue :
2
Database :
Complementary Index
Journal :
Journal of Chemical Technology & Biotechnology
Publication Type :
Academic Journal
Accession number :
112212831
Full Text :
https://doi.org/10.1002/jctb.4575