Journal
JOURNAL OF CATALYSIS
Volume 299, Issue -, Pages 249-260Publisher
ACADEMIC PRESS INC ELSEVIER SCIENCE
DOI: 10.1016/j.jcat.2012.11.027
Keywords
Catalyst; VPO; Conditioning; Micro-reactor; Kinetic modelling; Activity
Categories
Funding
- Engineering Doctorate Studentship
- Engineering and Physical Sciences Research Council (EPSRC)
- Johnson Matthey in the Industrial Doctoral Centre in Formulation Engineering, School of Chemical Engineering, University of Birmingham
Ask authors/readers for more resources
In heterogeneous catalysis, catalyst precursor activation and subsequent initial operation ('conditioning') under reaction conditions are often highly dynamic steps which are important in delivering effective catalyst performance over time scales of years. In many cases however, the phenomena occurring in both steps are often poorly understood. A novel approach to assess the conditioning step, comprising advanced catalyst testing methods in micro-reactors, catalyst characterisation and detailed kinetic and activity modelling techniques is demonstrated for a model system: the selective oxidation of n-butane to maleic anhydride (MA) using a pre-activated vanadium phosphorus oxide (VPO) catalyst. A transient kinetic model for the conditioning step is presented which describes the decline of population of active sites for three reaction pathways on the catalyst surface over time. Two reaction pathways, n-butane - -> MA and n-butane -> COx decay similarly with time whilst a third, MA - -> COx declines very sharply. The approach used provides important mechanistic information on catalyst reaction kinetics whilst also providing understanding the impact of reaction conditions on the catalyst during conditioning. (C) 2012 Elsevier Inc. All rights reserved.
Authors
I am an author on this paper
Click your name to claim this paper and add it to your profile.
Reviews
Recommended
No Data Available