CATALYTIC COMBUSTION OF METHANE

Authors
Citation
Jh. Lee et Dl. Trimm, CATALYTIC COMBUSTION OF METHANE, Fuel processing technology, 42(2-3), 1995, pp. 339-359
Citations number
48
Categorie Soggetti
Engineering, Chemical","Energy & Fuels","Chemistry Applied
Journal title
ISSN journal
03783820
Volume
42
Issue
2-3
Year of publication
1995
Pages
339 - 359
Database
ISI
SICI code
0378-3820(1995)42:2-3<339:CCOM>2.0.ZU;2-Y
Abstract
Palladium-based catalysts have been found to be the most efficient cat alysts for the catalytic oxidation of methane to carbon dioxide and wa ter. The catalytic oxidation is dependent on factors such as the oxyge n:methane feed ratio, the loading of precious metal on the support, th e nature of the support, the particle size of the precious metal and t he extent and nature of catalyst pretreatment. The reaction rate is fo und to be dependent on methane concentration, generally to the first o rder or less. The dependence of rate on oxygen pressure is found to de pend on the operating conditions. Because of overheating as a result o f high conversions of methane, chemical kinetics are often affected by mass and heat transfer. Deactivation of the catalyst can involve sint ering or poisoning. The thermal stability of the catalyst is strongly dependent on the support and the extent of overheating induced by oxid ation of methane. Sulphur oxides deactivate most noble metal catalysts with the exception of platinum.