The reaction mechanism of direct catalytic oxidation of methane to syngas o
ver a platinum catalyst under high temperature, short contact time conditio
ns was studied with a detailed reactor and reaction model. Based on a detai
led analysis of this mechanism, new integrated reactor concepts were deduce
d. Two concepts were studied in detail: a fixed bed reactor with integrated
recuperative heat exchange, and a catalytic membrane reactor with distribu
ted reactant feed. The reactor concepts are presented, and advantages and p
roblems of the concepts are discussed. (C) 2000 Elsevier Science B.V. All r
ights reserved.