The use of finite element simulations to characterize the operating behavio
r of a microchemical reactor and enhance its design is described. Important
design issues for a microreactor, specifically heat and mass transfer, are
explored with the design of a micro-flow sensor and the redesign of the re
actor heater. The impact of the design choices for a flow sensor is quantit
atively evaluated and an optimal design is proposed. This design was fabric
ated and testing confirmed the simulation work. The reaction channel heater
was redesigned to improve thermal uniformity in the reaction zone. Simulat
ions showed that before ignition significant non-uniformity still existed,
but this was dramatically reduced after ignition. The use of previously rep
orted kinetic models for ammonia oxidation in microreactor simulations is a
lso discussed. It was found that kinetic models evaluated in conventional r
eactor experiments are inadequate for use in microreactor simulations becau
se of the lower operating temperature and broader range of temperatures of
the microreactor. (C) 2000 Elsevier Science Ltd. All rights reserved.