作者: Benoit Chachuat , Alexander Mitsos , Paul I. Barton
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摘要: This paper presents the optimal design and operation of a micro power generation process that consists reactor, solid-oxide fuel cell (SOFC) two burners in stack fed with ammonia butane fuels. Hydrogen is produced from decomposition, while catalytically oxidized to produce heat maintain at sufficiently high temperature. In first part, novel model developed for predicting steady-state performance process. Subsequently, this used as basis study determine system. The optimization problem formulated so consumption rate utilities (ammonia butane) minimized, meeting specified demand maintaining its thermal equilibrium. dependence operating strategy on temperature losses system emphasized.