甲醇水蒸汽重整微反应器数学模拟

mathematical model analysis of a micro-channel reactor concerning steam reforming of methanol has been established. The concentration and temperature profiles in axial direction inside the micro-channel are obtained by orthogonal collection method. The effects of thickness of catalyst coating and size of micro-channel on the performance of the micro-channel steam reformer are shown. By comparing the results of model analysis and experiments, it is confirmed the mathematical model can be used qualitatively and can lay a theoretical foundation for the design and application of micro-channel reactor concerning steam reforming of methanol.