Abstract

Concentrated solar energy can be used to drive highly endothermic reactions, such as methane reforming. An attractive route is the parabolic trough technology, which is mature and relatively inexpensive but limited to temperatures below 600 °C, when methane conversions are low. However, high conversions are achievable if hydrogen is continuously removed from the reactive stream by a membrane selective to hydrogen. In this study, low temperature methane reforming in a membrane reactor is analyzed numerically by computational fluid dynamics over a wide range of operating parameters. Effects of temperature, steam-to-carbon ratio and space velocity on conversion, hydrogen recovery and carbon monoxide selectivity are specifically investigated. Our results show that concentration polarization can be significant. Below 500 °C the reactor performance is kinetically limited by the reforming reaction, while above this temperature hydrogen separation is a limiting factor. High hydrogen recovery is achievable even at high, industrially relevant space velocities. Importantly, hydrogen separation enhances water gas shift, reducing the concentration of carbon monoxide, the main source of coke formation at low temperatures.