Modeling of sorption enhanced steam methane reforming in an adiabatic fixed bed reactor

▸ Dynamic model to describe the SER operation in packed bed reactor. ▸ Adiabatic conditions to take advantage of thermal neutrality of overall SER reaction. ▸ Confirmation of theoretical viability of SER process at large scale for H2 production. ▸ High P, high S/C ratio, moderate T to yield 95% H2 purity and 85% CH4 conversion.