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This document describes a kinetic study of the steam reforming of methanol over a Pt/In2O3/Al2O3 catalyst. Kinetic measurements were performed in a microstructured monolithic reactor with external recycle to eliminate temperature and concentration gradients. The kinetic data revealed that the rate of methanol consumption depends mainly on methanol partial pressure and only slightly on water partial pressure. A mechanistic rate model was derived based on Langmuir-Hinshelwood rate equations and surface specie

Author

Hayat Yusuf

Language

EN