Modeling and Design of a Multi-Tubular Packed-Bed Reactor for Methanol Steam Reforming over a Cu/ZnO/Al<sub>2</sub>O<sub>3</sub> Catalyst

Modeling and Design of a Multi-Tubular Packed-Bed Reactor for Methanol Steam Reforming over a Cu/ZnO/Al<sub>2</sub>O<sub>3</sub> Catalyst

Methanol as a hydrogen carrier can be reformed with steam over Cu/ZnO/Al<sub>2</sub>O<sub>3</sub> catalysts. In this paper a comprehensive pseudo-homogenous model of a multi-tubular packed-bed reformer has been developed to investigate the impact of operating conditions and g...

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Bibliographic Details
Main Authors: Jimin Zhu, Samuel Simon Araya, Xiaoti Cui, Simon Lennart Sahlin, Søren Knudsen Kær
Format: Article
Language:English
Published: MDPI AG 2020-01-01
Series:Energies
Subjects:
methanol steam reforming
multi-tubular packed-bed reformer
hydrogen production
temperature profile
geometric parameter
Online Access:https://www.mdpi.com/1996-1073/13/3/610

Internet

https://www.mdpi.com/1996-1073/13/3/610

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