Abstract

Reforming processes are the backbone of hydrogen production routes, given the flexibility of their feedstock, such as methane, carbon dioxide, ammonia, waste plastics, or biomass. Heat transfer is a drawback at the industrial scale, reducing efficiency. We incorporate SiC in the technical composite, extrudate catalyst and develop a holistic approach to optimize and understand the effect of each constituent and its mixtures. We apply Ni-Ce as an active phase, bentonite or kaolin as a binder, alumina as a filler, and carborundum as the heat-transport carrier. We characterize the extrudate catalysts using various techniques, including crushing strength and thermal conductivity. We test the samples in the steam reforming of a model molecule, calculate the kinetics and deactivation, perform a multivariate analysis, and model an industrial reformer. The results lead to optimal catalyst formulations, demonstrating the authentic influence of individual and combined constituent at multiple scales: reaction, deactivation, properties, and reactor performance.

Department(s)

Mechanical and Aerospace Engineering

Publication Status

Open Access

Comments

King Abdullah University of Science and Technology, Grant BAS/1/1403

Keywords and Phrases

Hydrogen production; Kinetics and deactivation; Principal component analysis; Reactor modeling; Steam and dry reforming; Technical catalyst

International Standard Serial Number (ISSN)

0016-2361

Document Type

Article - Journal

Document Version

Citation

File Type

text

Language(s)

English

Rights

© 2025 Elsevier, All rights reserved.

Publication Date

01 Oct 2023

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