Logo image
Carbon deposition and gasification kinetics of used lanthanide-promoted Co-Ni/Al2O3 catalysts from CH4 dry reforming
Journal article   Peer reviewed

Carbon deposition and gasification kinetics of used lanthanide-promoted Co-Ni/Al2O3 catalysts from CH4 dry reforming

S.Y. Foo, C.K. Cheng, T-H Nguyen, E.M. Kennedy, B.Z. Dlugogorski and A.A. Adesina
Catalysis Communications, Vol.26, pp.183-188
2012
url
Link to Published Version *Subscription may be requiredView

Abstract

The kinetics of both carbon deposition and removal on lanthanide-promoted Co-Ni/Al 2O 3 dry reforming catalysts were investigated. Carbon deposition rate decreased with temperature in the range, 923-1023 K. Catalyst regeneration (via TPR-TPO-TPR and TPO-TPR) may be adequately modelled by the geometrical contracting volume gas-solid reaction model. Lanthanide promotion resulted in lower coke formation due to interaction of the rare-earth oxide with the more reactive surface carbonaceous matter in redox reactions, while the amount of the less reactive deposited carbon pool remained similar in all catalysts. Although both regeneration schemes studied were able to completely remove all carbon, samples from the TPO-TPR regime experienced marginal sintering.

Details

UN Sustainable Development Goals (SDGs)

This output has contributed to the advancement of the following goals:

#7 Affordable and Clean Energy
#13 Climate Action

Source: InCites

Metrics

InCites Highlights

These are selected metrics from InCites Benchmarking & Analytics tool, related to this output

Collaboration types
Domestic collaboration
Citation topics
2 Chemistry
2.41 Catalysts
2.41.546 Catalytic Hydrogenation
Web Of Science research areas
Chemistry, Physical
ESI research areas
Chemistry
Logo image