Journal
CURRENT OPINION IN CHEMICAL ENGINEERING
Volume 1, Issue 3, Pages 272-280Publisher
ELSEVIER SCI LTD
DOI: 10.1016/j.coche.2012.03.001
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Funding
- Australian Research Council
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The paper is a synopsis of recent investigations on hydrocarbon reforming processes for syngas production. It is shown that CO2 emission may be substantially reduced in the carbon-intensive petrochemical and allied industries if it used as co-feed to a forced periodically operated reformer to minimise coking even at the low steam: carbon ratio of about 1. Additional benefits include, better flexibility in H-2:CO ratio to meet downstream olefins or oxygenates manufacture; improved product yield and catalyst longevity. The survey revealed that a basic oxide supported Ni-containing catalyst appropriately promoted with alkaline-earth or rare-earth metals is favoured over more expensive noble metals.
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