Hydrogen Production and Carbon Formation during the Steam Reformer of Heptane in a Novel Circulating Fluidized Bed Membrane Reformer

Hydrogen production and carbon formation during the steam reforming of heptane over nickel-based catalyst are investigated in a circulating fluidized bed membrane reformer (CFBMR) at 723−823 K and 101.3−2026 kPa. A random carbon deposition and catalyst deactivation model is developed to account for...

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Veröffentlicht in:	Industrial & engineering chemistry research 2004-03, Vol.43 (6), p.1323-1333
Hauptverfasser:	Chen, Zhongxiang, Yan, Yibin, Elnashaie, Said S. E. H
Format:	Artikel
Sprache:	eng
Schlagworte:	Applied sciences Catalysis Catalytic reactions Chemical engineering Chemistry Exact sciences and technology General and physical chemistry Reactors Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
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