In this study reaction rate data are presented of potassium carbonate-catalysed CO, gasification of an activated carbon, measured in a Packed Bed Balance Reactor over a CO2 pressure range of 0.05-2.03 MPa at 1050 K. As a result of CO inhibition the reactor only behaves differentially at CO, conversi
Kinetics of catalyst loss during potassium-catalysed CO2 gasification of carbon
โ Scribed by David A. Sams; Tevan Talverdian; Farhang Shadman
- Publisher
- Elsevier Science
- Year
- 1985
- Tongue
- English
- Weight
- 755 KB
- Volume
- 64
- Category
- Article
- ISSN
- 0016-2361
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โฆ Synopsis
A significant fraction of the potassium catalyst can be lost by vaporization during catalysed carbon gasification. The extent of this loss depends primarily on the reaction start-up procedure. Temperature programmed experiments show that, under inert atmospheres, both KOH and K,CO, react with carbon to give a reduced form of potassium-carbon complex. The formation of this complex appears to be a prerequisite for the vaporization of potassium. The rate of vaporization at 800ยฐC follows a first-order expression. Under gasification conditions, only a fraction of the catalyst is in this reduced form; therefore, the rate of catalyst loss during gasification is lower than that under inert atmospheres.
The effect of catalyst loss on both the initial gasification rate and the variation in rate with conversion has been determined.
๐ SIMILAR VOLUMES
The literature on the potassium catalysed gasification of carbon in CO2 is critically reviewed with respect to the mechanism and the experimental 'facts' relevant to the mechanistic considerations. It is concluded that bulk intercalation compounds (CsK, r&K, etc.) are not present under gasification
The rates of the alkali catalysed water-gas shift reaction (WCS) and steam gasification of carbon have been studied at 1.5 x 10' Pa total pressure as a function of temperature (8OGlOOOK), feed composition (pure H,O or mixtures of H,O with either CO1, H, or CO), alkali metal (Na, K, Rb, Cs) and K,C03