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Carbon-carbon dioxide reaction: Langmuir-Hinshelwood kinetics at intermediate pressures

โœ Scribed by J.F. Strange; P.L. Walker Jr.


Publisher
Elsevier Science
Year
1976
Tongue
English
Weight
692 KB
Volume
14
Category
Article
ISSN
0008-6223

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โœฆ Synopsis


Abstraet-The gasification of a very high purity natural graphite was studied at temperatures between 900 and 1007"C, at total gas pressures between 1.5 and 150 torr, and CO/CO, ratios between 0.098 and 2.0. Reactivity, expressed as weight loss per unit time, was constant over the bum-off range between about l&50%. Rates of gasification were seen to obey the equation derived from Langmui-Hinshelwood theory, that is Rate = k,pco,/(l + k2pC0 t k3pco,). If it is assumed that the inhibition of gasification by CO is caused by its lowering the steady-state concentration of oxygen complex which breaks down to product CO, individual rate constants for the oxygen transfer and gasification steps can be= calculated. Values of these rate constants and the equilibrium constant for the oxygen transfer step are considered in the light of literature results and theory.


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pressures between 15 and 150 torr. Gasification rates were measured using a high sensitivity microbalance. Since the average burn-off per rate determination was cu. 0.015%, all the necessary kinetic data could be obtained on one graphite sample, with a minimum amount of total burn-off. Gasification