1958
DOI: 10.1021/ie50585a038
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Carbon-Steam Reaction Kinetics from Pilot Plant Data

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Cited by 14 publications
(9 citation statements)
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“…Carbon dioxide, which appears late in experiments above 1150°a nd throughout experiments at 1040°, must result from the shift reaction 2. May et al (1958) suggest that the forward rate of the shift reaction is slower than the carbonsteam reaction rate and decreases with temperature. The equilibrium constant for the shift reaction 2 also decreases with temperature (Lowry, 1963).…”
Section: Discussion Of the Carbon-steam Reactionmentioning
confidence: 97%
“…Carbon dioxide, which appears late in experiments above 1150°a nd throughout experiments at 1040°, must result from the shift reaction 2. May et al (1958) suggest that the forward rate of the shift reaction is slower than the carbonsteam reaction rate and decreases with temperature. The equilibrium constant for the shift reaction 2 also decreases with temperature (Lowry, 1963).…”
Section: Discussion Of the Carbon-steam Reactionmentioning
confidence: 97%
“…0196-4313/81/1020-0006301.00/0 May et al (1958) studied coke gasification in fluidized and fixed beds and presented correlations for design purposes. They derived rate constants from the results on the fixed-bed reactor with the assumption of plug flow.…”
Section: Introductionmentioning
confidence: 99%
“…Squires (1961) analyzed the gasification data obtained by May et al (1958) and discussed the difference between the gasification rate observed in the fixed bed and that in the fluidized bed. He stated that the intensive solid circulation between the oxidizing and the reducing zones in the fluidized bed gasifier might increase the reactivity of the surface of the carbon particles, and this effect might be more clearly observed as the reaction temperature increases.…”
Section: Resultsmentioning
confidence: 99%