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Boundary layer effects on catalytic reactions with volume change

โœ Scribed by Peter Kehoe; John B. Butt


Publisher
American Institute of Chemical Engineers
Year
1972
Tongue
English
Weight
228 KB
Volume
18
Category
Article
ISSN
0001-1541

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โœ J.P.G. Kehoe; J.B. Butt ๐Ÿ“‚ Article ๐Ÿ“… 1970 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 227 KB

GEL'PERCHIN N. I. er al., Determination of average particle velocity in fluidised bed of small dimension, Khim. Prom. 196945371. GONCHARENKO G. K. et al., Determination of drop size in dispersion of immiscible liquid in apparatus with stirrer,

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Analytic expressions for the concentration distribution of reactant and for effectiveness factor have been obtained for zero-order catalytic reactions of the type A -+ bB. They can be summarized for various physical forms of catalyst to be 1 + mC l + m and where f(J), g(&, h te, -, and M i are diffe

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The gas-phase ignition of a premixed boundary layer flow by a nonisothermal plate with very large catalytic efficiency is studied. The catalytic upper side of the plate is in contact with the premixed gas while the lower side is held at constant temperature. The catalytic reaction is assumed to be i

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A theoretical analysis is presented of a mass transfer process vvhlch is coupled with an instantaneous homogeneous chemical reaction between two substances. It is shown how the appropriate diffusion and energy equations for laminar boundary layer flows past arbitrary surfaces may be solved in closed