Mass transfer in the spinning catalyst b
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J.R. Pereira; P.H. Calderbank
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Article
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1975
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Elsevier Science
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English
β 662 KB
A mathematical model is derived for the evaluation of the relative velocity between the gas and the pellets in two configurations of the spinning catalyst basket reactor. This slip velocity is then used to calculate the particle Reynolds number and hence mass transfer coefficients from well known co