Selectivity and yield in complex reactions were calculated for CFBRs with reference to industrial processes; the effect of longitudinal dispersion, catalyst effectivness, heat dissipation and co-reactant axial distribution were also considered. Two mathematical models with and without longitudinal dispersion provided the theoretical results to be compared with experiments.

Theoretical and practical aspects of circulating fluidized bed reactors (CFBRs) for complex chemical systems / A., Gianetto; Pagliolico, SIMONETTA LUCIA; Rovero, Giorgio; Ruggeri, Bernardo. - In: CHEMICAL ENGINEERING SCIENCE. - ISSN 0009-2509. - 45:8(1990), pp. 2219-2225. [10.1016/0009-2509(90)80098-Y]

Theoretical and practical aspects of circulating fluidized bed reactors (CFBRs) for complex chemical systems

PAGLIOLICO, SIMONETTA LUCIA;ROVERO, Giorgio;RUGGERI, Bernardo
1990

Abstract

Selectivity and yield in complex reactions were calculated for CFBRs with reference to industrial processes; the effect of longitudinal dispersion, catalyst effectivness, heat dissipation and co-reactant axial distribution were also considered. Two mathematical models with and without longitudinal dispersion provided the theoretical results to be compared with experiments.
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11583/1652389
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