Approximate model for diffusion and reaction in a Porous catalyst with mass-transfer resistances

AIChE Journal ◽  
2001 ◽  
Vol 47 (9) ◽  
pp. 2131-2135 ◽  
Author(s):  
Mirosław K. Szukiewicz
1982 ◽  
Vol 47 (11) ◽  
pp. 3013-3018
Author(s):  
František Kaštánek ◽  
Jindřich Zahradník ◽  
Germanico Ocampo

Calculation procedure is suggested for flow intensity of substrate toward reaction interface of immobilized enzyme at simultaneous effect of enzymatic reaction and internal diffusion. The approximate model is presented in an analytical form for the basic type of Michaelis-Menten kinetics and for the case of inhibition in excess of substrate.


2020 ◽  
Vol 21 (1) ◽  
pp. 124-131
Author(s):  
V. V. Kalinchak ◽  
A. S. Chernenko ◽  
A. F. Fedorenko ◽  
A. N. Sofronkov ◽  
V. V. Kramarenko

The problem of heat and mass transfer of a porous catalyst particle is considered. On the her surface, including the inner surface of the pores, an irreversibly heterogeneous first-order reaction proceeds. It has been analytically shown that in a heated gas mixture, the catalyst's porosity reduces the minimum impurity's concentration of catalytic spontaneous combustion in the mixture and increases the catalyst particle's corresponding diameter. This concentration corresponds to the external kinetic and internal diffusion reaction's modes.


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