TY - JOUR
T1 - Dead-core solutions to fast diffusion–reaction equation for catalyst slabs with power-law reaction kinetics and external mass transfer resistance
AU - Skrzypacz, Piotr
AU - Kadyrbek, Alua
AU - Golman, Boris
AU - Andreev, Vsevolod V.
N1 - Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2022/10/15
Y1 - 2022/10/15
N2 - This paper investigates semi-analytic approaches used to solve a two-point boundary value problem for nonlinear fast diffusion–reaction equation for catalytic slabs with external mass resistance. The kinetics considered is the power-law type having a fractional reaction exponent. The semi-analytic approach for dead-core problems with Fickian diffusion is generalized to models with non-Fickian diffusion. The dimensionless steady-state equation for mass conservation in the catalyst slab for a single n-th order chemical reaction and the non-Fickian diffusion model is derived and studied. We show that the dead zone can appear close to the pellet center under certain combinations of the following parameters: slab size, effective diffusivity, mass transfer coefficient, bulk reactant concentration, reaction order, reaction rate constant, and diffusion exponent. We also study the effects of the process parameters on the concentration profiles and length of dead zones. Analytical findings are verified by numerical simulations.
AB - This paper investigates semi-analytic approaches used to solve a two-point boundary value problem for nonlinear fast diffusion–reaction equation for catalytic slabs with external mass resistance. The kinetics considered is the power-law type having a fractional reaction exponent. The semi-analytic approach for dead-core problems with Fickian diffusion is generalized to models with non-Fickian diffusion. The dimensionless steady-state equation for mass conservation in the catalyst slab for a single n-th order chemical reaction and the non-Fickian diffusion model is derived and studied. We show that the dead zone can appear close to the pellet center under certain combinations of the following parameters: slab size, effective diffusivity, mass transfer coefficient, bulk reactant concentration, reaction order, reaction rate constant, and diffusion exponent. We also study the effects of the process parameters on the concentration profiles and length of dead zones. Analytical findings are verified by numerical simulations.
KW - Catalytic pellet
KW - Dead zone
KW - Diffusion and reaction
KW - Fast diffusion equation
KW - Non-Fickian diffusion
KW - Power-law kinetics
KW - Semi-analytic solution
UR - https://www.scopus.com/pages/publications/85130381075
UR - https://www.scopus.com/pages/publications/85130381075#tab=citedBy
U2 - 10.1016/j.cej.2022.136722
DO - 10.1016/j.cej.2022.136722
M3 - Article
AN - SCOPUS:85130381075
SN - 1385-8947
VL - 446
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 136722
ER -