TY - JOUR
T1 - Analysis of the Effectiveness Factor in a Fixed-Bed Tubular Reactor System
T2 - Catalytic Dehydrogenation of Cyclohexanol
AU - Carrasco-Venegas, Luis Américo
AU - González-Fernández, José Vulfrano
AU - Castañeda-Pérez, Luz Genara
AU - Medina-Collana, Juan Taumaturgo
AU - Palomino-Hernández, Guido
AU - Martínez-Hilario, Daril Giovanni
AU - Trujillo-Pérez, Salvador Apolinar
N1 - Publisher Copyright:
© 2023 by the authors.
PY - 2023/3
Y1 - 2023/3
N2 - The modeling and simulation of the catalytic dehydrogenation process of cyclohexanol in a fixed-bed catalytic reactor is presented, leading to finding the relationship between the effectiveness factor, the Thiele modulus, and the Weisz–Prater modulus of the catalyst particles with respect to their axial and radial position, for which the external conditions of concentration and temperature around each particle were previously obtained by applying the material and energy balances in the catalyst bed considering a two-dimensional pseudo-homogeneous model with radial diffusion. Subsequently, the material balances are established in terms of the molar flux density and conversion, the energy balance in terms of the heat flux density, Fick’s law, Fourier’s law, and the differential form of the effectiveness factor non-isothermal for each particle chosen based on the proposed meshing. The Thiele modulus calculated for most of the points is between 0.8 and 0.25, with a tendency towards the lower limit, and the theoretical values established as the limit for the Thiele modulus fluctuate between (Formula presented.). Therefore, the effectiveness factor analyzed is between 1 and (Formula presented.) ; this indicates that both the reaction speed as well as the diffusion speed within the particle have an influence on the intraparticle process, which is confirmed by the calculation of the Weisz–Prater modulus whose values are not (Formula presented.) 1 nor (Formula presented.) 1. The results obtained are subjected to a statistical test leading to analyzing whether there are significant differences both in the Thiele modulus, as well as in the effectiveness factor with respect to the radius and length of the reactor. It has been determined that there are no significant differences between the effectiveness factor with respect to the radius of the reactor; however, according to the analysis of variance, there are significant differences in the effectiveness factor with respect to length and, likewise, there are significant differences in the Thiele modulus and the Weisz–Prater modulus with respect to radius and length.
AB - The modeling and simulation of the catalytic dehydrogenation process of cyclohexanol in a fixed-bed catalytic reactor is presented, leading to finding the relationship between the effectiveness factor, the Thiele modulus, and the Weisz–Prater modulus of the catalyst particles with respect to their axial and radial position, for which the external conditions of concentration and temperature around each particle were previously obtained by applying the material and energy balances in the catalyst bed considering a two-dimensional pseudo-homogeneous model with radial diffusion. Subsequently, the material balances are established in terms of the molar flux density and conversion, the energy balance in terms of the heat flux density, Fick’s law, Fourier’s law, and the differential form of the effectiveness factor non-isothermal for each particle chosen based on the proposed meshing. The Thiele modulus calculated for most of the points is between 0.8 and 0.25, with a tendency towards the lower limit, and the theoretical values established as the limit for the Thiele modulus fluctuate between (Formula presented.). Therefore, the effectiveness factor analyzed is between 1 and (Formula presented.) ; this indicates that both the reaction speed as well as the diffusion speed within the particle have an influence on the intraparticle process, which is confirmed by the calculation of the Weisz–Prater modulus whose values are not (Formula presented.) 1 nor (Formula presented.) 1. The results obtained are subjected to a statistical test leading to analyzing whether there are significant differences both in the Thiele modulus, as well as in the effectiveness factor with respect to the radius and length of the reactor. It has been determined that there are no significant differences between the effectiveness factor with respect to the radius of the reactor; however, according to the analysis of variance, there are significant differences in the effectiveness factor with respect to length and, likewise, there are significant differences in the Thiele modulus and the Weisz–Prater modulus with respect to radius and length.
KW - Thiele modulus
KW - Weisz–Prater modulus
KW - catalyst
KW - effectiveness factor
UR - http://www.scopus.com/inward/record.url?scp=85151962283&partnerID=8YFLogxK
U2 - 10.3390/catal13030585
DO - 10.3390/catal13030585
M3 - Article
AN - SCOPUS:85151962283
SN - 2073-4344
VL - 13
JO - Catalysts
JF - Catalysts
IS - 3
M1 - 585
ER -