Abstract
The problem of a three-dimensional catalyst pellet with three characteristic sizes a, b, and c under conditions of intradiffusion resistance and a first-order reaction has been discussed. Using an exact solution in the Cartesian coordinate system, dependences for calculating the equivalent size and effectiveness factor of the pellet on Thiele parameter ψ have been proposed. A specific feature of the solution is the dependence of the pellet shape on the Thiele parameter. In dimensionless coordinates, at ψ → 0, the pellet surface tends to a sphere with unit radius; at ψ → ∞, it assumes the shape of a regular octahedron, the vertices of which are localized on the coordinate axes at a unit distance from the origin. In dimensional coordinates, depending on the ratio of parameters a, b, and c, the pellet can assume shapes similar to those of ellipsoids, discs, or “cigars.” At high Thiele parameter values, the effectiveness factor of nonspherical and spherical pellets is described by a single dependence equal to 3/ψ.
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REFERENCES
Malinovskaya, O.A., Beskov, I.S., and Slin’ko, M.G., Modelirovanie kataliticheskikh protsessov na poristykh zernakh (Simulation of Catalytic Processes on Porous Grains), Novosibirsk: Nauka, 1975, p. 266.
Aris, R., Introduction to the Analysis of Chemical Reactors, Prentice-Hall: Englewood Cliffs, 1965, p. 337.
Aris, R., Chem. Eng. Sci., 1957, vol. 6, p. 262.
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This work was supported by the Ministry of Science and Higher Education of the Russian Federation (project no. 0239-2021-0005).
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Translated by M. Timoshinina
Abbreviations and designations: C, reactant concentration; C0, reactant concentration on the outer surface of the pellet; \(\bar {c}\), dimensionless concentration of the reactant; x, y, and z, Cartesian coordinates; \(\bar {x}\), \(\bar {y}\), and \(\bar {z}\), dimensionless Cartesian coordinates; x0, half-width of a flat pellet; r0, radius of a cylindrical pellet; R0, radius of a spherical pellet; \(\bar {r}\), dimensionless radius in a cylindrical coordinate system; \(\bar {R}\), dimensionless radius in a spherical coordinate system; Δ, Laplace operator; k, reaction rate constant; D, effective diffusion coefficient; ψ, Thiele parameter; η, pellet effectiveness factor; ch, sh, and th, hyperbolic cosine, sine, tangent; I0 and I1, modified zero- and first-order Bessel functions; V, pellet volume; \(\bar {V}\), pellet volume in dimensionless variables; S, outer surface of the pellet; Re, equivalent pellet size; j, specific flux of the reactant; X, Y, and Z, auxiliary functions; kx, ky, kz, and В, constants; L, characteristic size of a nonspherical pellet.
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Zavarukhin, S.G., Rodina, V.O. Effect of Intradiffusion Resistance on the Chemical Process in a Nonspherical Catalyst Pellet. Kinet Catal 62, 551–556 (2021). https://doi.org/10.1134/S0023158421040133
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DOI: https://doi.org/10.1134/S0023158421040133