Conversion in Chemical Reactors using Hollow Cylindrical Catalyst Pellet
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Conversion in Chemical Reactors using Hollow Cylindrical Catalyst Pellet

Authors: Mohammad Asif

Abstract:

Heterogeneous catalysis is vital for a number of chemical, refinery and pollution control processes. The use of catalyst pellets of hollow cylindrical shape provide several distinct advantages over other common shapes, and can therefore help to enhance conversion levels in reactors. A better utilization of the catalytic material is probably most notable of these features due to the absence of the pellet core, which helps to significantly lower the effect of the internal transport resistance. This is reflected in the enhancement of the effectiveness factor. For the case of the first order irreversible kinetics, a substantial increase in the effectiveness factor can be obtained by varying shape parameters. Important shape parameters of a finite hollow cylinder are the ratio of the inside to the outside radii (κ) and the height to the diameter ratio (γ). A high value of κ the generally helps to enhance the effectiveness factor. On the other hand, lower values of the effectiveness factors are obtained when the dimension of the height and the diameter are comparable. Thus, the departure of parameter γ from the unity favors higher effectiveness factor. Since a higher effectiveness factor is a measure of a greater utilization of the catalytic material, higher conversion levels can be achieved using the hollow cylindrical pellets possessing optimized shape parameters.

Keywords: Finite hollow cylinder, Catalyst pellet, Effectiveness factor, Thiele Modulus, Conversion

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1332628

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[1] Mars, P. and Gorgels, M. J., 1964, Hydrogenation of acetylene -a theory of selectivity. In Chemical Reaction Engineering: Proceedings of the Third European Symposium, Supplement to Chem. Eng. Sci., pp. 55-65. Oxford: Pergamon Press.
[2] Michalko, E., 1966a, Method for oxidizing gaseous combustible waste products, U.S. Patent 3,259,454.
[3] Michalko, E.,1966b, Preparation of catalyst for the treatment of combustible waste products, U.S. Patent 3,259,589.
[4] Kasaoka, S. and Sakata, Y., 1968, Effectiveness factors for non-uniform catalyst pellets, J. Chem. Eng. Japan 1: 138-142.
[5] Villadsen, J. and Michelsen, M.J., 1978, Solution of Differential Equations Models by Polynomial Approximation, Prentice-Hall, New Jersey
[6] Becker, E. R. and Wei, J., 1977, Non-uniform distribution of catalysts on supports. Bimolecular Langmuir reactions, J. Catal. 46: 365-371.
[7] Juang, H.-D. and Weng, H.-S., 1983. Performance of catalysts with nonuniform activity profiles 2. Theoretical analysis for non-isothermal reactions. Ind. Eng. Chem. Fundam. 22: 224-230.
[8] Johnson, D. L., and Verykios, X. E., 1983, Selectivity enhancement in ethylene oxidation employing partially impregnated catalysts, J. Catal. 79: 156-163.
[9] Johnson, D. L., and Verykios, X. E., 1984, Effects of radially nonuniform distributions of catalytic activity on performance of spherical catalyst pellets, AI.ChEJ. 30: 44-50.
[10] Morbidelli, M., Servida, A. and Varma, A., 1982, Optimal catalyst activity profiles in pellets 1. The case of negligible external mass transfer resistance, Ind. Eng. Chem. Fundam. 21: 278-284.
[11] Morbidelli, M., Gavriilidis, A. and Varma, A., 2001, Catalyst design, Optimal distribution of catalyst in pellets, reactors and membranes, Cambridge University Press, Cambridge, UK.
[12] Wu, H., Brunovska, A., Morbidelli, M. and Varma, A., 1990, Optimal catalyst activity profiles in pellets VIII. General nonisothermal reacting systems with arbitrary kinetics, Chem. Eng. Sci. 45: 1855-1862; 46: 3328-3329.
[13] Baratti, R., Gavriilidis, A., Morbidelli, M., and Varma, A., 1994, Optimization of a non-isothermal non-adiabatic fixed-bed reactor using Dirac-type silver catalysts for ethylene epoxidation, Chem. Eng. Sci. 49: 1925-1936
[14] Hwang, S., Linke, P. and Smith, R., 2004, Heterogeneous catalytic reactor design with optimum temperature profile II: application o nonuniform catalyst, Chem. Eng. Sci. 59: 4245-4260.
[15] Armor, J.N., 2005, Do you really have a better catalyst? Appl. Catal. A: General 282: 1-4.
[16] Khanaev, V.M., Borisova, E.S. and Noskov, A.S., 2004, Optimization of the active component through the catalyst bed, Chem. Eng. Sci. 59: 1213-1220.
[17] Macias, M.J. and Ancheyta, J., 2004, Simulation of an isotheral hydrodesulfurization small reactor with different catalyst particle shapes, Catalysis Today, 98: 243-252.
[18] Buffham, B.A., 2000a, Design relations for hollow catalyst pellets, Chem. Eng. Res. Des. 78 Part A: 269-282.
[19] Buffham, B. A., 2000b, The size and compactness of particle of arbitrary shape: application to catalyst effectiveness factor, Chem. Eng. Sci. 55: 5803- 5811.