Affiliation:
1. Universidade do Porto
2. Instituto Superior de Ciências da Saúde – Norte, CESPU
Abstract
In this work, consideration is given to the problem of dissolution of a buried solid sphere in the liquid flowing uniformly through the packed bed around it. The differential equations describing fluid flow and mass transfer by advection and diffusion in the interstices of the bed are presented and the method for obtaining their numerical solution is indicated.From the surface concentration fields, given by the numerical solution, the concentration boundary layer thickness as a function of the relevant parameters were undertaken. Mathematical expressions that relate the dependence with the Peclet number and d/d1 ratio of an immersed active sphere are proposed to describe the approximate size of the concentration boundary layer thickness.
Publisher
Trans Tech Publications, Ltd.
Subject
General Chemical Engineering
Reference18 articles.
1. Alves MA, Delgado JMPQ, Guedes de Carvalho JRF (2006). Mass transfer from cylinders and plane surfaces buried in packed beds in alignment with the flow direction. Chemical Engineering Science 61(4): 1174-1183.
2. Avedesian MM, Davidson JF (1973). Combustion of carbon particles in a fluidised bed. Transactions of the Institution of Chemical Engineers 51: 121-131.
3. Bear J, Verruijt A (1987). Modelling groundwater flow and pollution with computer programs for sample cases, D. Reidel Publishing Company, UK.
4. Coelho MAN, Guedes de Carvalho JRF (1988a). Transverse dispersion in granular beds: Part I- Mass transfer from a wall and the dispersion coefficient in packed beds. Chemical Engineering Research and Design 66(2): 165-177.
5. Coelho MAN, Guedes de Carvalho JRF (1988b). Transverse dispersion in granular beds: Part II- Mass transfer from large spheres immersed in fixed or fluidised beds of small inert particles. Chemical Engineering Research and Design 66(2): 178-189.
Cited by
1 articles.
订阅此论文施引文献
订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献