1994
DOI: 10.1016/0009-2509(94)80023-5
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Significance of the radial porosity profile for the description of heat transport in wall-cooled packed beds

Abstract: Abatmct-Theinfluence of a radial porosity and velocity profile on the predicted temperature and concentration profiles in wall-cooled packed beds is studied, with and without an exothermic first-order chemical reaction, on the basis of literature correlations for the effective transport coefficients. Furthermore, values for the effective heat transport coefficients are obtained from "cold-flow" experiments by means of model fitting, with and without taking the radial velocity profile into account. The radial p… Show more

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Cited by 33 publications
(18 citation statements)
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“…Borkink and Westerterp (1994) also used a two‐region model, but their wall region was quite broad and depended on N and Re. Their model retained k r and h w as their intent was to show the influence of v z ( r ) and ε ( r ) on the estimation of the traditional parameters.…”
Section: Alternatives To the Kr–hw Approachmentioning
confidence: 99%
“…Borkink and Westerterp (1994) also used a two‐region model, but their wall region was quite broad and depended on N and Re. Their model retained k r and h w as their intent was to show the influence of v z ( r ) and ε ( r ) on the estimation of the traditional parameters.…”
Section: Alternatives To the Kr–hw Approachmentioning
confidence: 99%
“…Vortmeyer and Winter (1984) and Dixon and Yoo (1991)]. At such small tube-to-particle diameter ratios the dimensions of the particle are not negligible in comparison with that of the tube diameter so the applicability of continuum models becomes quite doubtful_ Also a wall effect is present due to the structured arrangement of the particles near the wall, leading to an increased porosity near the wall and to wall channelling [see Vortmeyer and Haidegger (1991), Daszkowki and Eigenberger (1992) and Borkink and Westerterp (1994)]. Because particles are ordered only within the first layers from the wall, the effect is more pronounced for fewer particles on a diameter.…”
Section: Theoretical Backgroundsmentioning
confidence: 99%
“…where expressions for K, A, and B are given elsewhere (see Vortmeyer and Schuster, 1983;Borkink and Westerterp, 1994). The porosity and velocity distributions are shown in Figure 2, where the wall effect can be clearly discerned.…”
Section: Reactor Modelmentioning
confidence: 99%