Presently-available pressure drop correlations for trickle-bed reactors are not applicable over wide ranges of system conditions. The new, improved correlation for the pressure drop in a trickle-bed reactor presented here -derived from fundamental considerations and a wide-ranging data base of some
A simplified correlation for fixed bed pressure drop
✍ Scribed by Melda Özdinç Çarpinlioğlu; Emrah Özahi
- Publisher
- Elsevier Science
- Year
- 2008
- Tongue
- English
- Weight
- 670 KB
- Volume
- 187
- Category
- Article
- ISSN
- 0032-5910
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✦ Synopsis
An experimental study was conducted on the pressure drop characteristics of a variety of vertical packed beds in turbulent flow of air. The materials of different particle diameter, D p , with a range of sphericity Φ, 0.55 ≤ Φ ≤ 1.00 were used in random loose packing to produce beds of different lengths, L, with a range of porosity, ε, 0.36 ≤ ε ≤ 0.56. In the covered test cases the cross-sectional velocity distribution at the exit plane of the packed beds and the pressure drop ΔP Bed were measured in a particle Reynolds number range of Re p , 675 ≤ Re p ≤ 7772. The particular emphasis of the study was given to determine the influence of ε, Φ, D p , L, Re p on ΔP Bed . In this respect the measurements of ΔP Bed were compared with the well-known Ergun's Equation and the data were expressed in terms of correlations through introduced dimensionless parameters of pressure coefficient, ΔP ⁎ and exit Reynolds number Re exit . The proposed correlations of ΔP ⁎ = ΔP ⁎ (εRe p D p / L) and Re exit = Re exit (Re p D p / L) are found to be appropriate for the determination of ΔP Bed and mean exit velocity, U, respectively with an acceptable fit of experimental data in an error margin less than ± 20%. The methodology is presented in this paper as an alternative approach to the available literature on packed beds.
📜 SIMILAR VOLUMES
The pressure drop across a laboratory-scale catalyst packed bed with mechanical failure of catalyst pellets has been examined. It was found that the increased pressure drop can be described by a simplified model deduced from Ergun's equation. The pressure drop is determined mainly by the term of vis