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 new, improved liquid hold-up correlation for trickle-bed reactors
β Scribed by M.J. Ellman; N. Midoux; G. Wild; A. Laurent; J.C. Charpentier
- Publisher
- Elsevier Science
- Year
- 1990
- Tongue
- English
- Weight
- 917 KB
- Volume
- 45
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
Presently available liquid hold-up correlations for trickle-bed reactors are not applicable over wide ranges of system conditions. The new, improved correlation for the liquid hold-up in a trickle-bed reactor presented here, derived from fundamental considerations and a wide-ranging data base of some 5000 hydredynamic experimental results, is applicable to industrial trickle-bed reactors since it is based on wide variations of all the important variables, including measurements at higb pressures. No other previously derived correlations are applicable to high pressure operations. A comparison with recent data on liquid hold-up in co-current upflow of gas and liquid shows that the correlation proposed for high interaction downflow gives a fair estimate of the upflow data, as long as the liquid is not foaming.
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## Abstract Current correlations aimed at estimating the extent of liquid backβmixing, via an axial dispersion coefficient, in trickleβbed reactors continue to draw doubts on their ability to conveniently represent this important macroscopic parameter. A comprehensive database containing 973 liquid