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Pressure loss and liquid holdup in packed bed reactor with cocurrent gas-liquid down flow

TLDR
In this paper, a two-phase pressure loss based on an energy (not momentum) balance was correlated in terms of Lockhart-Martinelli parameters as follows : φl=1.30+1.40 as 1/3χ0.22 (as in mm-1)
Abstract
Paying attention to the discrepancy between available data, probably due to the uncertainty in void fraction, the entrance end effect and characteristics of the experimental method, newexperimental results were obtained for air-water flow in 65.8 and 122 mmφ. columns packed with glass spheres of six different sizes between 2.59 and 24.3 mm0.The two-phase pressure loss based on an energy (not momentum) balance was correlated in terms of Lockhart-Martinelli parameters as follows : φl=1.30+1.85χ-0.85, 0.1<χ<20The total liquid holdup Ri was determined by weighing the excess weight of bed in operation over the dry column. The result was dependent on the specific surface area of the bed as and correlated by Rl=0.40 as1/3χ0.22 (as in mm-1)The present result on total holdup was higher than available results obtained by quickclosing valve, which measured probably the operating holdup. Data of void fraction for spherical packings are appended and the differences in void fraction and its reproducibility due to packing procedure are noted.

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Book ChapterDOI

Mass-Transfer Rates in Gas-Liquid Absorbers and Reactors

TL;DR: In this paper, the authors present the techniques, results, and opinions on mass-transfer coefficients and interfacial areas in most types of absorbers and reactors in a gas-liquid mass transfer with chemical reaction.
Journal ArticleDOI

Pressure drop and liquid holdup for two-phase concurrent flow in packed beds

TL;DR: In this paper, a correlation valid for a free liquid trickling, modified in order to take into account the effect of the pressure drop, is proposed and used to correlate liquid holdup in the presence of a concurrent gas flow.
Journal ArticleDOI

Pressure drop and liquid holdup in high pressure trickle-bed reactors

TL;DR: In this paper, the effect of high pressure on pressure drop and liquid holdup in the trickle flow regime was investigated using a phenomenological analysis based on annular two-phase flow in a slit.
Journal ArticleDOI

A trickle-bed reactor model for hydrogenation of 2,4 dinitrotoluene: experimental verification

TL;DR: In this article, a trickle-bed reactor model has been developed for hydrogenation of 2,4 dinitrotoluene (DNT), which incorporates the contributions of partial wetting and stagnant liquid hold-up effects in addition to external and intraparticle mass transfer resistances for a complex consecutive/parallel reaction scheme represented by L-H-type kinetics.
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