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Journal ArticleDOI

Flow pattern of the phases and liquid saturation in gas‐liquid concurrent downflow through packed beds

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TLDR
In this article, a flow pattern was visually observed for non-foaming and foaming Newtonian and non-Newtonian liquids under concurrent downflow with air in packed beds using different configurations of column geometry and packins.
Abstract
Flow pattern was visually observed for non-foaming and foaming Newtonian and non-Newtonian liquids under concurrent downflow with air in packed beds using different configurations of column geometry and packins. Flow maps delineating the different flow regions were presented based on the present study as well as that of earlier investigations. The total and dynamic liquid saturation were experimentally measured and correlations were presented in terms of (i) the Lockhart-Martinelli parameter, χ, and (ii) the flow variables. On a observe de maniere visuelle les profils d'ecoulement pour des liquides newtoniens ou non newtoniens, moussants et non moussants, dans le cas d'un acoulement descendant de liquides et d'air dans un lit a garnissage. On a fait varier la gaomatrie de la colonne et le garnissage. Les diagrammes d'ecoulement delimitant les differentes regions d'ecoulement, presentes dans cette etude, s'appuient sur le travail actuel ainsi que sur des recherches anterieures. On a mesure de maniere experimentale la saturation du liquide dynamique et to tale, et les correlations sont presentes en fonction (i) du parametre Lockhart-Martinelli, χ, et (ii) des variables d'ecoulement.

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Citations
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Journal ArticleDOI

Experimental study of a trickle-bed reactor operating at high pressure: two-phase pressure drop and liquid saturation

TL;DR: In this article, the effect of pressure on the hydrodynamics of trickle-bed reactors is investigated, and two new correlations for the pressure drop and the liquid hold-up for non-foaming liquids are proposed; they are based on 1500 experimental results.
Journal ArticleDOI

A two-fluid hydrodynamic model for the transition between trickle and pulse flow in a cocurrent gas–liquid packed-bed reactor

TL;DR: In this article, a two-dimensional hydrodynamic model of cocurrent gas-liquid downflow through packed-bed reactors operating in the trickle flow regime is developed on the basis of a mechanistic approach.
Journal ArticleDOI

Hydrodynamics in a cocurrent gas-liquid trickle bed at elevated pressures

TL;DR: In this article, the influence of the gas density on the liquid holdup, the pressure drop, and the transition between trickle and pulse flow has been investigated in a tricklebed reactor operating up to 7.5 MPa and with nitrogen or helium as the gas phase.
Journal ArticleDOI

The transition between trickle flow and pulse flow in a cocurrent gas—liquid trickle-bed reactor at elevated pressures

TL;DR: In this article, the effect of reactor pressure in the range of 0.2-2.0 MPa on the transition between the trickle-flow and the pulse-flow regime has been investigated for the non-foaming water-nitrogen and aqueous 40% ethyleneglycolnitrogen systems.
Journal ArticleDOI

Onset of pulsing in trickle beds: Evaluation of current tools and state‐of‐the‐art correlation

TL;DR: In this article, a state-of-the-art explicit correlation of trickle-to-pulse flow changeover was derived relying on neural network modeling, and robustness of the proposed correlation was verified through systematic statistical testing over the constructed data base.
References
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Journal ArticleDOI

Trickle-bed reactors

TL;DR: Trickling filters have been used for removal of organic matter from wastewater streams by aerobic bacterial action as discussed by the authors, where biological growths are allowed to attach themselves to a bed of stone or other support over which the wastewater is allowed to trickle in contact with air.
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

Two‐phase concurrent flow in packed beds

TL;DR: In this article, pressure drop and liquid saturation data were obtained in terms of the single-phase friction losses for the liquid and the gas when each flows alone in the bed and deviations from the correlation with foaming systems were discussed and illustrated with sample data.
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