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A correlation for interfacial area in co-current gas-liquid downflow through packed beds

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TLDR
In this article, the interfacial area in cocurrent gas-liquid downflow through packed beds is correlated taking into consideration the physical properties of the fluids and the power dissipation in the system.
Abstract
Interfacial area in cocurrent gas-liquid downflow through packed beds is correlated taking into consideration the physical properties of the fluids and the power dissipation in the system. The correlation is tested with the experimental data covering a wide range in system variables including low and high porosity packings, the flow rates of the phases and their physical properties.

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Multiphase catalytic reactors: a perspective on current knowledge and future trends

TL;DR: In this paper, a review of the physical parameters for various multiphase reactors is presented, focusing on gas-phase catalyzed processes with an emphasis on unsteady state operation.
Journal ArticleDOI

Double‐slit model for partially wetted trickle flow hydrodynamics

TL;DR: In this paper, a double-slit model was developed to predict the frictional two-phase pressure drop, external liquid holdup, pellet-scale external wetting efficiency, and gas-liquid interfacial area in cocurrent downflow trickle-bed reactors operated under partially wetted conditions in the trickle flow regime.
Journal ArticleDOI

Gas}liquid interfacial mass transfer in trickle-bed reactors: state-of-the-art correlations

TL;DR: In this article, the state-of-the-art of the gas-liquid mass transfer characteristics in trickle-bed reactors was summarized and its quantification methods were reevaluated based on a wide-ranging data base of some 3200 measurements.
Journal ArticleDOI

Heat and Mass Transfer in Cocurrent Gas−Liquid Packed Beds. Analysis, Recommendations, and New Correlations

TL;DR: In this paper, a set of reliable correlations has been recommended for the prediction of the gas−liquid interfacial area (agl), the volumetric liquid- (kla) and gas-side (kga) mass-transfer coefficients, the wall heat-transfer coefficient (hw), the bed effective radial thermal conductivity (λe), and the particle-to-fluid heat transfer coefficient (hp).
Journal ArticleDOI

Gas-liquid interfacial mass transfer in trickle-bed reactors at elevated pressures

TL;DR: A phenomenological description and a semi-empirical two-zone model for the gas−liquid interfacial areas and the volumetric liquid-side mass-transfer coefficients in cocurrent downflow t... is proposed in this article.
References
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Journal ArticleDOI

Phénomènes d'Interférences dans un Lit Fixe d'Échangeur d'Ions sous: I'Effet d'un Changement de la Normalité de l'Alimentation

TL;DR: In this paper, le mecanisme de telles interferences, identifie, illustre et classe les differentes situations which en resultent dans le cas d'un systeme binaire, en operation isolee aussi bien qu'en regime cyclique.
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