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- W2013479261 abstract "The axial mixing in the liquid phase of a gas-liquid flow through a packed column was studied with air and water flowing counter-currently in a 1.33 ft. diameter column with 1/2-in. Raschig rings. The results for bubble flow (liquid continuous) indicate that liquid staging corresponds to about one ideal mixing stage per foot in the range of flow rates investigated. An approximate correlation for the axial diffusion coefficient has been established. In trickle operation strong tailing was found. This could be explained from exchange between the main stream and a static liquid hold-up. Le mélange axial dans la phase liquide d'un écoulement biphasé a été étudié avec l'eau et l'air circulant en contrecourant dans une colonne de garnissage d'un diamètre de 1.33 pied contenant des anneaux de raschig de 1/2″. Les résultats pour l'écoulement où la phase liquide est continue donnent environ un stage idéal de mélange par pied de longueur. Une corrélation approximative est aussi établie pour le coefficient de diffusion axiale. Pour l'écoulement où la phase gazeuse est continue, on note qu'il peut y avoir échange entre la phase gazeuse et le liquide retenu statiquement." @default.
- W2013479261 created "2016-06-24" @default.
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- W2013479261 date "1965-06-01" @default.
- W2013479261 modified "2023-10-16" @default.
- W2013479261 title "Axial mixing of liquid in gas-liquid flow through packed beds" @default.
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- W2013479261 doi "https://doi.org/10.1002/cjce.5450430306" @default.
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