Counter current gas-liquid vertical flow, model for flow pattern and pressure drop
โ Scribed by Yehuda Taitel; Dvora Barnea
- Publisher
- Elsevier Science
- Year
- 1983
- Tongue
- English
- Weight
- 614 KB
- Volume
- 9
- Category
- Article
- ISSN
- 0301-9322
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๐ SIMILAR VOLUMES
## A phenomenological, pore-scale, hydrodynamic model is developed for representation of the uniform, two-phase, gas-liquid cocurrent flow in the low interaction regime in trickle bed reactors. The model provides improved predictions for both the pressure drop and liquid holdup using the parameters
Experimental results related to the pressure drop in steady and fully developed gas-liquid-solid three-phase slug flows in vertical pipes are presented. The experiment was carried out in pipes of 20.9, 30.6, and 50.8 mm I.D. and with solid particles of 2.57 mm mean diameter. Air and water were used