Packing size effects on the liquid circulation property in an external‐loop packed bubble column

Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and 40.7 mm) in the riser were investigated. The overall gas holdup, liquid circulating velocity and gas–liquid mass transfer coefficient were res...

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Published inAIChE journal Vol. 68; no. 12
Main Authors Tang, Yanling, Luo, Gang, Cheng, Zhenmin
Format Journal Article
LanguageEnglish
Published Hoboken, USA John Wiley & Sons, Inc 01.12.2022
American Institute of Chemical Engineers
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ISSN0001-1541
1547-5905
DOI10.1002/aic.17851

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Abstract Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and 40.7 mm) in the riser were investigated. The overall gas holdup, liquid circulating velocity and gas–liquid mass transfer coefficient were respectively measured by volume expansion, tracer‐response, and dynamic oxygen‐absorption techniques. CFD simulation with the Euler–Euler two‐fluid method was used to predict the liquid circulating velocity by treating the packing as a porous medium. Compared to the empty column, the gas holdup was found to increase in the presence of packing, however, the liquid circulating velocity and gas–liquid mass transfer coefficient are rather complicated. Specifically, the gas holdup increases with the decrease of packing size, while the liquid circulating velocity is on the contrary, and the maximal gas–liquid mass transfer coefficient is achieved under packing diameter of 14.1 mm.
AbstractList Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and 40.7 mm) in the riser were investigated. The overall gas holdup, liquid circulating velocity and gas–liquid mass transfer coefficient were respectively measured by volume expansion, tracer‐response, and dynamic oxygen‐absorption techniques. CFD simulation with the Euler–Euler two‐fluid method was used to predict the liquid circulating velocity by treating the packing as a porous medium. Compared to the empty column, the gas holdup was found to increase in the presence of packing, however, the liquid circulating velocity and gas–liquid mass transfer coefficient are rather complicated. Specifically, the gas holdup increases with the decrease of packing size, while the liquid circulating velocity is on the contrary, and the maximal gas–liquid mass transfer coefficient is achieved under packing diameter of 14.1 mm.
Author Cheng, Zhenmin
Luo, Gang
Tang, Yanling
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Snippet Packing size effects on the fluid dynamics in an external‐loop packed bubble column with Raschig rings of three different effective diameters (4.9, 14.1, and...
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SubjectTerms Bubble columns
Column packings
Diameters
external‐loop packed bubble column
Fluid dynamics
gas holdup
gas–liquid mass transfer
Hydrodynamics
liquid circulation
Mass transfer
Packing
Porous media
porous medium
Size effects
Thermal expansion
Velocity
Title Packing size effects on the liquid circulation property in an external‐loop packed bubble column
URI https://onlinelibrary.wiley.com/doi/abs/10.1002%2Faic.17851
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