Effect of Static Liquid Height on Gas-Liquid Mass Transfer in a Draft-Tube Bubble Column and Three-Phase Fluidized Bed

Bavarian, Farshad; Linn, Chia-Jui; Ramesh, T.S.; Fan, Liang‐Shih

doi:10.1080/00986449108910966

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Submerged and Fluidized Biofilm Reactors1

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1992

1997

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Cited by 7 publications

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“…The effect of static liquid height on the gas-liquid mass-transfer coefficient (KLa) in a draft-tube bubble column and a draft-tube three-phase fluidized bed was investigated under batch conditions. 50 The results indicated that for a system with a porous plate gas distributor and low superficial gas velocities, KLawas inversely proportional to the static fluid head (SLH). For a system with a perforated gas distributor, KLa was found to be independent ofSLH.…”

Section: Submerged and Fluidized Biofilm Reactorsmentioning

confidence: 99%