Oxygen absorption rates into water were measured to determine volumetric mass transfer coefficients,
kLa, in bubble and slug flow regimes of gas-liquid two-phase upflow through a 0.03m i.d. vertical tube. Axial local values of
kLa decreased rapidly downstream from gas inlet. Axial averaged values of
kLa, which is denoted by (
kLa) z, were affected by gas velocity,
uGO, liquid velocity,
uLO, and distance from gas inlet, z, being correlated by the following equation:(
kLa) z=0.38u
GO0.69u
LO0.33Z
-0.27Moreover, the liquid-side mass transfer coefficients,
kL, were calculated with the gas-liquid interfacial area obtained by the photographs of flow. The values of
kL were correlated well with the energy dissipation rate, which was consistent with the eddy cell model.
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