Difficulty: Medium
Correct Answer: ε = Vs / Vt
Explanation:
Introduction / Context:
Gas hold-up (ε) is the volumetric fraction of gas in a gas–liquid dispersion and is a key parameter for mass transfer, residence time, and hydrodynamics in bubble columns and aerated bioreactors. A simple kinematic relation links ε to the superficial gas velocity (Vs) and the bubble rise velocity (Vt) when the liquid phase is not flowing on average.
Given Data / Assumptions:
Concept / Approach:
The volumetric gas flux Jg equals the product of gas volume fraction and bubble rise speed: Jg = ε * Vt. By definition, Vs = Jg. Therefore, ε = Vs / Vt. This relation captures how more gas flux or slower-rising bubbles (e.g., due to smaller size or higher viscosity) increase hold-up.
Step-by-Step Solution:
Define gas flux: Jg = volumetric gas flow per area = Vs.Relate phases: Jg = ε * Vt (gas fraction times slip velocity).Equate: Vs = ε * Vt.Solve: ε = Vs / Vt.
Verification / Alternative check:
Dimensional check: Vs and Vt both have units of length/time, so their ratio is dimensionless as required for ε. Empirically, increased aeration (higher Vs) at fixed bubble rise speed raises ε, consistent with observations.
Why Other Options Are Wrong:
Forms with Vs ± Vt in numerator/denominator do not follow from the flux balance in a static liquid.ε = (Vs + Vt)/Vs would exceed 1 for typical conditions, which is non-physical for hold-up.
Common Pitfalls:
Confusing bubble rise velocity relative to liquid (Vt) with superficial gas velocity (Vs); applying this relation when there is significant liquid co-current flow, which requires modified expressions.
Final Answer:
ε = Vs / Vt
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