Abstract
Gas holdup has been measured in an 83-mm diameter, 2.2-m high column at high gas superficial velocities - 0.22 to 2.7 m/s - and at liquid (water) superficial velocities of 0 to 0.47 m/s, by means of a differential pressure transducer. The equation of Hills (1976) based on the slip velocity gives good predictions of the gas holdup for 0.1 ≤ εg ≤ 0.4. However, the holdups predicted by this approach are considerably higher than the experimental values at gas velocities high enough that εg > 0.4. Other equations from the literature are also shown to be inadequate. The new data and earlier data at high gas velocities are therefore correlated with a new dimensional equation for U1 ≤ 0.23 m/s.
| Original language | English |
|---|---|
| Pages (from-to) | 1006-1010 |
| Number of pages | 5 |
| Journal | Canadian Journal of Chemical Engineering |
| Volume | 78 |
| Issue number | 5 |
| DOIs | |
| State | Published - 2000 |
| Externally published | Yes |
Keywords
- Bubble column
- Gas holdup
- Gas-liquid flow
- Two-phase flow
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