✍ Scribed by J.C. Merchuk; R. Yunger
No coin nor oath required. For personal study only.
📜 SIMILAR VOLUMES
Gas hold-up and liquid circulation velocity measurements were made using a 167 dm 3 external loop airlift reactor. The gas-separator was of the open channel con®guration. The reactor height was 2.5 m with riser and downcomer diameters of 0.19 m and 0.14 m respectively. The systems investigated were
## Abstract The role of the gas–liquid separator on hydrodynamic characteristics in an internal‐loop airlift reactor (ALR) was investigated. Both gas holdup and liquid velocity were measured in a 30 dm^3^ airlift reactor with two different head configurations: with and without an enlarged separator
A physical model is presented which descri'bes the local mixing in the liquid phase of twophase gas-liquid flows agitated by rising bubbles. It corresponds to the stochastic mathematical model descrii by Nassar et al (1992). The transport of liquid in the bubble wakes is assumed to be the dominating