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In this study, experiments are carried out for a high-pressure bubble column with a perforated plate as the distributor under the operating pressure up to 15 MPa.
The experimental study concerning gas holdup measurements was conducted in a large-diameter and large-scale bubble column (with a height of 5.3 m and inner diameter of 0.24 m) operated in the batch mode.
The gas holdup in an 8-m high bubble column with a perforated plate distributor is measured over a superficial gas velocity range of 0.0075 to 0.54 m/s for an air-tap water system.
An energy balance, which was used by Miyahara (1986) for the conventional bubble column with a draught tube, is employed to predict the fluid circulation velocity using gas holdup and pressure drop correlations.
A bubble column with a draught tube was applied as a small scale treatment unit of anaerobic-aerobic activated sludge processes in which nitrogen and phosphorus compounds were removed together with BOD sources.
Interfacial areas and gas hold-ups have been determined at pressures up to 8.0 MPa in a mechanically agitated gas liquid reactor and a bubble column with a diameter of 81 mm for superficial gas velocites between 1 and 5 and 1 and 10 cm/s, respectively.
Similar(53)
Effect of the liquid-phase viscosity (0.7 25 mPa s) and surface tension (33 65 mN m−1) on hydraulic and mass-transfer characteristics in a bubble column with an up-flow ejector-type gas distributor was studied.
This paper reviews the flow patterns in bubble columns with a focus on transient flow structures.
Common optical methods are limited in bubble columns with a large void fraction.
CFD simulations of gas liquid flows have been carried out in a full 3D, unsteady, Euler/Euler framework by means of the commercial software FLUENT®, and discussed in connection with laboratory scale bubble columns, with a particular interest in churn-turbulent flows.
Mass transfer measurements in two bubble columns with an inner diameter of 100 resp.
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