A new type of mechanically agitated gas-liquid contactor is proposed. In this contactor, bubble breakup is assigned to a sparger with larger ring diameter than impeller diameter, and circulation of gas-liquid mixture to an axial impeller with high discharge performance.
The performance was evaluated by measuring the rate of oxygen absorption into tap water and CMC aqueous solutions (viscosity 10–70 mPa·s), the gas holdup and the power consumption in comparison with the conventional type.
The new type of contactor prevents the concentration of aeration gas around the impeller and the formation of stable cavities in viscous liquid, resulting in the efficient discharge of gas-liquid mixture from the impeller. As a result, the performance of gas absorption, especially into viscous liquids, was improved. The relative contribution of aeration power to
KLa became larger than that of agitation power in contrast to the conventional type.
KLa increased with decreasing diameter of the sparger holes under the same superficial gas velocity, but no effects of the number of sparger holes were found.
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