Liquid circulation, gas holdup and pressure drop in bubble column with draught tube.
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概要
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The effects of gas velocity and geometrical dimensions of apparatus on the flow rate QL of circulating liquid, gas holdups and pressure drops in bubble columns with draught tube were examined. It was found that QL increases with increasing gas velocity, column diameter, draught tube length, and height of the lower end of draught tube, and decreases with increasing liquid viscosity. It was also found that the maximum value of QL is observed for constant values of gas velocity and column diameter, when the diameter ratio of draught tube and column is about 0.6. Empirical equations for gas holdups in draught tube and annulus and the pressure drops due to flow reversals, necessary for estimating QL, are proposed.
- 公益社団法人 化学工学会の論文
著者
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Iwamoto Shinji
Department Of Civil Engineering
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Kubota Hiroshi
Research Laboratory Of Resources Utilization Tokyo Institute Of Technology
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Kimura Motohiko
Department Of Biochemical Engineering Faculty Of Pharmaceutical Sciences Osaka University
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Koide Kozo
Department Fo Chemical Engineering Tokyo Institute Of Technology
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TAKASAKA YUKITOSHI
Department of Chemical Engineering, Shizuoka University
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MATSUURA SHINJI
Department of Chemical Engineering, Shizuoka University
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TAKAHASHI ETSUO
Department of Chemical Engineering, Shizuoka University
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IWAMOTO SHINJI
Department of Chemical Engineering, Shizuoka University
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