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Overall gas-liquid mass transfer from Taylor bubbles flowing upwards in a circular capillary

机译:从泰勒气泡在圆形毛细管中向上流动的整体气液传质

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摘要

Overall liquid side volumetric mass transfer coefficient kLa was determined experimentally for co-current Taylor flow moving upwards in a glass tube of internal diameter 3mm. Experiments were performed for physical absorption of oxygen in 20% aqueous solution of ethanol. Shadowgraph technique was deployed for precise measurements of bubble lengths and velocities. Experimental values of volumetric mass transfer coefficient kLa were evaluated by use of oxygen sensor and contributions of two possible mass transfer mechanisms: bubble to liquid slug and bubble to liquid film, were discussed. Effects of various hydrodynamic parameters like superficial velocity, length of bubble and slug, etc. on kLa have also been presented. A correlation has been proposed for the estimation of kLa for a wide range of bubble to slug lengths ratio and superficial velocities of gas and liquids.
机译:对于在内部直径为3mm的玻璃管中向上移动的并流泰勒流,实验确定了总的液体侧体积传质系数kLa。进行了氧在20%乙醇水溶液中的物理吸收实验。阴影图技术用于精确测量气泡的长度和速度。通过使用氧气传感器评估了体积传质系数kLa的实验值,并讨论了两种可能的传质机理:气泡至液团和气泡至液膜的贡献。还提出了各种流体动力学参数,如表观速度,气泡长度和段塞等对kLa的影响。已经提出了一种相关性,用于估计大范围的气泡与段塞长度之比以及气体和液体的表观速度时的kLa。

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