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Modeling and experiment of gas desorption of bubble column with an external loop in the heterogeneous flow regime

机译:非均相流态下带外环的鼓泡塔气体脱附模型与实验

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This work introduces an external loop to a bubble column and presents enhanced gas exchange in the heterogeneous flow regime. Gas exchange experiments under the same amount of gas input were carried out with varying gas velocity to understand the difference of bubble characteristic between the bubble column (BCR) and the bubble column with an external loop (BCR-EL). The observation of rise and descending velocity of bubbles in the BCR-EL showed that the fraction of bubbles passing the downcomer continuously increases with the incremental superficial gas velocity. A gas molecule in the liquid phase is desorbed by another gas molecule, and this gas exchange was assumed to be a phenomenon that a reactant in the liquid phase is converted to a product. To test the validity of the assumed gas exchange as a reaction in the experiments with the BCR-EL, a modeling study was performed using Fisher-Tropsch synthesis. It prevailed that the syngas conversion was higher in the BCR at the homogeneous flow regime, while the BCR-EL at the heterogeneous flow regime (above 0.08 m/s) had higher syngas conversion than the BCR due to higher gas recycle to the downcomer.
机译:这项工作为气泡塔引入了一个外部回路,并在非均相流态下提出了增强的气体交换。在相同的气体输入量下,以不同的气体速度进行了气体交换实验,以了解鼓泡塔(BCR)和带外部环路的鼓泡塔(BCR-EL)之间的鼓泡特性差异。对BCR-EL中气泡上升和下降速度的观察表明,通过降液管的气泡分数随表观气体速度的增加而连续增加。液相中的气体分子被另一种气体分子解吸,并且这种气体交换被认为是液相中的反应物转化为产物的现象。为了在使用BCR-EL的实验中测试假定的气体交换作为反应的有效性,使用Fisher-Tropsch合成进行了模型研究。普遍认为,在均相流态下,BCR中的合成气转化率更高,而在非均相流态下(高于0.08 m / s)的BCR-EL具有比BCR高的合成气转化率,这是由于更高的气体再循环至降液管。

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