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Experimental Study on Multistage Air-lift Loop Reactor

机译:多级气举环流反应器的实验研究

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A new type of multi-stage air-lift loop reactor has been developed, which consists of four tubes, two gas separators and two bases, and forms one circulating path. Experimental study completed with measurements of gas hold-up in two risers and liquid circulation rate for air-water system within a wide range of gas velocity for five D_d/D_r ratios. The model of gas hold-up has proposed by omogeneous flow model and the liquid circulation flow equation including the reactor geometries and all energy loss oefficients has derived in terms of energy balance. The gas voidage and liquid rate are agreed with those, which calculated by incorporating these two model equations.
机译:研制了一种新型的多级气举环流反应器,该反应器由四个管,两个气体分离器和两个基座组成,并形成一个循环路径。实验研究完成后,在五个D_d / D_r比率的大范围气体速度下,测量了两个立管中的气体滞留率和空气-水系统的液体循环速率。均质流模型提出了气体滞留率模型,并根据能量平衡推导了包括反应器几何形状和所有能量损失系数在内的液体循环流方程。气体空隙率和液体率与通过合并这两个模型方程式计算得出的值一致。

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