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Gas Holdup in Bubble Column with Draft Tube for Gas Dispersion into Annulus

机译:带引流管的鼓泡塔中的气体滞留量,用于将气体扩散到环空中

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References(8) Cited-By(2) The effect of kind of gas sparger, outer diameter Do and length Ld of draft tube, lower clearance, superficial gas velocity and clear liquid height HL on gas holdup εG in a 0.16 m I.D. bubble column with a draft tube for gas dispersion into the annulus and for an air-water system was experimentally studied.εG depended on the kind of gas sparger in the range of φ ≤ 0.713, but hardly depends on them at φ = 0.875. φ is the ratio of (Do/DT) and DT is the inner diameter of the bubble column.At a given HL and in the range of φ ≤ 0.713, εG hardly depends on φ and Ld. But εG decreases clearly with increasing Ld at φ = 0.875.εG decreases with increasing HL. The effect of HL is well expressed by the modified three-region model.The experimental data for εG is correlated.
机译:参考文献(8)Cited-By(2)气体分布器的种类,外径Do和引流管的长度Ld,下间隙,表观气体速度和透明液体高度HL对0.16 m I.D中的气体滞留率εG的影响。实验研究了带有引气管的气泡塔,该引气管用于将气体分散到环空中和用于空气-水系统。εG取决于在φ≤0.713范围内的气体分布器,但在φ= 0.875时几乎不依赖于它们。 φ是(Do / DT)的比,DT是气泡柱的内径。在给定的HL且在φ≤0.713的范围内,εG几乎不依赖于φ和Ld。但是εG在φ= 0.875时随着Ld的增加而明显降低.εG随着HL的增加而降低。改进的三区域模型很好地表达了HL的作用。εG的实验数据是相关的。

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