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Oxygen Transfer from a Free Surface and Dispersed Bubbles in an Aeration Tank

机译:曝气池中自由表面的氧气转移和分散的气泡

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摘要

Conventionally, both aeration tanks and bubble columns are supplied oxygen from dispersed bubbles. However, the geometry of the aeration tanks is greatly different from that of bubble columns. Although almost all oxygen is absorbed from dispersed bubbles in the water for bubble columns, the aeration tank has such a large free surface area that the oxygen transfer from atmosphere cannot be neglected. Therefore, it is very important to investigate oxygen transfer from not only the free surface, but also bubbles. In this study, the volumetric oxygen transfer coefficient, gas holdup and its two dimensional profile were measured in a large scaled aeration tank of typical size for industrial sewage treatment. Moreover, the effect of the aeration method on gas holdup and water circulation such as spiral flow aeration and whole floor aeration were also investigated. By analyzing the experimental results, a simultaneous oxygen transfer model which consists of the sum of oxygen transfer coefficients not only between bubbles and water, but also between the atmosphere and the free surface, is proposed. The model was evaluated by comparing with two alternative models for the experimental overall oxygen transfer coefficients. The proposed model estimated the experimental results better than the other models.
机译:通常,曝气池和鼓泡塔均由分散的气泡供氧。但是,曝气池的几何形状与鼓泡塔的几何形状有很大不同。尽管几乎所有氧气都从气泡塔用水中分散的气泡吸收,但曝气池的自由表面积很大,无法忽略从大气中转移的氧气。因此,研究氧气不仅从自由表面转移而且还从气泡转移非常重要。在这项研究中,在典型尺寸的大型曝气池中测量了用于工业污水处理的体积氧传递系数,气体滞留率及其二维分布。此外,还研究了曝气方法对气体滞留和水循环的影响,例如螺旋流曝气和整个地板曝气。通过对实验结果的分析,提出了同时由氧气在气泡和水之间,以及大气与自由表面之间的氧气转移系数之和组成的氧气转移模型。通过与两个替代模型的实验总氧气传输系数进行比较来评估该模型。提出的模型比其他模型更好地估计了实验结果。

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