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Photocatalytic reactors for treating water pollution with solar illumination: A simplified analysis for n-steps flow reactors with recirculation

机译:用于处理日光照射下水污染的光催化反应器:带有再循环功能的n阶流反应器的简化分析

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摘要

The concentration of dissolved oxygen in water, in equilibrium with atmospheric air (ca. 8 ppm at 20℃), defines the limits of all practical oxidizing processes for removing pollutants in photocatalytic reactors. To solve this limitation, an alternative approach to that of a continuously aerated reactor is the use of a recirculating system with aeration performed after every cycle at the reactor entering stream. As defined by the nature of a single recirculating step (the need of a reactor operation at a rather low concentration range), this procedure results in a very low photonic efficiency (thus requiring a large photon collecting area and consequently increasing the capital cost). The design engineer will have to resort to a series of several reactors with recirculation. This solution may then lead to a very high Photonic Efficiency for the entire process (i.e., a reduced light harvesting area) at the price of an increase in the required capital cost (due to the larger number of reactors). This paper provides a very simple analysis and analytical expressions that can be used to estimate, for a desired degree of degradation, a trade-off solution between a high number of reactors and a very large surface area to collect the solar photons.
机译:水中溶解氧的浓度与大气(在20℃时约为8 ppm)保持平衡,定义了在光催化反应器中用于去除污染物的所有实际氧化工艺的极限。为了解决该限制,对于连续充气反应器的替代方法是使用循环系统,该循环系统在每个循环之后在反应器进入物流的过程中进行曝气。如单个循环步骤的性质所定义(需要在较低浓度范围内进行反应器操作),此过程导致光子效率非常低(因此需要较大的光子收集面积,因此增加了投资成本)。设计工程师将不得不诉诸一系列具有再循环功能的反应堆。然后,该解决方案可以以增加所需的资本成本(由于反应器的数量较大)为代价,导致整个过程非常高的光子效率(即减小的光收集面积)。本文提供了一种非常简单的分析和分析表达式,可用于针对所需的降解程度来估计大量反应堆和非常大的表面积之间的权衡解决方案,以收集太阳光子。

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