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Influence of mass transfer on the ozonation of wastewater from the glass fiber industry

机译:传质对玻璃纤维废水臭氧氧化的影响

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The mass transfer rate (kLa) is one of the most important parameters in the ozonation of wastewater, because it frequently constitutes the rate-determining step. This study investigated the influence of k(L)a on the ozonation of glass fiber wastewater using a high-performance jet loop reactor (HJLR), which is well known for its high mass transfer property, and compared the results of this investigation with those obtained using the bubble column reactor. It was found that the higher kLa achieved by increasing the energy input did not lead to higher ozonation efficiency, since the reaction involving the OH radical was greatly hindered at the low pH produced as a result of ozonation. By maintaining the pH at a value greater than 8.0, the higher k(L)a in the HJLR reactor contributed to increasing not only the TOC removal of wastewater, but also the ozone consumption efficiency, as expressed by the specific ozone consumption. The specific ozone consumption in the HJLR reactor (7.1 g ozone/g TOC) was 20% better than that in the bubble column reactor.
机译:传质速率(kLa)是废水臭氧化过程中最重要的参数之一,因为它通常构成速率确定步骤。这项研究使用高性能射流环流反应器(HJLR)研究了k(L)a对玻璃纤维废水臭氧化的影响,该反应器以其高传质性能而著称,并将该研究结果与使用鼓泡塔反应器获得。已经发现,通过增加能量输入而获得的更高的kLa并没有导致更高的臭氧化效率,因为在由于臭氧化而产生的低pH值下,大大阻碍了涉及OH自由基的反应。通过将pH值保持在8.0以上,HJLR反应器中更高的k(L)a不仅有助于提高废水的TOC去除率,而且还有助于提高臭氧消耗效率(以特定的臭氧消耗量表示)。 HJLR反应器中的特定臭氧消耗量(7.1 g臭氧/ g TOC)比鼓泡塔反应器中的臭氧消耗量好20%。

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