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Oxygen transfer and aeration efficiency - Influence of diffuser submergence, diffuser density, and blower type

机译:氧气传输和曝气效率-扩散器浸没,扩散器密度和鼓风机类型的影响

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The main factors of fine bubble aeration systems in uniform arrangement in clean water are the air flow rate, the depth of submergence of the diffusers, and the diffuser density. While the influence of the air flow rate on the oxygen transfer parameters is known, knowledge of the influence of the depth of submergence and the diffuser density on the specific oxygen transfer efficiency SOTE [%/m] and on the specific oxygen absorption SOA [g/m(3).m at STP] is very limited. Both parameters are of great importance in dimensioning fine bubble aeration systems. Therefore, a literature review was conducted to show the influence of the diffuser submergence and density and the type of blower on oxygen transfer and aeration efficiency. The main review results are, that higher values of specific oxygen absorption can be obtained at higher diffuser density; secondly, the volumetric oxygen transfer rate VOTR [g/m(3).h] is higher with increasing depth of submergence at the same air flow rate. Also it can be stated that with greater depth of submergence the specific oxygen absorption [g/m(3).m at STP] is reduced. Dependent on the air flow rate and the pressure head, the energy consumption [Wh/m(3).m at STP] of the blowers used in wastewater treatment plants is different. For example, the energy consumption varies from 4.3 [Wh/m(3).m at STP] (positive displacement blower) to 3.0 [Wh/m(3).m at STP] (turbo-compressors) at a pressure of 10 m and an air flow rate of 5,000 m(3)/h at STP. From the results of the literature review the following conclusions can be drawn: (1) High specific oxygen absorption values (SOA) [g/m(3).m at STP] can be achieved applying shallow tanks,high diffuser densities and low specific air flow rates; (2) High aeration efficiencies (AE) [kg/kWh] can be obtained by applying high volumetric oxygen transfer rates and adequate selection of the blowers used at the wastewater treatment plants. (C) 1998 Published by Elsevier Science Ltd. All rights reserved. [References: 2]
机译:在洁净水中均匀布置的细微气泡曝气系统的主要因素是空气流速,扩散器的浸没深度和扩散器密度。虽然空气流速对氧气传输参数的影响是已知的,但要了解浸没深度和扩散器密度对特定氧气传输效率SOTE [%/ m]和特定氧气吸收SOA [g]的影响。 /m(3).m在STP]是非常有限的。这两个参数在确定细气泡曝气系统的尺寸时都非常重要。因此,进行了文献综述,以显示扩散器的浸没和密度以及鼓风机的类型对氧气传输和曝气效率的影响。主要的审查结果是,在较高的扩散器密度下可以得到较高的比氧吸收值。其次,在相同的空气流速下,随着浸没深度的增加,氧气的体积传输速率VOTR [g / m(3).h]更高。还可以说,随着更大的浸没深度,比氧吸收[STP时的g / m(3).m]降低了。取决于空气流量和压头,废水处理厂中使用的鼓风机的能耗[STP处的Wh / m(3).m]不同。例如,在压力为10时,能耗从4.3 [STP(正排量鼓风机)[Wh / m(3).m](正排量鼓风机)变化到3.0 [STP](涡轮压缩机)的Wh / m(3).m(涡轮压缩机) m和STP时的空气流速为5,000 m(3)/ h。从文献综述的结果可以得出以下结论:(1)使用浅罐,高扩散器密度和低比氧比可以实现高比氧吸收值(SOA)[g / m(3).m at STP]空气流速; (2)通过采用高体积氧气传输速率并适当选择废水处理厂使用的鼓风机,可以获得较高的曝气效率(AE)[kg / kWh]。 (C)1998由Elsevier Science Ltd.出版。保留所有权利。 [参考:2]

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