UNSW Water Research Centre, School of Civil and Environmental Engineering, The University of New South Wales, Sydney, NSW, 2052, Australia.
Department of Environmental Engineering, Universidade Federal do Espírito Santo, Av. Fernando Ferrari 514, 29.060-970 Vitória, ES, Brazil.
Water Res. 2018 Mar 1;130:388-406. doi: 10.1016/j.watres.2017.12.001. Epub 2017 Dec 11.
Emission models are useful tools for the study and management of atmospheric emissions from passive liquid surfaces in wastewater treatment plants (WWTPs), which are potential sources of odour nuisance and other environmental impacts. In this work, different theoretical and empirical models for the gas-side (k) and liquid-side (k) mass transfer coefficients in passive surfaces in WWTPs were critically reviewed and evaluated against experimental data. Wind forcing and the development of the wind-wave field, especially the occurrence of microscale wave breaking, were identified as the most important physical factors affecting mass transfer in these situations. Two approaches performed well in describing the available data for k for water vapour. One is an empirical correlation whilst the other consists of theoretical models based on the description of the inner part of the turbulent boundary layer over a smooth flat plate. We also fit to the experimental data set a new, alternate equation for k, whose performance was comparable to existing ones. However, these three approaches do not agree with each other in the whole range of Schmidt numbers typical for compounds found in emissions from WWTPs. As to k, no model was able to satisfactorily explain the behaviour and the scatter observed in the whole experimental data set. Excluding two suspected biased sources, the WATER9 (US EPA, 1994. Air Emission Models for Waste and Wastewater. North Carolina, USA. EPA-453/R-94-080A) approach produced the best results among the most commonly used k models, although still with considerably high relative errors. For this same sub-set, we propose a new, alternate approach for estimating k, which resulted in improved performance, particularly for longer fetches. Two main gaps were found in the literature, the understanding of the evolution of the mass transfer boundary layer over liquid surfaces, and the behaviour of k for larger fetches, especially in the range from 40 to 60 m.
排放模型是研究和管理污水处理厂(WWTP)中被动液体表面大气排放的有用工具,这些排放是臭味和其他环境影响的潜在来源。在这项工作中,对 WWTP 中被动表面的气体侧(k)和液体侧(k)传质系数的不同理论和经验模型进行了批判性回顾,并根据实验数据进行了评估。风的强制作用和风波场的发展,特别是微尺度波浪破碎的发生,被确定为影响这些情况下传质的最重要物理因素。两种方法在描述水蒸气 k 的可用数据方面表现良好。一种是经验相关,另一种是基于对光滑平板上湍流边界层内部描述的理论模型。我们还根据实验数据集拟合了一个新的、替代的 k 方程,其性能与现有方程相当。然而,在整个污水处理厂排放物中化合物典型的施密特数范围内,这三种方法彼此不一致。至于 k,没有一个模型能够令人满意地解释整个实验数据集所观察到的行为和离散性。排除两个可疑的有偏差的来源,WATER9(美国环保署,1994 年。废物和废水空气排放模型。美国北卡罗来纳州。EPA-453/R-94-080A)方法在最常用的 k 模型中产生了最好的结果,尽管仍然存在相当高的相对误差。对于同一子集,我们提出了一种新的、替代的 k 估计方法,该方法提高了性能,特别是在更长的 fetches 上。文献中有两个主要的空白,一个是对液体表面上传质边界层的演化的理解,另一个是 k 在更大 fetches 下的行为,特别是在 40 到 60 m 的范围内。