UNSW Water Research Centre, School of Civil and Environmental Engineering, The University of New South Wales, Sydney, NSW, 2052, Australia.
Departamento de Engenharia Ambiental, Universidade Federal do Espírito Santo, Av. Fernando Ferrari 514, 29.060-970, Vitória, ES, Brazil.
Water Res. 2017 Nov 1;124:49-66. doi: 10.1016/j.watres.2017.07.030. Epub 2017 Jul 17.
Emission models are widely applied tools for estimating atmospheric emissions from wastewater treatment plants (WWTPs). The friction velocity u is a key variable for the modelling of emissions from passive liquid surfaces in WWTPs. This work evaluated different parametrisations of u for passive liquid surfaces at the scale of WWTP units, which present relatively small fetches, based on available wind friction and wave data measured at wind-wave tanks (fetches spanning from approximately 3 to 100 m, and wind speeds from 2 to 17 m s). The empirical correlation by Smith (1980; J. Phys. Oceanogr. 10, 709-726), which has been frequently adopted in air emission models (despite the fact that it was originally derived for the ocean) presented a general tendency to overestimate u, with significant (although not extreme) relative errors (mean and maximum errors of 13.5% and 36.6%, respectively); the use of Charnock's relation, with Charnock constant 0.010, performed in a very similar manner (mean and maximum errors of 13.3% and 37.8%, respectively). Better estimates of u were achieved by parametrisations based on the significant wave steepness. Simplified correlations between the wind drag and the non-dimensional fetch were obtained. An approach was devised, comprising the use of Charnock's relation (with Charnock constant 0.010) and of these simplified correlations, depending on the ranges of frequency of the peak waves, fetch and wind speed. The proposed approach predicted u with improved accuracy (mean, maximum and 95%-percentile relative errors of 6.6%, 16.7% and 13.9%, respectively), besides being able to incorporate the influence of the fetch in the wind drag, thus taking into account the size of the tanks in the WWTPs.
排放模型是用于估计污水处理厂(WWTP)大气排放的广泛应用工具。摩擦速度 u 是 WWTP 中无源液体表面排放建模的关键变量。本工作评估了基于风-波水槽中可用的风摩擦和波浪数据(范围从大约 3 到 100 m,风速从 2 到 17 m/s),针对 WWTP 单元规模上无源液体表面的 u 的不同参数化。Smith(1980 年;《物理海洋学杂志》,第 10 卷,第 709-726 页)的经验相关关系经常被用于空气排放模型(尽管它最初是为海洋推导的),总体上倾向于高估 u,具有显著的(尽管不是极端的)相对误差(平均和最大误差分别为 13.5%和 36.6%);使用 Charnock 关系,Charnock 常数为 0.010,表现得非常相似(平均和最大误差分别为 13.3%和 37.8%)。基于显著波陡的参数化方法可以更好地估计 u。获得了风阻力与无量纲风区之间的简化相关关系。设计了一种方法,包括使用 Charnock 关系(Charnock 常数为 0.010)和这些简化相关关系,取决于峰值波的频率范围、风区和风速。所提出的方法以改进的精度预测了 u(平均、最大和 95%百分位相对误差分别为 6.6%、16.7%和 13.9%),此外还能够在风阻力中纳入风区的影响,从而考虑到 WWTP 中水箱的大小。