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Explore an Approach to Determine Odour Emissions from Water Surfaces

机译:探索确定水面气味排放的方法

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Odour emissions from water surfaces such as primary tanks or aeration tanks in waste water treatment plant have become an increasing nuisance to the neighboring communities. In order to assess the odour nuisance level, the flux chamber technique has been used to quantify the odour emissions from the water surfaces. However, field measurements with portable wind tunnels have indicated that the odour emissions are highly dependent on environmental variables, such as wind speed and temperature. In the past some studies indicated that flux chamber technique underestimates the odour emissions. The transfer of odour between the air and water is governed by turbulent and molecular transport processes. Both transport processes can be characterized by diffusion coefficients and the concentration gradient between air and water surface. Away from the water surface, the turbulent transfer is typically orders of magnitude higher than the molecular transfer. We developed a two-step approach for estimating odour emissions from the water surfaces and our approach is based on turbulent transfer. The first step uses the static flux chamber to measure the odour concentration gradient between the air and water surface. The second step quantifies the odour emission rates by applying the turbulent transfer rates estimated by a micrometeorological model. We applied this approach to one waste water treatment plant to quantify the odour emission rates from aeration tanks and aerobic bio-solids complexes. In order to verify our approach, we measured the ambient odour concentrations at various downwind distances under different meteorological conditions and input the quantified odour emission rates into an air dispersion model (the US EPA AERMOD model), to predict the downwind odour concentrations. In this study, the modelled and measured downwind ambient odour concentrations agree well, demonstrating that this approach is plausible and can be applied to other surfaces as well.
机译:从废水处理厂的主水箱或曝气池等水面发出的臭味已成为对邻近社区的越来越多的滋扰。为了评估气味的滋扰程度,已使用助焊剂室技术对水面的气味排放进行量化。但是,便携式风洞的现场测量表明,气味排放高度依赖于环境变量,例如风速和温度。在过去的一些研究表明通量室技术低估了气味的排放。空气和水之间的气味转移受湍流和分子传输过程的控制。两种传输过程都可以通过扩散系数和空气与水表面之间的浓度梯度来表征。远离水面,湍流传递通常比分子传递高几个数量级。我们开发了一种分两步的方法来估算水面的气味排放,而我们的方法是基于湍流传递。第一步使用静态通量室测量空气和水表面之间的气味浓度梯度。第二步通过应用由微气象模型估算的湍流传递速率来量化气味排放速率。我们将此方法应用于一个废水处理厂,以量化曝气池和好氧生物固体复合物的气味排放率。为了验证我们的方法,我们在不同的气象条件下测量了不同顺风距离下的环境气味浓度,并将量化的气味排放速率输入到空气扩散模型(美国EPA AERMOD模型)中,以预测顺风气味浓度。在这项研究中,建模和测量的顺风环境气味浓度非常吻合,表明这种方法是合理的,也可以应用于其他表面。

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