Rosso Diego, Stenstrom Michael K
Civil and Environmental Engineering Department, University of California, Los Angeles, 90095-1593, USA.
Water Res. 2006 Apr;40(7):1397-404. doi: 10.1016/j.watres.2006.01.044. Epub 2006 Mar 20.
Aeration in wastewater treatment processes accounts for the largest fraction of plant energy costs. Aeration systems function by shearing the surface (surface aerators) or releasing bubbles at the bottom of the tank (coarse- or fine-bubble aerators). Surfactant accumulation on gas-liquid interfaces reduces mass transfer rates, and this reduction in general is larger for fine-bubble aerators. This study evaluates mass transfer effects on the characterization and specification of aeration systems in clean and process water conditions. Tests at different interfacial turbulence regimes show higher gas transfer depression for lower turbulence regimes. Contamination effects can be offset at the expense of operating efficiency, which is characteristic of surface aerators and coarse-bubble diffusers. Results describe the variability of alpha-factors measured at small scale, due to uncontrolled energy density. Results are also reported in dimensionless empirical correlations describing mass transfer as a function of physiochemical and geometrical characteristics of the aeration process.
废水处理过程中的曝气占工厂能源成本的最大部分。曝气系统通过剪切水面(表面曝气器)或在池底释放气泡(粗气泡或细气泡曝气器)来运行。表面活性剂在气液界面上的积累会降低传质速率,一般来说,这种降低对细气泡曝气器更为明显。本研究评估了在清洁水和工艺水条件下传质对曝气系统特性和规格的影响。在不同界面湍流状态下的测试表明,较低湍流状态下的气体传输抑制作用更大。污染影响可以以运行效率为代价来抵消,这是表面曝气器和粗气泡扩散器的特点。结果描述了由于能量密度不受控制,在小规模下测得的α因子的变异性。还报告了无量纲经验关联式的结果,该关联式将传质描述为曝气过程的物理化学和几何特征的函数。