某污水处理厂生物反应器的CFD建模与优化-一个案例研究

A. Elshaw, N. Hassan, Mmk Khan
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引用次数: 6

摘要

本研究旨在通过将计算流体动力学(CFD)建模结果与从处理厂收集的物理数据进行比较,确定壁挂式混合器的最佳配置。该研究开发了一个缺氧区-1的CFD模型,并使用ANSYS代码“Fluent”模拟流体流动。建立了活性污泥工艺生物反应器缺氧区的二维模型,对不同入口进水的水动力特性和进水影响进行了模拟。此外,模拟还试图评估结构几何形状对水动力性能的影响。2D模型能够模拟区域内的流动模式,CFD模型的结果在关键位置变化在3%到10%之间。建立了缺氧区的三维模型,进一步评价了缺氧区的水动力性能。3D模型产生的结果与从工厂收集的物理数据一致。通过CFD模拟和收集的速度读数和悬浮固体的物理样品,可以评估缺氧区的流体动力性能。在关键位置,CFD模拟结果与物理数据一致。缺氧区的流速低于预期的0.3米/秒。然而,悬浮固体样品表明,该区域仍在可接受的范围内的具体功耗。因此,增加操作参数,增加进入该区域的流量,可以减少对潜水混合器的需求。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
CFD Modelling and Optimisation of a Waste Water Treatment Plant Bioreactor - A Case Study
This This study aims to determine the optimal configuration for wall mounted mixers based on the comparison of computational fluid dynamics (CFD) modelling results to physical data collected from the treatment plant. The study was developing a CFD model of an anoxic zone-1 and simulating the fluid flow using ANSYS code 'Fluent'. A 2D model of an activated sludge process bioreactor anoxic zone was simulated to evaluate the hydrodynamic performance and influence of the inflow through the various inlets. Furthermore, the simulation also sought to evaluate the influence on the hydrodynamic performance from structure geometry. The 2D model was able to simulate the flow pattern within the zone and results from the CFD model varied between 3% and 10% at key locations. A 3D model was also developed of the anoxic zone to further evaluate the hydrodynamic performance. The 3D model produced consistent results to the physical data collected from the plant. The hydrodynamic performance of the anoxic zone was able to be evaluated from the CFD simulations and from the physical samples collected for velocity readings and suspended solids. In the key locations, the CFD simulation showed the consistent results with the physical data. The anoxic zone was subject to velocity lower than the desired 0.3 meters per second. However suspended solid samples suggest that the zone is still within the acceptable range for specific power dissipation. Therefore, an increase in operating parameter which increases the inflow into the zone can mitigate the need for submersible mixers.
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