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Numerical simulation of secondary clarifier with activated sludge and suction lift removal system: Modified Casson model and sludge withdrawing sensitivity analysis

机译:具有活性污泥和吸力提升系统的二级澄清池的数值模拟:改进的Casson模型和污泥抽取敏感性分析

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A computational fluid dynamics model that predicts the sedimentation of activated sludge in a circular secondary clarifier with activated sludge is developed. The axisymmetric single-phase flow is simulated by using a CFD code that has been written with Intel Visual Fortran. First, sludge withdrawing by suction-lift in the near-bottom region of the clarifier is simulated using suction at the bottom of clarifier. The flow and settling processes are simulated using k-ε turbulence model on a two-dimensional and orthogonal grid. A convection-dispersion equation that is extended to incorporate the sedimentation of activated sludge in the field of gravity is used. The computational domain includes the sludge blanket where the viscosity is affected by the rheological behavior of the sludge. Experimental data provided by Weiss et al. show that the relationship between shear stress and shear rate follows the Casson law for the shear rates lower than 50 s~(-1). Plastic viscosity of activated sludge is not removed from the concentration diffusion, so using regular non-Newtonian models leads to overestimation of blanket height. Modified Casson model is introduced to overcome the blanket height overestimation problem. Results show that the local sludge distribution in the clarifier has excellent agreement with concentration profile measurements of Weiss et al., for different treatment plant loadings. Alternative sludge withdrawing methods include withdrawing from pipes position at the bottom of clarifier and withdrawing by using sink terms in governing equations are used. Results show that the first withdrawing method gives less error comparing to these withdrawing methods.
机译:建立了计算流体动力学模型,该模型可预测含活性污泥的圆形二级澄清池中活性污泥的沉降。轴对称单相流通过使用已经用Intel Visual Fortran编写的CFD代码进行模拟。首先,使用澄清池底部的吸力模拟在澄清池底部附近通过吸力提升产生的污泥。在二维和正交网格上使用k-ε湍流模型模拟了流动和沉降过程。对流扩散方程式被扩展为在重力场中结合活性污泥的沉降。计算域包括污泥层,其中粘度受污泥的流变行为影响。 Weiss等提供的实验数据。结果表明,当剪切速率低于50 s〜(-1)时,剪切应力与剪切速率之间的关系遵循卡森定律。活性污泥的塑性粘度不会从浓度扩散中消除,因此使用常规的非牛顿模型会导致高估覆盖层高度。引入了改进的Casson模型来克服毯子高度过高的问题。结果表明,对于不同的处理厂负荷,澄清池中的局部污泥分布与Weiss等人的浓度曲线测量结果具有极好的一致性。替代性污泥排放方法包括从澄清池底部的管道位置排放,并在控制方程式中使用沉项进行排放。结果表明,与这些撤回方法相比,第一种撤回方法产生的错误更少。

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