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GFD investigation of turbulence models for mechanical agitation of non-Newtonian fluids in anaerobic digesters

机译:GFD研究厌氧消化池中非牛顿流体机械搅拌的湍流模型

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摘要

This study evaluates six turbulence models for mechanical agitation of non-Newtonian fluids in a lab-scale anaerobic digestion tank with a pitched blade turbine (PBT) impeller. The models studied are: (1) the standard κ-ε model, (2) the RNG κ-ε model, (3) the realizable k-ε model, (4) the standard κ-ω model, (5) the SST κ-ω model, and (6) the Reynolds stress model. Through comparing power and flow numbers for the PBT impeller obtained from computational fluid dynamics (CFD) with those from the lab specifications, the realizable κ-ε and the standard κ-ω models are found to be more appropriate than the other turbulence models. An alternative method to calculate the Reynolds number for the moving zone that characterizes the impeller rotation is proposed to judge the flow regime. To check the effect of the model setup on the predictive accuracy, both discretization scheme and numerical approach are investigated. The model validation is conducted by comparing the simulated velocities with experimental data in a lab-scale digester from literature. Moreover, CFD simulation of mixing in a full-scale digester with two side-entry impellers is performed to optimize the installation.
机译:这项研究评估了在带有桨叶涡轮(PBT)叶轮的实验室规模厌氧消化池中对非牛顿流体进行机械搅拌的六个湍流模型。研究的模型为:(1)标准κ-ε模型,(2)RNGκ-ε模型,(3)可实现的k-ε模型,(4)标准κ-ω模型,(5)SST κ-ω模型,以及(6)雷诺应力模型。通过将通过计算流体动力学(CFD)获得的PBT叶轮的功率和流量数与实验室规范中的功率和流量数进行比较,发现可实现的κ-ε模型和标准κ-ω模型比其他湍流模型更合适。提出了一种替代方法来计算表征叶轮旋转的运动区域的雷诺数,以判断流动状态。为了检查模型设置对预测精度的影响,研究了离散化方案和数值方法。通过将模拟速度与文献中实验室规模的蒸煮器中的实验数据进行比较来进行模型验证。此外,对带有两个侧入式叶轮的全尺寸蒸煮器中的混合进行CFD模拟,以优化安装。

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