首页> 外文会议>American Society of Mechanical Engineers international mechanical engineering congress and exposition >INVESTIGATION OF SINGLE PHASE MODELS FOR PREDICTING PRESSURE DROP IN NANOFLUID FLOW IN CIRCULAR PIPES
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INVESTIGATION OF SINGLE PHASE MODELS FOR PREDICTING PRESSURE DROP IN NANOFLUID FLOW IN CIRCULAR PIPES

机译:预测圆管纳米流中压降的单相模型研究

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Macroscopic modeling of hydrodynamic behavior of nanofluid flow in a uniformly heated circular pipe is considered. Single-phase models with Brownian and dispersion viscosity models are evaluated by comparing predicted pressure drop and apparent friction factor with experimental and two-phase Eulerian-Eulerian model results from literature. Single-phase models are capable of predicting heat transfer of nanofluids better when dispersion models are used. However, they fail to accurately predict pressure drop when used with standard viscosity models. Two-phase models on the other hand, can accurately predict both thermodynamic and hydrodynamic field at the expense of computational time. A new viscosity model, which is based on dispersion viscosity, is proposed to increase accuracy of single-phase models in predicting hydrodynamic field of nanofluid flow. Results suggest that single-phase dispersion viscosity model is the most accurate single-phase model.
机译:考虑了均匀加热的圆形管道中纳米流体流动的流体动力学行为的宏观模型。通过将预测的压降和表观摩擦系数与文献中的实验和两相欧拉-欧拉模型结果进行比较,可以评估具有布朗氏和分散粘度模型的单相模型。当使用分散模型时,单相模型能够更好地预测纳米流体的传热。但是,当与标准粘度模型一起使用时,它们无法准确预测压降。另一方面,两相模型可以准确地预测热力学和流体力学场,但会浪费计算时间。提出了一种基于分散粘度的新粘度模型,以提高单相模型在预测纳米流体流动的流体动力场中的准确性。结果表明,单相分散体粘度模型是最准确的单相模型。

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