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Influences of Boundary Condition on Laminar Natural Convection of Bingham Fluids in Square Cross-Sectioned Cylindrical Annular Enclosures with Differentially Heated Vertical Walls

机译:边界条件对带有垂直加热壁的方形横截面圆柱环形壳体中宾厄姆流体层流自然对流的影响

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摘要

Numerical simulations have been carried out to analyze steady-state laminar natural convection of yield stress fluids obeying Bingham model in square cross-sectioned cylindrical annular enclosures with differentially heated vertical walls for both constant wall temperature and constant wall heat flux boundary conditions for active walls. The simulations have been performed under the assumption of axisymmetry for a nominal Rayleigh number range of 103 to 106 and nominal Prandtl number range of 10 to 10~3 for different ratio of internal cylinder radius to cylinder height range of 0.125 to 16. The mean Nusselt number on the inner periphery for the constant wall heat flux configuration has been found to be smaller than that in the case of constant wall temperature configuration for a given set of values of nominal Rayleigh and Prandtl numbers for both Newtonian and Bingham fluid cases. The mean Nusselt number normalized by the corresponding value obtained for pure conductive transport increases with increasing internal radius before approaching the corresponding mean Nusselt number for square enclosures regardless of the boundary conditions. Detailed physical explanations have been provided for the effects of the aforementioned parameters on the mean Nusselt number on the inner periphery. Finally, the new Nusselt number correlations have been proposed for laminar natural convection of both Newtonian and Bingham fluids in square cross-sectioned cylindrical annular enclosures for both constant wall temperature and constant wall heat flux boundary conditions.
机译:进行了数值模拟,以分析屈服应力流体的稳态层流自然对流,服从Bingham模型,在方形截面的圆柱环形外壳中,对恒定壁温和恒定壁热通量边界条件,对活动壁采用垂直加热差壁。对于内圆柱半径与圆柱高度范围之比为0.125到16的标称瑞利数范围为103到106,标称普兰特数范围为10到10〜3,在轴对称的假设下进行了仿真。对于给定的一组牛顿流体和宾汉流体情况的瑞利数和普朗特数的给定值,发现恒定壁热通量配置的内周上的数值小于恒定壁热配置的情况下的数值。由纯导电传输获得的相应值归一化的平均努塞尔数随内半径的增加而增加,然后接近方形外壳的相应平均努塞尔数,而不受边界条件的影响。对于上述参数对内周平均努塞尔数的影响,已经提供了详细的物理解释。最后,对于恒定壁温和恒定壁热通量边界条件,已经提出了新的Nusselt数相关性用于牛顿流体和宾汉流体在正方形截面的圆柱环形罩中的层流自然对流。

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  • 来源
    《Heat Transfer Engineering》 |2018年第4期|319-338|共20页
  • 作者单位

    School of Mechanical and Systems Engineering, Newcastle University, Newcastle-Upon-Tyne, UK;

    School of Mechanical and Systems Engineering, Newcastle University, Newcastle-Upon-Tyne, UK;

    School of Mechanical and Systems Engineering, Newcastle University, Newcastle-Upon-Tyne, UK;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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