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Experimental verification of a heat/mass transfer analogy in two dimensional laminar and turbulent boundary layers.

机译:在二维层流和湍流边界层中进行热/质传递类比的实验验证。

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摘要

Heat and mass transfer from a solid surface into a fluid stream both are diffusion driven processes. Their mathematical model equations are identical for identical flow and boundary conditions. Problems with engineering applications are transformed from one domain to another for practical and economical advantages. A mass transfer technique using naphthalene sublimation is faster, of higher resolution, economical and more accurate than a direct heat transfer measurement. The diffusion rates of heat transfer in air and naphthalene in air are quantitatively different. Hence, the advantages of naphthalene sublimation technique are justified when the heat/mass transfer analogy is experimentally verified and an analogy factor (F = Nu/Sh) is determined.;Heat/mass transfer analogy is experimentally verified for two dimensional laminar and turbulent boundary layer flows. Thermal boundary layer technique is used to measure local heat transfer coefficient (Nu) and naphthalene sublimation technique is used to measure local mass transfer coefficient (Sh) for two identical plates subjected to identical boundary layer flows. The accuracy of the thermal boundary layer technique is determined using a constant heat flux plate made of steel shim subjected to constant electrical power. The convective heat flux is determined using this electrical power after correcting for conduction and radiation effects. These results are compared to the heat flux values determined using the thermal boundary layer technique and are found to agree within 2%.;The effect of conduction within the thermocouple wires is studied with a numerical model using fin analysis and a variable convective heat transfer load. The equilibrium thermocouple temperature is solved for various locations of the thermocouple probe within the boundary layer to simulate an equivalent experiment for an analytically calculated laminar boundary layer flow. The predictions of the model agree within 1% of the experimental measurements and are used to correct them for laminar case.;The heat/mass transfer analogy factor is calculated using the corrected Nu and Sh. It is found to agree with the analytical prediction of 0.677 within 2% for the laminar case and is found to be a constant of 0.667 for the turbulent case.
机译:从固体表面到流体流的热量和质量传递都是扩散驱动的过程。对于相同的流动和边界条件,它们的数学模型方程式是相同的。工程应用的问题已从一个领域转换为另一个领域,从而具有实用和经济优势。与直接传热测量相比,使用萘升华的传质技术更快,更高分辨率,更经济,更准确。空气中的传热扩散与空气中的萘的扩散扩散速度在数量上是不同的。因此,当通过实验验证热/质量传递类比并确定一个类比因子(F = Nu / Sh)时,可以证明萘升华技术的优势。;通过实验验证了二维层流和湍流边界的热/质量传递类比。层流。热边界层技术用于测量局部传热系数(Nu),萘升华技术用于测量经受相同边界层流的两个相同板的局部传质系数(Sh)。热边界层技术的精度是使用由恒定功率的钢垫片制成的恒定热通量板确定的。对流热通量是在校正传导和辐射效应后使用此电能确定的。将这些结果与使用热边界层技术确定的热通量值进行比较,发现一致在2%以内。;使用鳍分析和可变对流传热负载的数值模型,研究了热电偶导线内的传导效应。 。求解边界层内热电偶探针的各个位置的平衡热电偶温度,以模拟用于分析计算的层状边界层流的等效实验。该模型的预测值在实验测量值的1%之内,并用于层流情况下对其进行校正。对于层流情况,发现其与0.677的分析预测相吻合,误差在2%以内,而对于湍流情况,它的常数为0.667。

著录项

  • 作者

    Kulkarni, Kaustubh Shankar.;

  • 作者单位

    University of Minnesota.;

  • 授予单位 University of Minnesota.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 2008
  • 页码 258 p.
  • 总页数 258
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 机械、仪表工业;
  • 关键词

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