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Turbulent scalar transport in non-reacting and reacting flows.

机译:非反应流和反应流中的湍流标量传输。

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摘要

In this work, flow databases from direct numerical simulations were used to study the physics of turbulent heat and mass transfer in non-reacting and reacting flows. Statistical analysis and visualizations were used to gather information about turbulent scalar transport to help scalar transport model development and validation.; Passive heat transfer in non-reacting flows was investigated using simulations of a channel flow and a plane Couette flow. Flow databases were created for each case, for a Reynolds number of 3000, based on the mean velocity and the channel half-width. The flows were bounded by isothermal walls with one wall at a higher temperature than the other. Near the wall, the heat transfer mechanisms are similar in both flows. In this near wall heat transfer, streamwise vortices play a significant role. At the centerline, however, the Couette flow has large scale flow structures, not present in the channel flow, that transport heat across the centerline. These structures are possible due to the non-zero turbulent production at the centerline of the Couette flow. For the channel flow, the lower turbulence levels at the centerline are not effective in breaking up packets of hot or cold fluid that originate at the walls. Instead, these packets convect with the mean flow resulting in a less efficient heat transfer than in the Couette flow.; To study heat and mass transfer in reacting flows, a statistical analysis was performed on existing databases of spatially developing, three-dimensional, reacting and non-reacting shear layers. Turbulent Prandtl and Schmidt numbers were calculated to characterize turbulent heat and mass transfer. The time averaged scalar equations and the budgets for fluctuating scalars showed interesting similarities between temperature in the non-reacting shear layer and oxidizer mass fraction in the reacting case. These similarities correspond to the similarity in the mean profiles for these quantities. In the budgets for fluctuating scalars in the reacting flow, however, the turbulent transport term is more important than in the non-reacting case and counters the peaks in turbulent production.
机译:在这项工作中,直接数值模拟的流量数据库用于研究非反应性和反应性流动中湍流传热和传质的物理学。统计分析和可视化用于收集有关湍流标量运输的信息,以帮助标量运输模型的开发和验证。使用通道流和平面库埃特流的模拟研究了非反应流中的被动传热。基于平均速度和通道半宽度,针对每种情况创建了流量数据库,雷诺数为3000。流动被等温壁限制,其中一个壁的温度高于另一个壁的温度。在壁附近,两种流动的传热机制都相似。在这种近壁热传递中,沿流的涡流起着重要作用。然而,在中心线处,库埃特流具有在通道流中不存在的大尺度流动结构,该结构在整个中心线上传递热量。由于Couette流中心线处的非零湍流产生,因此这些结构是可能的。对于通道流,中心线处较低的湍流水平无法有效地分解源自壁的热流体或冷流体。相反,这些小包与平均流对流,导致热传递效率低于库埃特流。为了研究反应流中的传热和传质,对空间发展,三维,反应和非反应剪切层的现有数据库进行了统计分析。计算了湍流Prandtl和Schmidt数以表征湍流传热和传质。时间平均标量方程和标量波动的预算显示出非反应性剪切层中的温度与反应情况下的氧化剂质量分数之间的有趣相似性。这些相似之处对应于这些数量的平均轮廓的相似性。但是,在用于使反应流中的标量波动的预算中,湍流输运项比非反应情况更重要,并且可以抵消湍流产生的峰值。

著录项

  • 作者

    Debusschere, Bert Jan.;

  • 作者单位

    The University of Wisconsin - Madison.;

  • 授予单位 The University of Wisconsin - Madison.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 2001
  • 页码 151 p.
  • 总页数 151
  • 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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