首页> 外文期刊>International Journal of Heat and Fluid Flow >Mixed convection heat transfer to and from a horizontal cylinder in cross-flow with heating from below
【24h】

Mixed convection heat transfer to and from a horizontal cylinder in cross-flow with heating from below

机译:混合对流传热与来自水平圆柱体的横流交叉传热,下方加热

获取原文
获取原文并翻译 | 示例
       

摘要

Heat transfer to and from a circular cylinder in a cross-flow of water at low Reynolds number was studied both experimentally and numerically. The experiments were carried out in a high aspect ratio water channel. The test section inflow temperature and velocity, channel lower surface temperature and cylinder surface temperature were controlled to yield either laminar or turbulent flow for a desired Richardson number. When the lower surface was unheated, the temperatures of the lower surface and water upstream of the cylinder were maintained approximately equal and the flow was laminar. When the lower surface was heated, turbulence intensities as high as 20% were measured several cylinder diameters upstream of the cylinder due to turbulent thermal plumes produced by heating the lower surface. Variable property, two-dimensional simulations were undertaken using a variant of the v~2-f turbulence model with buoyancy production of turbulence accounted for by a simple gradient diffusion model. Predicted and measured heat flux distributions around the cylinder are compared for values of the Richardson number, Gr_d/Re_d~2, from 0.3 to 9.3. For laminar flow, the predicted and measured heat flux results agreed to within the experimental uncertainty. When the lower surface was heated, and the flow was turbulent, there was qualitative agreement between predicted and measured heat flux distributions around the cylinder. However the predicted spatially averaged Nusselt number was from 37% to 53% larger than the measured spatially averaged Nusselt number. Additionally, spatially averaged Nusselt numbers are compared to correlations in the literature for mixed convection heat transfer to/from cylinders in cross-flow. The results presented here are larger than the correlation values. This is believed to be due to the effects of buoyancy-induced turbulence resulting from heating the lower surface and the proximity of the cylinder to that surface.
机译:以低雷诺数的水在横流中与圆柱体之间的热传递进行了实验和数值研究。实验是在高纵横比的水通道中进行的。控制测试部分的流入温度和速度,通道下表面温度和圆柱体表面温度,以产生所需理查森数的层流或湍流。当下表面不加热时,下表面的温度与气缸上游的水保持大致相等,并且流动呈层流状态。当加热下表面时,由于加热下表面产生的湍流热羽流,在气缸上游几个气缸直径处测得的湍流强度高达20%。使用v〜2-f湍流模型的变体进行了可变性质的二维模拟,其中湍流的浮力产生是由简单的梯度扩散模型引起的。比较在汽缸周围的预测和测量的热通量分布,以比较Richardson数Gr_d / Re_d〜2的值(从0.3到9.3)。对于层流,预测和测量的热通量结果在实验不确定性范围内是一致的。当下表面被加热并且流动湍流时,圆柱体周围的预测和测量的热通量分布之间存在定性一致性。但是,预测的空间平均Nusselt数比测量的空间平均Nusselt数大37%至53%。此外,将空间平均的努塞尔数与文献中的相关性进行了比较,以进行横流向/从汽缸的混合对流传热。此处显示的结果大于相关值。认为这是由于加热下表面以及圆柱体靠近该表面而产生的浮力引起的湍流的影响。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号