首页> 外文期刊>International Journal of Heat and Mass Transfer >Thermal transport due to liquid jet impingement on superhydrophobic surfaces with isotropic slip: Isoflux wall
【24h】

Thermal transport due to liquid jet impingement on superhydrophobic surfaces with isotropic slip: Isoflux wall

机译:由于各向同性滑动的超疏水表面上的液体喷射冲击导致的热运输:异氟壁壁

获取原文
获取原文并翻译 | 示例
           

摘要

Thermal transport due to a liquid water jet impinging an isoflux superhydrophobic surface with isotropic slip was modeled analytically. An integral analysis of the transport equations resulting in a system of ordinary differential equations was solved numerically. impingement on superhydrophobic surfaces greatly reduces the heat transfer that occurs relative to a smooth surface due to gas trapped in cavities on the surface. This results in an apparent slip velocity and temperature jump at the surface. Local and average Nusselt numbers are presented as a function of radial position (0 to 45 jet radii), jet Reynolds number (3 x 10(3) to 1.5 x 10(4)), liquid Prandtl number (2 to 11), normalized slip length (0 to 0.2), and normalized temperature jump length (0 to 0.2). All results are compared to classical (no-slip, no temperature jump) behavior on a smooth surface. Although local Nusselt numbers for the isoflux scenario are greater than the corresponding isothermal case, the difference in Nusselt number between these two heating conditions becomes negligible as the temperature jump length increases to quantities realizable on superhydrophobic surfaces. These results may be utilized to explore heat transfer degradation in applications where smooth surfaces are replaced by superhydrophobic surfaces to avoid fouling. (C) 2019 Elsevier Ltd. All rights reserved.
机译:由于液体水射流而导致具有各向同性滑移的异氟超疏水表面的液体水射流的热传输被分析地进行了分析建模。在数值上解决了导致常微分方程系统的传输方程的积分分析。在超疏水表面上冲击大大减少了由于在表面上捕获的空腔中的气体而发生的热传递。这导致表观滑动速度和温度跳跃在表面。局部和平均露珠数量作为径向位置(0至45次喷射半径),射流雷诺数(3×10(3)至1.5×10(4)),液体PRANDTL数(2至11),标准化滑动长度(0至0.2),归一化温度跳长(0至0.2)。将所有结果与光滑表面上的经典(无滑动,无温度跳跃)行为进行比较。尽管ISOflux场景的本地营养数字大于相应的等温案例,但由于温度跳跃长度增加到超疏水表面可实现的量,因此这两个加热条件之间的泡沫数的差异变得忽略不计。这些结果可用于探讨液体过度表面代替的应用中的传热劣化,以避免污垢。 (c)2019 Elsevier Ltd.保留所有权利。

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