首页> 外文会议>Japan-Korea symposium on nuclear thermal hydraulics and safety >INTERFACIAL CONDENSATION FOR COUNTERCURRENT STEAM-WATER STRATIFIED SMOOTH/WAVY FLOW IN A HORIZONTAL PIPE
【24h】

INTERFACIAL CONDENSATION FOR COUNTERCURRENT STEAM-WATER STRATIFIED SMOOTH/WAVY FLOW IN A HORIZONTAL PIPE

机译:逆流蒸汽水分层光滑/波状流动的界面凝结

获取原文

摘要

The main objective of the present work is to extend the previous work of Chun et al. (1999) on the interfacial condensation heat transfer in stratified smooth flow. In contrast to the previous work where only the interfacial condensation heat transfer in stratified smooth flow of steam-water has been investigated, in the present extension work both regions of stratified smooth and stratified wavy flow of steam-water are investigated. For the purpose of the present work, a few modifications of the test section and instrumentation were made to be more suitable for the investigation of interfacial condensation heat transfer at wavy flow condition. To show the difference in the heat transfer characteristics depending on the interface condition, in particular, the results obtained for both the smooth and wavy interface of steam-water stratified flow are presented and compared. A total of 174 average interfacial condensation heat transfer coefficients for a smooth interface and 105 local interfacial condensation heat transfer coefficients for a wavy interface have been obtained. The parametric effects of steam and water flow rates and the degree of subcooling on condensation heat transfer were also examined. Two empirical Nusselt number correlations, one for smooth and the other for wavy interface region, were developed based on the bulk flow properties. Comparisons of the present circular pipe data with two existing correlations developed for wide rectangular channels showed that the existing correlations underpredict Nusselt numbers for a smooth interface, whereas these existing correlations give conflicting results for stratified wavy flow.
机译:本工作的主要目标是扩展春等人的前一项工作。 (1999)关于分层平滑流动的界面凝结热传递。与先前的工作相比,在已经研究了蒸汽水的分层光滑流动中的界面凝结热传递的相反,在本发明的延伸工作中,研究了分层平滑和分层波浪流的两个区域进行了研究。出于本作本作的目的,对测试部分和仪器进行了一些修改,更适合于在波状流动条件下调查界面凝结热传递。为了表明根据界面条件的传热特性的差异,特别是呈现并比较了蒸汽水分层流动的平滑和波浪界面获得的结果。已经获得了总共174个平均界面凝结传热系数,用于光滑界面和105个局部界面凝结传热系数用于波浪界面。还研究了蒸汽和水流速的参数效应和过冷却对冷凝热传递的过冷度。基于散装流量,开发了两个经验露天数相关性,一个用于波浪接口区域的另一个用于波浪接口区域。本发明的循环管数据的比较具有两个用于宽矩形通道的相关性的相关性,显示了现有的相关性涉及光滑界面的漏斗数,而这些相关性给出了分层波浪流的矛盾的结果。

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