首页> 外文会议>Second Japan-Korea Symposium on Nuclear Thermal Hydraulics and Safety Oct 15-18, 2000 Denki Bldg., Chuo-ku, Fukuoka, Japan >INTERFACIAL CONDENSATION FOR COUNTERCURRENT STEAM-WATER STRATIFIED SMOOTH/WAVY FLOW IN A HORIZONTAL PIPE
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INTERFACIAL CONDENSATION FOR COUNTERCURRENT STEAM-WATER STRATIFIED SMOOTH/WAVY FLOW IN A HORIZONTAL PIPE

机译:水平管中逆流蒸汽分层的光滑/波浪状流动的界面冷凝

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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:当前工作的主要目的是扩展Chun等人的先前工作。 (1999)关于界面凝结传热的分层平稳流动。与仅研究蒸汽分层水流中的界面冷凝传热的先前工作相反,在本扩展工作中,研究了蒸汽分层水流和分层波浪流的两个区域。为了本工作的目的,对测试部分和仪器进行了一些修改,使其更适合于研究波浪状流动条件下的界面冷凝传热。为了显示出取决于界面条件的传热特性的差异,特别是,提出并比较了汽水分层流的光滑和波浪形界面所获得的结果。光滑界面的平均总界面凝结换热系数为174,波浪界面的平均局部凝结换热系数为105。还检查了蒸汽和水流量以及过冷度对冷凝传热的参数影响。基于整体流动特性,开发了两个经验努塞尔数相关性,一个用于光滑,另一个用于波浪形界面区域。现有圆形管道数据与为宽矩形通道开发的两个现有相关性的比较表明,现有相关性对光滑界面的Nusselt数预测不足,而这些现有相关性为分层波浪流提供了矛盾的结果。

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