首页> 外文会议>ICONE18;International conference on nuclear engineering >Heat Transfer Experiments and Analyses on Double-Tube Bundle Heat Exchanger
【24h】

Heat Transfer Experiments and Analyses on Double-Tube Bundle Heat Exchanger

机译:双管束式换热器的传热实验与分析

获取原文

摘要

Experiments were performed on the double-tube bundle heat exchanger. The hot side of the heat exchanger consists of parallel flow channels of the inner tubes and the space between the shell and the double-tube bundle, and the cold side is the narrow annular flow channels between the inner and outer tubes. The test fluid in both hot and cold sides is de-ionized water. The heat-transfer coefficients were obtained from the experiment in the range of Reynolds number from 2000 to 38000. The detached coefficients method was used in the absence of direct measurement of the tube temperature. It is found that the ranges of laminar flow in both internal and external flow passages are wider than regular circular tube. The heat transfer coefficient of internal side is lower than those from Dittus-Boelter formula, while the heat transfer coefficient of external side in this experiment is higher than that for the corrugated pipe. The heat transfer coefficient of the narrow annularchannel is significantly determined by its structure.;
机译:实验在双管束式换热器上进行。热交换器的热侧由内管的平行流道以及壳体和双管束之间的空间组成,而冷侧是内管和外管之间的狭窄环形流道。冷热两面的测试液都是去离子水。从实验中获得了2000到38000雷诺数范围内的传热系数。在没有直接测量管温的情况下,采用了分离系数法。发现内部和外部流动通道中的层流范围都比常规的圆形管宽。内侧的传热系数低于Dittus-Boelter公式中的数值,而本实验中外侧的传热系数高于波纹管的传热系数。窄环形通道的传热系数明显取决于其结构。

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