化工进展 ›› 2023, Vol. 42 ›› Issue (3): 1187-1194.DOI: 10.16085/j.issn.1000-6613.2022-0838

• 化工过程与装备 • 上一篇    下一篇

竖管渗流降膜蒸发式冷凝器传热特性分析

谢迎春1,2(), 马洪亭1, 徐畅1(), 马硕1, 陈默1, 刘军2, 孙国强2   

  1. 1.天津大学环境科学与工程学院,天津 300350
    2.中核坤华能源发展有限公司,浙江 杭州 311113
  • 收稿日期:2022-05-07 修回日期:2022-05-29 出版日期:2023-03-15 发布日期:2023-04-10
  • 通讯作者: 徐畅
  • 作者简介:谢迎春(1973—),女,博士研究生,高级工程师,主要从事传热传质和能源管理研究。E-mail:xieyc01@cnnp.com.cn
  • 基金资助:
    国家自然科学基金(51876137);中核集团横向课题(0505000281)

Analysis of heat transfer characteristics in vertical tube of seepage falling film evaporative condenser

XIE Yingchun1,2(), MA Hongting1, XU Chang1(), MA Shuo1, CHEN Mo1, LIU Jun2, SUN Guoqiang2   

  1. 1.School of Environmental Science and Engineering, Tianjin University, Tianjin 300350, China
    2.CNNP Kunhua Energy Development Co. , Ltd. , Hangzhou 311113, Zhejiang, China
  • Received:2022-05-07 Revised:2022-05-29 Online:2023-03-15 Published:2023-04-10
  • Contact: XU Chang

摘要:

为研究竖管渗流降膜蒸发式冷凝器,通过仿真和实验相结合的手段,探究了冷凝器单管在不同管外温度、空气雷诺数与液体雷诺数等多工况下的传热特性。结合此前研究中存在的问题,合理选择了物理模型与边界条件,获得了降膜过程的轴向温度、热通量分布等并对径向位置进行了时间序列分析。结果表明逆向通风传热效果优于顺向通风,但易加剧管段下部液膜不稳定甚至出现干壁。通过时间序列分析发现干壁区域会被液膜快速覆盖,因此短暂干壁对整体传热影响并不十分明显,仍需注意逆向通风强度过高会对管子下部液膜的稳定性造成显著影响,本文工况下推荐单管空气雷诺数不宜超过3500。此外,测试结果显示本文单管传热量约为2200W,与模拟结果相差6.7%,单管综合传热系数为1400W/(m2·K)左右。

关键词: 降膜蒸发, 冷凝器, 竖直管, 传热特性

Abstract:

In order to study the vertical pipe seepage falling film evaporative condenser, the heat transfer characteristics of the single condenser tube under different external temperature, air Reynolds number and liquid Reynolds number were explored by using the combination of simulation and experiment method. Combined with the problems in previous research, the physical model and boundary conditions were selected reasonably, the axial distribution of temperature and heat flux density of the falling film process were obtained, and the radial position was analyzed in time series. The results showed that the heat transfer effect of reverse ventilation was better than that of co-directional ventilation, but it was easy to aggravate the instability of the liquid film in the lower part of the pipe section and even cause dry wall. It was found that the dry wall area would be covered by the liquid film immediately through time series analysis. Therefore, the effect of short-term dry wall on the overall heat transfer would not very obvious. It was still necessary to pay attention to the great influence of the high reverse ventilation intensity on the stability of the lower liquid film. It was recommended that the single-pipe air Reynolds number should not exceed 3500 under the working conditions of this paper. In addition, the test results showed that the heat transfer of a single tube in this paper was about 2200W, which was 6.7% different from the simulation results, and the comprehensive heat transfer coefficient of the single tube was about 1400W/(m2·K).

Key words: falling film evaporation, condenser, vertical tube, heat transfer characteristics

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