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  • 中国标准连:ISSN1005-2895
  • 续出版物号: CN 33-1180/TH
  • 主管单位:轻工业杭州机电设计研究院有限公司
  • 主办单位:轻工业杭州机电设计研究院有限公司、中国轻工机械协会、中国轻工业机械总公司
  • 社  长:刘安江
  • 主  编:黄丽珍
  • 地  址:杭州市余杭区高教路970号西溪联合科技广场4-711
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吕彤, 李庆生.水平管降膜蒸发器管外膜状流流动特征研究[J].轻工机械,2020,38(1):35-40
水平管降膜蒸发器管外膜状流流动特征研究
Study of Sheet Flow Characteristics Outside Tube of Horizontal Tube Falling Film Evaporator
  
DOI:10.3969/j.issn.1005 2895.2020.01.007
中文关键词:  水平管降膜蒸发器  膜状流  液膜厚度  布液高度
英文关键词:horizontal tube falling film evaporator  sheet flow  liquid film thickness  liquid film distribution height
基金项目:
作者单位
吕彤, 李庆生 南京工业大学 机械与动力工程学院 江苏 南京211816 
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中文摘要:
      为了探究水平管降膜蒸发器管外液膜分布的优劣对其传热性能的影响,课题组建立了水平管三维模型对管外膜状流流动进行数值模拟,得到液膜沿水平管轴向和周向的分布规律,并对膜厚波动幅度Δ进行研究;分析了流量、布液高度及管外径对管外液膜厚度的影响。结果表明:当周向角度一定时,液膜厚度沿水平管轴向小幅波动;膜厚波动幅度Δ在θ为10°~20°时逐渐减小,其最大值为0.168 62;在θ为150°~170°时逐渐增大,其最大值为0.362 91;当θ为20°~150°时,膜厚波动幅度Δ<0.075 00,液膜流动呈现平稳发展的趋势。研究表明液膜沿水平管周向流动可划分为3个区域:θ为10°~20°时为冲击区,θ为20°~150°时为稳定区,θ为150°~170°时为尾流区。液膜厚度随流量的增大而增大,随布液高度和管外径的增大而减小。
英文摘要:
      In order to investigate the influence of outer liquid film distribution of the horizontal tube falling film evaporator on its heat transfer performance, a three dimensional model was established to numerically simulate the sheet flow outside the tube of horizontal tube falling film evaporator. The distribution law of liquid film along the horizontal tube in axial and circumferential directions was obtained, and the fluctuation amplitude of film thickness was studied.The effects of flow rate, distribution height and outer diameter of tube on the film thickness outside the horizontal tube were analyzed. The results show that when the circumferential angle is constant, the liquid film thickness slightly fluctuates along the axial direction of the horizontal tube. The fluctuation amplitude of film thickness decreased gradually at θ=10°~20° and increased at θ=150°~170°, with the maximum value of 0.168 62 and 0.362 91 respectively. When θ=20°~150°, the fluctuation amplitude of film thickness is less than 0.075 00, and the liquid film flow showed a steady development trend. The circumferential flow of the liquid film along the horizontal tube can be divided into three zones: the impact zone at θ=10°~20°, the stable zone at θ=20°~150° and the wake zone at θ=150°~170°. The liquid film thickness increases with the increase of flow rate and decreases with the increase of distribution height and outer diameter.
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