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Research on film condensation heat transfer at the inside of spiral coil tube

机译:螺旋盘管内部薄膜凝结换热的研究

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In this paper, especially considering the influence of viscous force, gravity and centrifugal force on condensation heat transfer, a theoretical model of laminar flow for film condensation heat transfer of pure steam in the spiral coil tube was presented. The solution method of film thickness and heat transfer coefficient was analyzed theoretically, the condensation heat transfer coefficient in the spiral coil tube under different steam volume flow rates was obtained. In order to verify the correctness of the new correlation, the experimental platform of film condensation heat transfer was designed and built up. Heat transfer measurements were performed for the saturated steam volume flow rate from 2.7 to 5.2 m~3/min, and for the cooling water volume flow rate from 1.5 to 7.0m~3/h, and cooling tube wall temperature is 20 ℃. The experimental results were compared with the calculation results of the well-known Kang's correlation and the new correlation. The relative error of results between the new correlation and the experiment is within 15%, which verifies the accuracy of the new correlation proposed in this paper. And the new correlation can be used to calculate the heat transfer coefficient of film condensation in the spiral coil tube. In addition, the experimental results show that the condensation heat transfer coefficient increase with the increasement of steam volume flow rate.
机译:本文特别考虑粘性力,重力和离心力对凝结换热的影响,提出了螺旋盘管中纯蒸汽膜凝结换热的层流理论模型。从理论上分析了膜厚与传热系数的求解方法,得到了不同蒸汽流量下螺旋盘管中的凝结传热系数。为了验证新关系的正确性,设计并建立了薄膜冷凝传热实验平台。对于饱和蒸汽体积流量为2.7至5.2 m〜3 / min,冷却水体积流量为1.5至7.0 m〜3 / h,冷却管壁温度为20℃进行传热测量。将实验结果与著名的康氏相关性和新的相关性的计算结果进行了比较。新相关性与实验结果的相对误差在15%以内,验证了本文提出的新相关性的准确性。新的相关性可用于计算螺旋盘管中膜凝结的传热系数。另外,实验结果表明,凝结换热系数随蒸汽体积流量的增加而增加。

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