化工进展

• 节能技术专栏 • 上一篇    

管翅式换热器管路布置优化设计的数值研究

陶于兵,何雅玲,唐连伟,陶文铨   

  1. 西安交通大学能源与动力工程学院,动力工程多相流国家重点实验室
  • 出版日期:2007-06-25 发布日期:2007-06-25

Numerical study on optimization design of circuit arrangement for tube-fin heat exchanger

TAO Yubing,HE Yaling,TANG Lianwei,TAO Wenquan   

  1. State Key Laboratory of Multiphase Flow in Power Engineering,School of Energy and Power Engineering,Xi’an Jiaotong University
  • Online:2007-06-25 Published:2007-06-25

摘要: 采用分布参数法模型对常见的双流程管翅式换热器,在不同的空气及制冷剂进口状态下的工作性能进行了数值研究,对管路布置提出了改变不同流程管径比的优化设计方案,并从数值模拟的角度给出了验证。数值计算结果表明改变两流程之间的管径比可以优化换热器的换热性能,而且两流程的管径之间存在一个最佳比值0.8,在该最佳管径比下,换热器的换热性能在不同工况下均比相同管径提高6%~11%,同时可以使空气侧的阻力损失减少2%。

Abstract: The numerical study on the performance of a double flow-pass tube-fin heat exchanger was performed with different air and refrigerant inlet parameters. An optimization design of circuit arrangement was presented and was validated by the numerical simulation results. The results showed that there was an optimal ratio between the two flow-pass tube diameters in the heat exchangers. In this paper the optimal ratio was 0.8 and with this optimal ratio,the heat transfer performance of the heat exchanger could be enhanced by 6%~11%,at the same time the pressure drop of the air side could be decreased by 2%.

京ICP备12046843号-2;京公网安备 11010102001994号
版权所有 © 《化工进展》编辑部
地址:北京市东城区青年湖南街13号 邮编:100011
电子信箱:hgjz@cip.com.cn
本系统由北京玛格泰克科技发展有限公司设计开发 技术支持:support@magtech.com.cn