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基于螺旋片强化的套管换热器性能
引用本文:王定标,董永申,向飒,夏春杰,王艺玮,张光辉. 基于螺旋片强化的套管换热器性能[J]. 化工学报, 2014, 65(4): 1208-1214. DOI: 10.3969/j.issn.0438-1157.2014.04.008
作者姓名:王定标  董永申  向飒  夏春杰  王艺玮  张光辉
作者单位:郑州大学化工与能源学院, 河南 郑州 450001
基金项目:河南省科技创新杰出青年人才计划项目(124100510020)。
摘    要:基于RNG k-ε模型对螺旋片强化的套管换热器的传热进行模拟,通过模拟结果与文献中的实验结果进行对比来验证模拟的可行性;分析了Reynolds数为2362~16860范围内的螺旋升角α变化对Nusselt数和摩擦阻力系数f的影响;并考察了等泵功率下的综合传热性能PEC值的变化规律。结果表明:Nu和f的平均误差分别为7.1%和1.3%,证明所采用的研究方法是可行的;α在15°~75°范围内,Nu和f均随着α的减小而增大,特别地,当α小于35°时,f随α的减小剧烈增大;在等泵功率下,PEC值为0.84~1.93;α在15°~45°时,α为35°具有较好的综合传热性能,α为55°、65°和75°时,虽然其PEC值比35°时略高,但其Nu与35°时相比要小很多,实际应用中考虑到传热速率的问题,选择35°的螺旋升角较为合适,此时,PEC值为1.26~1.62。另外,为减小f,提出倾斜螺旋片强化的方法;螺旋升角α为35°、螺旋片倾斜角β为10°时,与普通螺旋片相比,Nu基本一致,甚至略大,而f减小了12.5%~14.5%,此时,PEC值为1.38~1.71;场协同理论也很好地验证了这一结果。

关 键 词:传热  套管式换热器  螺旋片  螺旋升角  数学模拟  计算流体力学  
收稿时间:2013-07-02
修稿时间:2013-11-29

Performance of double-pipe heat exchanger enhanced by helical fins
WANG Dingbiao,DONG Yongshen,XIANG Sa,XIA Chunjie,WANG Yiwei,ZHANG Guanghui. Performance of double-pipe heat exchanger enhanced by helical fins[J]. Journal of Chemical Industry and Engineering(China), 2014, 65(4): 1208-1214. DOI: 10.3969/j.issn.0438-1157.2014.04.008
Authors:WANG Dingbiao  DONG Yongshen  XIANG Sa  XIA Chunjie  WANG Yiwei  ZHANG Guanghui
Affiliation:School of Chemical Engineering and Energy, Zhengzhou University, Zhengzhou 450001, Henan, China
Abstract:In this paper, RNG k-ε model is used to simulate the heat transfer of a double-pipe heat exchanger enhanced by helical fins. The simulation results are verified with experimental results. With the Reynolds number from 2362 to 16860, the effect of helix angle α on the Nusselt number and frictional resistance coefficient f are analyzed. The change of performance evaluation criteria(PEC) value and the comprehensive heat transfer performance at the same pump power are examined. The average error of Nu and f are 7.1% and 1.3%, respectively, indicating that the method used is appropriate. For α from 15° to 75°, both Nu and f increase as α decreases. In particular, for α values less than 35°, f increases dramatically as α decreases. With the same pump power, the value of PEC varies from 0.84 to 1.93. In the α range from 15° to 45°, the comprehensive heat transfer performance is better with 35°. Although the PEC values with α of 55°, 65° and 75° are slightly higher than that of 35°, Nu is much smaller. Considering the rate of heat transfer in applications, helix angle of 35° is more appropriate, with PEC of 1.26—1.62. Besides, it is proposed to use oblique helical fins to reduce the value of f. Compared with double-pipe heat exchanger enhanced by common helical fins, the Nu value of that enhanced by oblique helical fins with α of 35° and β of 10° is a little higher, f is reduced by 12.5%—14.5%, and PEC varies from 1.38—1.71. The field synergy principle also verifies the result.
Keywords:heat transfer  double-pipe heat exchanger  helical fins  helix angle  mathematical modeling  computational fluid dynamics  
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