• CN:11-2187/TH
  • ISSN:0577-6686

机械工程学报 ›› 2015, Vol. 51 ›› Issue (12): 137-145.doi: 10.3901/JME.2015.12.137

• 可再生能源与工程热物理 • 上一篇    下一篇

扫码分享

基于计算流体力学数值模拟的板式换热器传热与流动分析及波纹参数优化

张晶1, 文珏1, 赵力1, 李德育2, 王毅2   

  1. 1.天津大学中低温热能高效利用教育部重点实验室 天津 300072;
    2.天津市津能技术中心 天津 300384
  • 出版日期:2015-06-20 发布日期:2015-06-20
  • 基金资助:
    国家高技术研究发展计划(863计划,2012AA051103)和天津市科技支撑(11ZCZDGX19800)资助项目

Heat Transfer and Flow Analysis and Corrugation Parameters Optimization of the Plate Heat Exchanger Based on Computational Fluid Dynamics Numerical Simulation

ZHANG Jing1, WEN Jue1, ZHAO Li1, LI Deyu2, WANG Yi2   

  1. Key Laboratory of Efficient Utilization of Low and Medium Grade Energy (Tianjin University), Ministry of Education, Tianjin 300072;
    Tianjin Energy Technology Center, Tianjin 300384
  • Online:2015-06-20 Published:2015-06-20

摘要: 基于计算流体力学(Computational fluid dynamics, CFD)方法对板式换热器整板和局部计算域进行数值模拟。建立1 000 mm数量级冷热双流道的人字形板式换热器整板片的流动及换热计算模型,利用FLUENT软件对集中供暖系统中的水-水换热工况进行模拟研究,分析冷热流体在换热器中的流动形态以及换热情况;与此同时建立200 mm×200 mm冷热双流道的局部计算域模型,对不同波纹倾角β,波纹截距λ的板片单元进行模拟分析,根据波纹参数对板式换热器的流动及换热情况的影响优化波纹参数。结果表明,整板LPM77板片流道中流体分布十分不均,且人字形尖点和流道边缘处流速较低,湍流程度较小,换热效果较差;随着波纹倾角β增大,板片换热能力先增后减,极值点在β等于60°左右,流体的压降同样先增后减,然而压降的最大值点出现在60°之后。综合考虑换热情况以及流动压降,一般工况下波纹倾角β选择在60°左右较为适宜;随波纹截距λ增大,流体的换热性能以及流动压降均呈现降低趋势,波纹截距λ对压降的影响程度大于波纹倾角β对其的影响。

关键词: 板式换热器, 波纹参数优化, 数值模拟, 双流道

Abstract: Plate heat exchanger (PHE) is simulated based on the computational fluid dynamics (CFD) method. A 1 000 mm-order-of-magnitude calculation model is established for fluid flow and heat transfer in cold and hot flow channels of a chevron-type PHE. The flow pattern and heat transfer effect of the cold and hot fluids are analyzed under the water-to-water heat transfer condition in the central heating system by using the simulation software, FLUENT; At the same time, the 200 mm×200 mm double-channel calculation models of the local computation domains for the PHE are simulated at different corrugated inclination angle β and pitch λ. The corrugation parameters are optimized according to their influences on the fluid flow and heat transfer. The results show that an obvious non-uniformity of the flow distribution exists in the whole plate named LPM77. The flow rate of the fluid is low at the sharp point of the chevron-type and at the edge of the flow channel, which leads to the low degree of turbulence and poor heat transfer effect; with the rise of the corrugated inclination angle β, the heat transfer ability and the pressure drop both increase at first and then decrease. The heat transfer ability reaches the extreme point around the value of 60° for β. While the extreme point of the pressure drop appears after the value of 60°. Therefore, in general working condition of the PHE the corrugated inclination angle β should be set at 60° when taking both heat transfer and pressure drop into consideration; Along with increase of the corrugated pitch λ, the heat transfer ability and the pressure drop both decrease. Besides, the influence of the corrugated pitch λ on the pressure drop is stronger than that of the corrugated inclination angle β.

Key words: corrugation parameters optimization, double-channel, numerical simulation, plate heat exchanger (PHE)

中图分类号: