板式换热器波纹通道的流动与传热机理

doi:10.11949/j.issn.0438-1157.20170673

化工学报 ›› 2017, Vol. 68 ›› Issue (S1): 71-82.DOI: 10.11949/j.issn.0438-1157.20170673

板式换热器波纹通道的流动与传热机理

王茜¹, 韩怀志², 李炳熙¹

1. 哈尔滨工业大学能源科学与工程学院, 黑龙江哈尔滨 150001;
2. 哈尔滨工程大学动力与能源工程学院, 黑龙江哈尔滨 150001

收稿日期:2017-05-23 修回日期:2017-05-26 出版日期:2017-08-31 发布日期:2017-08-31
通讯作者: 李炳熙,libx@hit.edu.cn
基金资助:
国家自然科学基金项目（51506034）。

Flow and heat transfer mechanism of corrugated plate heat exchanger

WANG Qian¹, HAN Huaizhi², LI Bingxi¹

1. School of Energy Science and Engineering, Harbin Institute of Technology, Harbin 150001, Heilongjiang, China;
2. School of Power and Energy Engineering, Harbin Engineering University, Harbin 150001, Heilongjiang, China

Received:2017-05-23 Revised:2017-05-26 Online:2017-08-31 Published:2017-08-31
Supported by:
supported by the National Natural Science Foundation of China(51506034).

摘要/Abstract

摘要：

采用Realizable k-ε湍流模型，针对一种人字形板间波纹通道的流动与传热机理进行了数值模拟研究。考察了不同Reynolds数湍流状态下波纹通道中沿壁面的平均以及局部表面特征数（Nu和f）的变化规律，揭示了流动与传热参数在波纹通道不同横向剖面的分布规律。结果表明在Re<7860时，凹壁面Nu更大；Re>7860时，凸壁面Nu更大；随着Re的增大凹壁面f大于凸壁面。凹壁面的Nu在近入口和近出口处存在两个峰值，并且在近出口处存在极大值；而凸壁面在近入口处存在一个极大值，在近出口处存在极小值。凹壁面的f在近出口处出现陡升现象，而凸壁面则在近入口处出现陡升。随着Re增大，剖线v和TKE增大，而T减小。另外，v、T和TKE在近凹壁面区域皆突然增大。

关键词: 板式换热器, 数值模拟, 强化换热, 传热机理

Abstract:

In this paper,the Realizable k-ε turbulence model is used to simulate the flow and heat transfer mechanism of a corrugated channel. Considering various Re in turbulence regions,the variation of the averaged characteristic number on wall surface (Nu and f) and the local characteristic number along the wall surfaces of the corrugated channel are investigated. The distribution of internal flow and heat transfer parameters in different transverse sections is analyzed. The results show that when Re<7860, Nu of concave wall is larger; when Re>7860, Nu of convex wall is larger; while f on the convex wall is always larger than that on the concave wall. Nu reached two peak values near entrance and exit of the convex wall,moreover,the maximum value in located near the exit. However,a maximum Nu is located near the entrance and a minimum is located near the exit for the concave wall. As for f,steep rising occurs near the exit of the convex wall,while steep rising appears near the entrance of the concave wall. With the increase of Re, v and TKE at all profiles also increase,while T decrease. In addition,v,T and TKE all suddenly increase near the region of convex wall.

Key words: plate heat exchanger, numerical simulation, enhanced heat transfer, heat transfer mechanism

中图分类号:

TK124

王茜, 韩怀志, 李炳熙. 板式换热器波纹通道的流动与传热机理[J]. 化工学报, 2017, 68(S1): 71-82.

WANG Qian, HAN Huaizhi, LI Bingxi. Flow and heat transfer mechanism of corrugated plate heat exchanger[J]. CIESC Journal, 2017, 68(S1): 71-82.

参考文献 21

[1]	POLLEY G T,PODDAR T K. Optimize shell-and-tube heat exchanger design[J]. Chemical Engineering Progress,2000,96(9):41-46.
[2]	马学虎,林乐,兰忠,等. 低Re下板式换热器性能的实验研究及热力学分析[J]. 热科学与技术,2007,6(1):38-44. MA X H,LIN L,LAN Z,et al. Experimental investigation and thermodynamic analysis of performance of plate heat exchanger for low Reynolds number[J]. J. Therm. Sci. Tech.,2007,6(1):38-44.
[3]	程宝华,李先瑞. 板式换热器及换热装置技术应用手册[M]. 北京:中国建筑出版社,2005:3-4. CHENG B H,LI X R. Plate Heat Exchanger and Heat Exchanger Technology Application Manual[M]. Beijing:China Construction Press,2005:3-4.
[4]	GILLHAM M W H. A new composite material for plate heat exchanger[J]. Materials & Design,1988,9(4):192-194.
[5]	PANCHAL C B. Condensation heat transfer in plate heat exchangers[J]. Two-Phase Heat Exchanger Symposium,1985,44:45-52.
[6]	MANGLIK R M,WILKINS R L. Forced convective boiling of a non-newtonian liquid in a multipass plate heat exchanger[J]. AIChE Symposium Series,1993,89:230-235.
[7]	谢静如. 板式换热器的调研[J]. 北京节能,1990,(4):6-8. XIE J R. A survey of plate heat exchangers[J]. Beijing Energy Conservation,1990,(4):6-8.
[8]	蔡毅,贾志刚,周文学,等. 人字形波纹板式换热器性能数值模拟的研究[J]. 计算机与应用化学,2009,26(1):105-108. CAI Y,JIA Z G,ZHOU W X,et al. Study on numerical simulation of chevron-type plate heat exchanger[J].Computer and Applied Chemistry,2009,26(1):105-108.
[9]	CIOFALO M,PIAZZA I D,STASIEK J A. Investigation of flow and heat transfer in corrugated-undulated plate heat exchanger[J]. Heat and Mass Transfer,2000,365:449-462.
[10]	ISLAMOGLU Y,PARMAKSIZOGLU C. The effect of channel height on the enhanced heat transfer characteristic in a corrugated heat exchanger channel[J]. Applied Thermal Engineering,2003,23(8):979-987.
[11]	阴继翔,李国君,丰镇平. 两种波纹通道内周期性充分发展对流换热的研究[J]. 热能动力工程,2005,20(3):252-256. YIN J X,LI G J,FENG Z P. Numerical study on periodically fully developed convection heat transfer in two kinds of wavy channels[J]. J. Eng. Thermal Energy and Power,2005,20(3):252-256.
[12]	LEE J Y,LEE K S. Flow characteristics and thermal performance in chevron type plate heat exchangers[J]. International Journal of Heat and Mass Transfer,2014,78:699-706.
[13]	ZHANG J H,KUNDU J,MANGLIK RM. Effect of fin waviness and spacing on the lateral vortex structure and laminar heat transfer in wavy-plate-fin-cores[J]. Journal of Heat and Mass Transfer,2004,47(8/9):1719-1730.
[14]	李国君,阴继翔,丰镇平. 波纹通道板间距对通道内流动与换热影响的数值研究[J]. 热科学与技术,2005,4(2):123-129. LI G J,YIN J X,FENG Z P. Numerical investigation of effects of plate spacing on flow and heat transfer in sinusoidal channels[J]. Journal of Thermal Science and Technology,2005,4(2); 123-129.
[15]	徐志明,王月明,张仲斌,等. 板式换热器性能的数值模拟[J]. 动力工程学报,2011,31(3):198-202. XU Z M,WANG Y M,ZHANG Z B,et al. Numerical simulation on performance of plate heat exchanger[J]. Journal of Chinese Society of Power Engineering,2011,31(3):198-202.
[16]	杨崇麟. 板式换热器工程设计手册[M]. 北京:中国机械出版社,1994:23. YANG C L. Engineering Design Handbook of Plate Heat Exchanger[M]. Beijing:China Machine Press,1994:23.
[17]	王福军. 计算流体力学分析——CFD软件原理与应用[M]. 北京:清华大学出版社,2004:35. WANG F J. Analysis of Computational Fluid Dynamics-Principle and Application of CFD[M]. Beijing:Tsinghua University Press,2004:35.
[18]	李晓亮. 人字形板式换热器强化传热研究及场协同分析[D]. 济南:山东大学,2009. LI X L. Research on heat transfer enhancement and field synergy principle of chevron-type plate heat exchanger[D]. Jinan:Shandong University,2009.
[19]	陶文铨. 传热学[M]. 2版. 西安:西安交通大学出版社,2001:209. TAO W Q. Heat Transfer[M]. 2nd ed. Xi'an:Xi'an Jiaotong University Press,2001:209.
[20]	杨刚. 波纹板形状参数对换热器性能影响的数值研究[D].太原:太原理工大学,2012. YANG G. Numerical study of heat exchangers with different geometric parameters[D].Taiyuan:Taiyuan University of Technology,2012.
[21]	陈卓如,金朝铭,王洪杰,等. 工程流体力学[M]. 2版.北京:高等教育出版社,2004:347. CHEN Z R,JIN C M,WANG H J,et al. Engineering Fluid Mechanics[M]. 2nd ed. Beijing:Higher Education Press,2004:347.

板式换热器波纹通道的流动与传热机理

Flow and heat transfer mechanism of corrugated plate heat exchanger

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