3种管内强化管沸腾换热性能对比

doi:10.11949/j.issn.0438-1157.20150051

化工学报 ›› 2015, Vol. 66 ›› Issue (6): 2076-2081.DOI: 10.11949/j.issn.0438-1157.20150051

3种管内强化管沸腾换热性能对比

欧阳新萍¹, 陈静竹¹, 李泰宇²

1. 上海理工大学制冷与低温工程研究所, 上海 200093;
2. 电装中国投资有限公司上海技术中心, 上海 201108

收稿日期:2015-01-13 修回日期:2015-03-17 出版日期:2015-06-05 发布日期:2015-03-25
通讯作者: 陈静竹

Boiling heat transfer performance in three internal enhanced tubes

OUYANG Xinping¹, CHEN Jingzhu¹, LI Taiyu²

1. Institute of Refrigeration and Cryogenics, University of Shanghai for Science and Technology, Shanghai 200093, China;
2. Denso China Investment Co., Ltd., Shanghai Technical Center, Shanghai 201108, China

Received:2015-01-13 Revised:2015-03-17 Online:2015-06-05 Published:2015-03-25

摘要/Abstract

摘要：

对3种不同螺纹结构的强化管的管内沸腾换热性能进行对比实验研究, 采用R22为实验工质。3种强化管的内径和外径相同, 分别为6.9 mm和7.92 mm;管外均为光滑表面, 管内的强化结构参数则不同:螺纹的螺旋角变化范围为14°~18°, 螺纹高为0.15~0.22 mm, 螺纹槽宽度为0.1~0.2 mm。在给定进口和出口制冷剂的状态下, 通过改变管内工质的质量流速, 测试3根强化管的换热特性与质量流速的关系, 并进行性能对比。实验结果表明:3种螺纹管管内沸腾传热系数分别比光管高出60%~80%, 80%~120%和80%。分析认为, 当流动处于层状流或者层状流与环状流的过渡区时, 较大的螺旋角有利于换热;当流体处于环状流时, 较多的螺纹头数有利于换热。

关键词: 热力学, 传热, 气液两相流, 沸腾, 内螺纹管

Abstract:

An experimental study was carried out on the boiling heat transfer of R22 flowing inside three internal thread tubes with different geometrical parameters. Three enhanced tubes have the same inner and outer diameters, which are 6.9 mm and 7.92 mm respectively. The outside surface of the tube is smooth, while the inside enhanced structure is different. The variation range of the helix angle is from14° to18°, the thread height is between 0.15 mm and 0.22 mm, and the thread width is from 0.1 mm to 0.2 mm. The relationship between the heat transfer performance and the mass velocity in three enhanced tubes and a smooth tube was tested by changing the mass velocity of refrigerant under given condition of import and export of refrigerant, and their performance is compared. Experimental results indicate that the heat transfer coefficients of three internal thread tubes are 60%—80%, 80%—120% and 80% higher than that of smooth tube. Analysis suggests that the larger helix angle is advantageous to the heat transfer,when fluid is on laminar flow or the transition of laminar flow and annular flow, and more of thread amount is advantageous to the heat transfer,when the fluid is on annular flow.

Key words: thermodynamics, heat transfer, gas-liquid flow, boiling, internal thread tube

中图分类号:

TK124

欧阳新萍, 陈静竹, 李泰宇. 3种管内强化管沸腾换热性能对比[J]. 化工学报, 2015, 66(6): 2076-2081.

OUYANG Xinping, CHEN Jingzhu, LI Taiyu. Boiling heat transfer performance in three internal enhanced tubes[J]. CIESC Journal, 2015, 66(6): 2076-2081.

参考文献 21

[1]	Gu Weizao (顾维藻). Heat Transfer Enhancement (强化传热) [M]. Beijing: Science Press, 1990.
[2]	Lin Zonghu (林宗虎), Wang Jun (汪军), Li Ruiyang (李瑞阳). Heat Transfer Enhancement Technology (强化传热技术) [M]. Beijing: Chemical Industry Press, 2007.
[3]	Li Jun'an (李军安), Xing Guiju (刑贵菊), Zhou Liwen (周丽雯). Progress in study on technology of heat transfer enhancement for heat exchanger [J]. Energy for Metallurgical Industry (冶金能源), 2008, (1): 50-54.
[4]	Chen Jianbo (陈剑波), Cai Zuhui (蔡祖恢), Ding Yiming (丁一鸣). Study on boiling heat transfer of R12 flowing inside horizontal smooth [J]. Journal of Shanghai Institute of Mechanical (上海机械学院学报), 1992, 14 (30): 1-10.
[5]	Hideyuki Kimura, Masaaki Ito. Evaporating heat transfer in horizontal internal spiral-grooved tubes in the region of low flow rates [J]. Bulletin of the JSME, 1981, 24 (195):1602-1607.
[6]	Timothy A Shedd, Ty A Newell. Visualization of two-phase flow through micro grooved tubes for understanding enhanced heat transfer [J]. International Journal of Heat and Mass Transfer, 2003, 46: 4169-4177.
[7]	Timothy A Shedd, Ty A Newell, Pei Keow Lee. The effects of the number and angle of microgrooves on the liquid film in horizontal annular two-phase flow [J]. International Journal of Heat and Mass Transfer, 2003, 46: 4179-4189.
[8]	Zhou Jie (周杰), Xin Mingdao (辛明道). Two-phase flow pattern in three-dimensional rib tube flow boiling heat transfer [J]. Journal of Chongqing University (重庆大学学报), 2003, 26 (8): 109-113.
[9]	Akhavan-Behabadi M A, Mohseni S G, Najafi H, et al. Heat transfer and pressure drop characteristics of force convective evaporation in horizontal tubes with coiled wire inserts [J]. International Communications in Heat and Mass Transfer, 2009, 36: 1089-1095.
[10]	Murata K, Hashizume K. Forced convective boiling of nonazeotropic refrigerant mixtures inside tubes [J]. Heat Transfer-JapRes, 1990, 19 (2): 95-109.
[11]	Eckels S J, Pate M B. An experimental comparison of evaporation and condensation heat transfer coefficients for HFC-134a and CFC-12 [J]. Int. J. Refrigeration, 1991, 14 (3): 70-77.
[12]	Oh Se-Yoon, Bergles Arthur E. Experimental study of the effects of the spiral angle on evaporative heat transfer enhancement in micro-fin tubes [J]. ASHRAE Transactions, 1998, 19 (1): 1137-1143.
[13]	Zhang Yifan (张一帆), Li Huixiong (李会雄), Zhang Yuqian (张煜乾). The influence of internally ribbed tube geometry on pipe flow resistance [J]. Journal of Engineering Thermophysics(工程热物理学报), 2011, 32 (7): 1161-1164.
[14]	Zhang Xiaoyan (张小艳), Yuan Xiuling (袁秀玲), Tian Huanzhang (田怀璋). Evaporation heat transfer of R417A flowing inside horizontal smooth and internally grooved tubes [J]. Journal of Xi'an Jiaotong University (西安交通大学学报), 2007, 41 (1): 18-22.
[15]	Cheng Jian (程建), Tao Leren (陶乐仁), Wei Yiping (魏义平). Experimental study on evaporation heat transfer of R410A and R22 in a rifled tube [J]. Fluid Machinery (流体机械), 2013, 41 (3): 54-57.
[16]	Akhavan-Behabadi M A,Ravi Kumar, Jamali M. Investigation on heat transfer and pressure drop during swirl flow boiling of R134a in a horizontal tube [J]. International Journal of Heat and Mass Transfer, 2009, 52:1918-1927.
[17]	Liu Rong (刘荣), Tao Leren (陶乐仁), Gao Libo (高立博). Experimental study on boiling heat transfer of R410A without lubricant oil in the inner-grooved copper tubes [J]. Journal of Refrigeration (制冷学报), 2011, 32 (4): 20-24.
[18]	Kuo C S, Wang C C. In tube evaporation of HCFC-22 in a 9.52mm micro-fin/smooth tube [J]. Int. J. Heat Mass Transfer, 1996, 39 (12): 2559-2569.
[19]	Kimura Hideyuki, Ito Masaaki. Evaporating heat transfer in horizontal internal spiral-grooved tubes in the region of low flow rates [J]. Bulletin of the JSME, 1981, 195 (24): 1602-1607.
[20]	Muzzio A, Niro A, Arosio S. Heat transfer and pressure drop during evaporation and condensation of R22 inside 9.52mm O.D.microfin tubes of different geometries [J]. Enhanced Heat Transfer, 1998, (5): 39-52.
[21]	Kubanek G R, Miletti D L. Evaporative heat transfer and pressure drop performance of internally-finned tubes with refrigerant 22 [J]. J. Heat Transfer, 1979, 101: 447-452.

3种管内强化管沸腾换热性能对比

Boiling heat transfer performance in three internal enhanced tubes

PDF (PC)

可视化

被引次数

摘要/Abstract

引用本文

使用本文

参考文献 21

相关文章 15

编辑推荐

Metrics

本文评价

[1]	张双星, 刘舫辰, 张义飞, 杜文静. R-134a脉动热管相变蓄放热实验研究[J]. 化工学报, 2023, 74(S1): 165-171.
[2]	张义飞, 刘舫辰, 张双星, 杜文静. 超临界二氧化碳用印刷电路板式换热器性能分析[J]. 化工学报, 2023, 74(S1): 183-190.
[3]	陈爱强, 代艳奇, 刘悦, 刘斌, 吴翰铭. 基板温度对HFE7100液滴蒸发过程的影响研究[J]. 化工学报, 2023, 74(S1): 191-197.
[4]	刘明栖, 吴延鹏. 导光管直径和长度对传热影响的模拟分析[J]. 化工学报, 2023, 74(S1): 206-212.
[5]	王志国, 薛孟, 董芋双, 张田震, 秦晓凯, 韩强. 基于裂隙粗糙性表征方法的地热岩体热流耦合数值模拟与分析[J]. 化工学报, 2023, 74(S1): 223-234.
[6]	江河, 袁俊飞, 王林, 邢谷雨. 均流腔结构对微细通道内相变流动特性影响的实验研究[J]. 化工学报, 2023, 74(S1): 235-244.
[7]	杨欣, 王文, 徐凯, 马凡华. 高压氢气加注过程中温度特征仿真分析[J]. 化工学报, 2023, 74(S1): 280-286.
[8]	晁京伟, 许嘉兴, 李廷贤. 基于无管束蒸发换热强化策略的吸附热池的供热性能研究[J]. 化工学报, 2023, 74(S1): 302-310.
[9]	常明慧, 王林, 苑佳佳, 曹艺飞. 盐溶液蓄能型热泵循环特性研究[J]. 化工学报, 2023, 74(S1): 329-337.
[10]	程成, 段钟弟, 孙浩然, 胡海涛, 薛鸿祥. 表面微结构对析晶沉积特性影响的格子Boltzmann模拟[J]. 化工学报, 2023, 74(S1): 74-86.
[11]	张化福, 童莉葛, 张振涛, 杨俊玲, 王立, 张俊浩. 机械蒸汽压缩蒸发技术研究现状与发展趋势[J]. 化工学报, 2023, 74(S1): 8-24.
[12]	宋瑞涛, 王派, 王云鹏, 李敏霞, 党超镔, 陈振国, 童欢, 周佳琦. 二氧化碳直接蒸发冰场排管内流动沸腾换热数值模拟分析[J]. 化工学报, 2023, 74(S1): 96-103.
[13]	李艺彤, 郭航, 陈浩, 叶芳. 催化剂非均匀分布的质子交换膜燃料电池操作条件研究[J]. 化工学报, 2023, 74(9): 3831-3840.
[14]	王玉兵, 李杰, 詹宏波, 朱光亚, 张大林. R134a在菱形离散肋微小通道内的流动沸腾换热实验研究[J]. 化工学报, 2023, 74(9): 3797-3806.
[15]	袁佳琦, 刘政, 黄锐, 张乐福, 贺登辉. 泡状入流条件下旋流泵能量转换特性研究[J]. 化工学报, 2023, 74(9): 3807-3820.