高热通量水平管外池沸腾传热

doi:10.11949/j.issn.0438-1157.20160706

化工学报 ›› 2016, Vol. 67 ›› Issue (S1): 28-32.DOI: 10.11949/j.issn.0438-1157.20160706

高热通量水平管外池沸腾传热

冀文涛¹, 张定才², 赵创要¹, 何雅玲¹, 陶文铨¹

1 西安交通大学能源与动力工程学院, 热流科学与工程教育部重点实验室, 陕西西安 710049;
2 中原工学院能源与环境学院, 河南郑州 450007

收稿日期:2016-05-24 修回日期:2016-06-01 出版日期:2016-08-31 发布日期:2016-08-31
通讯作者: 冀文涛,wentaoji@xjtu.edu.cn
基金资助:
国家自然科学基金项目（51306140）；高等学校博士学科点专项科研基金项目（20130201120057）。

Pool boiling heat transfer outside horizontal tubes at higher heat flux

JI Wentao¹, ZHANG Dingcai², ZHAO Chuangyao¹, HE Yaling¹, TAO Wenquan¹

1 Key Laboratory of Thermo-Fluid Science and Engineering, Ministry of Education, School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an 710049, Shaanxi, China;
2 School of Energy & Environment, Zhongyuan University of Technology, Zhengzhou 450007, Henan, China

Received:2016-05-24 Revised:2016-06-01 Online:2016-08-31 Published:2016-08-31
Supported by:
supported by the National Natural Science Foundation of China (51306140) and the Research Fund for the Doctoral Program of Higher Education of China (20130201120057).

摘要/Abstract

摘要：

在制冷空调的满液式蒸发器中，制冷剂在壳侧沸腾蒸发，管内为水的单相对流传热。实验研究了高热通量下R134a在一根光管和一根强化管（No.1）外的池沸腾传热，并将光管实验结果和Cooper公式进行了比较。在不同的饱和温度下，热通量10～250 kW·m^-2的范围内，研究了R134a在光管和强化管外的沸腾传热系数随热通量的变化关系。光管和强化管外径分别为15.93 mm 和 25.36 mm。通过研究发现，在热通量10～250 kW·m^-2的范围内，光管的池沸腾传热系数和Cooper公式符合较好，偏差小于±15%。在双对数坐标下传热系数和热通量实验结果拟合直线斜率为0.67。在较高热通量，即热通量大于250 kW·m^-2时，光管的传热系数相对Cooper公式偏差开始增大。对于高效管，在小于40 kW·m^-2热通量下的传热效果最好。强化管的强化倍率随热通量增加一直减小，在较高热通量250 kW·m^-2下，强化管的传热系数和光管相同，甚至比光管小。

关键词: 池沸腾, 热通量, 饱和温度, 传热系数, 强化管

Abstract:

For the flooded evaporator in refrigeration or air conditioning systems, refrigerant is boiling on the shell side and water is flowing in the tube side. The pool boiling heat transfer coefficient of R134a outside one smooth tube and one reentrant cavity enhanced tube No.1 is investigated with an experimental approach. At the saturate temperature of 6, 10 and 16℃, the heat flux of 10-250 kW·m^-2, the heat transfer coefficient versus heat flux of smooth tube is investigated and compared with Cooper correlation. The external diameter of smooth tube and enhanced tube are 15.93 mm and 25.36 mm, respectively. At the heat flux of 10-250 kW·m^-2, it is found that the deviation of experimental result and Cooper correlation is within ±15%. the average value of m in h∝q^m, is 0.67. For the enhanced tube, the enhanced ratio is the largest at the heat flux less than 40 kW·m^-2. The enhanced ratio is decreasing as the increment of heat flux. At the heat flux larger than 250 kW·m^-2, the heat transfer coefficient of enhanced tube is approaching the smooth tube, and even smaller than smooth tube.

Key words: pool boiling, heat flux, saturate temperature, heat transfer coefficient, enhanced tube

中图分类号:

TK124

冀文涛, 张定才, 赵创要, 何雅玲, 陶文铨. 高热通量水平管外池沸腾传热[J]. 化工学报, 2016, 67(S1): 28-32.

JI Wentao, ZHANG Dingcai, ZHAO Chuangyao, HE Yaling, TAO Wenquan. Pool boiling heat transfer outside horizontal tubes at higher heat flux[J]. CIESC Journal, 2016, 67(S1): 28-32.

参考文献 20

[1]	JI W T, NUMATA M, HE Y L, et al. Nucleate pool boiling and filmwise condensation heat transfer of R134a on the same horizontal tubes[J]. International Journal of Heat and Mass Transfer, 2015, 86:744-754.
[2]	JI W T, ZHAO C Y, HE Y L, et al. Experimental validation of Cooper correlation at higher heat flux[J]. International Journal of Heat and Mass Transfer, 2015, 90:1241-1243.
[3]	ZHAO C Y, JI W T, JIN P H, et al. Heat transfer correlation of the falling film evaporation on a single horizontal smooth tube[J]. Applied Thermal Engineering, 2016, 103:177-186.
[4]	WEBB R L. Odyssey of the enhanced boiling surface[J]. Journal of Heat Transfer, 2004, 126(6):1051-1059.
[5]	WEBB R L, KIM N H. Principle of Enhanced Heat Transfer[M]. Boca Raton:Taylor & Francis, 2005.
[6]	VAN ROOYEN E, THOME J. Pool boiling data and prediction method for enhanced boiling tubes with R-134a, R-236fa and R-1234ze (E)[J]. International Journal of Refrigeration, 2013, 36(2):447-455.
[7]	JI W T, ZHANG D C, HE Y L, et al. Prediction of fully developed turbulent heat transfer of internal helically ribbed tubes-an extension of Gnielinski equation[J]. International Journal of Heat and Mass Transfer, 2011, 55(4):1375-1384.
[8]	MANGLIK R M. Current progress and new developments in enhanced heat and mass transfer[J]. Journal of Enhanced Heat Transfer, 2013, 20(1):1-15.
[9]	JI W T, JACOBI A M, HE Y L, et al. Summary and evaluation on single-phase heat transfer enhancement techniques of liquid laminar and turbulent pipe flow[J]. International Journal of Heat and Mass Transfer, 2015, 88:735-754.
[10]	冀文涛, 张定才, 冯楠, 等. 水平管外含油及纯R134a池沸腾换热特性比较[J]. 工程热物理学报, 2008, 29(7):1195-1198.JI W T, ZHANG D C, FENG N, et al. Pool boiling heat transfer comparison of pure R134a and R134a with oil additive outside horizontal tubes[J]. Journal of Engineering Thermophysics, 2008, 29(7):1195-1198.
[11]	冀文涛, 冯楠, 张定才, 等. 润滑油对水平管外R134a池沸腾换热的影响[J]. 工程热物理学报, 2009, 30(5):821-823.JI W T, FENG N, ZHANG D C, et al. Influence of oil additive on pool boiling heat transfer of R134a outside horizontal tubes[J]. Journal of Engineering Thermophysics, 2009, 30(5):821-823.
[12]	冀文涛, 屈治国, 郭剑飞, 等. 水平管外开孔铜泡沫R134a池沸腾换热实验研究[J]. 工程热物理学报, 2010, 31(7):1185-1188.JI W T, QU Z G, GUO J F, et al. Pool boiling heat transfer of R134a outside horizontal open-cell copper foam tubes[J]. Journal of Engineering Thermophysics, 2010, 31(7):1185-1188.
[13]	郭剑飞, 李增耀, 屈治国, 等. 水平金属泡沫管外R134a凝结传热实验研究[J]. 工程热物理学报, 2011, 32(5):839-842.GUO J F, LI Z Y, QU Z G, et al. An experimental study of condensation heat transfer characteristics outside the horizontal metal foam tubes[J]. Journal of Engineering Thermophysics, 2011, 32(5):839-842.
[14]	WANG C C, HAFNER A, KUO C S, et al. Influence of lubricant on the nucleate boiling heat transfer performance of refrigerant-a review[J]. Heat Transfer Engineering, 2014, 35(6/7/8):651-663.
[15]	LEE Y, KANG D G, KIM J H, et al. Nucleate boiling heat transfer coefficients of HFO1234yf on various enhanced surfaces[J]. International Journal of Refrigeration, 2014, 38:198-205.
[16]	JI W T, ZHAO C Y, ZHANG D C, et al. Effect of vapor flow on the falling film evaporation of R134a outside a horizontal tube bundle[J]. International Journal of Heat and Mass Transfer, 2016, 92:1171-1181.
[17]	JI W T, ZHANG D C, FENG N, et al. Nucleate pool boiling heat transfer of R134a and R134a-PVE lubricant mixtures on smooth and five enhanced tubes[J]. Journal of Heat Transfer, 2010, 132(11):11502.
[18]	JI W T, QU Z G, LI Z Y, et al. Pool boiling heat transfer of R134a on single horizontal tube surfaces sintered with open-celled copper foam[J]. International Journal of Thermal Sciences, 2011, 50(11):2248-2255.
[19]	GNIELINSKI V. New equations for heat and mass transfer in turbulent pipe and channel flows[J]. Int. Chem. Eng., 1976, 16:359-368.
[20]	COOPER M G. Saturation nucleate pool boiling-a simple correlation[J]. International Chemical Engineering Sym-posium Series, 1984, 86:785-792.

高热通量水平管外池沸腾传热

Pool boiling heat transfer outside horizontal tubes at higher heat flux

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