超临界压力下航空煤油传热恶化的分析与预测

doi:10.11949/j.issn.0438-1157.20180250

化工学报 ›› 2018, Vol. 69 ›› Issue (12): 5056-5064.DOI: 10.11949/j.issn.0438-1157.20180250

超临界压力下航空煤油传热恶化的分析与预测

王彦红¹, 李素芬², 赵星海¹

1. 东北电力大学能源与动力工程学院, 吉林省吉林市 132012;
2. 大连理工大学能源与动力学院, 辽宁大连 116024

收稿日期:2018-03-12 修回日期:2018-09-13 出版日期:2018-12-05 发布日期:2018-12-05
通讯作者: 王彦红
基金资助:
国家自然科学基金项目（51576027）；东北电力大学博士科研启动基金项目（BSJXM-2017205）。

Analysis and prediction of heat transfer deterioration of aviation kerosene under supercritical pressures

WANG Yanhong¹, LI Sufen², ZHAO Xinghai¹

1. School of Energy and Power Engineering, Northeast Electric Power University, Jilin 132012, Jilin, China;
2. School of Energy and Power Engineering, Dalian University of Technology, Dalian 116024, Liaoning, China

Received:2018-03-12 Revised:2018-09-13 Online:2018-12-05 Published:2018-12-05
Supported by:
supported by the National Natural Science Foundation of China(51576027) and the Scientific Research Foundation for Doctors of Northeast Electric Power University(BSJXM-2017205).

摘要/Abstract

摘要：

对竖直上升圆管内超临界压力航空煤油的传热恶化进行了实验研究。考察了浮升力和热加速对换热的影响机制，通过判别准则的适用性分析，选取能较好描述传热恶化的因子组，修正得到了合理的临界值，从而获得了适用于航空煤油的判别准则。基于可控参数建立了传热恶化临界热通量预测公式。阐述了传热恶化引发热声流动不稳定的过程。通过浮升力因子和热加速因子修正建立了换热关联式。结果表明：浮升力因子Bu和热加速因子Ac分别高于1.57×10^-5和4.92×10^-6时，两者将削弱边界层内剪切力，引发传热恶化现象。拟沸腾也是传热恶化和热声流动不稳定的诱因。

关键词: 超临界压力, 航空煤油, 对流, 传热恶化, 预测

Abstract:

Experimental study on heat transfer deterioration of aviation kerosene in a vertical upward circular tube at supercritical pressures was conducted. The influence mechanisms of buoyancy and thermal acceleration on heat transfer were investigated. Based on the applicability analysis of determination criteria, the factors team which can better reflect the heat transfer deterioration were selected, and the reasonable critical values were obtained, thus the determination criteria for aviation kerosene was proposed. The prediction formula of critical heat flux of heat transfer deterioration was established based on the controllable parameters. The process of thermo-acoustic flow instability owing to heat transfer deterioration was analyzed. The heat transfer correlation was developed by the amendments of buoyancy and thermal acceleration factors. Results indicate that when the buoyancy factor Bu and the thermal acceleration factor Ac are higher than 1.57×10^-5 and 4.92×10^-6, respectively, the heat transfer deterioration appears due to the weakened shearing stress in the boundary layer. The quasi-boiling is also the reason for heat transfer deterioration and thermo-acoustic flow instability.

Key words: supercritical pressure, aviation kerosene, convection, heat transfer deterioration, prediction

中图分类号:

V231.1

王彦红, 李素芬, 赵星海. 超临界压力下航空煤油传热恶化的分析与预测[J]. 化工学报, 2018, 69(12): 5056-5064.

WANG Yanhong, LI Sufen, ZHAO Xinghai. Analysis and prediction of heat transfer deterioration of aviation kerosene under supercritical pressures[J]. CIESC Journal, 2018, 69(12): 5056-5064.

参考文献 30

[1]	ZHANG C B, XU G Q, DENG H W, et al. Investigation of flow resistance characteristics of endothermic hydrocarbon fuel under supercritical pressures[J]. Propulsion and Power Research, 2013, 2(2):119-130.
[2]	ZHU K, XU G Q, TAO Z, et al. Flow frictional resistance characteristics of kerosene RP-3 in horizontal circular tube at supercritical pressure[J]. Experimental Thermal and Fluid Science, 2013, 44(1):245-252.
[3]	ZHONG F Q, FAN X J, YU G, et al. Heat transfer of aviation kerosene at supercritical conditions[J]. Journal of Thermophysics and Heat Transfer, 2009, 23(3):543-550.
[4]	HUANG D, RUAN B, WU X Y, et al. Experimental study on heat transfer of aviation kerosene in a upward tube at supercritical pressure[J]. Chinese Journal of Chemical Engineering, 2015, 23(2):425-434.
[5]	WANG H, ZHOU J, PAN Y, et al. Experimental investigation on the onset of thermo-acoustic instability of supercritical hydrocarbon fuel flowing a small-scale channel[J]. Acta Astronautica, 2015, 117:296-304.
[6]	罗毓珊, 陈听宽, 胡志宏, 等. 高参数小管径内煤油的传热特性研究[J]. 工程热物理学报, 2005, 26(4):609-612. LUO Y S, CHEN T K, HU Z H, et al. Investigation on heat transfer characteristics for kerosene under high parameter and in small diameter tube[J]. Journal of Engineering Thermophysics, 2005, 26(4):609-612.
[7]	胡志宏, 陈听宽, 罗毓珊, 等. 高热通量下超临界压力煤油流过小直径管的传热特性[J]. 化工学报, 2002, 53(2):134-138. HU Z H, CHEN T K, LUO Y S, et al. Heat transfer to kerosene at supercritical pressure in small-diameter tube with large heat flux[J]. Journal of Chemical Industry and Engineering(China), 2002, 53(2):134-138.
[8]	李中洲, 朱惠人. 超临界压力下航空煤油传热特性[J]. 推进技术, 2011, 32(2):261-265. LI Z Z, ZHU H R. Heat transfer characteristics of kerosene in micro-channel under supercritical pressure[J]. Journal of Propulsion Technology, 2011, 32(2):261-265.
[9]	YANG Z Q, BI Q C, LIU Z H, et al. Heat transfer to supercritical pressure hydrocarbons flowing in a horizontal short tube[J]. Experimental Thermal and Fluid Science, 2015, 61:144-152.
[10]	ZHANG C B, XU G Q, GAO L, et al. Experimental investigation on heat transfer of a specific fuel(RP-3) flows through downward tubes at supercritical pressure[J]. Journal of Supercritical Fluids, 2012, 72(9):90-99.
[11]	DENG H W, ZHU K, XU G Q, et al. Heat transfer characteristics of RP-3 kerosene at supercritical pressure in a vertical circular tube[J]. Journal of Enhanced Heat Transfer, 2012, 19(5):409-421.
[12]	王夕, 刘波, 祝银海, 等. 超临界压力下RP-3在细圆管内对流换热实验研究[J]. 工程热物理学报, 2015, 36(2):360-365. WANG X, LIU B, ZHU Y H, et al. Experimental investigation on convection heat transfer of supercritical pressure RP-3 in a small pipe[J]. Journal of Engineering Thermophysics, 2015, 36(2):360-365.
[13]	BRAD H, MICHAEL K. Experimental investigation of heat transfer and flow instabilities in supercritical fuels[R]. AIAA 1997-3043.
[14]	LIU Z H, BI Q C, GUO Y, et al. Convective heat transfer and pressure drop characteristics of near-critical-pressure hydrocarbon fuel in a minichannel[J]. Applied Thermal Engineering, 2013, 51(1/2):1047-1054.
[15]	赵国柱, 宋文艳, 张若凌, 等. 超临界压力下正十烷流动传热的数值模拟[J]. 推进技术, 2014, 35(4):537-543. ZHAO G Z, SONG W Y, ZHANG R L, et al. Numerical simulation on flow and heat transfer of n-decane under supercritical pressure[J]. Journal of Propulsion Technology, 2014, 35(4):537-543.
[16]	DANG G X, ZHONG F Q, CHEN L H, et al. Numerical investigation on flow and convective heat transfer of aviation kerosene at supercritical conditions[J]. Science China Technological Sciences, 2013, 56(2):416-422.
[17]	DANG G X, ZHONG F Q, ZHANG Y J, et al. Numerical study of heat transfer deterioration of turbulent supercritical kerosene flow in heated circular tube[J]. International Journal of Heat and Mass Transfer, 2015, 85:1003-1011.
[18]	WANG Y H, LI S F, DONG M. Numerical study on heat transfer deterioration of supercritical n-decane in horizontal circular tubes[J]. Energies, 2014, 7(11):7535-7554.
[19]	LI X F, HUAI X L, CAI J, et al. Convective heat transfer characteristics of China RP-3 aviation kerosene at supercritical pressure[J]. Applied Thermal Engineering, 2011, 31(14/15):2360-2366.
[20]	ZHANG C B, TAO Z, XU G Q, et al. Heat transfer investigation of the sub-and supercritical fuel flow though a U-turn tube[C]//Turbine-09 International Symposium on Heat Transfer in Gas Turbine System. 2009:1-13.
[21]	王彦红. 超临界压力航空煤油热声振荡与传热恶化的机理及预测研究[D]. 大连:大连理工大学, 2016. WANG Y H. Studies on mechanism and prediction of thermoacoustic oscillation and heat transfer deterioration of aviation kerosene in at supercritical pressures[D]. Dalian:Dalian University of Technology, 2016.
[22]	JIANG P X, LIU B, ZHAO C R, et al. Convection heat transfer of supercritical pressure carbon dioxide in a vertical micro tube from transition to turbulent flow regime[J].International Journal of Heat and Mass Transfer, 2013, 56(1/2):741-749.
[23]	LIU S H, HUANG Y P, LIU G X, et al. Improvement of buoyancy and acceleration parameters for forced and mixed convective heat transfer to supercritical fluids flowing in vertical tubes[J]. International Journal of Heat Mass and Transfer, 2017, 106:1144-1156.
[24]	YAMAGATA K, NISHIKAWA K, HASEGAWA S, et al. Forced convective heat transfer to supercritical water flowing in tubes[J]. International Journal of Heat Mass Transfer, 1972, 15(12):2575-2593.
[25]	KIM J K, JEON H K, LEE J S. Wall temperature measurement and heat transfer correlation of turbulent supercritical carbon dioxide flow in vertical circular/non-circular tubes[J]. Nuclear Engineering and Design, 2007, 237(15/16/17):1795-1802.
[26]	URBANO A, NASUTI F. Onset of heat transfer deterioration in supercritical methane flow channels[J]. Journal of Thermophysics and Heat Transfer, 2013, 27(2):298-308.
[27]	ZHOU W X, BAO W, QIN J. Deterioration in heat transfer of endothermal hydrocarbon fuel[J]. Journal of Thermal Science, 2011, 20(2):173-180.
[28]	张春本, 邓宏武, 徐国强, 等. 超临界压力下航空煤油RP-3焓值的测量及换热研究[J].航空动力学报, 2010, 25(2):331-335. ZHANG C B, DENG H W, XU G Q, et al. Enthalpy measurement and heat transfer investigation of RP-3 kerosene at supercritical pressure[J]. Journal of Aerospace Power, 2010, 25(2):331-335.
[29]	胡江玉, 周进, 潘余, 等. 超临界压力煤油传热不稳定实验研究[J]. 气体物理, 2017, 2(1):57-63. HU J Y, ZHOU J, PAN Y, et al. Experimental investigation on heat transfer instability of kerosene at supercritical pressure[J]. Physics of Gases, 2017, 2(1):57-63.
[30]	YAN J J, ZHU Y H, ZHAO R, et al. Experimental investigation of the flow and heat transfer instabilities in n-decane at supercritical pressures in a vertical tube[J]. International Journal of Heat and Mass Transfer, 2018, 120:987-996.

超临界压力下航空煤油传热恶化的分析与预测

Analysis and prediction of heat transfer deterioration of aviation kerosene under supercritical pressures

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