[1]何 阔,鲍泽威,雷志良,等.超临界压力下正癸烷在螺旋管内流动与传热特性的数值模拟[J].常州大学学报(自然科学版),2018,30(05):51-57.[doi:10.3969/j.issn.2095-0411.2018.05.007]
 HE Kuo,BAO Zewei,LEI Zhiliang,et al.Numerical Investigation of the Flow and Heat Transfer of n-Decane in Helical-Coiled Tubes at Supercritical Pressure[J].Journal of Changzhou University(Natural Science Edition),2018,30(05):51-57.[doi:10.3969/j.issn.2095-0411.2018.05.007]
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超临界压力下正癸烷在螺旋管内流动与传热特性的数值模拟()
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常州大学学报(自然科学版)[ISSN:2095-0411/CN:32-1822/N]

卷:
第30卷
期数:
2018年05期
页码:
51-57
栏目:
化学化工
出版日期:
2018-09-28

文章信息/Info

Title:
Numerical Investigation of the Flow and Heat Transfer of n-Decane in Helical-Coiled Tubes at Supercritical Pressure
作者:
何 阔鲍泽威雷志良黄 琴李象远
四川大学 化学工程学院,四川 成都 610065
Author(s):
HE Kuo BAO Zewei LEI Zhiliang HUANG Qin LI Xiangyuan
College of Chemical Engineering, Sichuan University, Chengdu 610065, China
关键词:
螺旋管 导程 数值模拟 正癸烷 传热
Keywords:
helical-coiled tubes helical pitch numerical simulation n-decane heat transfer
分类号:
O 621.3
DOI:
10.3969/j.issn.2095-0411.2018.05.007
文献标志码:
A
摘要:
使用高比热容的航空燃料对航空发动机的冷却空气进行预冷却是改善航空发动机冷却性能的有效方法。采用数值模拟方法研究了超临界压力下正癸烷在不同导程参数的螺旋管内速度场和温度场分布特性,结果表明:螺旋管离心力引起的二次流是使截面速度出现差异的主要原因,流体速度的最大值位于外侧壁面处; 流体温度较高的区域靠近螺旋管内侧壁面处且随着螺旋上升角度的增大而逐渐扩大; 模拟所得的努塞尔数和压降与Petukhov等的经验公式吻合较好,说明该公式同样适用正癸烷在螺旋管内的流动传热计算; 螺旋管导程对管内流体的流动和传热性能影响很小,在螺旋管换热器优化设计中应作为次要优化参数。
Abstract:
It is an effective method to improve the cooling performance of aero-engine by using high thermal capacity aviation fuel to cool the cooling air. Numerical simulation of the helical-coiled tubes with different helical pitch was carried out to analyze the distributions of both velocity and temperature fields. The results show that the secondary flow caused by the centrifugal force of the helical-coil tubes is the main reason for the difference in the distribution of both velocity and temperature. The maximum velocity is found at the outer side while the high temperature zone is found at the inner side. Moreover, the area of the high temperature zone expands gradually with the increase of the helix angel. The simulation results of Nusselt number and pressure drop accord well with those of the empirical formulas presented by Petukhov et al, which shows that these formulas are also applicable to the calculation of the flow and heat transfer of n-decane in the helical-coiled tube. The helical pitch has little influence on the flow performance and heat transfer in helical-coiled tubes, and it should be considered as a secondary factor in optimal design of helical-coiled tubes heat exchanger.

参考文献/References:


[1] 于霄,吕多,李洪莲,等. 空气冷却器在航空发动机上的应用及流动传热试验分析技术研究[J].计测技术,2017,37(3):34-38.
[2]MIN J K,JI H J,MAN Y H,et al.High temperature heat exchanger studies for applications to gas turbines[J].Heat & Mass Transfer,2009,46(2):175.
[3]MISSIRLIS D,DONNERRHACK S,SEITE O,et al.Numerical development of a heat transfer and pressure drop porosity model for a heat exchanger for aero engine applications[J].Applied Thermal Engineering,2010,30(11):1341-1350.
[4]曹兴,孔祥鑫,王凯,等.螺旋管内传热与流动性能的场协同分析[J].化工机械,2018,45(1):96-101,113.
[5]NAPHON P,WONGWISES S.A review of flow and heat transfer characteristics in curved tubes[J].Renewable & Sustainable Energy Reviews,2006,10(5):463-490.
[6]MOAWED M.Experimental study of forced convection from helical coiled tubes with different parameters[J].Energy Conversion & Management,2011,52(2):1150-1156.
[7]DANG G,ZHONG F,ZHANG Y,et al.Numerical study of heat transfer deterioration of turbulent supercritical kerosene flow in heated circular tube[J].International Journal of Heat & Mass Transfer,2015,85:1003-1011.
[8]PIAZZA I D,CIOFALO M.Numerical prediction of turbulent flow and heat transfer in helically coiled pipes[J]. International Journal of Thermal Sciences,2010,49(4):653-663.
[9]FENG Z G,MICHAELIDES E E.Secondary flow within a river bed and contaminant transport[J].Environmental Fluid Mechanics,2009,9(6):617-634.
[10]LOPEZ M,GRAHAM M D.Enhancement of mixing and adsorption in microfluidic device by shear-induced diffusion and topography-induced secondary flow [J].Physics of Fluids,2008,20(5):1-12.
[11]王占卫,张香文,米镇涛,等.超临界状态下正癸烷的催化裂解[J].石油化工,2005,34(6):518-522.
[12]PETUKHOV B S.Heat transfer and friction in turbulent pipe flow with variable physical properties[J].Advances in Heat Transfer,1970,6:503-564.

[13]包旭东,徐国强,闻洁,等.超临界压力正癸烷在竖直圆管内的流动阻力实验[J].航空动力学报,2018,33(3):628-634.

备注/Memo

备注/Memo:
收稿日期:2018-03-20。
作者简介:何阔(1994—),男,四川遂宁人,硕士生。通信联系人:鲍泽威(1985—),E-mail:baozewei@126.com
更新日期/Last Update: 2018-09-28