燃-滑油换热器壳侧换热特性研究

推进技术 ›› 2016, Vol. 37 ›› Issue (5): 900-906.

燃-滑油换热器壳侧换热特性研究

王冬兰¹,朱卫兵²,平登科²,张小彬²

北京动力机械研究所，北京 100074,哈尔滨工程大学航天与建筑工程学院，黑龙江哈尔滨 150001,哈尔滨工程大学航天与建筑工程学院，黑龙江哈尔滨 150001,哈尔滨工程大学航天与建筑工程学院，黑龙江哈尔滨 150001

发布日期:2021-08-15
作者简介:王冬兰，女，学士，高级工程师，研究领域为航空发动机滑油系统。E-mail: kuding666@sohu.com 通讯作者:朱卫兵，男，博士，教授，研究领域为燃烧、传热与多相流体动力学。

A Study of Heat Transfer Characteristics on Shell-Side of

Beijing Power Machinery Institute，Beijing 100074，China,College of Aerospace and Civil Engineering，Harbin Engineering University，Harbin 150001，China,College of Aerospace and Civil Engineering，Harbin Engineering University，Harbin 150001，China and College of Aerospace and Civil Engineering，Harbin Engineering University，Harbin 150001，China

Published:2021-08-15

摘要/Abstract

摘要： 针对航空发动机滑油系统所使用的小管径燃-滑油换热器，开展了壳侧换热特性实验研究。研究表明:当壳侧为滑油单相流时，壳侧对流换热系数可以采用Kern经验公式计算；在换热器可能的工作范围内，壳侧气液两相流流型为泡状流；保持液相折算速度(或气相折算速度)不变，两相对流换热系数随气相折算速度(或液相折算速度)的增大而增大，相同液相速度时，两相对流换热系数要大于单相，最大可达2.3倍；最后根据泡状流特点，基于L-M模型给出了壳侧两相换热系数计算公式，计算平均相对误差为3.6%，可满足工程需要。

关键词: 航空发动机；动压式油气分离器；含气率；分离性能

Abstract: An experimental research of heat transfer characteristics on shell-side is carried out for the small diameter fuel-oil heat exchanger used in aviation engine oil system. Research shows that convective heat transfer coefficient on shell-side can be calculated using Kern empirical formula when the shell-side has single-phase oil. In the working range of heat exchanger，gas-liquid two-phase flow on shell-side is bubbly flow. Convective heat transfer coefficient of two-phase flow increases with the increase of gas superficial velocity (or liquid superficial velocity) when liquid superficial velocity (or gas superficial velocity) are held constant. Convective heat transfer coefficient of the two-phase flow is greater than that of the single-phase flow in the same liquid phase velocity，and the maximum is up to 2.3 times. At last，according to the characteristics of bubbly flow，a calculation formula of the two-phase convective heat transfer coefficient on shell-side is provided based on L-M model. The average relative error is about 3.6%，which can satisfy the engineering demand.

Key words: Heat transfer coefficient；Bubbly flow；Gas-liquid two-phase flow；Fuel-oil heat exchanger

王冬兰,朱卫兵,平登科,张小彬. 燃-滑油换热器壳侧换热特性研究[J]. 推进技术, 2016, 37(5): 900-906.

WANG Dong-lan¹,ZHU Wei-bing²,PING Deng-ke²,ZHANG Xiao-bin². A Study of Heat Transfer Characteristics on Shell-Side of[J]. Journal of Propulsion Technology, 2016, 37(5): 900-906.

参考文献

[1] 刘波, 周强, 程礼. 构建航空发动机滑油系统稳态模型[J]. 推进技术, 2005, 26(6): 556-559. (LIU Bo, ZHOU Qiang, CHENG Li. Construction of Steady Model for an Engine Oil System[J]. Journal of Propulsion Technology, 2005, 26(6): 556-559.)
[2] 黎林林, 谢光华. 某型号涡喷发动机滑油系统设计[J]. 推进技术, 2001, 22(6): 493-495. (LI Lin-lin, XIE Guang-hua. Oil System Design of a Certain Turbo-Jet Engine[J].Journal of Propulsion Technology, 2001, 22(6): 493-495.)
[3] Lockhart R W, Martinelli R C. Proposed Correlation of Data for Isothermal Two-Phase, Two-Component Flow in Pipes[J]. Chemical Engineering Progress, 1949, 45(1): 39-48.
[4] Hemamalini R R, Partheeban P, Chandrababu J S, et al. The Effect on Pressure Drop across Horizontal Pipe and Control Valve for Air/Palm Oil Two-Phase Flow[J]. International Journal of Heat and Mass Transfer, 2005, 48(14): 2911-2921.
[5] Vijayarangan B R, Jayanti S, Balakrishnan A R. Pressure Drop Studies on Two-Phase Flow in Uniformly Heated Vertical Tube at Pressure up to the Critical Point[J]. International Journal of Heat and Mass Transfer, 2007, 50, 1879-1891.
[6] 杨小琼, 王启杰, 王伟. TEMA-F 型换热器壳侧油-气混合物两相流流动特性[J]. 化工学报, 1994, 6.
[7] 杨小琼, 王启杰. TEMA—F 型换热器壳侧单相压降的预测模型及其测量[J]. 化工学报, 1996, 47(3): 332-339.
[8] 黄兴华, 王启杰. 不互溶双组分气液两相混合物在 TEMA—F 型换热器壳侧的传热[J]. 化工学报, 1999, 50(1): 80-87.
[9] 黄兴华, 王启杰. 管壳式换热器壳程流动和传热的三维数值模拟[J]. 化工学报, 2000, 51(3): 297-302.
[10] 徐斌, 王启杰, 罗来勤. 管壳式换热器壳侧气液两相流路分析法的研究[J]. 热科学与技术, 2003, 2(2): 129-135.
[11] Vlasogiannis P, Karagiannis G, Argyropoulos P, et al. Air-Water Two-Phase Flow and Heat Transfer in a Plate Heat Exchanger[J]. International Journal of Multiphase Flow, 2002, 28(5): 757-772.
[12] Ramachandran S, Kalaichelvi P, Sundaram S. Experimental Heat Transfer Correlations for a Liquid-Liquid Two-Phase System in a Compact Heat Exchanger[J]. Indian Journal of Chemical Technology, 2006, 1: 14-19.
[13] Ramachandran S, Kalaichelvi P, Sundaram S. Heat Transfer Studies in a Spiral Plate Heat Exchanger for Water-Palm Oil Two-Phase System[J]. Brazilian Journal of Chemical Engineering, 2008, 25, 483-490.
[14] Alagesan V, Sundaram S. Two-Phase Experimental Heat Transfer Studies on a Water-Diesel System in a Shell and Tube Heat Exchanger[J]. Brazilian Journal of Chemical Engineering, 2012, 29(2): 275-283.
[15] Kandlikar S G. Fundamental Issues Related to Flow Boiling in Minichannels and Microchannels[J]. Experimental Thermal and Fluid Science, 2002, 26(2): 389-407.
[16] 杨小琼, 王启杰. 流体物性对壳侧不互溶双组分两相流动特性的影响[J]. 化工学报, 1994, (3): 313-320.
[17] 陈听宽. 两相流与传热研究[M]. 西安:西安交通大学出版社, 2004.
[18] 蔡继勇, 陈听宽, 罗毓珊. 垂直上升管内油水乳状液流动特性的研究[J]. 石油学报, 1998, 19(4): 94-98. 　　　　　　　　　　　　　*　收稿日期:2014-08-12；修订日期:2015-02-03。作者简介:王冬兰,女,学士,高级工程师,研究领域为航空发动机滑油系统。E-mail: kuding666@sohu.com通讯作者:朱卫兵,男,博士,教授,研究领域为燃烧、传热与多相流体动力学。E-mail: zhuweibing@hrbeu.edu.cn(编辑:史亚红)