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收稿日期:
2024-01-14
修回日期:
2024-03-03
出版日期:
2024-04-02
通讯作者:
林梅
作者简介:
谢磊(2000—),男,硕士研究生,1976875090@qq.com
基金资助:
Lei XIE1(), Yongsheng XU2, Mei LIN1()
Received:
2024-01-14
Revised:
2024-03-03
Online:
2024-04-02
Contact:
Mei LIN
摘要:
基于任意拉格朗日-欧拉(ALE)方法,利用动网格技术和重叠网格技术数值模拟研究了不同的Reynolds数、截面形状以及长径比下的肋柱-软尾结构在通道中的双向流固耦合换热问题。模拟工况为:Reynolds数Re = 200; 275; 351;肋柱截面形状: 圆形和方形;长径比k = 2; 3; 4。研究表明:(1)在Re = 275时,圆形截面肋柱-软尾结构的流动换热综合能力优于方形截面的结构;在k = 3时,圆形截面肋柱-软尾结构的流动换热综合能力最佳;而肋柱周围的局部换热能力方形截面的结构要好于圆形截面的结构;(2)在k = 3时,随着Reynolds数的增大,不同截面形状的肋柱-软尾结构的流动换热综合能力逐渐升高。并且,高Reynolds数、高长径比的圆形截面综合流动换热能力最佳;(3)与不加软尾肋柱结构的流动换热能力进行对比发现,对于圆形截面形状的肋柱结构,增加软尾后综合换热能力增大了19.46%。
中图分类号:
谢磊, 徐永生, 林梅. 不同截面肋柱-软尾结构单相流动传热比较研究[J]. 化工学报, DOI: 10.11949/0438-1157.20240068.
Lei XIE, Yongsheng XU, Mei LIN. Comparative study on single-phase flow and heat transfer of different cross-section rib-soft tail structures[J]. CIESC Journal, DOI: 10.11949/0438-1157.20240068.
振幅A/mm | 周期T/s | 频率f/Hz | |
---|---|---|---|
文献[ | 12.475 | 0.320 | 3.13 |
文献[ | 9.843 | 0.319 | 3.14 |
本文 | 10.361 | 0.314 | 3.18 |
表 1 软尾自由端的振幅、周期和频率
Table 1 Amplitude, period and frequency of the free end of the soft tail
振幅A/mm | 周期T/s | 频率f/Hz | |
---|---|---|---|
文献[ | 12.475 | 0.320 | 3.13 |
文献[ | 9.843 | 0.319 | 3.14 |
本文 | 10.361 | 0.314 | 3.18 |
图 4 不同截面形状、不同长径比对温度场、涡量场和速度场的影响(Re=275)
Fig.4 Effect of different cross-sectional shapes and length-to-diameter ratios on temperature, vorticity and velocity fields(Re = 275)
图 8 两种截面流动和传热特性比较:(a)进出口压降的变化;(b)传热系数的变化
Fig.8 Comparison of flow heat transfer performances for two cross-sectional channels: (a) Pressure drop between inlet and outlet and (b)Heat transfer coefficient
图 11 不同Reynolds数,不同截面形状肋柱的温度场、涡量场和速度场的变化 (k = 3)
Fig.11 Variation of temperature, vorticity and velocity fields for different Reynolds numbers and cross-section shapes (k = 3)
图 13 不同Reynolds数下方柱的温度场、涡量场和速度场变化(k = 2)
Fig.13 Variation of temperature, vorticity and velocity fields of square rib at different Reynolds numbers (k = 2)
图 14 肋柱通道流动传热特性随Reynolds数的变化:(a)进出口压降ΔP的变化;(b)平均传热系数的变化
Fig.14 Variation of flow and heat transfer performance for rib channels with Reynolds numbers: (a) Pressure drop between inlet and outlet; (b) Average heat transfer coefficient
肋柱截面形状 | 方形 | 圆形 | ||
---|---|---|---|---|
长径比 | k = 0 | k = 4 | k = 0 | k = 4 |
Nuxt | 7.867 | 7.271 | 11.797 | 8.398 |
fd | 0.177 | 0.164 | 0.207 | 0.123 |
J | 44.337 | 44.208 | 56.975 | 68.064 |
表 2 长径比k = 0和4的流动换热参数对比
Table 2 Comparison of flow and heat transfer parameters for length-to-diameter ratio k = 0 and 4
肋柱截面形状 | 方形 | 圆形 | ||
---|---|---|---|---|
长径比 | k = 0 | k = 4 | k = 0 | k = 4 |
Nuxt | 7.867 | 7.271 | 11.797 | 8.398 |
fd | 0.177 | 0.164 | 0.207 | 0.123 |
J | 44.337 | 44.208 | 56.975 | 68.064 |
图 16 方柱结构在一个摆动周期内,不同时刻温度、涡量、速度和压力云图变化情况(Re = 351, k = 4)
Fig.16 Variation of temperature, vorticity, velocity and pressure contours of the square rib at different moments during an oscillation period (Re = 351, k = 4)
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