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3D numerical study on shell side heat transfer and flow characteristics of rod-baffle heat exchangers with spirally corrugated tubes

机译:带螺旋波纹管的棒形折流板换热器壳侧传热和流动特性的3D数值研究

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This article presents a numerical simulation of the shell side flow in rod-baffle heat exchangers with spirally corrugated tubes (RBHXsSCT). Results are compared with those in rod-baffle heat exchanger with plain tubes (RBHX). Simulation is conducted to improve the thermo-hydraulic performance in longitudinal flow heat exchangers and to obtain an understanding of the physical behavior of thermal and fluid flow in the RBHXsSCT with Reynolds number ranging from 6000 to 18,000. Simulation results show that the Nusselt number in RBHXSCT with one-start spirally corrugated tubes can be 1.2 times that in RBHX when the Reynolds number is 18,000. The heat transfer quantities in the RBHXsSCT with one-start, two-start, three-start, and four-start spirally corrugated tubes are 104.6%, 105.4%, 106.7%, and 109.6%, respectively, higher than that in RBHX. The pressure drop in RBHX is 1.21, 1.16, 1.12, and 1.08 times that in RBHXsSCT with one-start, two-start, three-start, and four-start spirally corrugated tubes, respectively. The RBHXSCT with one-start spirally corrugated tubes can achieve an efficiency evaluate coefficient of 1.35. Physical quantity synergy analysis is performed to investigate heat transfer and flow resistance performance. Results verify the synergy regulation among the physical quantities of fluid particle in the flow field of the convective. (C) 2014 Elsevier Masson SAS. All rights reserved.
机译:本文介绍了带有螺旋波纹管(RBHXsSCT)的杆式折流板换热器中壳侧流的数值模拟。将结果与带有普通管的杆式折流板热交换器(RBHX)的结果进行了比较。进行仿真以改善纵向流动热交换器中的热工液压性能,并获得对雷诺数范围为6000至18,000的RBHXsSCT中热和流体流动的物理行为的理解。仿真结果表明,当雷诺数为18,000时,带有一头螺旋波纹管的RBHXSCT中的Nusselt数可以是RBHX中的1.2倍。具有一启动,二启动,三启动和四启动螺旋波纹管的RBHXsSCT中的传热量分别比RBHX高104.6%,105.4%,106.7%和109.6%。 RBHX的压降分别是带有一启动,二启动,三启动和四启动螺旋波纹管的RBHXsSCT的1.21、1、16、1.12和1.08倍。带有单头螺旋波纹管的RBHXSCT的效率评估系数为1.35。进行物理量协同分析以研究热传递和流阻性能。结果验证了对流流场中流体颗粒物理量之间的协同调节。 (C)2014 Elsevier Masson SAS。版权所有。

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