An assessment of performance of bifurcations in thermal systems with new correlations for estimating Nusselt number and loss coefficient

IF 6.2 2区 工程技术 Q1 MECHANICS
Sarangrab Roy Chowdhury, Kaustav Pradhan
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引用次数: 0

Abstract

Branching networks are continuously being contemplated for use in compact heat transfer systems. They are constructed by connecting straight tubes through bifurcations. The present study investigates the thermo-hydraulic performance of three different bifurcation geometries, viz. symmetric Y-bifurcation, T-bifurcation and asymmetric Y-bifurcation. The velocity and temperature contours show a complementary nature wherein low velocity regions correspond to high temperatures and vice-versa. New quantitative parameters viz. relative secondary strength (Es/t), velocity non-uniformity (δv), temperature non-uniformity (δt) and the performance index (ξ) are introduced to understand the effects of the geometry on the flow field and thermal performance. The T-bifurcation shows the best heat transfer performance, but also the worst hydraulic performance. On the other hand, the asymmetric Y-bifurcation shows the worst heat transfer performance, but the best hydraulic performance. Based on the values of the performance index, it is concluded that the performance of the asymmetric Y-bifurcation is better than that of the symmetric Y-bifurcation, which in turn performs better than the T-bifurcation. However, the non-uniform flow distribution in the asymmetric geometry may lead to issues when such bifurcations are connected in series and parallel to form a distribution network. A comparison of the pressure loss obtained by the CFD simulations with theoretical estimations shows the utility of the comprehensive numerical framework. New correlations are also proposed to determine the Nusselt number and loss coefficient as functions of the bifurcation angle and Reynolds number.
热系统分岔性能的评估与估计努塞尔数和损失系数的新相关性
分支网络不断被考虑用于紧凑的传热系统。它们是通过分岔连接直管而构成的。本文研究了对称y分岔、t分岔和非对称y分岔三种不同分岔几何形式的热水力性能。速度和温度等高线显示出互补性质,其中低速区域对应于高温,反之亦然。引入了相对二次强度(Es/t)、速度不均匀性(δv)、温度不均匀性(δt)和性能指数(ξ)等新的定量参数,以了解几何形状对流场和热性能的影响。t型分岔的传热性能最好,但水力性能最差。另一方面,非对称y分叉的传热性能最差,但水力性能最好。根据性能指标的取值,得出非对称y分岔的性能优于对称y分岔,而对称y分岔的性能又优于t分岔。然而,当这些分岔以串并联方式连接形成配电网时,不对称几何结构中不均匀的流量分布可能会导致问题。将CFD模拟得到的压力损失与理论计算结果进行了比较,表明了综合数值框架的有效性。本文还提出了新的关系式来确定努塞尔数和损失系数作为分岔角和雷诺数的函数。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
11.00
自引率
10.00%
发文量
648
审稿时长
32 days
期刊介绍: International Communications in Heat and Mass Transfer serves as a world forum for the rapid dissemination of new ideas, new measurement techniques, preliminary findings of ongoing investigations, discussions, and criticisms in the field of heat and mass transfer. Two types of manuscript will be considered for publication: communications (short reports of new work or discussions of work which has already been published) and summaries (abstracts of reports, theses or manuscripts which are too long for publication in full). Together with its companion publication, International Journal of Heat and Mass Transfer, with which it shares the same Board of Editors, this journal is read by research workers and engineers throughout the world.
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