微通道中的过冷沸腾:通过拓扑优化和微泡发射的瞬态特性增强传热

IF 5.8 2区 工程技术 Q1 ENGINEERING, MECHANICAL
Jianhong Zhou, Yuanle Zhang, Qiang Li, Xuemei Chen
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引用次数: 0

摘要

近年来,微通道内的过冷流动沸腾因其在高热流密度冷却场景中的应用而引起了广泛的研究关注。本研究通过流动可视化实验,研究了具有基线构型(BC)和两种拓扑优化构型(TOC-I和TOC-II)的微通道中的过冷流动沸腾。研究了质量通量(330.1、660.2和1320.3 kg/m2·s)、进口过冷度(40、60和80 K)和加热器热流通量(0-700 W/cm²)对两相流模式和热水力特性的影响。重点研究了微泡发射沸腾(MEB)现象的气泡动力学和壁面温度和压降的瞬态响应。结果表明:三种构型均表现为i型气泡流(TIBF)、段塞流(SF)和液滴流(DF)。相比之下,ii型气泡流(TIIBF)和环状流(AF)是BC所特有的,而蒸发流(EF)只出现在TOC-I和TOC-II中。在相同热流密度条件下,TOC-II的壁面过热度最低,这是由于其换热面积大,且微针脚翅具有拓扑优化结构,增强了流体的混合,破坏了热边界层的形成。与BC相比,壁面过热度最大降低了29.5 K。在大多数工况下,TOC-I的传热系数高于BC和TOC-II,在SF工况下达到80.4 kW/m2·K的峰值,比BC工况下57.3 kW/m2·K的峰值高出40.2%。在大多数操作条件下,TOC-I的时间平均压降与BC相当,略低于TOC-II。值得注意的是,在BC中观察到MEB具有两种不同的进化模式,其完整的进化周期约为30-70 ms。此外,在MEB强烈活动期间,随着热通量的增加,观察到壁面过热度的瞬态和异常下降,伴随着温度和压力下降的振荡,振幅分别高达8 K和6.4 kPa。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Subcooled flow boiling in microchannels: Heat transfer enhancement via topology optimization and transient characteristics of microbubble emission
In recent years, subcooled flow boiling in microchannels has attracted extensive research attention due to its applications in high heat flux cooling scenarios. In this study, subcooled flow boiling in microchannels with a baseline configuration (BC) and two topologically optimized configurations (TOC-I and TOC-II) is investigated through flow visualization experiments. The effects of mass flux (330.1, 660.2, and 1320.3 kg/m2·s), inlet subcooling (40, 60, and 80 K), and heater heat flux (0-700 W/cm²) on two-phase flow patterns and thermo-hydraulic characteristics are examined. Particular focus is given to the bubble dynamics and transient responses of wall temperature and pressure drop associated with the microbubble emission boiling (MEB) phenomenon. The results show that all three configurations exhibit Type-I Bubbly Flow (TIBF), Slug Flow (SF), and Droplet Flow (DF). In contrast, Type-II Bubbly Flow (TIIBF) and Annular Flow (AF) are unique to BC, while Evaporated Flow (EF) appears exclusively in TOC-I and TOC-II. TOC-II exhibits the lowest wall superheat under identical heat flux conditions, owing to its large heat transfer area and the micro pin fins with topologically optimized configuration, which enhances fluid mixing and disrupts the formation of the thermal boundary layer. Compared to BC, the maximum reduction in wall superheat reaches 29.5 K. Under most operating conditions, TOC-I demonstrates a higher heat transfer coefficient than both BC and TOC-II, reaching a peak value of 80.4 kW/m2·K under the SF regime, which is 40.2 % higher than the peak value of 57.3 kW/m2·K observed in BC. The time-averaged pressure drop in TOC-I is comparable to that in BC and slightly lower than that in TOC-II, under most operating conditions. Notably, MEB with two distinct evolution modes is observed in BC, with a complete evolution cycle lasting approximately 30-70 ms. Furthermore, during intense MEB activity, a transient and anomalous drop in wall superheat is observed as heat flux increases, accompanied by temperature and pressure drop oscillations with amplitudes of up to 8 K and 6.4 kPa, respectively.
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来源期刊
CiteScore
10.30
自引率
13.50%
发文量
1319
审稿时长
41 days
期刊介绍: International Journal of Heat and Mass Transfer is the vehicle for the exchange of basic ideas in heat and mass transfer between research workers and engineers throughout the world. It focuses on both analytical and experimental research, with an emphasis on contributions which increase the basic understanding of transfer processes and their application to engineering problems. Topics include: -New methods of measuring and/or correlating transport-property data -Energy engineering -Environmental applications of heat and/or mass transfer
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