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研究生: 張軒豪
Chang, Hsuan-Hao
論文名稱: 不同混合式微通道配置下散熱性能之數值分析研究
Numerical Investigation of Heat Dissipation Performance in Different Hybrid Microchannel Configurations
指導教授: 吳毓庭
Wu, Yu-Ting
學位類別: 碩士
Master
系所名稱: 工學院 - 工程科學系
Department of Engineering Science
論文出版年: 2026
畢業學年度: 114
語文別: 英文
論文頁數: 79
中文關鍵詞: 微流道散熱器回流腔混合式微流道熱傳增強熱流性能
外文關鍵詞: Microchannel Heat Sink, Reentrant Cavity, Hybrid Microchannel, Heat Transfer Enhancement, Thermal-Hydraulic Performance
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  • 本研究以數值模擬方式探討不同回流腔微流道散熱器之熱流性能。首先建立三種基本微流道結構,包含矩形微流道(R)、扇形回流腔微流道(F)與三角形回流腔微流道(T)。進一步以此三種基本幾何為基礎,設計多組二階與三階混合排列微流道,藉此分析回流腔幾何形狀與排列順序對流場發展、熱傳增強與流動阻力之影響。
    本研究使用 ANSYS Fluent 進行數值模擬,工作流體為水,矽基板底部施加均勻熱通量 (0.6 MW/m²),雷諾數範圍為 150 至 800。模擬採用穩態、層流、壓力基求解器,並考慮流體與固體之共軛熱傳效應。為確保數值結果之可靠性,本研究先針對網格獨立性進行分析,並將平均努塞爾數與表觀摩擦因子與 Chai 等人之實驗結果進行比較。結果顯示,約 9.6 百萬網格數可在計算精度與計算成本之間取得良好平衡,因此作為後續模擬分析之網格設定。
    研究結果顯示,回流腔結構可有效擾動熱邊界層並促進冷卻流體混合,進而提升對流熱傳能力。相較於傳統矩形微流道,單一回流腔與混合排列微流道皆能降低壁面溫度與總熱阻。在代表性案例中,三角形–扇形混合微流道(TF)於 (Re=474.6) 時具有最低峰值溫度,可將 T 型微流道之最高溫度由 308.7 K 降至 303.7 K。三角形–扇形–矩形混合微流道(TFR)亦展現良好散熱能力,可作為三階混合排列設計之代表案例。
    流場分析結果指出,混合式回流腔排列可維持較強之高速主流核心,並改善流道內之動量傳遞。渦度分析進一步顯示,矩形流道僅在壁面附近產生有限渦度,而扇形與三角形回流腔會因幾何變化產生不同程度之旋轉流動。其中,三角形回流腔可形成較強之局部渦度,而混合式排列則能延伸高渦度區域並增強流體混合。綜合而言,適當排列不同回流腔幾何可在維持合理流動阻力的同時,有效降低局部熱累積並提升微流道散熱器之整體熱流性能。

    This study numerically investigates the thermal-hydraulic performance of microchannel heat sinks with different reentrant cavity configurations. Three basic microchannel geometries, including the rectangular microchannel (R), fan-shaped reentrant cavity microchannel (F), and triangular reentrant cavity microchannel (T), were first considered. Based on these basic structures, several two-stage and three-stage hybrid configurations were further developed to examine the influence of cavity geometry and arrangement sequence on flow development and heat transfer enhancement.
    The numerical simulations were performed using ANSYS Fluent. Water was employed as the working fluid, and a uniform heat flux of 0.6 MW/m² was applied to the bottom surface of the silicon substrate. The Reynolds number ranged from 150 to 800. A steady, laminar, pressure-based solver with conjugate heat transfer was adopted. Mesh independence and model validation were conducted by comparing the predicted average Nusselt number and apparent friction factor with the experimental data reported by Chai et al. The mesh containing approximately 9.6 million cells was selected for subsequent simulations because it provided a suitable balance between numerical accuracy and computational cost.
    The results show that the introduction of reentrant cavity structures enhances convective heat transfer by disturbing the thermal boundary layer and promoting coolant mixing. Compared with the conventional rectangular microchannel, both single-cavity and hybrid configurations reduce wall temperature and total thermal resistance. Among the representative configurations, the triangular–fan hybrid microchannel (TF) exhibits the lowest peak temperature at Re = 474.6, decreasing from 308.7 K for the T configuration to 303.7 K. The triangular–fan–rectangular configuration (TFR) also demonstrates improved thermal performance and provides a representative three-stage hybrid design.
    Flow field analysis indicates that hybrid cavity arrangements maintain a stronger high-velocity core and improve momentum transport along the channel. The vorticity analysis further confirms that the rectangular channel generates limited rotational motion, while fan-shaped and triangular cavities produce different vortex characteristics. In particular, triangular cavities generate stronger localized vorticity, whereas hybrid arrangements extend the high-vorticity region and enhance fluid mixing. These findings demonstrate that properly arranged hybrid reentrant cavity structures can effectively improve heat transfer performance while maintaining acceptable hydraulic resistance, providing a useful design strategy for high-performance microchannel heat sinks.

    摘要 I ABSTRACT II CONTENTS IV LIST OF TABLES VII LIST OF FIGURES VIII NOMENCLATURE X Chapter1 INTRODUCTION 1 1.1 Preface 1 1.2 Background 2 1.3 Motivation and Objectives 3 1.4 Literature Review 4 Chapter2 THEORY AND NUMERICAL METHODS 10 2.1 ANSYS Introduction 10 2.1.1 Fundamental Assumptions 11 2.2 Establishment of Theoretical Model 12 2.3 Governing Equations 13 2.3.1 Continuity Equation 14 2.3.2 Momentum Equation 14 2.3.3 Energy Equation 15 2.3.4 Heat Conduction Equation in Solid Domain 16 2.3.5 Conjugate Heat Transfer 16 2.4 Performance Evaluation Parameters 17 2.4.1 Average Heat Transfer Coefficient 17 2.4.2 Average Nusselt Number 18 2.4.3 Reynolds Number and Non-dimensional Flow Length 18 2.4.4 Local Apparent Friction Factor 18 2.4.5 Local Heat Transfer Coefficient and Local Nusselt Number 19 Chapter3 Numerical Methodology 21 3.1 Geometry Definition 21 3.2 Mesh Generation 24 3.3 Mesh Independence Analysis and Model Validation 26 3.3.1 Validation Using Average Nusselt Number 26 3.3.2 Validation Using Apparent Friction Factor 28 3.4 Boundary Conditions and Solver Settings 30 3.4.1 Boundary Conditions 30 3.4.2 Solver Settings 33 Chapter4 RESULT AND DISCUSSION 35 4.1 Thermal-Hydraulic Characteristics of Different Microchannel Configurations 35 4.1.1 Local Pressure Distribution 36 4.1.2 Wall Temperature Distribution 37 4.1.3 Local Apparent Friction Factor Distribution 39 4.1.4 Local Nusselt Number Distribution 40 4.2 Overall Thermal–Hydraulic Performance Evaluation 43 4.3 Flow Development Analysis 44 4.3.1 Flow Development in the Triangular Reentrant Cavity Microchannel 44 4.3.2 Flow Development in the Triangular–Fan Reentrant Cavity Microchannel (TF) 46 4.3.3 Flow Development in the Triangular–Fan–Rectangular Reentrant Cavity Microchannel (TFR) 47 4.4 Temperature Distribution Analysis 50 4.5 Vorticity Analysis 52 4.5.1 Effect of Basic Cavity Geometry on Vorticity Generation 53 4.5.2 Vorticity Distribution in the Triangular–Fan Reentrant Cavity Microchannel 55 4.5.3 Vorticity Distribution in the Triangular–Fan–Rectangular Reentrant Cavity Microchannel (TFR) 56 4.5.4 Summary of Vorticity Analysis 57 Chapter5 Conclusions and Future Work 59 5.1 Conclusions 59 5.2 Future Work 61 Reference 63

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