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研究生: 顏榮毅
Yen, Jung-Yi
論文名稱: 奈米相變化乳液/奈米流體分別流於外壁加熱同心圓環道/內管共軛強制對流熱傳遞增益特性模擬研究
Conjugate forced convection enhancement characteristics of concurrent flows of nano-PCM emulsion and nanofluid through an externally heated concentric duct - A numerical study
指導教授: 何清政
Ho, Ching-Jenq
學位類別: 碩士
Master
系所名稱: 工學院 - 機械工程學系
Department of Mechanical Engineering
論文出版年: 2017
畢業學年度: 105
語文別: 英文
論文頁數: 142
中文關鍵詞: 奈米乳液奈米流體雙管同心圓管層流強制對流等熱通量
外文關鍵詞: Nanoemulsion, PCM, Nanofluid, Double pipe, Concentric tube, Laminar forced convection, constant heat flux
相關次數: 點閱:110下載:2
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  • 本文使用Fortran compiler無因次化模擬奈米相變化乳液與Al2O3奈米流體以同方向分別流於外壁等熱通量加熱之水平同心圓管外環與內管層流強制對流熱傳遞效應。從物理面來看,高熱傳導係數的奈米流體和相變化過程中能發揮潛熱效應的奈米乳液則在下述這些參數的變化過程中扮演影響溫度場的重要角色:無因次外管半徑 、外內管平均速度比 、奈米流體體積分率 、奈米相變化乳液之質量分率 、修正的史蒂芬數 與次冷參數 。此外,熱傳遞效益與考慮等效壓降的FOM則被使用來評估各種不同流體組合的雙管速度完全發展共軛流之熱傳遞增益,比較的對象則是內外管都以水為工作流體的雙管或是以水為工作流體的單管。結果顯示,當外管的奈米乳液可以充分在整個加熱段表現出它的潛熱優勢,並且有不錯的對流強度和潛熱量時,最高的熱傳遞效應與FOM可以分別達到10.1和3.71,如此好的熱傳增益已經超過過去使用機能性流體在單管內的相關研究。而結果也近一步發現,內管無論是純水或是奈米流體,對於抑制外管壁溫的上升並沒有太顯著的效果,主要原因來自於內管和外管外壁仍然不是直接的接觸,因此影響的效果相當有限。

    In present study, conjugate laminar forced convection heat transfer characteristics of separated nano-PCM suspension in the annulus space and nanofluid in the inner tube by a horizontal concentric double-pipe duct are investigated under the constant heat flux over the external surface of the annular tube through the dimensionless numerical simulation with Fortran compiler. The parameters including dimensionless outer tube radius , the bulk velocity ratio of outer tube over inner tube , volumetric concentration of nanofluid , mass concentration , Stefan number and subcooling factor of nano-PCM suspension are used to explore the temperature profile distribution concerned with the high thermal conductivity of nanofluid complementary with the latent heat mechanism from nano-PCM emulsion during the melting process. Furthermore, the heat transfer effectiveness and FOM, which incorporates the effective pressure drop, are introduced to evaluate the overall heat transfer enhancement of the hydrodynamically fully developed concurrent parallel flows for various fluids combination in the annulus and inner tube compared with the condition of double tube or single tube employing pure water as working fluid. The results show the highest heat transfer effectiveness and FOM at the end of heated section could reach up to 10.1 and 3.71 as the melting nano-PCM emulsion with the great fluid convection and quantity of latent heat covers the whole heated section in the outer tube. Such a great enhancement has exceeded previous single tube study. Moreover, the results also indicate the inner tube flow could not play a crucial role in the outer tube wall suppression due to the non-direct contact of the two tubes whether the fluid is pure water or nanofluid.

    CONTENTS Abstract I 中文摘要 II CONTENTS III LIST OF TABLES VII LIST OF FIGURES IX NOMENCLATURE XXVI CHAPTER 1:INTRODUCTION 1 1.1 Physical Problem Statement 1 1.2 Literature Review 2 1.3 Motivation and Objectives 7 CHAPTER 2:MATHEMATICAL MODEL AND NUMERICAL FORMULATION 9 2.1 Physical Configuration 9 2.2 Mathematical Model 11 2.2.1 Governing equations 11 2.2.2 Boundary conditions 12 2.3 Thermophysical Properties of Working Fluids 14 2.3.1 Pure water 14 2.3.2 Nano-PCM emulsion / Nanofluid 15 2.4 Dimensionless Mathematical Formulation 17 2.4.1 Dimensionless governing equations 18 2.4.2 Dimensionless boundary conditions 20 2.4.3 Dimensionless parameters 21 2.5 Quantities of Interest 22 2.5.1 Local mean temperature and liquid-phase fraction 22 2.5.2 Heat transfer rate 23 2.5.3 Heat transfer coefficient 24 2.5.4 Heat transfer effectiveness 27 2.5.5 Effective pressure drop 27 2.5.6 Figure of Merit (FOM) 29 2.6 Numerical Formulation 29 2.6.1 Grid system 29 2.6.2 Discretization method 30 2.6.3 Numerical solution methodology 30 2.6.4 Verification 31 2.6.5 Test of grid-size convergence 33 CHAPTER 3:CONVECTION EFFICACY OF USING CONCURRENT FLOWS OF VARIOUS COMBINATIONS OF WORKING FLUIDS SEPARATELY THROUGH AN EXTERNALLY HEATED CONCENTRIC DOUBLE-TUBE DUCT 37 3.1 Problem Statement and Objectives 37 3.2 Flow-rate-controlled and Pressure-driven Concurrent Flows in the Concentric Double-tube Duct 38 3.2.1 Pressure-driven concurrent flow distribution 38 3.2.2 Flowrate-controlled concurrent flow distribution 39 3.3 Combinations of Concurrent Working Fluids in the Concentric Double-tube Duct 40 3.4 Results and Discussion 41 3.4.1 Convection characteristics for the concurrent flows of water/water through the concentric double-tube duct 41 3.4.2 Convection characteristics for the concurrent flows of nano-PCM-emulsion/water through the concentric double-tube duct 49 3.4.3 Convection characteristics for the concurrent flows of water/water-Al2O3-nanofluid through the concentric double-tube duct 72 3.4.4 Convection characteristics for the concurrent flows of nano-PCM-emulsion /water-Al2O3-nanofluid through the concentric double-tube duct 79 3.5 Summary 91 CHAPTER 4:HEAT TRANSFER ENHANCEMENT FOR LAMINAR WATER FLOW THROUGH AN ISO-FLUX HEATED CIRCULAR DUCT BY INSERTING A CONCENTRIC CIRCULAR TUBE AND/OR USING NANO-PCM EMULSION AND/OR WATER-ALUMINA NANOFLUID AS THE WORKING FLUIDS 98 4.1 Conversion of single tube to double tube configuration 98 4.2 Heat Transfer and Pressure Drop for Thermally Fully-developed Water Flow in an Iso-flux Heated Circular Duct 99 4.3 Comparison of Convection Characteristics of the Concurrent Water/Water Flows through Concentric Double-tube Duct against that of Single-Tube Water Flow 102 4.4 Comparison of Convection Characteristics of the Concurrent Flows of Nano-PCM-Emulsion/Water through Concentric Double-tube Duct against that of Single-Tube Water Flow 106 4.5 Comparison of Convection Characteristics of the Concurrent Flows of Water/Water-Al2O3-Nanofluid through Concentric Double-tube Duct against that of Single-Tube Water Flow 114 4.6 Comparison of Convection Characteristics of the Concurrent Flows of Nano-PCM-Emulsion/Water-Al2O3-Nanofluid through Concentric Double-tube Duct against that of Single-Tube Water Flow 118 4.7 Summary 127 CHAPTER 5: CONCLUSION AND FUTURE WORKS 133 5.1 Conclusion 133 5.2 Future Works 135 REFERENCES 137

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