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研究生: 孫慶玲
Sun, Ching-Ling
論文名稱: 結合分層化、分合流及渦流引發結構之微混合器
A micromixer combining laminating, splitting/recombination and vortex-inducing structures
指導教授: 吳志陽
Wu, Chih-Yang
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: 2020
畢業學年度: 108
語文別: 中文
論文頁數: 122
中文關鍵詞: 微混合器分合流渦流引發接頭粒子反向追跡
外文關鍵詞: micromixer, split-and-recombine mixing units, vortex-inducing junction, backward particle tracking
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  • 本研究探討具有對齊或不對齊T形匯流入口與分合流模組的微混合器,在入口處流體匯流後進入主混合流道,經由分合流模組的彎曲分岔處將流體分成上、下部分分別進入彎曲分支流道,利用彎曲流道使流體產生折疊拉伸效應促進混合,再使用T形接頭進行匯流。當匯流接頭不對齊時,會引發渦流,本研究主要探討此一渦流引發結構對微混合器之混合的影響,並比較主混合流道深寬比為2與1流體混合的情形。在高培克萊特數下,網格法會高估混合度,因此本研究進一步使用流體粒子反向追跡與近似擴散模式及反向蒙地卡羅法做模擬,本文主要以前者的模擬結果比較在微混合器中不同雷諾數的流動及混合。本研究也利用微影製程製作微混合器,並使用共軛焦顯微鏡觀察流體的混合情形,和數值模擬相互比較,發現兩者具有相似的濃度分佈。研究結果顯示主混合流道深寬比為2之具渦流引發結構分合流模組微混合器在低雷諾數時,利用分合流模組及不對齊接頭,使兩流體形成分層化的濃度分佈,大幅增加流體間接觸面積。在高雷諾數時,流體經由彎曲分支流道形成狄恩渦流,且藉由不對齊接頭引發渦流的橫向速度較大,使擴散介面產生折疊拉伸效應,因此混合度較高。

    This study explores micromixers with aligned or unaligned T-shaped inlets and split-and-recombine (SAR) mixing units. After two fluids merge at the T-shaped junction, the fluids enter the main mixing channel and are divided into upper and lower streams through the circular turn of the SAR mixing units. The two streams through the SAR mixing units are combined at the T-shaped junctions. When the confluence junction is unaligned, the vortex will be induced. This study investigates the influence of the vortex-inducing structures (VIS) on the fluid mixing in the micromixer, and compares the mixing of the mixers with different aspect ratios of main mixing channel (Ar). At high Peclet number, the degree of mixing is overestimated by the grid method. Thus, we also adopt the particle-tracking simulation with an approximate diffusion model and the Monte Carlo simulation. We mainly adopt the former to analyze the flow and mixing of the fluids at different Reynolds numbers. This study also uses the lithography process to fabricate a micromixer, and a confocal microscopy to observe the images of the mixing in the micromixer. The experimental images show similar concentration distributions with those obtained by numerical simulation. The results show that the micromixer composed of SAR mixing units with VIS and Ar=2 has the higher degrees of mixing because it uses SAR mixing units and unaligned junctions to cause stratification effect of the two fluids at low Reynolds numbers, and generates Dean vortex in the curved sub-channels and induces strong swirling flow in the VIS at high Reynolds numbers.

    摘要 i Extended Abstract ii 致謝 ix 目錄 x 表目錄 xiii 圖目錄 xiv 符號表 xxiii 第一章 緒論 1 1-1 研究背景 1 1-2 文獻回顧 1 1-4 研究方法 3 1-5 本文架構 4 第二章 流道幾何形狀與數值模擬方法 5 2-1微混合器之設計 5 2-2基本假設 6 2-3統御方程式與邊界條件 6 2-4無因次代數變換 8 2-5網格法數值模擬 10 2-6流體粒子的反向追跡與近似擴散模式 11 2-6-1 流體粒子反向追跡 11 2-6-2 近似擴散模式 13 2-7 反向蒙地卡羅模擬方法 13 2-8 混合度 13 第三章 微混合器製作與實驗觀察 15 3-1微混合器製作流程 15 3-1-1 光罩設計 15 3-1-2 母模製作 15 3-1-3 表面粗度儀量測流道高度與寬度 17 3-1-4 翻模製作微混合器 17 3-1-5微流道氧電漿接合與細流管黏合 18 3-2實驗觀測 18 3-2-1 工作流體與微量式注射幫浦 18 3-2-2 實驗影像擷取 18 第四章 結果與討論 20 4-1計算方法測試 20 4-1-1 網格法測試 20 4-1-2流體粒子反向追跡與近似擴散模式解法之目標截面粒子數測試 21 4-1-3反向蒙地卡羅模擬之驗證 21 4-1-4三種數值模擬方法比較 22 4-2數值模擬與實驗結果的驗證 23 4-3在不同T形匯流入口的流動與混合 23 4-4流體匯流前分支流道長度對流動的影響 24 4-5平面匯流結構及具渦流引發結構分合流模組之微混合器中的流動與混合 25 4-6微混合器在各分合流模組出口與微混合器出口的混合情況 30 4-6-1低雷諾數下各模組出口的混合情況 31 4-6-2高雷諾數下各模組出口的混合情況 32 4-6-3五個渦流引發結構分合流模組對微混合器出口之流體混合的貢獻 32 4-6-4主混合流道深寬比對具渦流引發結構分合流模組微混合器出口之流體混合的影響 33 4-6-5分合流模組之平面與不對齊匯流結構對微混合器出口之流體混合的影響 35 第五章 結論與未來展望 36 5-1結論 36 5-2未來展望 36 參考文獻 37 附錄 40 A-1流體粒子之速度內插 40 A-2目標截面之濃度擴散模式 41

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