本實驗採用直徑30 mm之水旋風分離器，使用馬鈴薯澱粉當粉體，分別進行實驗和模擬的分析，實驗方面探討不同進口壓力下和溢流管深淺之影響，分析溢流和底流的粒徑分佈以及分離效率，模擬方面以多相流VOF模式模擬空氣核心並分析流場，以實驗與數值模擬為基礎，進而發展新樣式水旋風分離器-薄膜水旋風分離器。
實驗結果顯示，當進口壓力越大則整體分離效率越好。在不同溢流管深的實驗結果顯示，不管任何溢流管的深淺皆會因進口壓力增大而分離效率有所提升，以溢流管深為30 mm最理想。本研究的薄膜水旋風分離器在相同的操作條件下，薄膜水旋風分離器的分流比和新定義的澄清效率(Ec)皆會優於傳統型式，而整體的平均效率提升約16 %以上，大大提升水旋風分離器的整體分離效率，具有一定發展性。

This study uses potato starch as particles to realize its classification in a 30 mm diameter hydrocyclone. In the experiment, the effects of variations in feed pressure and vortex finder depth on particle size distribution and separation efficiency were analyzed. In the simulation, the air core was simulated successfully by VOF model. Based on experimental and simulation results, a new kind of hydrocyclone, membrane hydrocyclone was developed.
According to experiment results, the higher the feed pressure, the higher the separation efficiency. The hydrocyclone with 30 mm vortex finder inserted into the cylindrical part of the hydrocyclone has the best separation efficiency. The new developing membrane hydrocyclone is better than the traditional hydrocyclone in flow split and clarification efficiency (Ec) under the same operation conditions.

中文摘要………………………………………………………………I
英文摘要………………………………………………………………II
目錄……………………………………………………………………III
圖表目錄………………………………………………………………VII
第一章 緒論……………………………………………………………1
1-1 前言…………………………………………………………………1
1-2 研究動機與目標……………………………………………………2
第二章 文獻回顧………………………………………………………3
2-1水旋風分離器之發展概要…………………………………………3
2-1-1水旋風分離器之簡介……………………………………………3
2-1-2 水旋風分離器之介紹與結構…………………………………4
2-1-3 水旋風分離器之規格…………………………………………6
2-1-4 水旋風分離器之優、缺點………………………………………7
2-1-5 水旋風分離器之應用…………………………………………8
2-2 水旋風分離器之特殊現象…………………………………………9
2-2-1魚鉤現象…………………………………………………………9
2-2-2空氣核心…………………………………………………………10
2-2-3 短路流現象……………………………………………………11
2-2-4 循環流…………………………………………………………11
2-3水旋風分離器在生化工程上的應用………………………………12
2-4數值計算在水旋風分離器的應用…………………………………15
第三章理論……………………………………………………………18
3-1 水旋風分離器之基本理論………………………………………18
3-1-1水旋風分離器的分離原理……………………………………18
3-1-2粒子在流體中的拖曳力………………………………………19
3-1-3兩相流動中的受力分析………………………………………19
3-1-4 平衡軌道理論…………………………………………………21
3-1-5無因次群組……………………………………………………22
3-2 水旋風分離器之性能和特性……………………………………24
3-2-1 幾何結構………………………………………………………24
3-2-2 物性參數………………………………………………………25
3-2-3 操作參數………………………………………………………26
3-3數值計算……………………………………………………………28
3-3-1模擬軟體與計算模式簡介……………………………………28
3-3-2 統御方程式……………………………………………………28
3-3-3 邊界條件………………………………………………………31
第四章 實驗裝置與模擬設定…………………………………………32
4-1 實驗物料…………………………………………………………32
4-2 實驗裝置…………………………………………………………33
4-3 實驗步驟…………………………………………………………36
4-4 模擬的基本假設…………………………………………………37
4-5 模擬的整體結構與網格…………………………………………38
4-6 數值方法與模擬模式設定………………………………………39
第五章 結果與討論……………………………………………………40
5-1 實驗結果…………………………………………………………40
5-1-1 壓降效應………………………………………………………42
5-1-2 溢流管深淺之影響……………………………………………45
5-2 模擬結果…………………………………………………………53
5-2-1 不同溢流管深淺的模擬結果…………………………………57
5-3 新樣式水旋風分離器-薄膜水旋風分離器(Membrane Hydrocyclone)……60
5-3-1 模擬測試………………………………………………………60
5-3-2 實驗裝置………………………………………………………61
5-3-3 實驗結果與比較………………………………………………62
第六章 結論……………………………………………………………68
符號說明………………………………………………………………71
參考文獻………………………………………………………………74

圖目錄：
第二章
圖2-1水旋風分離器之結構……………………………………………5
圖2-2兩個基本設計水旋風分離器之結構(a)小圓錐角；(b)大圓錐角……6
圖2-3水旋風分離器之魚鉤現象………………………………………9
第三章
圖3-1各截面軸速度分佈和零速包絡面(LZVV)………………………21
圖3-2水旋風分離器之基本幾何結構圖………………………………25
第四章
圖4-1馬鈴薯澱粉之粒徑分佈圖………………………………………32
圖4-2水旋風分離器之結構……………………………………………34
圖4-3實驗整體設備圖…………………………………………………35
圖4-4水旋風分離器之網格……………………………………………38
第五章
圖5-1不同進口壓力下，溢流、底流和進口的流量圖………………40
圖5-2進口壓力對進口速度和特性速度作圖…………………………41
圖5-3進口壓力對雷諾數作圖…………………………………………42
圖5-4在不同進口壓力下溢流之粒徑分佈(Lhco=30 mm)……………43
圖5-5在不同進口壓力下底流之粒徑分佈(Lhco=30 mm)……………43
圖5-6在不同進口壓力下之分級效率曲線(Lhco=30 mm)……………44
圖5-7在不同進口壓力下溢流之粒徑分佈(Lhco=0 mm)……………45
圖5-8在不同進口壓力下底流之粒徑分佈(Lhco=0 mm)……………46
圖5-9在不同進口壓力下溢流之粒徑分佈(Lhco=65 mm)……………47
圖5-10在不同進口壓力下底流之粒徑分佈(Lhco=65 mm)…………48
圖5-11在不同進口壓力下溢流之粒徑分佈(Lhco=90 mm)…………49
圖5-12在不同進口壓力下底流之粒徑分佈(Lhco=90 mm)…………50
圖5-13在不同溢流管深之分級效率曲線(Pi =0.9 bar)……………51
圖5-14進口壓力對分離效率在不同溢流管深作圖…………………52
圖5-15不同時間下的空氣體積分佈(vi=4.9 m/s, Lhco=30 mm, X=0)……54
圖5-16分佈圖 (a)壓力分佈 (b)軸速度 (c)徑向速度 (d)切線速度(vi=4.9 m/s, Lhco=30 mm, t=1.9 s, X=0)………………………56
圖5-17不同溢流管深的空氣體積分佈圖 (a) Lhco=0 mm (b) Lhco=30 mm(c) Lhco=65 mm (d) Lhco=90 mm (vi=4.9 m/s, t=1.9 s, X=0)……57
圖5-18不同溢流管深的壓力分佈圖(a) Lhco=0 mm (b) Lhco=30 mm
(c) Lhco=65 mm (d) Lhco=90 mm (vi=4.9 m/s, t=1.9 s, X=0)……58
圖5-19不同溢流管深的軸速度分佈圖 (a) Lhco=0 mm (b) Lhco=30 mm(c) Lhco=65 mm (d) Lhco=90 mm (vi=4.9 m/s, t=1.9 s, X=0)……59
圖5-20 (a)薄膜型式與(b)和(c)傳統型式之模擬結構……………60
圖5-21 (a)薄膜型式和(b)傳統型式之實驗的溢流管結構…………62
圖5-22薄膜型式和傳統型式的分流比之比較圖……………………63
圖5-23薄膜型式和傳統型式的溢流濃度比較圖……………………64
圖5-24薄膜型式和傳統型式的澄清效率比較圖……………………65
圖5-25薄膜型式與傳統型式的澄清效率曲線圖(Pi =0.3 bar)……66
圖5-26薄膜型式與傳統型式的澄清效率曲線圖(Pi =0.6 bar)……67
圖5-27薄膜型式與傳統型式的澄清效率曲線圖(Pi =0.9 bar)……67

表目錄：
第五章
表5-1進口、溢流和底流的實驗壓力數據……………………………41
表5-2 (a)薄膜型式與(b)和(c)傳統型式之模擬數據比較…………61

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