臺灣博碩士論文加值系統

本實驗裝置有兩個：二維噴流床與三維噴流床。兩者均採用角度為60�a的角錐底，二維噴流床上方接一高1000mm的壓克力矩形管所製成的噴流床，並使用0.785mm及1.7mm之玻璃珠。而三維噴流床上方接一高500mm的壓克力圓管所製成的噴流床。壓力探針分別置於粒子床下方進氣口處，角錐一半高處和床柱高2.5 cm、5 cm、7.5cm的管壁、管中心、管壁至管中心一半處，以量測壓降與壓力擾動標準偏差變化。探討不同之進氣管，不同粒徑，不同靜床高下的噴流情形。並研究以上各操作變數對最小噴流化速度的影響；並利用Fourier transform將原始數據轉換作分析。
實驗結果顯示，壓力擾動標準偏差S.D.不僅可以準確判斷流態變化，也可用來判斷最小噴流化速度。實驗中最小噴流化速度隨靜床高、粒徑增加而上升。又原始數據經FFT (快速傅利葉轉換)轉換後，發現主頻隨著流態而有所改變。

There are two spouted beds used in this study: two dimensional spouted bed and three dimensional one. They both consist of conical base with 60�a contact angle. The two dimensional spouted bed consists of a transparent plexiglas rectangular column of 1000mm height above the cone. The particles used are glass bead with average diameter of 0.785mm, 1.7mm respectively. And the three dimensional spouted bed consists of a transparent plexiglas circular column of 500mm height above the cone. The pressure taps are put below the bed, half of the conical section and 2.5, 5, 7.5cm height of the bed column. Three depths are measured: wall, center and 1/4 length of bed column. The effects of different inlet tubes, particle sizes and bed heights on the minimum spouting velocity and transition of regime, were studied with standard deviations and pressure drop. And analyzed these data with Fourier transform.
The results showed that standard deviations of pressure drop not only exactly described the transition of regime but also determine minimum spouting velocity. Minimum spouting velocity increased with increasing bed height, and particle diameter. After transforming these data with Fourier transform analysis, the major frequency was changed with the variation of hydrodynamics.

目 錄

中文摘要 Ⅰ
英文摘要 Ⅱ
目錄 Ⅲ
圖表索引 Ⅴ
一、 緒論 1

二、 文獻回顧 5
2-1. 噴流床之流態變化 5
2-2. 噴流床之構造 8
2-3. 噴流床的運動機構 10
2-4. 最小噴流化速度 14
2-5. 最大可噴流靜床高 14
2-6. 噴流床中之壓降變化 19
2-7. 噴流床的應用 20
2-8. 噴流床的設計 21
2-9. 以FFT之方法分析壓力訊號 23
2-10. 三維噴流床的流力行為 23

三、 實驗裝置與步驟 29
3-1. 實驗裝置 29
3-2. 實驗步驟 37
3-3. 數據分析 39
3-3.1. Fourier transform 39


四、 結果與討論 41
4-1. 不同探測位置與探測深度下壓降與流速的關係 41
4-2. 各探測位置之壓力擾動標準偏差S.D.與流速的關係 55
4-3. 利用Fourier transform之分析 56
4-4. 最小噴流化速度之決定 64
4-5. 粒徑、靜床高、改變進氣管(Inlet tube)對系統的影響 73
4-5.1. 靜床高對系統的影響 73
4-5.2. 粒徑對系統的影響 76
4-5.3. 改變進氣管(Inlet tube)對系統之影響 76
4-6. 最大壓降ΔPm、穩定壓降ΔPs與粒徑、靜床高的關係 79
4-7. 三維與二維噴流床之關係 81
五、 結論 85
六、 符號說明 87
七、 參考文獻 89
附錄 93

七、參考文獻
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