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| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 劉懷勝(Hwai-Shen Liu) | |
| dc.contributor.author | Yu-Chieh Wang | en |
| dc.contributor.author | 王鈺傑 | zh_TW |
| dc.date.accessioned | 2021-06-16T23:23:20Z | - |
| dc.date.available | 2014-12-31 | |
| dc.date.copyright | 2012-08-07 | |
| dc.date.issued | 2012 | |
| dc.date.submitted | 2012-07-31 | |
| dc.identifier.citation | 參考文獻
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| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/65087 | - |
| dc.description.abstract | 旋轉填充床為程序強化的重要項目之一，其係利用離心力所造成之高重力場取代地球之重力場，達到提升質傳效果之目的。氣液之間的質傳現象即相變化會伴隨著大量的潛熱，這顯示氣體液體之間會同時發生質量與熱量的傳遞。為了分析逆流式旋轉填充床中，液體和氣體之間的熱量質量傳遞現象，本研究以熱水和冷空氣作為系統，分別以實驗量測與理論模擬的方式，探討進料空氣的相對濕度與體積流速、進料熱水的體積流速與溫度、進料空氣與水的體積流速比例對系統的影響，並且驗證模擬與實驗之間的關聯性。
本研究於實驗中使用鈕扣型溫度記錄器，以得到各個實驗條件下床體內部不同半徑處的溫度(T_iButton)。此外，並以(Klimanek and Biaecki, 2009)提出的冷卻水塔理論作為基礎，使用簡化後的數學模型來描述旋轉填充床中水的質量流速、水的溫度、空氣溫度與空氣濕度這四個變數與徑向位置的關係；根據上述之流體變數，即可求出理論估計的溫度記錄器溫度(T_(iButton,est))。本研究中，經由實驗量測到的T_iButton與經由理論計算出的T_(iButton,est)，兩者之間的誤差不超過5%，由此可知本研究所提出之理論模型，能夠解釋氣體液體之間同時發生的熱量與質量傳遞現象，對於將旋轉填充床應用在蒸餾、化學反應等與溫度相關之程序上，提供了嶄新的思考方向與詳細的基礎研究資料。 | zh_TW |
| dc.description.abstract | A so-called rotating packed bed (RPB) which substitutes the centrifugal force for gravitational force plays an important role in field of process intensification. With the help of centrifugal force, a better mass transfer efficiency could be expected. Because gas-liquid mass transfer which is phase change involves a large amount of latent heat, heat transfer occurs simultaneously. In this study, the phenomena of heat and mass transfer were investigated in the water-air system. The air flow rate, water flow rate, air temperature, water temperature, humidity of air and the ratio of air to water flow rate were taken into consideration in simulation and experiments. Finally, the relationship between simulation and experiments was discussed.
The temperature profile (T_iButton) was obtained by iButton® temperature data loggers at different experimental conditions and positions. Based on the theory of cooling tower proposed by Klimanek and Biaecki, this study used the modified model to describe four dependent variables (temperature of water、 temperature of air、 humidity of air、 mass flow rate of water) and the independent variable (the radial position in the RPB). With the gas and liquid data from simulation, the T_iButton can be estimated (T_(iButton,est )). In this study, the error between T_iButton and T_(iButton,est ) was smaller than 5%, so the modified model in this study can explain the phenomena of heat and mass transfer between gas and liquid phases. Therefore, the study provided not only the brand-new thinking but also plenty of basic research data for the application of temperature-sensitive chemical engineering processes in the RPB. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-16T23:23:20Z (GMT). No. of bitstreams: 1 ntu-101-R99524032-1.pdf: 2815855 bytes, checksum: ddbc616d2d80d9229d37052b9ba6e682 (MD5) Previous issue date: 2012 | en |
| dc.description.tableofcontents | 目錄
摘要 I Abstract II 第一章 序論 1 第二章 文獻回顧 3 2-1旋轉填充床(Rotating packed bed, RPB) 3 2-1-1旋轉填充床之構造與床體設計 4 2-1-2旋轉填充床之壓降 9 2-1-3旋轉填充床之液體流態、液體滯留量、液體滯留時間 12 2-1-4旋轉填充床之有效質傳界面積與填充物結構 15 2-1-5旋轉填充床之液膜質傳係數與氣膜質傳係數 17 2-1-6旋轉填充床之微觀混合 21 2-1-7旋轉填充床之應用與發展 23 2-2冷卻水塔(Cooling tower)之數學模型 32 第三章 理論分析 34 3-1液體氣體之間熱量質量傳遞之數學模型建立 34 3-1-1傳統填充床中液體與氣體之間熱量質量傳遞之數學模型 34 3-1-2旋轉填充床中液體與氣體之間熱量質量傳遞之數學模型 39 3-2 總括氣膜體積質傳係數(overall volumetric mass transfer coefficient)分析 43 3-2-1雙膜理論 (Two-Film Theory) 43 3-2-2氣膜質傳係數之求法 46 3-2-3非恆溫環境下之總括氣膜體積質傳係數之推導 48 第四章 實驗方法 52 4-1 實驗裝置 52 4-2實驗藥品與儀器 53 4-3實驗流程 55 第五章 模擬結果與討論 60 5-1實際實驗操作條件下之模擬結果 64 5-2改變進料氣體之相對濕度對模擬結果之影響 69 5-2-1模擬進料氣體之空氣相對溼度為10 % 69 5-2-2模擬進料氣體之空氣相對溼度為30 % 72 5-2-3模擬進料氣體之空氣相對溼度為40 % 74 5-2-4模擬進料氣體之空氣相對溼度為60 % 76 5-2-5 比較不同相對濕度之進料氣體對模擬結果之影響 78 5-3改變進料氣體之空氣體積流速對模擬結果之影響 81 5-3-1模擬進料氣體之空氣體積流速為40 L/min 81 5-3-2模擬進料氣體之空氣體積流速為50 L/min 84 5-3-3模擬進料氣體之空氣體積流速為60 L/min 86 5-3-4模擬進料氣體之空氣體積流速為70 L/min 88 5-3-5模擬進料氣體之空氣體積流速為80 L/min 90 5-3-6 比較不同空氣體積流速之進料氣體對模擬結果之影響 92 5-4改變進料液體之熱水體積流速對模擬結果之影響 96 5-4-1模擬進料液體之熱水體積流速為0.1 L/min 96 5-4-2模擬進料液體之熱水體積流速為0.2 L/min 99 5-4-3模擬進料液體之熱水體積流速為0.3 L/min 101 5-4-4模擬進料液體之熱水體積流速為0.4 L/min 103 5-4-5模擬進料液體之熱水體積流速為0.5 L/min 105 5-4-6 比較不同熱水體積流速之進料液體對模擬結果之影響 107 5-5改變進料液體之熱水溫度對模擬結果之影響 111 5-5-1模擬進料液體之熱水溫度為40 ℃ 111 5-5-2模擬進料液體之熱水溫度為45 ℃ 114 5-5-3模擬進料液體之熱水溫度為50 ℃ 116 5-5-4模擬進料液體之熱水溫度為55 ℃ 118 5-5-5模擬進料液體之熱水溫度為60 ℃ 120 5-5-6 比較不同熱水溫度之進料液體對模擬結果之影響 122 5-6改變進料氣體與液體之體積流速比例對模擬結果之影響 125 5-6-1模擬進料氣體與液體之體積流速比例為40/0.2 125 5-6-2模擬進料氣體與液體之體積流速比例為50/0.2 128 5-6-3模擬進料氣體與液體之體積流速比例為60/0.2 130 5-6-4模擬進料氣體與液體之體積流速比例為40/0.1 132 5-6-5模擬進料氣體與液體之體積流速比例為50/0.1 134 5-6-6模擬進料氣體與液體之體積流速比例為60/0.1 136 5-6-7 比較不同之進料氣體與液體體積流速比例對模擬結果之影響 138 第六章 實驗結果與討論 143 6-1特定操作條件 144 6-1-1特定操作條件下之實驗結果 144 6-1-2特定操作條件下之實驗結果與模擬結果之比較 147 6-2進料氣體之相對濕度 148 6-2-1改變進料氣體之相對濕度對實驗結果之影響 148 6-2-2進料氣體之相對濕度對實驗與模擬之影響比較 152 6-3進料氣體之空氣體積流速 154 6-3-1改變進料氣體之空氣體積流速對實驗結果之影響 154 6-3-2進料氣體之空氣體積流速對實驗與模擬之影響比較 157 6-4進料液體之熱水體積流速 161 6-4-1改變進料液體之熱水體積流速對實驗結果之影響 161 6-4-2進料液體之熱水體積流速對實驗與模擬之影響比較 165 6-5進料液體之熱水溫度 169 6-5-1改變進料液體之熱水溫度對實驗結果之影響 169 6-5-2進料液體之熱水溫度對實驗與模擬之影響比較 172 6-6進料氣體與液體之體積流速比例 176 6-6-1改變進料氣體與液體之體積流速比例對實驗結果之影響 176 6-6-2進料氣體與液體之體積流速比例對實驗與模擬之影響比較 180 第七章 結論 185 參考文獻 188 符號說明 194 圖目錄 圖1.1 程序強化之項目 1 圖2-1-1.1 逆流式旋轉填充床 5 圖2-1-1.2 錯流式旋轉填充床 5 圖2-1-1.3分離填充物旋轉填充床 6 圖2-1-1.4葉片狀填充物旋轉填充床 7 圖2-1-1.5鋸齒狀旋轉填充床Rotating Zigzag Bed,RZB 8 圖2-1-1.6多層鋸齒狀旋轉填充床 8 圖2-1-2.1 壓降在不同操作狀態下之實驗結果 9 圖2-1-2.2 旋轉填充床壓降隨轉速變化之特性 10 圖2-1-2.3 壓降與氣體流速關係圖 11 圖2-1-3.1液體在旋轉填充床流動模式示意圖 12 圖2-1-3.2 假設的旋轉填充床模型 13 圖2-1-3.3壓降與液體滯留量隨氣體流量變化關係圖 14 圖2-1-3.4利用壓降去預測液體滯流量與實驗之液體滯留量比較圖 14 圖2-1-6.1不同混合器之微觀混合效果比較 22 圖2-1-6.2撞擊流-旋轉填充床 23 圖3-1-1 進料出料氣液體相關之變數於冷卻水塔內之位置關係圖 33 圖3-1-2 進料出料氣液體相關之變數於旋轉填充床內之位置關係圖 37 圖3-2-1.1雙膜理論示意圖 42 圖4-1.1 旋轉填充床主體裝置圖 51 圖4-2.1 iButton®元件之尺寸數據 53 圖4-3.1溫度記錄器(DS1921G)於旋轉填充床床體之 (A)下視圖 (B)上視圖 55 圖4-3.2溫濕度記錄器(DS1923)置於矽膠管內 56 圖4-3.3實驗過程中溫度記錄器(DS1921G)所測得之T_iButton原始數據 57 圖4-3.4實驗流程圖 58 圖5.1 進料出料氣液體相關之變數與旋轉填充床內外半徑之間的關係 59 圖5-1 模擬旋轉填充床內部， (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量，隨徑向變化之情形 66 圖5-1 模擬旋轉填充床內部， (C)液體之質量流速，隨徑向變化之情形 67 圖5-2-1模擬R.H. = 10%時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 70 圖5-2-2模擬R.H. = 30%時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 72 圖5-2-3 模擬R.H. = 40%時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 74 圖5-2-4 模擬R.H. = 60%時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 76 圖5-2-5 比較不同相對濕度之進料氣體，對模擬旋轉填充床內部 (A)每單位質量的乾空氣所具有的水蒸氣質量 (B)液體之質量流速，隨徑向變化之影響 78 圖5-2-5 比較不同相對濕度之進料氣體，對模擬旋轉填充床內部 (C)液體溫度 (D)氣體溫度，隨徑向變化之影響 79 圖5-3-1 模擬G =40 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 82 圖5-3-2 模擬G =50 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 84 圖5-3-3 模擬G =60 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 86 圖5-3-4 模擬G =70 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 88 圖5-3-5 模擬G =80 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 90 圖5-3-6 比較不同體積流速之進料氣體，對模擬旋轉填充床內部 (A)液體之質量流速 (B)每單位質量的乾空氣所具有的水蒸氣質量，隨徑向變化之影響 93 圖5-3-6 比較不同體積流速之進料氣體，對模擬旋轉填充床內部 (C)液體溫度 (D)氣體溫度，隨徑向變化之影響 95 圖5-4-1 模擬L = 0.1 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 97 圖5-4-2 模擬L = 0.2 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 99 圖5-4-3 模擬L = 0.3 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 101 圖5-4-4 模擬L = 0.4 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 103 圖5-4-5 模擬L = 0.5 L/min時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 105 圖5-4-6 比較不同體積流速之進料液體，對模擬旋轉填充床內部 (A)每單位質量的乾空氣所具有的水蒸氣質量 (B)液體之質量流速，隨徑向變化之影響 108 圖5-4-6 比較不同體積流速之進料液體，對模擬旋轉填充床內部 (C)氣體溫度 (D)液體溫度，隨徑向變化之影響 110 圖5-5-1 模擬Tw = 40℃時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 ..112 圖5-5-2 模擬Tw = 45℃時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形.. 114 圖5-5-3 模擬Tw = 50℃時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 ..116 圖5-5-4模擬Tw = 55℃時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形.. 118 圖5-5-5模擬Tw = 60℃，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 …..120 圖5-5-6比較不同熱水溫度之進料液體，對模擬旋轉填充床內部 (A)液體溫度 (B)氣體溫度，隨徑向變化之影響 123 圖5-5-6 比較不同熱水溫度之進料液體，對模擬旋轉填充床內部 (C)液體之質量流速 (D)每單位質量的乾空氣所具有的水蒸氣質量，隨徑向變化之影響 123 圖5-6-1 模擬G/L= 40/0.2時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 126 圖5-6-2 模擬G/L = 50/0.2時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 128 圖5-6-3 模擬G/L = 60/0.2時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 130 圖5-6-4模擬G/L = 40/0.1時，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 132 圖5-6-5模擬G/L = 50/0.1，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形.. 134 圖5-6-6模擬G/L = 60/0.1，旋轉填充床內部 (A)液體溫度與氣體溫度 (B)每單位質量的乾空氣所具有的水蒸氣質量 (C)液體之質量流速，隨徑向變化之情形 ..136 圖5-6-7 比較不同之進料氣體與液體體積流速比，對模擬旋轉填充床內部液體之質量流速，隨徑向變化之影響；進料液體之體積流速為(A) 0.2 L/min (B) 0.1 L/min 139 圖5-6-7比較不同之進料氣體與液體體積流速比，對模擬旋轉填充床內部 (C)每單位質量的乾空氣所具有的水蒸氣質量 (D)液體溫度，隨徑向變化之影響 140 圖5-6-7 比較不同之進料氣體與液體體積流速比，對模擬旋轉填充床內部(E)氣體溫度，隨徑向變化之影響 141 圖6.1 溫度記錄器(iButton® DS1921G)於床體內部之位置 142 圖6-1-1 轉速為 (A) 500 rpm (B) 800 rpm時，旋轉填充床內部之T_iButton 隨徑向變化之情形 145 圖6-1-1 轉速為 (C) 1000 rpm (D) 1300 rpm時，旋轉填充床內部之T_iButton隨徑向變化之情形 146 圖6-1-2 轉速為800 rpm時，實驗量測旋轉填充床內部之T_iButton 與模擬旋轉填充床內部之Tw 、Ta與T_(iButton,est)，隨徑向變化之情形 147 圖6-2-1 轉速為 (A) 500 rpm (B) 800 rpm時，不同相對濕度之進料氣體下， 旋轉填充床內部之T_iButton隨徑向變化之情形 150 圖6-2-1 轉速為 (C) 1000 rpm (D) 1300 rpm時，不同相對濕度之進料氣體下， 旋轉填充床內部之T_iButton隨徑向變化之情形 151 圖6-2-2 轉速為800 rpm時，不同相對濕度之進料氣體對實驗與模擬結果之影響(A) 實驗量測之Ta,out；與模擬床體內部之Ta隨徑向變化之情形 (B) 實驗量測之Xa,out、Xa,in；與模擬床體內部之Xa隨徑向變化之情形 153 圖6-3-1 轉速為 (A) 500 rpm時，不同空氣體積流速之進料氣體下， 旋轉填充床內部之T_iButton隨徑向變化之情形 155 圖6-3-1 轉速為 (B) 800 rpm (C) 1000 rpm時，不同空氣體積流速之進料氣體下，旋轉填充床內部之T_iButton隨徑向變化之情形 156 圖6-3-1 轉速為 (D) 1300 rpm時，不同空氣體積流速之進料氣體下，旋轉填充床內部之T_iButton隨徑向變化之情形 157 圖6-3-2 轉速為800 rpm時，不同體積流速之進料氣體對實驗與模擬結果之影響 (A) 床體內部實驗量測之T_iButton與模擬之Tw、Ta，隨徑向變化之情形 (B) 實驗量測之Ta,out；與模擬床體內部之Ta隨徑向變化之情形 160 圖6-3-2 轉速為800 rpm時，不同體積流速之進料氣體對實驗與模擬結果之影響 (C) 實驗量測之Xa,out；與模擬床體內部之Xa隨徑向變化之情形 161 圖6-4-1 轉速為 (A) 500 rpm (B) 800 rpm時，不同熱水體積流速之進料液體下，旋轉填充床內部之T_iButton隨徑向變化之情形 163 圖6-4-1 轉速為 (C) 1000 rpm (D) 1300 rpm時，不同熱水體積流速之進料液體下，旋轉填充床內部之T_iButton隨徑向變化之情形 164 圖6-4-2轉速為800 rpm時，不同體積流速之進料液體對實驗與模擬結果之影響 (A) 床體內部實驗量測之T_iButton與模擬之Tw、Ta，隨徑向變化之情形 167 圖6-4-2轉速為800 rpm時，不同體積流速之進料液體對實驗與模擬結果之影響 (B) 實驗量測之Ta,out；與模擬床體內部之Ta隨徑向變化之情形(C) 實驗量測之Xa,out；與模擬床體內部之Xa隨徑向變化之情形 168 圖6-5-1 轉速為 (A) 500 rpm時，不同熱水溫度之進料液體下， 旋轉填充床內部之T_iButton隨徑向變化之情形 170 圖6-5-1 轉速為 (B) 800 rpm (C) 1000 rpm時，不同熱水溫度之進料液體下， 旋轉填充床內部之T_iButton隨徑向變化之情形 171 圖6-5-1 轉速為 (D) 1300 rpm時，不同熱水溫度之進料液體下， 旋轉填充床內部之T_iButton隨徑向變化之情形 172 圖6-5-2轉速為800 rpm時，不同熱水溫度之進料液體對實驗與模擬結果之影響 (A) 床體內部實驗量測之T_iButton與模擬之Tw、Ta，隨徑向變化之情形 (B) 實驗量測之Ta,out；與模擬床體內部之Ta隨徑向變化之情形 175 圖6-5-2轉速為800 rpm時，不同熱水溫度之進料液體對實驗與模擬結果之影響 (C) 實驗量測之Xa,out；與模擬床體內部之Xa隨徑向變化之情形 176 圖6-6-1 轉速為 (A) 500 rpm時，不同之進料氣液體體積流速比下， 旋轉填充床內部之T_iButton隨徑向變化之情形 178 圖6-6-1 轉速為 (B) 800 rpm (C) 1000 rpm時，不同之進料氣液體體積流速比下，旋轉填充床內部之T_iButton隨徑向變化之情形 179 圖6-6-1 轉速為 (D) 1300 rpm時，不同之進料氣液體體積流速比下， 旋轉填充床內部之T_iButton隨徑向變化之情形 180 圖6-6-2轉速為800 rpm時，不同進料氣液體積流速比對實驗與模擬結果之影響 (A) 床體內部實驗量測之T_iButton與模擬之Tw、Ta，隨徑向變化之情形 (B) 實驗量測之Ta,out；與模擬床體內部之Ta隨徑向變化之情形 183 圖6-6-2轉速為800 rpm時，不同進料氣液體積流速比對實驗與模擬結果之影響 (C) 實驗量測之Xa,out；與模擬床體內部之Xa隨徑向變化之情形 184 表目錄 表2-1-7.1 旋轉填充床應用於吸收與氣提程序 24 表2-1-7.1 旋轉填充床應用於吸收與氣提程序(續) 24 表2-1-7.2 旋轉填充床應用於蒸餾程序 25 表2-1-7.3 旋轉填充床應用於吸附與脫附程序 26 表2-1-7.4 旋轉填充床應用於結晶與顆粒製備 27 表2-1-7.4 旋轉填充床應用於結晶與顆粒製備(續) 27 表2-1-7.5 旋轉填充床之其他應用 28 表2-1-7.5 旋轉填充床之其他應用(續) 28 表4-1 旋轉填充床規格 50 表6-1-2 模擬計算所得到的T_(iButton,est)與實驗量測所得到的T_iButton之比較 147 表6-2-1.1進料氣體之相對濕度為40％時之實驗數據 148 表6-2-1.2進料氣體之相對濕度為30％時之實驗數據 148 表6-3-1.1進料氣體之空氣體積流速為50 L/min時之實驗數據 154 表6-3-1.2進料氣體之空氣體積流速為70 L/min時之實驗數據 154 表6-3-2.1進料空氣體積流速為50 L/min時，T_(iButton,est)與T_iButton之比較 158 表6-3-2.2進料空氣體積流速為70 L/min時，T_(iButton,est)與T_iButton之比較 158 表6-4-1.1進料液體之熱水體積流速為0.1 L/min時之實驗數據 162 表6-4-1.2進料液體之熱水體積流速為0.2 L/min時之實驗數據 162 表6-4-2.1進料液體之體積流速為0.1 L/min時，T_(iButton,est)與T_iButton之比較 165 表6-4-2.2進料液體之體積流速為0.2 L/min時，T_(iButton,est)與T_iButton之比較 166 表6-5-1.1進料液體之熱水溫度為50℃時之實驗數據 169 表6-5-1.2進料液體之熱水溫度為40℃時之實驗數據 169 表6-5-2.1進料液體之熱水溫度為40℃時，T_(iButton,est)與T_iButton之比較 173 表6-5-2.2進料液體之熱水溫度為50℃時，T_(iButton,est)與T_iButton之比較 173 表6-6-1.1進料氣體與液體之體積流速比為40/0.2時之實驗數據 177 表6-6-1.2進料氣體與液體之體積流速比為60/0.2時之實驗數據 177 表6-6-1.3進料氣體與液體之體積流速比為60/0.1時之實驗數據 177 表6-6-2.1進料氣液體積流速比例為40 /20時，T_(iButton,est)與T_iButton之比較 181 表6-6-2.2進料氣液體積流速比例為60 /20時，T_(iButton,est)與T_iButton之比較 181 表6-6-2.3進料氣液體積流速比例為60 /10時，T_(iButton,est)與T_iButton之比較 181 | |
| dc.language.iso | zh-TW | |
| dc.subject | 旋轉填充床 | zh_TW |
| dc.subject | 熱質傳數學模型 | zh_TW |
| dc.subject | 床體內部之溫度量測 | zh_TW |
| dc.subject | the measurement of temperature in the RPBl | en |
| dc.subject | rotating packed bed(RPB) | en |
| dc.subject | HIGEE | en |
| dc.subject | the heat and mass transfer mode | en |
| dc.title | 旋轉填充床內部之溫度分佈 | zh_TW |
| dc.title | The Temperature Profile in a Rotating Packed Bed | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 100-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 陳昱劭,林佳璋 | |
| dc.subject.keyword | 旋轉填充床,熱質傳數學模型,床體內部之溫度量測, | zh_TW |
| dc.subject.keyword | rotating packed bed(RPB),HIGEE,the heat and mass transfer mode,the measurement of temperature in the RPBl, | en |
| dc.relation.page | 199 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2012-08-01 | |
| dc.contributor.author-college | 工學院 | zh_TW |
| dc.contributor.author-dept | 化學工程學研究所 | zh_TW |
| 顯示於系所單位： | 化學工程學系 | |
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