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研究生: 吳泰斌
Wu, Tia-Bin
論文名稱: 應用耦合化學反應動力之計算流體力學模式於挾帶床氣化爐之數值模擬分析
Numerical Simulation Analyses of an Entrained-bed Gasifier Using a CFD Model Coupled with Chemical Reaction Kinetics
指導教授: 江滄柳
Jiang, Tsung-Leo
王振源
Wang, Chen-Yuan
學位類別: 碩士
Master
系所名稱: 工學院 - 航空太空工程學系
Department of Aeronautics & Astronautics
論文出版年: 2011
畢業學年度: 99
語文別: 中文
論文頁數: 95
中文關鍵詞: 挾帶床氣化爐氣化數值模擬
外文關鍵詞: entrained-bed, gasification, numerical simulation.
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  • 煤炭氣化技術之應用,可有效降低燃燒煤炭產生之污染對環境造成衝擊,並可應用於高效率IGCC系統中,以達到43%以上之發電效率。而在其相當複雜之氣化過程當中,其化學動力反應機制是粉煤燃燒氣化過程之關鍵,必須要能掌握在氣化爐進料的化學動力反應的細節,才能進一步掌握以計算流體力學模擬氣化爐內燃燒與氣化等模擬結果之品質。故本文以挾帶床氣化爐為研究目標,建立一包含化學動力反應機制之完整多相紊流燃燒數值分析模式。參考實驗組之入口條件以及煤炭成分,使用商用計算軟體FLUENT模擬比對其出口成份和出口溫度,並建立一整合FLUENT計算流體力學軟體及CHEMKIN化學反應運算軟體之完整數值計算模式。其模擬結果與實驗比較,在各出口成分之比重之趨勢與實驗結果一致,出口溫度則是略高實驗值約71.6K。而在三組參數分析上:氣化爐壁面溫度測試、煤炭燃料含水比例測試以及二級式進料方式之設計,分別來評估最佳之產氫效能,其氣化爐壁面溫度在較低時,有助於產氫效能之提升;煤炭燃料含水比例測試,則會隨著加水量提高,出口成分氫氣亦隨之提高,達到產氫效能之提升;二級進料之方式,對出口產氫效能之有助於提升,且在溫度分布上,會導致出口溫度降低。

    Coal gasification technique is an effective and alternative method to reduce the environmental pollution by the traditional coal combustion. It also can be incorporated into the IGCC (Integrated Gasification Combined Circle) system and the attainable generation efficiency is 43%. The reaction kinetics of the coal oxidation/gasification is the essential part of the complicated gasification process. Reliable computational results can only be obtained when mastering the chemical reaction mechanism of the gasification reactor. The object of the present study is to develop the multi-phase, turbulent-combustion model incorporated with the detailed chemical reaction mechanism of the entrained-bed gasifier. Operating conditions, employed coal properties, outlet composition and temperature to be compared were adopted from the cited experimental study. The numerical model was built by the commercial software, FLUENT, integrated with the proposed CHEMKIN reaction mechanism. The tendency to the outlet temperature is consistent with experiment, and the outlet temperature has higher about 71.6 K . The effects of three operating parameters, i.e., the gasifier wall temperature, the steam fraction of fuel and the two-stage feeding design, on the gasification performance were investigated. Hydrogen fraction and mass flow rate at outlet increase with lower wall temperature of gasifier and with the increase of the steam fraction of fuel. Numerical results indicated that the effects of the two-stage feeding design on the gasification performance are improved, and caused outlet temperature to reduce.

    摘要 II ABSTRACT III 致謝 V 表目錄 IX 圖目錄 X 第一章、緒論 1 1.1研究背景 1 1.2氣化方式與原理 3 1.3文獻回顧 7 1.4研究動機及目的 23 第二章、物裡與數學模式 24 2-1問題假設 24 2-2連續相-守恆方程式 25 2-3分離相-傳輸式程式 27 2-4煤粒之相關性質 32 2-5非預混燃燒之FLAMELET模型 32 2-6 FLUENT結合CHEMKIN格式化學反應動力式之模型建立 34 2-7氣化如爐-幾何尺寸與入口條件 36 第三章 數值方法 37 3.1 計算程序 37 3.2 SIMPLE-運算法則 38 3.3 收斂標準 41 第四章 結果與討論 42 4.1 離散相追蹤參數分析 43 4.2 NON-PREMIXED COMBUSTION之PDF表格 45 4.3 出口成份結果與比較 45 4.4 與商用化學計算軟體CHEMKIN-CFD之結果比較 47 4.5 不同爐體壁面溫度之氣化效能評估 48 4.6 不同煤炭含水量之氣化效能評估 49 4.7 氣化爐分段進料之氣化效能評估 50 第五章 結論與建議 53 參考文獻 56 自述 94 著作權聲明 95

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