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研究生: 林立杰
Li-Jie Lin
論文名稱: Alpha-亞麻酸與正丁醇之非均相酯化反應動力行為研究
Kinetic Behavior Study on the Heterogeneous Esterification of 𝛂-Linolenic Acid with 1-Butanol
指導教授: 李明哲
Ming-Jer Lee
口試委員: 吳紀聖
Chi-Sheng Wu
陳良益
Liang-Yih Chen
學位類別: 碩士
Master
系所名稱: 工程學院 - 化學工程系
Department of Chemical Engineering
論文出版年: 2018
畢業學年度: 106
語文別: 中文
論文頁數: 101
中文關鍵詞: 反應動力Alpha-亞麻酸正丁醇非均相反應酯化反應觸媒反應
外文關鍵詞: Kinetic, 𝛂-Linolenic Acid, 1-Butanol, Heterogeneous reaction, Esterification, catalytic reaction
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  • 本研究使用批式反應器探討由α-亞麻酸與正丁醇合成α-亞麻酸正丁酯合成反應之非均相反應動力行為,反應中使用酸性陽離子交換樹脂Amberlyst 39為觸媒。實驗操作於343.15 K至363.15 K之間,並探討(醇/酸)進料莫耳比、觸媒質傳阻力以及觸媒添加量之效應。
    反應動力實驗結果顯示,隨著反應溫度的升高,反應速率能有效地加快,此外平衡轉化率也有些微的提升;而(醇/酸)進料莫耳比、觸媒量的提高,反應速率也有明顯得提升;此外,觸媒顆粒及轉速的改變對反應速率無顯著差異,由此得知本研究之實驗條件皆操作在非質傳阻力影響之前提下。
    α-亞麻酸正丁酯合成反應動力數據分別以理想溶液擬均相模式、非理想溶液擬均相動力模式、Eley-Rideal模式以及Langmuir-Hinshelwood-Hougen-Watson模式關聯,並求得最適化的動力參數值,NRTL模式則用於計算各反應成分之活性係數,關聯的結果顯示LHHW模式為描述α-亞麻酸正丁酯合成反應的非均相催化動力行為的最佳模式。


    The heterogeneous kinetics behavior was investigated with a batch reactor for the synthesis of linolenic acid n-butyl ester from linolenic acid and n-butanol over the cation-exchange resins, Amberlyat 39. The experiments were conducted at tempertures from 343.15 K to 363.15 K. Additionally, the effects of molar ratio of alcohol to acid in the feed stream, the mass transfer resistances on the catalytic reaction, and the different levels of catalyst loadings were also observed.
    Both reaction rate and equilibrium conversion of acid increased with increase of reaction temperature, while increasing molar ratio of alcohol to acid in the feed stream and catalyst loading increase the reaction rate. It was also found that the reaction rate is not apparently different when operating at different agitation rates and different particle sizes of catalyst. Therefore, these results show that the mass transfer resistances are neglegible over the entire operating conditions.
    The kinetic data of the synthesis of linolenic acid n-butyl ester were correlated with the ideal-quasi-homogeneous (IQH), the non-ideal-quasi-homogeneous (NIQH), the Eley-Rideal (ER), and the Langmuir-Hinshelwood-Hougen-Watson (LHHW) models, respectively. The NRTL model was used to calculate the activity coefficients for each reacting species. The optimal values of the kinetic parameters were determined from the data fitting. The LHHW model yielded the best representation for the kinetic behavior of heterogeneous catalytic synthesis of linolenic acid n-butyl ester.

    第一章 緒論 1 1-1 前言 1 1-2文獻回顧 3 1-3 本研究之重點 19 第二章 反應動力實驗 26 2-1 酯化反應動力數據量測 26 2-2 藥品 30 2-3 實驗步驟 31 2-4 組成分析 32 2-5 數據處理 35 2-6 動力反應實驗結果 37 2-7 結果與討論 38 第三章 反應動力數據關聯 58 3-1 動力模式 58 3-2理想溶液擬均相動力模式 59 3-3非理想溶液動力模式 62 3-4 速率常數與吸附常數的訂定 64 3-5 α-亞麻酸正丁酯之動力模式關聯結果 66 3-6 非理想溶液之平衡常數 67 第四章 結論與建議 86 4-1 結論 86 4-2 建議與注意事項 88 參考文獻 90 符號說明 97 附錄A觸媒篩目粒徑對照表 101

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