跳到主要內容

簡易檢索 / 詳目顯示

研究生: 李元芬
Yuan-Fen Li
論文名稱: 矽酸乙酯與乙醇在不同壓力之相平衡
指導教授: 李亮三
Liang-Sun Lee
口試委員:
學位類別: 碩士
Master
系所名稱: 工學院 - 化學工程與材料工程學系
Department of Chemical & Materials Engineering
畢業學年度: 89
語文別: 中文
論文頁數: 63
中文關鍵詞: 相平衡乙醇矽酸乙酯
外文關鍵詞: tetraethyl orthosilicate, ethanol
相關次數: 點閱:4下載:0
分享至:
查詢本校圖書館目錄 查詢臺灣博碩士論文知識加值系統 勘誤回報
  • 本文所研究的系統為矽酸乙酯與乙醇兩成份分別在400mmHg以及180mHg兩個壓力下利用汽相循環式汽液平衡裝置進行汽液平衡實驗。兩組實驗數據均可以通過Herington熱力學一致性測試。
    同時,針對所得到的實驗數據選擇不同的液相模式進行迴歸, 在本研究中選擇Wilson, UNIQUAC以及UNIFAC三個模式迴歸計算而得到最佳參數。由得到的殘差值判斷,以UNIQUAC模式對於矽酸乙酯與乙醇系統的擬合度較好。
    再以統計學的F-分配來比較同組實驗數據用不同的模式迴歸所得到的參數的優劣,比較結果,以UNIQUAC模式最佳。


    In this study, the isobaric vapor-liquid equilibrium data for tetraethyl- orthosilicate and ethanol were measured at 400 and 180mmHg using a dynamic recirculating still. The experimental VLE data were proved to pass the thermodynamic consistency test.
    The maximum likelihood principle was chosen as regression method to estimate the parameters of Wilson equation, UNIFAC model, and UNIQUAC model. The results of estimation show that the UNIQUAC model correlated with the experimental data has the smallest values of Root-Mean-Square-Deviation (RMSD).
    The statistical method of F-test was used to compare the superiority among the above-mentioned models. The result of comparison shows that the UNIQUAC model correlated the experimental data best.

    中文摘要I 英文摘要II 目錄III 圖目錄V 表目錄VII 符號說明IX 第一章 緒論1 第二章 文獻回顧2 2-1低壓汽液平衡研究2 2-2數據迴歸與分析3 第三章理論與數據處理10 3-1汽液相平衡理論10 3-2汽液平衡數據處理13 3-2-1熱力學一致性檢測13 3-2-2 目標函數14 第四章 實驗15 4-1實驗藥品15 4-2分析儀器及設備15 4-3分析條件16 4-3-1乙醇-水兩成份低壓汽液平衡-測試實驗16 4-3-2矽酸乙酯-乙醇二成份低壓汽液平衡實驗16 4-4檢量線配製17 4-5低壓實驗步驟17 第五章 結果與討論18 5-1乙醇-水二成份汽液平衡測試實驗18 5-1-1乙醇-水兩成份檢量曲線18 5-1-2乙醇-水兩成份汽液平衡數據處理18 5-2矽酸乙酯-乙醇二成份汽液平衡實驗19 5-2-1矽酸乙酯-乙醇檢量曲線19 5-2-2矽酸乙酯-乙醇兩成份汽液平衡19 5-3 實驗數據分析21 5-3-1 系統誤差檢測21 5-3-2 一致性檢測22 5-3-3 估計變異數的檢定23 5-3-4 最適模式之選擇24 第六章 結論28 參考文獻29 附錄 A液相模式58 附錄 B 統計學分佈密度函數61

    Abbott, M. M., and H. C. Van Ness, “Vapor-Liquid Equilibrium: Part III. Data Reduction with Precise Expressions for GE,” AIChE J., 21(1), 62-71, (1975).
    Anderson, T. F., D. S. Abrams, and E. A. Grens, “Evaluation of Parameters for Nonlinear Thermodynamic Models,” AIChE J., 24(1), 20-29, (1978).
    Anderson, T. F., and J. M. Prausnitz, “Application of the UNIQUAC Equation to Calculation of Multicomponent Phase Equilibria. 1. Vapor Liquid Equilibria,” Ind. Eng. Chem. Process Des Dev., 17(4), 552-561, (1978).
    Cova, D. R. and R. K. Rains, “ Vapor-Liquid Equilibria in Hydrocarbon- Alcohol Systems n-Decane-1-Heptanol and n-Decane-2-Methyl-1-Hexanol,” J. Chem. Eng. Data, 19 (3), 251-253, (1974).
    Darwish, N. A., and A. A. Al-Khateib, ”Isobaric Vapor-Liquid Equilibria of the System Ethyl Acetate/n-Butanol at 70.5 and 94.0 kPa, ” Fluid Phase Equilibr., 126, 105-113, (1996).
    Darwish, N. A., and Z. A. Al-Anber, “Vapor-Liquid Equilibrium Measurements and Data Analysis of Tert-Butanol-Isobutanol and Tert-Butanol-Water Binaries at 94.9 kPa,” Fluid Phase Equilibr., 131, 287-295, (1997).
    Dohnal, V., and D. Fenclova, “A New Procedure for Consistency Testing of Binary Vapour-Liquid Equilibrium Data,” Fluid Phase Equilibr., 21, 211-235, (1985).
    Fabries, J. F., and H. Renon, “Method of Evaluation and Reduction of Vapor-Liquid Equilibrium Data of Binary Mixture,” AIChE J., 21(4), 735-742, (1975).
    Fredenslund, Aa., Jones, R. L. and Prausnitz, J. M., “Group contribution estimation of activity coefficients in nonideal liquid mixtures,” AIChE, J., 21, 1086-1099, (1975).
    Kemèny, S. and J. Manczinger, “Treatment of Binary Vapour-Liquid Equilibrium Data,” Chem. Eng. Sci., 33, 71-76, (1978).
    Kemeny, S., and J. Manczinger, ”Reduction of Thermodynamic Data by Means of the Multiresponse Maximum Likelihood Principle,” AIChE J., 28(1), 20-30, (1982).
    Larsen, B. L., Rasmussen, P. and Fredenslund, Aa., “A modified UNIFAC group contribution model for prediction of phase equilibria and heats of mixing,” Ind. Eng. Chem. Res., 26, 2274-2286, (1987).
    Ortega, J., and P. Hernandez, “Isobaric Vapor-Liquid Equilibria for Methyl Ester + Butan-2-ol at Different Pressures,” Fluid Phase equilibr., 118, 249-270, (1996).
    Pantio-Leal H. and P. M. Reilly, “ Statistical Estimation of Parameters in Vapor-Liquid Equilibrium,” AIChE J., 28(4) 580-587, (1982).
    Prausnitz, J. M., T. F. Anderson, E. A. Grens, C. A. Eckert, R. Hsieh, and J. P. O’Connell, “Computer Calculation Multicomponent Vapor-Liquid Equilibria,” Prentice-Hall Inc. Englewood Cliffs, N. J. (1980).
    Rao, K. V., A. Raviprased, and C. Chiranjivi, “ Isobaric Vapor-Liquid Equilibrium of binary Mixtures of 1-propanol + chlorobenzene and 1-butanol+chlorobenzene,” J. Chem. Eng. Data, 22 (1), 44-47, (1977).
    Rotter, J. M., and H. N. Knickle, “Isobaric Vapor-Liquid Equilibrium Data for the System n-Hexane-2-Propanol,” J. Chem. Eng. Data, 22(3), 246-248, (1977).
    Sutton T. L. and J. F. MacGreogor, “ The Analysis and Design of Binary Vapor-Liquid equilibrium Experiments Part I: Parameter Estimation and Consistency Tests.” The Can. J. Chem. Eng, 55, 602-608, (1977)
    Van Ness H. C., S. M. Byer, and R. E. Gibbs, “Vapor-Liquid Equilibrium,” Part I A Appraisal of Data Reduction Methods,” AIChE J., 19 (2) 238-244,(1973).
    Van Ness H. C., F. Pedersen, and P. Rasmussen, “Vapor-Liquid Equilibrium: Part V. Data Reduction by Maximum Likelihood,” AIChE J., 24(6), 1055-1063, (1978).
    Weidlich, U. and Gmehling, J., “ A modified UNIFAC model. 1. Prediction of VLE and HE,” Ind. Eng. Chem. Res., 26, 1372-1381, (1987).
    Wisniak J., and A. Tamir, “Vapor-Liquid in the System Propanol-Isopropylbenzene,” J. Chem. Eng. Data, 29, 171-180, (1984).
    黃士勳, 「丙烯醇-水共沸系統於72mmHg至常壓之汽液相平衡研究」,碩士論文,國立中央大學,中壢 (1992)。
    許秀菱,「正丙醇與異丁醇雙成份系統常壓下汽液相平衡之研究」,碩士論文,國立中央大學,中壢 (1994)。

    QR CODE
    :::