博碩士論文 90344001 詳細資訊




以作者查詢圖書館館藏 以作者查詢臺灣博碩士 以作者查詢全國書目 勘誤回報 、線上人數:32 、訪客IP:18.220.97.161
姓名 林慶峰(Ching-Feng Lin)  查詢紙本館藏   畢業系所 化學工程與材料工程學系
論文名稱 無參數模式預測非均相混合物的共沸點
(A prediction algorithm for homogeneous and heterogeneous azeotrpes by parameter-free models)
相關論文
★ 高速旋轉填充床應用於分離異丙醇-水共沸混合物之研究★ 水-醋酸-對位二甲苯-乙酸甲酯-乙酸異丁酯之汽液平衡
★ 進料不純物作為系統內自體共沸劑模擬回收醋酸之醋酸脫水程序及其效益分析★ 單電解水溶液離子活性係數與溫度之關係
★ 在超臨界CO2之溶解度量測及Poynting factor之探討★ 矽酸乙酯與乙醇在不同壓力之相平衡
★ 水-酚-對甲酚-鄰甲酚四成份系統之液液相平衡研究★ 單電解質水溶液離子活性係數之探討
★ 高速旋轉填充床於分離共沸混合物之研究★ 乙烯在甲苯、冰片烯及COC混合溶液之溶解度量測與關聯
★ 間氯酚與對氯酚之固液相平衡研究★ 高速旋轉填充床於分離乙醇-水共沸混合物之研究
★ 二價單電解質水溶液之個別離子活性係數 量測與關聯★ 雙參數個別離子活性係數模式應用於雙電解質水溶液蒸汽壓之估算
★ β-胡蘿蔔素-二丁基羥基甲苯於超臨界二氧化碳之溶解度量測與關聯★ 共溶劑對β-胡蘿蔔素於超臨界二氧化碳溶解度影響之研究
檔案 [Endnote RIS 格式]    [Bibtex 格式]    [相關文章]   [文章引用]   [完整記錄]   [館藏目錄]   [檢視]  [下載]
  1. 本電子論文使用權限為同意立即開放。
  2. 已達開放權限電子全文僅授權使用者為學術研究之目的,進行個人非營利性質之檢索、閱讀、列印。
  3. 請遵守中華民國著作權法之相關規定,切勿任意重製、散佈、改作、轉貼、播送,以免觸法。

摘要(中) 本論文主要的研究目的在於使用四種無參數活性係數模式來預估及計算均相及非均相混合物的共沸溫度及組成。在數學技巧上用以完成非線性計算是採用牛頓-拉普森法(Newton-Rapson method)及虛擬弧長連續法(pseudo-arclength continuation)及同倫法(homotopy)的觀念。對於液相活性係數的估算是採用下列四種無參數模式:Scatchard-Hildebrand、UNIFAC、Vetere-NRTL、及Ash-Wilson等方法。
對於本論文的資料來源是採用Horsley資料書及文獻所搜集的共沸系統數據取得之共沸點文獻值。首先,我們以無參數活性係數模式演算Lee等預估均相共沸混合物的性質,其結果獲得很好的一致性。再者,我們成功的預估混合物的共沸溫度及組成,並發現許多在Horsley資料中的均相共沸物都呈現為非均相行為於預估及計算過程。藉由比較分析提出各無參數活性係數模式的預測能力,並提出一個預測混合物系統共沸點的建議流程及程序說明。
摘要(英) In this study, the capabilities of four parameter-free models for predicting the heterogeneous and homogeneous azeotropic behavior of multi-component mixtures were evaluated. The present work was basically extended from that of Lee et al. (1996) for homogeneous azeotrope determination. The mathematical techniques of Newton-Raphson, pseudo-archlength continuation and concept of homotopy were used to accomplish the mathematical computations. Four parameter-free models, Schatchard-Hildebrand (1931); UNIFAC (1975); Vetere-NRTL (1994); and Ash-Wilson (1992), were employed for liquid phase activity coefficient estimations. The azeotropic mixtures from Horsley’s data book were adopted for this study. We have succeeded in predicting the azeotropic temperatures and compositions in these mixtures. It is very interesting and important to observe that many homogeneous azeotropes in Horsley’s data book (1973) appeared to be heterogeneous in our calculations.
關鍵字(中) ★ 共沸混合物
★ 預測
★ 無參數模式
關鍵字(英) ★ Azeotropic mixture
★ Parameter-free model
★ Prediction
論文目次 第一章 緒論 1
1-1 前言 1
1-2 共沸物研究之回顧 2
第二章 理論分析 6
2-1 汽液相平衡理論 6
2-1-1 汽相逸壓係數 8
2-1-2 活性係數 9
2-2尋求共沸組成與溫度之數值方法
2-2-1 液液相平衡的分析及求解 10
2-2-2 非均相共沸混合物汽液相平衡的分析及求解 12
第三章 無參數活性係數模式 15
3-1 Scatchard-Hildebrand模式 16
3-2 Ash-Wilson模式 18
3-3 Vetere-NRTL模式 21
3-4 UNIFAC 模式 24
第四章 無參數活性係數模式預測結果與討論 26
4-1 系統分類 26
4-2 資料庫的建構 27
4-3 資料流程設計 28
4-4 程式程序設計 28
4-5 系統的測試 28
4-6 非均相共沸系統 29
4-7 不同壓力之共沸預測 32
4-8 連續數值合併同倫法之預測及演算 32
第五章 結論 35
參考文獻 36
圖 42
表 55
附錄A Correlation equations for calculating parameters of Vetere –NRTL model 77
附錄B Sequence number for chemicals in data bank 79
附錄C Dataset format 80
附錄D The computation procedure of the program 84
附錄E Computer program description 85
附錄F Hierarchy of program 89
參考文獻 Abrams, D.S. and J.M. Prausnitz, "Statistical Thermodynamics of Liquid Mixture: A New Expression for the Excess Gibbs Energy of Partly or Completely Miscible System," AIChE J., 21, 116(1975).
Ash, S.N., P. Ray and B.K. Dutta, "Activity Coefficients for Binary and Multicomponent Liquid Mixtures from Unary Property Model for Wilson Parameters," AIChE J., 31(5), 821(1985).
Ash, S.N. "Group Unary Wilson Model for Liquid Mixtures without Arbitrary Parameters," Chem. Eng. J., 48, 183(1992).
Bondi, A. "Physical Properties of Molecular Crystals, Liquids, and Gases," Wiley, New York(1968).
Bruin, S. and J.M. Prausnitz, "One-Parameter Equation for Excess Gibbs Energy of Strongly Nonideal Liquid Mixtures," Ind. Eng. Chem. Process Des. Dev., 10(4), 562(1971).
Connemann, M., J. Gaube, L. Karrer, A. Pfennig, and U. Reuter, “Measurement and Representation of Ternary Vapor-Liquid-Liquid Equilibria”, Fluid Phase Equilibria, 60, 99 (1990).
Doedel, E., H.B. Keller, and J.P. Kernevez, "Numerical Analysis and Control of Bifurcation Problems (I) Bifurcation in Finite Dimension," Int. J. Bifurcation and Chaos, 1(3), 493(1991).
Eckert, E. and M. Kubicek, “Computing Heterogeneous Azeotropes in Multicomponent Mixtures”, Computers Chem. Engng., 21, 347 (1997).
Eduljee, G.H. and K.K. Tiwari, "Correlation of Azeotrope Data," Chem. Eng. Sci., 31,535(1976).
Fidkowski, Z.T., M.F. Malone and M.F. Doherty, "Computing Azetropes in Multicomponent Mixture," Computers Chem. Eng., 17(12), 1141(1993)
Fredenslund, A., R.L. Jones and J.M. Prausnitz, "Group-Contribution estimation of Activity Coefficients in Nonideal Liquid Mixtures," AIChE J., 21(6), 1086(1975).
Genco, J.M., A.S. Teja and W.B. Kay, "Study of the Critical and Azeotropic Behavior of Binary Mixtures. 2. PVT-x Data and Azeotropic States of Perfluoromethylcyclohexane-Isomeric Hexane Systems," J. Chem. Eng. Data, 25, 355(1980).
Ghosh, S.K. and S.J. Chopra, "Activity Coefficients from the Wilson Equation," Ind. Eng. Chem. Process Des. Dev., 14(3), 304(1975).
Gmehling, J., U. Onken and W. Arlt, "Vapor-Liquid Equilibrium Data Collection ", DECHEMA, Frankfurt am Main, Germany (1981).
Gmehling, J., P. Rasmussen and A. Fredenslund, "Vapor-Liquid Equilibria by UNIFAC Group Contribution. Revsion and Extension. 2," Ind. Eng. Chem. Process Des. Dev., 21, 118(1982).
Gothard, F.A., M.F.C. Ciobanu, D.G. Breban, C. I. Bucur and G. V. Sorescu, "Predicting the Parameters in the Wilson Equations for Activity Coefficients in Binary Hydrocarbon Systems," Ind. Eng. Chem. Process Des. Dev., 15(2), 333(1976).
Hankinson, R.W., B.D. Langfitt and D.P. Tassios, "A Single Parameter Equation for the Prediction of Multicomponent Vapor-Liquid Data from Binary Isobaric Data," Can. J. Chem. Eng., 50, 511(1972).
Hayden, J.G. and J.P. O'Connell, "A Generalized Method for Predicting Second Virial Coefficients," Ind. Eng. Chem. Process Des. Dev., 14(3), 209(1975).
Hildebrand, J.H. and S.E. Wood, "The Derivation of Equations for Regular Solutions," J. Chem. Phys., 1(12), 817(1933).
Hiranuma, M., "Parameters in Wilson Equation," Ind. Eng. Chem. Process Des. Dev., 11, 631(1972).
Hiranuma, M. and K. Honma, "Estimation of Unlike-Pair Potential Parameter in Single-Parameter Wilson Equation," Ind. Eng. Chem. Process Des. Dev., 14(3), 221(1975).
Horsley, L.H., "Azeotropic Data-III," American Chemical Society, Washington, D.C.(1973).
Keller, H.B., "Numerical Solution of Bifurcation and Nonlinear Eigenvalue Problems," in Applications of Bifurcation Theory, ed. Rabinowitz, P. H. (Academic Press), 359-384(1977).
Kurtyka, Z.M. and A. Kurtyka,"Azeotropic Composition from the Boiling Point of Components and of the Azeotropes," Ind. Eng. Chem. Fundam., 19, 225(1980).
Krumins, A.E., A.K. Rastogi, M. E. Rusak and D. Tassios, "Prediction of Binary Vapor-Liquid Equilibrium from One-Parameter Equation," Can. J. Chem. Eng., 58, 663(1980).
Ladurelli, A.J., C.H. Eon and G. Guiochon, "Failibilities Inherent in the Wilson Equation Applied to Systems Having a Negative Excess Gibbs Energy,"Ind. Eng. Chem. Fundam., 14(3), 191(1975).
Lee, L. S., H. L. Kang, and M. Z. Kuo, “Prediction of Azeotrope by Activity Coefficient Models without Parameters,” J. Chin. I. Ch. E., 27, 295 (1996)
Malesinski, W., "Azeotropy and Other Theoretical Problems of Vapor-Liquid Equilibrium," Interscience, New York, N. Y.(1965).
Prausnitz, J.M., T.F. Anderson, E.A. Grens, C.A. Eckert, R. Hsieh, and J.P. O'Connell, "Computer Calculations for Multicomponent Vapor-Liquid and Liquid-Liquid Equilibria," Englewood Cliffs, N. J. : Prentic-Hall, Inc.(1980).
Prausnitz, J.M., R.N. Lichtenthaler and E.G. Azevedo, "Molecular Thermodynamics of Fluid-Phase Equilibria," Second Edition, Englewood Cliffs, N. J. : Prentic-Hall, Inc.(1986).
Reid, R.C., J.M. Prausnitz and B.E. Poling "The Properties of Gases & Liquid," Fourth Edition, McGraw-Hill, New York(1987).
Renon, H. and J.M. Prausnitz, "Local Composition in Thermodynamic Excess Functions for Liquid Mixtures," AIChE J., 14(1), 135(1968).
Sandler, S.I., "Chemical and Engineering Thermodynamics," Second Edition, John Wiley & Sons, Singapore(1989).
Scatchard, G., "Equilibria in Non-Electrolyte Solutions in Relation to the Vaopr Pressures and Densities of the Components," Chem. Rev., 8, 321(1931).
Schreiber, L.B. and C.A. Eckert, "Use of Infinite Dilution Activity Coefficients with Wilson's Equation," Ind. Eng. Chem. Process Des. Dev., 10(4), 572(1971).
Seydel, R., "Tutorial on Continuation," Int. J. Bifurcation and Chaos, 1(1), 3(1991).
Sorensen, J.M. and W. Arlt, “Liquid-Liquid Equilibrium Data Collection “, DECHEMA, Frankfurt am Main, Germany (1979).
Spencer, C.F. and R.P. Danner, "Improved Equation for Prediction of Saturated Liquid Density," J. Chem. Eng. Data, 17(2), 236(1972).
Stephan, K. and W. Wagner, "Application of the Wilson equation to Azeotropic Mixtures," Fluid Phase Equilibria, 19, 201(1985).
Swietoslawski, W., "Azeotropy and Polyazeotropy," Pergamon Press, Oxford, London(1963).
Seymour, K.M., R.H. Carmichael, J.Carter, J. Ely, E. Isaacs, J. King, R. Naylor, and T. Northern, "An Empirical Correlation among Azeotropic Data," Ind. Eng. Chem. Fumdam., 16(2), 200(1977).
Tamir, A. "New Correlations for Fitting Multicomponent Vapor-Liquid Equilibria Data and Prediction of Azetropic Behavior," Chem. Eng. Sci., 36(9), 1453(1981).
Tamir, E., A. Tamir, and M.B. King, "Explaining Characteristic Azeotropic Behaviour," Chem. Eng. Sci., 36, 759(1980).
Tanaka, T., "Attempting the Predicition of an Azeotrope and Its x-y Curve on the Basis of the Molecular Parameters," Fluid Phase Equilibria , 24, 187(1985).
Tassios, D., "A Single-Parameter Equation for Isothermal Vapor-Liquid Equilibrium Correlations," AIChE J., 17(6), 1367(1971).
Tochigi, K., H. Inoue and K. Kojima, "Determination of Azeotropes in Binary Systems at Reduced Pressures," Fluid Phase Equilibria, 22, 343(1985).
Vetere, A., "Prediction of Vapor-Liquid Equilibria of Non-Aqueous Systems in the Subcritical Range by Using the NRTL Equation," Fluid Phase Equilibrium, 91 265(1993).
Vetere, A., "Prediction of Vapor-Liquid Equilibria of Aqueous Systems in the Subcritical Range by Using the NRTL Equation," Fluid Phase Equilibrium, 99, 63(1994).
Wilson, G.M.,"Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing," J. Am. Chem. Soc., 86, 127(1964).
Wong, K.F., and C.A. Eckert, "Dilute Solution Behavior of Two Cyclic Anhydrides," Ind. Eng. Chem. Fundam., 10(1), 20(1971).
指導教授 李亮三(Liang-Sun Lee) 審核日期 2007-1-11
推文 facebook   plurk   twitter   funp   google   live   udn   HD   myshare   reddit   netvibes   friend   youpush   delicious   baidu   
網路書籤 Google bookmarks   del.icio.us   hemidemi   myshare   

若有論文相關問題,請聯絡國立中央大學圖書館推廣服務組 TEL:(03)422-7151轉57407,或E-mail聯絡  - 隱私權政策聲明