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  1. NTU Theses and Dissertations Repository
  2. 工學院
  3. 化學工程學系
請用此 Handle URI 來引用此文件: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/32768
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor陳誠亮(Cheng-Liang Chen)
dc.contributor.authorYou-Nian Laien
dc.contributor.author賴佑年zh_TW
dc.date.accessioned2021-06-13T04:15:09Z-
dc.date.available2006-07-28
dc.date.copyright2006-07-28
dc.date.issued2006
dc.date.submitted2006-07-25
dc.identifier.citation[1] Biegler, L.T., Grossmann, I.E., and Westerberg, A.W. Synthesis Methods of Chemical Process Design, Prentice Hall PTR, 1997.
[2] Bjork, K.M., and Pettersson, F. 'Optimization fo large-scale heat exchanger network synthesis problem,' In In IAESTED International Conference, Modeling and Simulation (2003), p. 313.
[3] Bjork, K.M., and Roger Nordmanb 'Solving large-scale retro t heat exchanger network synthesis problems with mathematical optimization methods,' Chem. Eng. Processing, vol. 44, pp. 869, 2005.
[4] Bjork, K.M., and Westerlund, T. 'Global optimization of heat exchanger network synthesis problems with and without the isothermal mixing assumption,' Comp. Chem. Eng., vol. 26, pp. 1581, 2002.
[5] Brooke, A., Kendrick. D., Meeraus, A., Raman, R., and Rosenthal, R. E. GMAS : A User's Guide, GAMS Development Corporation, 1988.
[6] Cerda, J. and Westerberg, A.W. 'Synthesizing heat exchanger networks having restricted stream/stream matches using transportation problem formulation,' Chem. Eng. Sci., vol. 38, pp. 1723, 1983.
[7] Chen, J.J.J. 'Letter to the editor: comments on improvement on a replacement for the logarithmic mean,' Chem. Eng. Sci., pp. 2488, 1987.
[8] Floudas, C.A. Nonlinear and Mixed-Integer Optimization: Fundamentals and Applications, Oxford Univ. Press, New York, 1995.
[9] Floudas, C.A., and Grossmann, I.E. 'Synthesis of flexible heat exchanger networks with uncertain flowrates and temperatures,' Comp. Chem. Eng., vol. 11, pp. 319, 1987.
[10] Floudas, C.A., Ciric, A.R., and Grossmann, I.E. 'Automatic synthesis of optimum heat exchanger network con gurations,' AIChE J, vol. 32, pp. 276, 1986.
[11] Furman, K.C., and Sahinidis, N.V. 'A critical review and annotated bibliography for heat exchanger network synthesis in the 20th century,' Ind. Eng. Chem. Res, vol. 41, pp. 2335, 2002.
[12] Konukman, A.E.S., Camurdan, M.C., and Akman, U. 'Simultaneousflexbility targeting and synthesis fo minimum-utility heat exchanger networks with superstructure-based MILP formulation,' Chem. Eng. Processing, vol. 41, pp. 501, 2002.
[13] Linnhoff, B., and Ahmad, S. 'Cost optimum heat exchanger networks-I. Minimum energy and captial using simple models for captial cost,' Comp. Chem. Eng., vol. 14, pp. 729, 1990.
[14] Linnhoff, B. and Flower, J.R. 'Synthesis of heat exchanger networks,' AIChE, vol. 24, pp. 633, 1978.
[15] Linnhoff, B., and Hindmarsh, E. 'The pinch design method for heat exchanger networks,' Chem. Eng. Sci., vol. 38, pp. 745, 1983.
[16] Linnhoff, B., Mason, D. and Wardle, I. 'Understanding heat exchanger networks,' Comp. Chem. Eng., vol. 3, pp. 91, 1979.
[17] Pettersson, F. 'Synthesis of large-scale heat exchanger networks using a sequential match reduction approach,' Comp. Chem. Eng., vol. 29, pp. 993, 2005.
[18] Shethna, H.K., Jezowski, J.M., and Castillo, F.J.L. 'A new methodology for simultaneous optimization and operating cost targets in heat exchanger network design,' App. The. Eng., vol. 20, pp. 1577, 2000.
[19] Tjoe, T.N., and Linnhoff, B. 'Using pinch technology for process retro t,' Chem. Eng., vol. 93, pp. 47, 1986.
[20] Yee, T.F., and Grossmann, I.E. 'Simultaneous optimization models for heat integration-II. Heat exchanger network synthesis,' Comp. Chem. Eng., vol. 14, pp. 1165, 1990b.
[21] Yee, T.F., Grossmann, I.E., and Kravanja, Z. 'Simultaneous optimization models for heat integration-I. Area and energy targeting and modeling fo multi-stream exchangers,' Comp. Chem. Eng., vol. 14, pp. 1151, 1990a.
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/32768-
dc.description.abstract本研究針對大規模的熱交換器網路設計提出一個分段完成的設計策略,並且考慮到多種且不固定位置之公用能源的使用。這個設計策略分成以下四個步驟:
1.先利用簡單的線性模式對所有程序 流體進行初步的配對;
2.再使用混合整數線性模式將第一步驟中不經濟的配對刪除;
3.將剩下的配對利用一個混合整數非線性模式區分成數個子群;
4.最後使用混合整數非線性模式對每個子群做各別的設計,再把每個子群的設計結果加總起來。
經由上述四個步驟,我們即可設計出大規模的熱交換器網路;不過,因為這是一個分段的設計策略,所以得到的解不能說是最好,但至少提供我們一個設計的方向。
在本論文最後,利用提出的設計策略對兩個範例進行設計,
用以應證其可行性,並且討論其優缺點。
zh_TW
dc.description.abstractThis thesis proposes a sequential design strategy for synthesis of large scale heat exchanger networks.The use of multiple utility at non-fixed position is considered.This strategy steps are:(1)process stream was matched roughly by using a simple linear model;(2)non-economic matches were removed form results of step1;(3)the surplus matches were decomposed into several subgroup;(4)each subgroup was designed individually by MINLP model and sum up result of subgroup.By the sequential strategy, we can design a large scale heat exchanger network.Though the sequential method can't guarantee obtaining solution, it is found that this proposed method can provide us acceptable results for large-scale HEN design problem.
Finally, two examples from literature are employed to demonstrate the applicability of the proposed strategy and discuss their advantage.
en
dc.description.provenanceMade available in DSpace on 2021-06-13T04:15:09Z (GMT). No. of bitstreams: 1
ntu-95-R93524082-1.pdf: 3035236 bytes, checksum: 99255dcee33f0ea9662c617063b5b3c5 (MD5)
Previous issue date: 2006
en
dc.description.tableofcontents1 緒論                          1
 1.1 前言............................................. 1
 1.2 熱交換器網路之發展介紹........................... 2
 1.3 文獻回顧......................................... 4
 1.4 研究動機與目的................................... 5
 1.5 組織章節......................................... 6
2 大規模熱交換器網路之設計流程建構            9
 2.1 設計流程建立之背景說明........................... 9
 2.2 設計流程之介紹................................... 10
 2.3 第一步驟 - 初步配對.............................. 11
   2.3.1 模式之符號、集合、系統參數與系統變數
      (Indices, Sets, Parameter, and Variable).. 11
   2.3.2 前置作業................................... 15
   2.3.3 目標函數與限制式
      (Objective Function and Constrains)....... 17
   2.3.4 輸出資訊(Output Data).................... 19
 2.4 第二步驟 - 配對縮減.............................. 19
   2.4.1 模式之符號、集合、系統參數與系統變數
      (Indices, Sets, Parameter, and Variable).. 20
   2.4.2 目標函數與限制式
      (Objective Function and Constrains)....... 22
   2.4.3 輸出資訊(Output Data).................... 23
 2.5 第三步驟 - 區分群組.............................. 24
   2.5.1 基本想法................................... 24
   2.5.2 模式之符號、集合、系統參數與系統變數
      (Indices, Sets, Parameter, and Variable).. 25
   2.5.3 目標函數與限制式
      (Objective Function and Constrains)....... 26
   2.5.4 輸出資訊(Output Data).................... 28
 2.6 第四步驟 - 群組各別計............................ 29
   2.6.1 模式之符號、集合、系統參數與系統變數
      (Indices, Sets, Parameter, and Variable).. 31
   2.6.2 目標函數與限制式
      (Objective Function and Constrains)....... 33
   2.6.3 輸出資訊(Output Data).................... 43
3 模式之情境模擬暨模擬結果分析與討論          45
 3.1 最適化軟體....................................... 46
 3.2 例一:小規模問題之情境模擬....................... 46
   3.2.1 例一之模擬結果分析與討論................... 47
 3.3 例二:大規模問題之情境模擬....................... 52
   3.3.1 例二之模擬結果分析與討論................... 54
4 結論與未來展望                    65
 4.1 結論............................................. 65
 4.2 未來展望........................................ 66
作者簡歷 71
dc.language.isozh-TW
dc.subject分段完成的方法zh_TW
dc.subject熱交換器網路zh_TW
dc.subject大規模zh_TW
dc.subject數學規劃法zh_TW
dc.subjectlarge scaleen
dc.subjectmathematical programming approachen
dc.subjectsequential methoden
dc.subjectheat exchanger networken
dc.title大規模熱交換器網路設計之研究zh_TW
dc.titleSynthesis of Large Scale Heat Exchanger Networken
dc.typeThesis
dc.date.schoolyear94-2
dc.description.degree碩士
dc.contributor.oralexamcommittee黃孝平(Hsiao-Ping Huang),余政靖(Cheng-Ching Yu),林顯聖,陳文智
dc.subject.keyword熱交換器網路,大規模,分段完成的方法,數學規劃法,zh_TW
dc.subject.keywordheat exchanger network,large scale,sequential method,mathematical programming approach,en
dc.relation.page71
dc.rights.note有償授權
dc.date.accepted2006-07-25
dc.contributor.author-college工學院zh_TW
dc.contributor.author-dept化學工程學研究所zh_TW
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