請用此 Handle URI 來引用此文件：
http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/67813完整後設資料紀錄
| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 吳哲夫(Jeffrey D. Ward) | |
| dc.contributor.author | Yuan-Wei Ni | en |
| dc.contributor.author | 倪沅煒 | zh_TW |
| dc.date.accessioned | 2021-06-17T01:51:24Z | - |
| dc.date.available | 2022-07-27 | |
| dc.date.copyright | 2017-07-27 | |
| dc.date.issued | 2017 | |
| dc.date.submitted | 2017-07-24 | |
| dc.identifier.citation | [1] Roger W. Thompson, C. Judson King. System Synthesis of Separation Schemes. AIChE Journal. 1972; 18(3): 941-948.
[2] King, C. J. Separation Processes. McGraw-Hill, New York, 2nd ed. 1980. [3] Andrecovich, M. J.; A. W. Westerberg. A Simple Synthesis Method Based on Utility Bounding for Heat-Integrated Distillation Sequences. AIChE Journal. 1985(b); 31: 363-375. [4] Nishida N.; G. Stephanopoulous; A. W. Westerberg. A review of process synthesis. AIChE Journal 1981, 27, 321-351. [5] Tedder D. W; Rudd D. F. Parametric Studies in Industrial Distillation Part I. Design Comparisons. AIChE Journal 1978, 24, 303-315. [6] Stephanopoulos G; Westerberg A. W. Studies in Process Synthesis–II. Evolutionary Synthesis of Optimal Process Flowsheets. Chemical Engineering Science 1976, 31, 195-204. [7] Malone M. F.; K. Glinos; F. E. Marquez; J. M. Douglas. Simple analytical criterion for the sequencing of distillation columns. AIChE Journal 1985, 31, 686-689. [8] P. B. Gadkari; R. Govind. Analytical Screening Criterion for Sequencing of Distillation Columns. Computer & Chemical Engineering 1988, 12, 1199-1213. [9] M. Bezzina; L. Pibouleau; S. Domenech. A Statistical Approach to the Synthesis of Separation Sequences. Computer & Chemical Engineering 1989, 13, 651-660. [10] F. Martins; Carlos A. V. Costa. Economic, Environmental and Mixed Objective Functions in Non-Linear Process Optimization Using Simulated Annealing and Tabu Search. Computer & Chemical Engineering 2010, 34, 306-317. [11] Chaudhuri, P. D.; Diwekar, U. M. Process Synthesis under Uncertainty: A Penalty Function Approach. AIChE Journal 1996, 42, 742-752. [12] Floquet, P.; L. Pibouleau.; S. Domenech. Separation Sequence Synthesis: How to Use Simulated Annealing Procedure? Computer. Chem. Eng 1994, 18, 1141-1148. [13] An, W-Z.; Yuan X-G. A Simulated Annealing-Based Approach to the Optimal Synthesis of Heat-Integrated Distillation Sequences. Computers and Chemical Engineering 2009, 33, 199-212. [14] F. Wang; Y. Luo; X. Yuan; A Formulation Methodology for Multicomponent Distillation Sequences Based on Stochastic Optimization. Chinese Journal of Chemical Engineering 2016, 24, 1229-1235.F [15] Dolan, W. B.; Cummings, P. T.; Levan, M. D. Process Optimization Via Simulated Annealing - Application to Network Design. AIChE Journal 1989, 35, 725-736. [16] Y. Wang; G. Bu; T. Wang; T. Zhao; Z. Zhang; Z. Zhu. Application of A Simulated Annealing Algorithm to Design and Optimize a Pressure-Swing Distillation Process. Computer & Chemical Engineering 2016, 95, 91-107. [17] Cheng, J.-K; Lee, H.-Y; Huang H.-P; Yu C.-C. Optimal steady-state design of reactive distillation processes using simulated annealing. Journal of the Taiwan Institute of Chemical Engineers 2009, 40, 188-196. [18] F. I. Gómez-Castro; J. G. Segovia-Hernández; S. Hernández; C. Gutiérrez-Antonio; A. Briones-Ramírez. Dividing Wall Distillation Columns: Optimization and Control Properties. Chemical Engineering & Technology 2008, 31, 1246-1260. [19] Boozarjomehry R. B.; A. Pourahmadi Laleh; W. Y. Svrcek. Automatic Design of Conventional Distillation Column Sequence by Genetic Algorithm. The Canadian Journal of Chemical Engineering 2009, 87, 477-492. [20] Boozarjomehry R. B.; A. Pourahmadi Laleh; W. Y. Svrcek. Evolutionary Design of Optimum Distillation Column Sequence. The Canadian Journal of Chemical Engineering 2012, 90, 956-972. [21] J. Leboreiro; J. Acevedo. Process Synthesis and Design of Distillation Sequences Using modular Simulators: A Genetic Algorithm framework. Computers & Chemical Engineering 2004, 28, 1223-1236. [22] P. Linke; A. Kokossis. On the Robust Application of Stochastic Optimization Technology for the Synthesis of Reaction/Separation Systems. Computer & Chemical Engineering 2003, 27, 733-758. [23] Chan, L. M.; Srinivasan, R.; A Hybrid CPU-Graphics Processing Unit (GPU) Approach for Computationally Efficient Simulation-Optimization. Computer & Chemical Engineering 2016, 87, 49-62. [24] Fu, M.C.; Glover, F.W. Simulation Optimization: A Review, New Developments, and Application. Winter Simul Conf Proc. 2005, 83-95. [25] Carson Y.; Maria A. Simulation Optimization: Methods and Applications. Winter Simul Conf Proc. 1997, 118-126. [26] Tekin E.; Sabuncuoglu I. Simulation Optimization: A Comprehensive Review on Theory and Applications. IIE Trans. 2004, 36, 1067-1081. [27] Jang, W. H.; Hahn, J.; Hall, K. R. Genetic/Quadratic Search Algorithm for Plant Economic Optimizations Using a Process Simulator. Computers & Chemical Engineering 2005, 30, 285-294. [28] Ram N. S. Rathore; Kenneth A. Van Wormer; Gary J. Powers. Synthesis Strategies for Multicomponent Separation Systems with Energy Integration. AIChE Journal 1974, 20, 491-502. [29] Andrecovich, M. J.; A. W. Westerberg. An MILP Formulation for Heat-Integrated Distillation Sequence Synthesis. AIChE Journal 1985(a), 31, 1461-1474. [30] Andrecovich, M. J.; A. W. Westerberg. Utility Bounds for Nonconstant QΔT for Heat-Integrated Distillation Sequence Synthesis. AIChE Journal 1985(c), 31, 1475-1479. [31] C. A. Floudas; G. E. Paules IV. A Mixed-Integer Nonlinear Programming Formulation for the Synthesis of Heat-Integrated Distillation Sequences. Computers & Chemical Engineering 1988, 12, 531-546. [32] Jaroslav, J.; Radim Ptacnlk. Synthesis of heat integrated rectification systems. Comput. Chem. Engng 1988, 12, 427-432. [33] Wang, K.; Qian, Y.; Yuan, Y.; Yao, P. Synthesis and Optimization of Heat Integrated Distillation Systems Using an Improved Genetic Algorithm. Computers and Chemical Engineering 1998, 23, 125-136. [34] Seider, W. D.; Seader, J. D.; Lewin, D. R., Product & Process Design Principles: Synthesis, Analysis and Evaluation, (with CD). 3 ed.; John Wiley & Sons: 2009. [35] Aspen Plus User Guide Version 10.2 [36] Metropolis N.; Rosenbluth, A. W.; Rosenbluth, M. N.; Teller, A. H.; Teller, E. Equation of State Calculations by Fast Computing Machines. Journal of Chemical Physics 1953, 21. [37] Kirkpatrick, S.; Gelatt, C. D.; Vecchi, M. P. Optimization by Simulated Annealing. Science 1983, 220 [38] Aarts, E. H. L.; Vanlaarhoven, P. J. M. Statistical Cooling- a General-Approach to Combinatorial Optimization Problems. Philips Journal of Research 1985, 40. [39] Patel, A.N.; Mah, R. S. H.; Karimi, I. A. Preliminary Design of Multiproduct Noncontinuous Plants Using Simulated Annealing. Computers & Chemical Engineering 1991, 15. [40] Painton, L. A.; Diwekar, U. M. Synthesizing Optimal-Design Configurations for a Brayton Cycle Power-Plant. Computers & Chemical Engineering 1994, 18. [41] Luyben, W. L. Comparison of extractive distillation and pressure-swing distillation for acetone/chloroform separation. Computers & Chemical Engineering 2013, 50, 1-7. [42] Vasudevan, S.; Rangaigh, G. P; Murthy Konda, N. V. S. N.; Tay, W. H. Application and Evaluation of Three Methodologies for Plantwide Control of the Styrene Monomer Plant. Ind. Eng. Chem. Res 2009, 48, 10941-10961. [43] Luyben, W. L. Design and Control of the Styrene Process. Ind. Eng. Chem. Res 2011, 50, 1231-1246. [44] Rama V. Mahajanam.; Alex Zheng.; J. M. Douglas. A Shortcut Method for Controlled Variable Selection and Its Application to the Butane Alkylation Porcess. Ind. Eng. Chem. Res 2001, 40, 3208-3216. [45] Luyben, W. L. Design and Control of an Autorefrigerated Alkylation Process. Ind. Eng. Chem. Res 2009, 48, 11081-11093. [46] Turton, R.; Bailie, R. C.; Whiting, W. B.; Shaelwitz, J. A.; Analysis, Synthesis and Design of Chemical Processes, 2nd ed.; Prentice Hall: Upper Saddle River, NJ, 2003. [47] Luyben, W. L. Design and Control of the Cumene Process. Ind. Eng. Chem. Res 2010, 49, 719-734. [48] Douglas, J. M. Conceptual Design of Chemical Processes. McGraw-Hill: New York, 1988. [49] M. F. Doherty; M. F. Malone. Conceptual Design of Distillation System. McGraw-Hill, New York, 2001. | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/67813 | - |
| dc.description.abstract | 本篇利用模擬最適化，藉由在客戶端MATLAB使用模擬退火演算法與在伺服端Aspen Plus建立單一蒸餾塔，來完成近似最適化的塔序列與熱整合程序設計。塔序列中的每座單塔都能獨立完成，且每個塔序列的總年度成本可以被加總計算。此法優點不僅在程序模擬器中建立嚴謹模型與序列程序靈活運用，還能在程式語言中建構非微分導向最適化方法。使用此法，單塔可以在六分鐘以內完成最適化。再者，在適當的堆疊整合流程與可行性溫度範圍的蒸氣營運條件下，近似最適化的熱整合序列塔可以自動化完成。本篇用兩個塔序列程序來演示結果。最後本篇提出兩個結合序列塔與熱整合的整廠程序。反應段的出料決定分離段的進料，規格定義用來控制此兩段的進料與出料。結果顯示在整廠程序眾多的設計變數下 (13與11個變數)，最適化是可行的。 | zh_TW |
| dc.description.abstract | Simulation-optimization is applied to determine nearly optimal process designs in column sequencing and stacking problems using a simulated annealing algorithm (SAA) in the client (MATLAB) and a single distillation column in the server (Aspen Plus). Each column in every sequence is optimized separately and the total cost of each sequence is calculated. This method benefits both from the rigor of column modeling in a process simulator and the flexibility of implementing sequential procedures and derivative-free optimization in a procedural programming language. Using this method, a single column can be optimized within six minutes of computer time. Furthermore, when stacking rules and available utilities are specified, a nearly optimal heat-integrated distillation column sequence can be designed automatically. Results are illustrated using two case studies of column sequencing problems. Finally, two plantwide processes combined with column sequencing and stacking were proposed. The outputs of reaction section will determine the inputs of separation section. Some specifications are defined to govern the inputs and outputs between two sections. The results demonstrate that optimization from numerous design variables (13 and 11 variables) in plantwide process is feasible. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-17T01:51:24Z (GMT). No. of bitstreams: 1 ntu-106-R04524051-1.pdf: 5918250 bytes, checksum: 4139bd7f06f4f9bc4c85dc95a655115e (MD5) Previous issue date: 2017 | en |
| dc.description.tableofcontents | 口試委員會審定書 i
誌謝 iii 摘要 v Abstract vii Contents ix List of Figures xiii List of Tables xvii 1. Introduction 1 1.1. Overview 1 1.2. Literature survey 3 1.3. Motivation 8 1.4. Thesis organization 9 2. Method 10 2.1. Single column simulation 10 2.2. Vacuum system 12 2.3. Aspen Plus ActiveX automation server 14 2.4. Using variable explorer to search cell paths 17 2.5. Resolution of Aspen Plus crash 18 2.6. Simulated annealing 20 2.6.1. Overview 20 2.6.2. Simulated annealing parameters 25 3. Application 29 3.1. Column sequence and stacking – Alcohol case study 29 3.1.1. Overview 29 3.1.2. Column sequence 30 3.1.3. Column stacking 44 3.2. Column sequence and stacking – Styrene case study 60 3.2.1. Overview 60 3.2.2. Column sequence 61 3.2.3. Column stacking 72 3.3. Plantwide process design– Alkylation case study 85 3.3.1. Overview 85 3.3.2. Flowsheet 86 3.3.3. Economic evaluation 89 3.3.4. Optimization 91 3.3.5. Results and discussion 92 3.4. Plantwide process design – Cumene case study 101 3.4.1. Overview 101 3.4.2. Flowsheet 102 3.4.3. Economic evaluation 105 3.4.4. Optimization 108 3.4.5. Results and discussion 109 4. Conclusion 122 References 124 Appendix A: Nomenclature 131 Appendix B: MATLAB code 133 Appendix C: Total annual cost calculation 137 | |
| dc.language.iso | en | |
| dc.title | 利用Aspen Plus ActiveX自動化伺服器進行塔序列、整合與整廠最適化 | zh_TW |
| dc.title | Column Sequencing, Stacking and Plantwide Optimization Using Aspen Plus ActiveX Automation Server | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 105-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 錢義隆(I-Lung Chien),陳誠亮(Cheng-Liang Chen),李豪業(Hao-Yeh Lee) | |
| dc.subject.keyword | 序列塔,熱整合,模擬退火演算法,最適化,單塔, | zh_TW |
| dc.subject.keyword | distillation column sequence,heat integration,simulated annealing algorithm,optimization,single distillation column, | en |
| dc.relation.page | 141 | |
| dc.identifier.doi | 10.6342/NTU201701778 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2017-07-25 | |
| dc.contributor.author-college | 工學院 | zh_TW |
| dc.contributor.author-dept | 化學工程學研究所 | zh_TW |
| 顯示於系所單位： | 化學工程學系 | |
文件中的檔案：
| 檔案 | 大小 | 格式 | |
|---|---|---|---|
| ntu-106-1.pdf 目前未授權公開取用 | 5.78 MB | Adobe PDF |
系統中的文件，除了特別指名其著作權條款之外，均受到著作權保護，並且保留所有的權利。