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تعیین چیدمان بهینه برج‌های تقطیر با در نظر گرفتن ادغام حرارتی به روش برنامه‌نویسی ریاضی مبتنی بر بهینه‌سازی اَبَرساختار | ||
| نشریه مهندسی مکانیک امیرکبیر | ||
| مقاله 1، دوره 48، شماره 3، مهر 1395، صفحه 227-238 اصل مقاله (3.47 M) | ||
| نوع مقاله: مقاله پژوهشی | ||
| شناسه دیجیتال (DOI): 10.22060/mej.2016.548 | ||
| نویسندگان | ||
| مرتضی محمودی منش1؛ نوراله کثیری* 2؛ جواد ایوک پور3 | ||
| 1کارشناسی ارشد، دانشکده مهندسی شیمی، دانشگاه علم و صنعت، تهران، ایران | ||
| 2دانشیار، دانشکده مهندسی شیمی، دانشگاه علم و صنعت، تهران، ایران | ||
| 3استادیار، پژوهشکده مهندسی پالایش، پژوهشگاه صنعت نفت، تهران، ایران | ||
| چکیده | ||
| در این مقاله مسأله تعیین چیدمان بهینه برج‌های تقطیر در یک سیستم تقطیر چند جزئی، با در نظر گرفتن ادغام حرارتی بین کندانسور و ریبویلر برج‌های مختلف، به روش برنامه‌نویسی ریاضی بررسی شده است. مساله مورد بحث در اینجا به دلیل وجود قیود غیرخطی و همین‌طور متغیرهای گسسته و پیوسته در مدل بهینه‌سازی، یک برنامه غیرخطی آمیخته با عدد صحیح، MINLP، خواهد بود. مدل MINLP حاصل از برنامه‌نویسی ریاضی به کمک نرم‌افزار گمز حل شده است. جامعیت مدل بهینه‌سازی و انعطاف‌پذیری آن در تعریف شرایط عملیاتی جدید از ویژگی‌های این کار به حساب می‌آید. بهینه‌سازی همزمان چیدمان و مصرف انرژی امکان ارزیابی تأثیر ادغام حرارتی بر انتخاب چیدمان بهینه فراهم کرده است. در نظر گرفتن ادغام حرارتی در کاهش مصرف انرژی با متغیر بودن فشار برج تقطیر امکان‌پذیر شده است بطوریکه نتایج حاصل از حل مدل MINLP برای یک جداسازی چهار جزئی، میزان صرفه‌جویی برابر 25% در هزینه کلی سالانه که شامل هزینه‌های سرمایه‌گذاری، عملیاتی و میزان مصرف انرژی می‌شود، را نشان می‌دهد. | ||
| کلیدواژه‌ها | ||
| چیدمان برج‌های تقطیر؛ ادغام حرارتی؛ بهینه‌سازی مصرف انرژی؛ برنامه‌نویسی ریاضی؛ برنامه غیرخطی آمیخته با عدد صحیح (MINLP) | ||
| عنوان مقاله [English] | ||
| Synthesis of Optimal Heat-Integrated Distillation Columns Sequence with Mathematical Programming method based on Superstructure Optimization | ||
| نویسندگان [English] | ||
| Morteza Mahmudimanesh1؛ Norollah Kasiri2؛ Javad Ivakpour3 | ||
| 1M.Sc in Chemical Engineering Iran University of Science and Technology School of Chemical Engineering | ||
| 2Faculty member of staff Iran University of Science and Technology School of Chemical Engineering | ||
| 3Faculty member of staff Reseach Institute of Petroleum Industry | ||
| چکیده [English] | ||
| In this paper, the problem of optimal distillation columns sequence determination for a multicomponent distillation system with heat integration between condensers and reboilers of various columns with using mathematical programming approach considered. Existence of nonlinear constraints also discrete and continuous variables in optimization model is reason that the problem will be a Mixed-Integer-Non-Linear-Program (MINLP). MINLP model that obtained from mathematical programming is solved with GAMS. Some of proposed method features are generality and flexibility for defining new operating conditions. In proposed MINLP model, the effect of heat integration on optimal sequence has been considered by simultaneous optimization of sequencing and energy demand. Energy saving using heat integration has become possible by regarding column pressure as a variable in optimization model. The Results obtained from solution of MINLP model for a four components separation, shows 25% saving in total annual cost that includes investment, operation costs and energy consumption. . . | ||
| کلیدواژه‌ها [English] | ||
| Distillation columns sequence, Heat integration, optimization, Mathematical program, Mixed-Integer-Non-Linear-Programming (MINLP) | ||
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| مراجع | ||
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[1] Hilde K. Engelien and Sigurd Skogestad, 2003.“Selecting appropriate control variables for a heat integrated distillation system with prefractionator”,Computer Aided Chemical Engineering, 28, pp. 407–412. [2] Amiya K. Jana, 2010. “Heat integrated distillation operation”, Applied Energy, 87, pp. 1477– 1494. [3] R. Agrawal, 2001. “Multicomponent distillation columns with partitions and multiple reboilers and condensers”, Ind. Eng. Chem. Res, 40, pp. 4258–4266. [4] E. Rev, M. Etmir, Z. Szitkai, P. Mizsey and Z. Fonyo,2001. “Energy savings of integrated and coupled distillation systems”, Computers and Chemical Engineering, 25, pp. 119– 140. [5] S. Hernández, S. Pereira-Pech, A. Jiménez and V. Rico-Ramírez, 2003. “Energy Efficiency of an Indirect Thermally Coupled Distillation Sequence”,The Canadian Journal of Chemical Engineering, 81,No. 5, pp. 1087- 1091. [6] J. G. Segovia-Hernández, S. Hernández, V. Rico-Ramírez and A. Jiménez, 2004. “A comparison of the feedback control behavior between thermally coupled and conventional distillation schemes”, Computers & Chemical Engineering, 28, No. 5, pp. 811- 819. [7] R. B. Boozarjomehry, A. P. Laleh and W. Y. Svrcek,2009. “Automatic Design of Conventional Distillation Column Sequence by Genetic Algorithm”, The Canadian Journal of Chemical Engineering, 87, pp.477- 492. [8] R. B. Boozarjomehry, A. P. Laleh and W. Y. Svrcek,2011. “Evolutionary design of optimum distillation column sequence”, The Canadian Journal of Chemical Engineering, 9999. [9] W. D. Seider, J. D. Seader and D. R. Lewin, 2009.“Product and Process Design Principles, 3rd Ed.,John Wiley & Sons. [10] L. T. Biegler, I. E. Grossmann and A. W. Westerberg,1997. “Systematic Methods of Chemical Process Design, Prentice Hall. [11] R. Smith, 2005. “Chemical Process Design and Integration”, 2nd Ed., John Wiley & Sons. [12] J. D. Seader and A. W. Westerberg, 1977. “A Combined Heuristic and Evolutionary Strategy for Synthesis of Simple Separation Sequences”, AICHE,23, No. 6, pp. 951- 954. [13] J. M. Douglas, 1988. “Conceptual Design of Chemical Processes, McGraw-Hill. [14] J. Ivakpour and N. Kasiri, 2009. “Symthesis of distillation columnsequences for nonsharp separations”, Industrial and Engineering Chemistry Research, 48. No. 18, pp. 8635- 8649. [15] K. Wang, Y. Qian, Y. Yuan and P. Yao, 1998.“Synthesis and optimization of heat integrated distillation systems using an improved genetic algorithm”, Computers & Chemical Engineering, 23,No. 1, pp. 125- 136. [16] Wei-Zhong and Y. Xi-Gang, 2009. “A simulated annealing-based approach to the optimal synthesis of heat-integrated distillation sequences”, Computers & Chemical Engineering, 33, No. 1, pp. 199- 212. [17] L. Yiqing and Y. Xi-gang, 2010. “Synthesis and heat integration of thermally coupled complex distillation system” International Journal of Energy Research,34, No. 7, pp. 626- 534. [18] X. Wang and Y. Li, 2010. “Stochastic GP synthesis of heat integrated Nonsharp distillation sequences”,chemical engineering research and design, 88. No.1, pp. 45- 54. [19] M. J. Andercovich and A. W. Westerberg, 1985. “An MILP Formulation for Heat-Integrated Distillation Sequence Synthesis”, AICHE, 31, No. 9, pp. 1461-1474. [20] C. A. Floudas and G. E. Paules, 1988. “A Mixed-Integer Nonlinear Programming Formulation for the Synthesis of Heat-Integrated Distillation Sequences”,Computers & Chemical Engineering, 12, No. 6, pp.531- 546. [21] C. A. Floudas and S. H. Anastasiadis, 1988.“Synthesis of distillation sequences with several multicomponent feed and product streams”, Chemical Engineering Science, 43, No. 9, pp. 2407- 2419. [22] G. E. Paules and C. A. Floudas, 1988. “Synthesis of flexible distillation sequences for multiperiod operation”, Computers & Chemical Engineering, 12,No. 4, pp. 267- 280. [23] A. Aggarwal and C.A. Floudas, 1990. “Synthesis of general distillation sequences—nonsharp separations”, Computers & Chemical Engineering,14, No. 6, pp. 631- 653. [24] A. Aggarwal and C.A. Floudas, 1992. “Synthesis of Heat-Integrated Nonsharp distillation squences”,Computers & Chemical Engineering, 16, No. 2, pp.89- 108. [25] Z. Novak, Z. Kravanja and I. E. Grossmann, 1996. “Simultaneous synthesis of distillation sequences in overall process schemes using an improved minlp approach”, Computers & Chemical Engineering, 20,No. 12, pp. 1425- 1440. [26] R. W. H. Sargent, 1998. “A functional approach to process synthesis and its application to distillation systems”, Computers & Chemical Engineering, 22,No. 1-2, pp. 31- 45. [27] H. Yeomans and I. E. Grossmann, 1999. “Nonlinear disjunctive programming models for the synthesis of heat integrated distillation sequences”, Computers & Chemical Engineering, 23, No. 9, pp. 1135- 1151. [28] H. Yeomans and I. E. Grossmann, 2000. “Disjunctive Programming Models for the Optimal Design of Distillation Columns and Separation Sequences”, Industrial and Engineering Chemistry research, 39.No. 6, pp. 1637- 1648. [29] H. Yeomans and I. E. Grossmann, 2000. “Optimal Design of Complex Distillation Columns Using Rigorous Tray-by-Tray Disjunctive Programming Models”, Industrial and Engineering Chemistry research, 39. No. 11, pp. 4326- 4335. [30] J. A. Caballero and I. E. Grossmann, 2001.“Generalized Disjunctive Programming Model for the Optimal Synthesis of Thermally Linked Distillation Columns”, Industrial and Engineering Chemistry research, 40. No. 10, pp. 2260- 2274. [31] J. A. Caballero and I. E. Grossmann, 2004. “Design of distillation sequences: from conventional to fully thermally coupled distillation systems”, Computers & Chemical Engineering, 28, No. 11, pp. 2307- 2329. [32] J. A. Caballero and I. E. Grossmann, 2006.“Structural Considerations and Modeling in the Synthesis of Heat-Integrated-Thermally Coupled Distillation Sequences”, Industrial and Engineering Chemistry research, 45. No. 25, pp. 8454- 8474. [33] J. A. Caballero and I. E. Grossmann, 2007. “Logic Based Algorithms for the Rigorous Design of Thermally Coupled Distillation Sequences”, 17th European Symposium on Computer Aided Process Engineering-ESCAPE 17. [34] T. Farkas, B. Czuczai, E. rev and Z. Lelkes,2008. “New MINLP Model and Modified Outer Approximation Algorithm for Distillation Column Synthesis”, Industrial and Engineering Chemistry research, 47. No. 9, pp. 3088- 3103. [35] J. A. Caballero and I. E. Grossmann, 2010. “Hybrid Simulation-Optimization Algorithms for Distillation Design”, 20th European Symposium on Computer Aided Process Engineering-ESCAPE 17. [36] I. E. Grossmann, J. A. Caballero and H. Yeomans,1999. “Mathematical Programming Approaches to the Synthesis of Chemical Process Systems”, Korean Journal of Chemical Engineering, 16, No. 4, pp. 407-426. [37] H. Yeomans and I. E. Grossmann, 1999. “A systematic modeling framework of superstructure optimization in process synthesis”, Computers & Chemical Engineering, 23, No. 6, pp. 709- 731. [38] C. A. Floudas, 1995. “Nonlinear and Mixed-Integer Optimization: Fundamental and Applications”,Oxford University Press. [39] S. Lee and I. E. Grossmann, 2000. “New algorithms for nonlinear generalized disjunctive programming”,Computers & Chemical Engineering, 24, No. 9, pp.2125- 2141. | ||
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