C_4分离序列综合优化研究
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摘要
分离序列综合指:给定一进料流股,已知流股状态(流量、温度、压力和组成)系统的化的设计出能从进料中分离出所要求的产品,并使总费用最小。
     C_4分离序列由于其组分沸点接近,较难分离。本文结合某厂C_4分离系统节能改造,通过该序列的优化综合,实现生产系统的节能。
     本文的主要工作简述如下:
     1.利用直观推断法和能量集成的策略,针对原系统拟定三个不同特点的初始节能分离序列。
     2.利用化工模拟软件对该系统进行了模拟。由于该分离系统结构较复杂,且各个分离单元的分离任务和分离条件差别较大,本文对不同的分离单元采用了多个热力学方程和多种方法的尝试,最终通过模拟结果与现场数据的吻合,确认各分离单元的热力学方程。
     3.应用确认的热力学模型,对初始方案进行模拟,并利用灵敏度分析和轮换变量法对初始方案中分离序列中关键操作参数进行讨论和优化,确定优化参数。结果表明三个用能优化序列均可完成分离任务,且具有一定的节能效果。
     4.上述节能序列均从该系统内一子系统用能情况来考虑。但若从全系统考虑,仍然存在较大的节能潜力,后续工段中的一乙腈回收塔所分离物系物性稳定,有利于提压操作,提压后塔顶蒸气可以作为其它塔底再沸器热源,同时塔底釜液热量也要进行回收。通过全系统热集成可显著提高以上序列的用能完善程度。
     5.对BP人工神经网络的设计参数和训练过程进行分析,并结合任务分解法的思想,利用BP人工神经网络对其中一用能优化序列建立黑箱数学模型。神经网络模型预测结果与ASPEN模拟结果的误差表明该模型能够满足模拟该过程的要求。
     6.分析遗传算法的机理,用MATLAB建立改进的遗传算法并通过测试函数的测试。用该算法对人工神经网络所建立的数学模型进行优化。比较遗传算法和轮换变量法优化结果,表明神经网络和遗传算法相结合能够对分离序列进行优化,对工程应用具有一定的指导作用。
Separation process synthesis is a manipulation to deal with mixtures to be separated at the low expense of energy consumption and capital cost. And it is often used in the pretreatment of raw material, the purification of the product, the disposal of scrap, etc.
    Due to the close boiling points, C4 hydrocarbons are difficult to be separated. In this paper, combining with the refit plan in a factory, the energy efficiency of the whole separation system is increased through synthesis and optimization of the separation sequence.
    The six points are summarized as follows:
    1. The draft is designed by means of the tool of heuristic rules and technique of energy integration.
    2. The C4 hydrocarbons separation system is simulated using the simulator ASPEN PLUS. For each unit, the thermodynamics function is confirmed.
    3. Based on the simulation results and energy analysis of the system, the plans are simulated with the established thermodynamics functions, and the operation parameters are optimized by the sensitivity analysis. Calculation shows that all of the proposed plans are applicable to effectively separated the mixtures at lower expense of energy consumption.
    4. The acetoniltrile recovery column is considered to increase the operation pressure. The energy integration plan is designed to further increase the energy efficiency of the whole system.
    5. Mathematical model of the thermally coupled distillation is established with artificial neural network. Calculation shows that the model can simulate the process rigorously.
    6. A modified genetic algorithm is used to optimize the model by artificial neural network. It shows that the separation process can be optimized with the established model and optimization algorithm.
引文
[1] Takamatsu T. The nature and rule of process systems engineering. Comp.&Chem. Engng, 1983, 7(4):203-218
    [2] 侯芙生.过程能量综合技术讲义.北京:石化出版社,1995.2
    [3] 周忠清.金国山.大化工系统工程.化学反应工程与工艺,1999,15(2):204-206
    [4] 周忠清.分子化学工程的进展.现代化工,1993,13(3):10
    [5] 周忠清.分子化学工程学.科学.1994,46(1):58
    [6] Linda Raber. Green chemistry challenge awards honor cutting pollution et.source. C&EN, 1996, 29:9
    [7] 周忠清.二氧化碳催化还原成碳的进展.化学反应工程与工艺,1994,10(4):421
    [8] Lawrence R Sits, Jason R Babcock, Rimo Xi. Facile metathetical exchange between carbon dioxide and the diva-lent group 14bisamides M[N(Si Me3)2] 2(M=Ge and Sn). JAm Chem Soc, 1996,12,118:109
    [9] Colin A, Houston, Associates. Asia-Pacific will remain largest consumer of linear alkylbenzene Sulfonates. C&EN, 1996,4:40
    [10] NEWS FOCUS. Four main objectives seen as the focus of future chemical engineering research.C&EN, 1996, 34:12
    [11] 杨友麒,成思危.过程系统工程面临的挑战和发展趋势.化工进展,2002,2l(8):527-535
    [12] Cervantes A, Tonelli S, Brandolin A, Bandoni A, Biegler L. Large-scale dynamic optimization of a low density polyethylene plant. Comp.&Chem. Engng, 2000, 24:983-989
    [13] Barbase Jr V P, Wolf MRM, R Maciel Fo. Development of data reconciliation for dynamic nonlinear system application the polymerization reactor. Comp. &Chem. Engng, 2000, 24:501-506
    [14] Baker K R. Introduction to Sequencing & Scheduling. New York: Wiley, 1974
    [15] Egli U M, Rippin D W T. Short- term Scheduling for Multiproduct Batch Chemical Plants. Comp.& Chem. Engng, 1986, 10 (4):303-325
    [16] Shah N, Pantelides C C, Sargent R W H. A General Algorithm for Short-term Scheduling of Batch Operations-Ⅱ. Comutational Issues. Comp,&Chem. Engng, 1993, 17(2):229-244
    [17] Rechard S H M. Chemical Process Structure and Information Flows. Boston, U.S.A: Butterworth Publishers: 1990, 241-299
    [18] Pekny JF, Miller D L, Mcrae G J. An Exact Parallel Algorithm for Scheduling When Production Costs Depend on Consecutive System States. Comp,&Chem. Engng, 1990, 14(9): 1009-1023
    [19] Pekny JF, Miller D L, Kudva G K. An Exact Algorithm for Resource Constrained Sequencing with Application to Pro-duction Scheduling under an Aggregate Deadline. Comp,&Chem. Engng, 1993, 17(7):671-682
    [20] Muiser R F H, Evans L B. An Approximate Method for the Production Scheduling of Industrial Batch
    
    Processes with Parallel Units. Computers Chem. Engng, 1989,13 (1/2):229-238
    [21] Schumacher J. A framework for batch-operation analysis within the context of disturbance management. Comp&Chem. Engng, 2000, 24:1175-1180
    [22] Rickard JG, Colantonio M G, Shah N. Integration in hierarchical structure for batch process operation. Comp.&Chem. Engng, 2000, 24:1159-1165
    [23] 徐用懋.流程工业的CIMS.化工自动化及仪表,1997,24(3):58-62
    [24] 扬家本.连续过程CIMS中生产计划/调度系统.化工自动化及仪表,1997,24(6):52-56
    [25] 周章玉,杨少华,成思危,华贲.过程工业企业模型系统及战略建模.华南理工大学内部报告,2000
    [26] Bose S D, Subramanian S, Orcun, Pekny JF. e PIMA:and electrnment environment for process integration and management analysis. Comp. &Chem. Engng, 2000, (24): 1654-1655
    [27] 成思危,复杂科学与组织管理.新华文摘,2001,(5):147.
    [28] Grossmann I E, Arthur W Westerberg. Research challenges in process systems engineering. AICh E Juwn, 2000, 46 (9):1700-1703.
    [29] Bakshi B R. A thermodynamic framework for ecologically conscious process systems engineering. Comp.&Chem Engng, 2001, 24:1763-1773
    [30] Gunderson T. An IEA initiative on process integration. Proc of Aspen World' 97. Boston: 1997.
    [31] Spear Mike. Site integration moves beyond pinch. Process Engng, 2000, 24-25
    [32] Fraga E S, Hagemann J A, Estrada-Villagrana, Bogle I D L. Incorporation of dynamic behavior in an automated process synthesis system. Computer & Chem Engng, 2000, (24): 189-194
    [33] Hendry J.E., Hughes R.R.. Synthesis in the design of chemical processes. Chem. Eng. Prog., 1972,68,69
    [34] Westerberg, A.W., The synthesis of distillation-based separation systems. Comp. &Chem. Engng,1985, (21): 9, 421
    [35] Nath, R, Motard, R.L..Evolutionary synthesis of separation processes. AIChE J, 1981, (27):578-587
    [36] Triantafyllou, C., Simth, R.. The design and optimization of fully thermally coupled distillation columns. Trans. Ichem.E., 1992, (3):118-132
    [37] Andrecovich, M.J., Westerberg, A W.. An MILP formulation of heat-integrated distillation sequence synthesis. AIChE J, 1985, 31:1461-1474
    [38] Hu, Z.B., He, X..Heuristic synthesis for multi-component products with simple and sharp separation.Comp. &Chem. Engng, 1993, (17):379-397
    [39] 姚平经.全过程系统能量优化综合.大连:大连理工大学出版社,1995.111-122
    [40] 陈志奎.原油蒸馏过程的数学模型和各类软件(Ⅱ)-常减压蒸馏塔系统模型中的设计核算型快捷
    
    法.计算机与应用化学,1999,16(1):29-34
    [41] Sanjay Gupta, Pi-Hsin Liu, Spyros Sanjay Gupta, Pi Hsin Liu, Spyros A Svoronos. Hybrid First-Principles/Neural Networks Model Force Column Flotation. AIChE Journal, 1999, 45(3): 557-566
    [42] Rohani S,haeri M, Wood H C. Modeling and Control of continuous Crystallization Process: Partl Linear and Non-linear Modeling. Comp. &Chem. Engng, 1999, 23:263 -277
    [43] Arun Tholudur, Fred Ramirez W. Neural-Network Modeling and Optimization of Induced Foreign Protein Production. AIChE Journal, 1999, 45(8): 1660-1670
    [44] 何险峰,周家驹.遗传算法及其在化学化工中的应用.化工进展,1998,10(3):312
    [45] Jose L R. Genetic Algorithm Programming Environments. Computer, 1994, (6):29-43.
    [46] Srinivas M. Genetic Algorithms: Surver. Computer. 1994, (6):17-26
    [47] Androulakis I P. A genetic Algorithm framework for process design and optimization. Comp. &Chem. Engng,, 1991, 15(4):217-278
    [48] 周金荣,黄道,蒋慰孙.遗传算法的改进及其应用研究.控制与决策,1995,10(3):261-264
    [49] Omori R, Sakakibara Y, Suzuki A. Design of polarized-positron generation system. Nucl. Technol.,1997, 118(1):26-31
    [50] 雷志刚,周荣琪,段占庭.C_4萃取精馏工艺流程优化.石油化工,1999,29(6):399-401
    [51] 贾自成,董俊国,董满祥,贾俊.我国抽提丁二烯生产装置的技术进展与述评.石油化工,1998,27(12):920-924
    [52] 张爱民.丁二烯生产技术现状及发展方向.石化技术,2002,9(2):105-110
    [53] 王崇智.乙腈萃取精馏分离丁二烯的工艺流程模拟.弹性体,1998,8(1):30-35
    [54] 王文华,任万忠,许文有,虞乐舜.用萃取精馏法分离C_4烷烃与烯烃的研究进展.广西化工,1999,28(2):20-23
    [55] 谢安俊,刘世华.大型化工流程模拟软件—ASPEN PLUS.石油与天然气化工,1995,24(4):76-89
    [56] 朱自强,徐汛.化工热力学.北京:化学工业出版社,1997.35-40
    [57] 杨友麒.热偶精馏塔操作特性的模拟研究.化工学报,1990,4(4):491-497
    [58] 沈静珠.过程系统优化.北京:清华大学出版社,1986
    [59] 谢桂兰.对求解约束优化问题中的变量轮换法的改进.机械,2001,28(1),19-20
    [60] 张莹.最优化技术基础.北京:清华出版社,1982.11
    [61] 曹正芳,浦伟光.采用中间再沸器的精馏塔热力学分析.金山油化纤,2001,(4):46-48
    [62] 杨友麒.精馏过程节能.现代化工,1994,(5):9-15
    [63] 杨友麒.化工过程模拟.化工进展,1994,(5):9-15
    [64] 王延敏.碳五分离序列综合优化研究.大连理工大学硕士论文,2002
    [65] 尹航,曹玉波.TCS-R热偶精馏过程的模拟优化计算.吉林化工学院学报,2001,18(4):8-10
    
    
    [66] 姚克俭,张颂红,祝铃钰.夹点技术在精馏系统优化中的应用.石油化工,2000,29(4):275
    [67] 俞红梅,全国系统能量综合方法的研究.大连理工大学博士研究生论文,1998
    [68] 朱美玲,赵淳生.一种万能的数学运算“演算纸”.振动,测试与诊断,1995,15:57-62
    [69] 张延华.面向多学科的新一代程序设计语言——MATLAB 5.1概述.计算机应用研究,1998,(6):4-8
    [70] 麻德贤.人工神经网络及其应用.计算机与应用化学,1997,14(supp):35-38
    [71] 赵晓光,何小荣,陈丙珍.神经元网络用于建立油品质量模型的研究.石油炼制,1993,24(9):9-14
    [72] 陈明.神经网络模型.大连:大连理工大学出版社,1995.5-85
    [73] 张立明.人工神经网络的模型及其应用.上海:复旦大学出版社,1993.56-72
    [74] 谭羽飞,陈家新.城市燃气短期负荷预测的神经网络等维信息模型,计算机仿真,2001 18(5):81
    [75] Stirling W C, Goodrich M A, Frosty R L. Procedurally rational decision-making and control. IEEE Control Systems, 1996, (11) 66-75
    [76] Jong-Hwan Kim, Hong-Kook Chae, Jeong-Yui Jeon, Seon-Woo Lee. Identification and control of systems with friction using accelerated evolutionary programming. IEEE Control Systems, 1996, (13) 38-47
    [77] 张晓缋,戴冠中,徐乃平.一种新的优化搜索算法——遗传算法.控制理论与应用,1995,12(3):226-227
    [78] 周明,孙树栋.遗传算法原理及应用.北京:国防工业出版社,1999.11-56
    [79] Jian-Xin Xu, Chang-Chieh Hang, Chen Liu. Parallel structure and tuning of a fuzzy PID controller. Automatic. 2000, 36 (5):673-684
    [80] 谢晓锋,张文俊,杨之廉.一种防止浮点遗传算法早熟收敛的父代选择策略.控制与决策,2002,17(5):626-633