氯乙烯精馏高沸塔的双层结构模型预测控制策略

苏宝玉, 邹涛, 臧春华, 孔庆儒

苏宝玉, 邹涛, 臧春华, 孔庆儒. 氯乙烯精馏高沸塔的双层结构模型预测控制策略[J]. 信息与控制, 2015, 44(4): 403-410. DOI: 10.13976/j.cnki.xk.2015.0403
引用本文: 苏宝玉, 邹涛, 臧春华, 孔庆儒. 氯乙烯精馏高沸塔的双层结构模型预测控制策略[J]. 信息与控制, 2015, 44(4): 403-410. DOI: 10.13976/j.cnki.xk.2015.0403
SU Baoyu, ZOU Tao, ZANG Chunhua, KONG Qingru. Double-layered Model Predictive Control Strategy of High Boiling Column of Vinyl Chloride Distillation[J]. INFORMATION AND CONTROL, 2015, 44(4): 403-410. DOI: 10.13976/j.cnki.xk.2015.0403
Citation: SU Baoyu, ZOU Tao, ZANG Chunhua, KONG Qingru. Double-layered Model Predictive Control Strategy of High Boiling Column of Vinyl Chloride Distillation[J]. INFORMATION AND CONTROL, 2015, 44(4): 403-410. DOI: 10.13976/j.cnki.xk.2015.0403
苏宝玉, 邹涛, 臧春华, 孔庆儒. 氯乙烯精馏高沸塔的双层结构模型预测控制策略[J]. 信息与控制, 2015, 44(4): 403-410. CSTR: 32166.14.xk.2015.0403
引用本文: 苏宝玉, 邹涛, 臧春华, 孔庆儒. 氯乙烯精馏高沸塔的双层结构模型预测控制策略[J]. 信息与控制, 2015, 44(4): 403-410. CSTR: 32166.14.xk.2015.0403
SU Baoyu, ZOU Tao, ZANG Chunhua, KONG Qingru. Double-layered Model Predictive Control Strategy of High Boiling Column of Vinyl Chloride Distillation[J]. INFORMATION AND CONTROL, 2015, 44(4): 403-410. CSTR: 32166.14.xk.2015.0403
Citation: SU Baoyu, ZOU Tao, ZANG Chunhua, KONG Qingru. Double-layered Model Predictive Control Strategy of High Boiling Column of Vinyl Chloride Distillation[J]. INFORMATION AND CONTROL, 2015, 44(4): 403-410. CSTR: 32166.14.xk.2015.0403

氯乙烯精馏高沸塔的双层结构模型预测控制策略

基金项目: 国家自然科学基金资助项目(61374112);中国科学院网络化控制系统重点实验室自主课题资助项目(WLHKZ2014010)
详细信息
    作者简介:

    苏宝玉(1987-),男,硕士生.研究领域为工业模型预测控制.
    邹涛(1975-),男,副研究员.研究领域为工业过程实时优化与模型预测控制.
    臧春华(1963-),男,教授.研究领域为复杂系统建模与控制,智能测控技术.

    通讯作者:

    苏宝玉,405637186@qq.com

  • 中图分类号: TP273

Double-layered Model Predictive Control Strategy of High Boiling Column of Vinyl Chloride Distillation

  • 摘要: 针对氯乙烯精馏高沸塔存在的高耗能,多变量耦合,大滞后,高沸物排放控制及回流优化问题,提出一种高沸塔双层结构模型预测控制策略.该策略考虑了精馏段的温差,在实现高沸塔精馏过程控制的前提下,具有优化回流节能的功能.通过考虑塔底温度和塔底液位设计出高沸物排放逻辑,并结合双层结构模型预测控制实现高沸物自动排放.最后实验仿真结果表明该方法可以减少进料该量变化引起的过程波动、实现高沸物自动排放和优化回流.
    Abstract: A double-layered model predictive control strategy is designed for the process of vinyl chloride distillation in order to address problems associated with high energy consumption, multivariable coupling, large time delays, high-boiling compounds that cannot be automatically discharged, and reflux optimization control of a high-boiling column. The strategy considers the temperature difference of the rectification section; thus, with the aim of achieving process control in high-boiling column distillation, the developed strategy optimizes reflux energy savings. In addition, the logic associated with the auto discharge of high-boiling compounds is designed by considering the rectifier-bottom temperature and level, and it is shown that this logic is effective for its purpose. Simulation results show that the proposed strategy can indeed reduce the process fluctuation of high-boiling columns caused by feed disturbance and achieve auto discharge of high-boiling compounds and optimization of the reflux.
  • [1] 郑石子, 颜才南, 胡志宏. 聚氯乙烯生产与操作[M]. 北京: 化学工业出版社, 2007: 1-320. Zheng S Z, Yan C N, Hu Z H. PVC production and operation[M]. Beijing: Chemical Industrial Press, 2007: 1-320.
    [2] 邴涓林, 黄志明. 聚氯乙烯工艺技术[M]. 北京: 化学工业出版社, 2008: 1-86. Bing J L, Huang Z M. Process technology of PVC[M]. Beijing: Chemical Industrial Press, 2008: 1-86.
    [3] 王纲, 臧春华, 陈未如, 等. 氯乙烯精馏过程计算机控制系统[J]. 化工自动化及仪表, 1994, 21(6): 18-20. Wang G, Zang C H, Chen W Z, et al. Computer control system for the rectification of vinyl chloride[J]. Control and Instruments in Chemical Industry, 1994, 21(6): 18-20.
    [4] 夏亮, 朱锦生. 氯乙烯精馏控制模式的分析及实践[J]. 控制工程, 2005, 12(S1): 23-26. Xia L, Zhu J S. Theoretical analysis and practice on the control mode of chloroethylene rectifying[J]. Control Engineering of China, 2005, 12(S1): 23-26.
    [5] 苏宏业, 葛姜新, 毛维杰, 等. 氯乙烯精馏过程多变量预测控制的应用研究[J]. 自动化仪表, 2000, 21(8): 6-8, 13. Su H Y, Ge J X, Mao W J, et al. The study on application of multiple-variable forecast control in chlorethene ctification process[J]. Process Automation Instrumentation, 2000, 21(8): 6-8, 13.
    [6] 王朝辉, 古勇, 毛维杰, 等. 氯乙烯精馏过程的先进控制系统[J]. 化工自动化及仪表, 2000, 27(6): 22-25. Wang Z H, Gu Y, Mao W J, et al. Advanced control system of chlorethene rectification process[J]. Control and Instruments in Chemical Industry, 2000, 27(6): 22-25.
    [7] 李纪强, 张海平, 姜金锁. 专家控制系统在氯乙烯精馏高沸塔中的应用[J]. 化工自动化及仪表, 2007, 34(5): 88-90. Li J Q, Zhang H P, Jiang J S. The application of expert control system in high boiling column of vinyl chloride distillation[J]. Control and Instruments in Chemical Industry, 2007, 34(5): 88-90.
    [8] Holkar K S, Waghmare L M. An overview of model predictive control[J]. International Journal of Control and Automation, 2010, 3(4): 47-63.
    [9] 李少远. 工业过程系统的预测控制[J]. 控制工程, 2010, 17(4): 407-415. Li S Y. Model-based predictive control for industrial process - A survey[J]. Control Engineering of China, 2010, 17(4): 407-415.
    [10] 邹涛, 王丁丁, 潘昊, 等. 从区间模型预测控制到双层结构模型预测控制[J]. 化工学报, 2013, 64(12): 4474-4483. Zou T, Wang D D, Pang H, et al. From zone model predictive control to double-layered model predictive control[J]. CIESC Journal, 2013, 64(12): 4474-4483.
    [11] 邹涛, 魏峰, 张小辉. 工业大系统双层结构预测控制的集中优化与分散控制策略[J]. 自动化学报, 2013, 39(8): 1366-1373. Zou T, Wei F, Zhang X H. Strategy of centralized optimization and decentralized control for two-layered predictive control in large-scale industrial systems[J]. Acta Automatica Sinica, 2013, 39(8): 1366-1373.
    [12] 潘红光, 高海南, 孙耀, 等. 基于多优先级稳态优化的双层结构预测控制算法及软件实现[J]. 自动化学报, 2014, 40(3): 405-414. Pan H G, Gao H N, Sun Y, et al. The algorithm and software implementation for double-layered model predictive control based on multi-priority rank steady-state optimization[J]. Acta Automatica Sinica, 2014, 40(3): 405-414.
    [13] Qin S J, Badgwell T A. A survey of industrial model predictive control technology[J]. Control Engineering Practice, 2003, 11(7): 733-764.
    [14] 胡泽新, 蒋慰孙. 精馏过程的专家控制[J]. 信息与控制, 1993, 22(2): 125-128. Hu Z X, Jiang W S. Expert control of distillation process[J]. Information and Control, 1993, 22(2): 125-128.
    [15] 吴迎春, 黄俊斌, 陈国良, 等. 精馏过程的神经网络控制系统的设计[J]. 电子学报, 1996, 24(4): 82-85. Wu Y C, Huang J B, Cheng G L, et al. Design of neural network control system in distillation process[J]. Acta Electronica Sinica, 1996, 24(4): 82-85.
    [16] Darby M L, Nikolaou M. MPC: Current practice and challenges[J]. Control Engineering Practice, 2012, 20(4): 328-342.
    [17] 金晓明, 葛娟娟. 多目标优化策略在精馏过程中的应用研究[J]. 控制工程, 2012, 19(1): 161-164. Jin X M, Ge J J. Applied research of multi-objective optimal control strategy in distillation column[J]. Control Engineering of China, 2012, 19(1): 161-164.
    [18] 陈国定, 饶宁. 混凝投药系统的双层结构模型预测控制策略[J]. 浙江工业大学学报, 2013, 41(4): 436-439, 451. Chen G D, Rao N. Two-layered predictive control strategy of coagulant dosing system[J]. Journal of Zhejiang University of Technology, 2013, 41(4): 436-439, 451.
    [19] Shi H Y, Wang D D, Yuan D C, et al. Two-layer predictive control of a continuous biodiesel transesterification reactor[J]. Journal of Applied Mathematics, 2013, 2013: ID 587841: 1-14.
    [20] 刘兴高. 精馏过程的建模、优化与控制[M]. 北京: 科学出版社, 2007: 3-36. Liu X G. Modeling, optimization and control of distillation process[M]. Beijing: Science Press, 2007: 3-36.
    [21] 邹涛, 李海强, 丁宝苍, 等. 多变量预测控制系统稳态解的相容性与唯一性分析[J]. 自动化学报, 2013, 39(5): 519-529. Zou T, Li H Q, Ding B C, et al. Compatibility and uniqueness analysis of steady state solution for multi-variable predictive control system[J]. Acta Automatica Sinica, 2013, 39(5): 519-529.
    [22] 邹涛, 丁宝苍, 张端. 模型预测控制工程应用导论[M]. 北京: 化学工业出版社, 2010: 76-114. Zou T, Ding B C, Zhang D. MPC: An introduction to industrial application[M]. Beijing: Chemical Industrial Press, 2010: 76-114.
    [23] Cutler C R, Ramakar B L. Dynamic matrix control - A computer algorithm[C]//The AIChE 86th National Meeting. Piscataway. NJ, USA:IEEE, 1979.
    [24] 薛美盛, 祁飞, 吴刚, 等. 精馏控制与节能优化研究综述[J]. 化工自动化及仪表, 2006, 33(6): 1-7. Xue M S, Qi F, Wu G, et al. Survey on control and energy-saving optimization of distillation column[J]. Control and Instruments in Chemical Industry, 2006, 33(6): 1-7.
    [25] 乔艳伟. 精馏过程模型简化与节能控制[D]. 哈尔滨: 哈尔滨工业大学, 2010. Qiao Y W. Model simplification and energy-saving control of distillation process[D]. Harbin: Harbin Institute of Technology, 2010.
    [26] 袁忠勋. 苯精馏塔的“灵敏”塔盘与温差控制[J]. 石油炼制与化工, 1998, 29(3): 40-43. Yuan Z X. The “sensitive” tray and temperature differential control of benzene rectifying column[J]. Petroleum Processing and Petrochemicals, 1998, 29(3): 40-43.
    [27] 黄克谨, 吴宁, 陈胜海, 等. 隔离壁精馏塔的简化温差控制[J]. 中国科技论文, 2013, 8(9): 878-882. Huang K J, Wu N, Chen H S, et al. Simplified temperature control strategies for dividing-wall distillation column[J]. Sciencepaper Online, 2013, 8(9): 878-882.
    [28] 徐博文, 彭认沛, 唐杰. 双温差控制系统的改进[J]. 化工自动化及仪表, 1992, 19(3): 4-7. Xu B W, Peng R P, Tang J. An improvement of a dual temperature differential control system[J]. Control and Instruments in Chemical Industry, 1992, 19(3): 4-7.
    [29] 吴俊生, 邵惠鹤. 精馏设计、操作和控制[M]. 北京: 中国石化出版社, 1997: 295-304. Wu J S, Shao H H. Distillation: Design, operation and control[M]. Beijing: China Petrochemical Press, 1997: 295-304.
计量
  • 文章访问数:  1055
  • HTML全文浏览量:  0
  • PDF下载量:  321
  • 被引次数: 0
出版历程
  • 收稿日期:  2014-07-08
  • 发布日期:  2015-08-19

目录

    /

    返回文章
    返回
    x