期刊文献+

催化裂化装置补充吸收剂流量操作优化及其控制实现 被引量:2

Optimization and Control of FCCU Supplementary Absorbent Flow
下载PDF
导出
摘要 利用流程模拟软件UniSim Design对某石化厂60万吨/年催化裂化装置的吸收稳定系统进行稳态和动态的流程模拟。利用稳态模型,以能耗最小为优化目标,以产品质量指标为约束条件对补充吸收剂流量进行操作优化。利用动态模型作为虚拟装置并用控制的手段将操作优化的结果予以实现,通过实验对比分析,应该以产品质量指标作为被控变量才能保证优化实现的过程中质量不超标,同时多变量预测控制的效果要比单回路控制效果好,但是将补充吸收剂流量分多次加载,可以改善单回路控制的控制效果。 The steady and dynamic process simulation based on 0.6 Mt/a FCCU absorption and stabilization system were established with UniSim Design software.For the goal of minimization of energy cost,operation optimization of supplementary absorbent flow was done on the basis of steady model while satisfying the product within quality restriction.The result above was realized by the means of control system in the dynamic model.By experiments analysis,in order to ensure quality not exceeding during the implementation process of optimization,the product quality index should be taken as controlled variable.The performance of multi-variable prediction control is better than that of single-loop control,but the latter one can be improved if the change of supplementary absorbent flow is divided into several times.
出处 《化工自动化及仪表》 CAS 北大核心 2010年第5期72-77,共6页 Control and Instruments in Chemical Industry
关键词 催化裂化 吸收稳定 补充吸收剂 流程模拟 操作优化 优化实现 FCCU absorption and stabilization system supplementary absorbent process simulation operation optimization optimization implement
  • 相关文献

参考文献9

二级参考文献21

  • 1皮红梅,董晓燕,王红梅.HYSYS软件在芳烃装置上的应用[J].化学工业与工程,2005,22(1):77-78. 被引量:3
  • 2袁璞,左信,郑海涛.状态反馈预估控制[J].自动化学报,1993,19(5):569-577. 被引量:55
  • 3郑陵,杜英生,王颖昕.吸收稳定系统解吸塔双股进料工艺的探讨[J].化学工程,1995,23(5):39-43. 被引量:11
  • 4徐孝民.石油馏分的假组分处理方法[J].石油炼制与化工,1995,26(3):40-44. 被引量:9
  • 5杜平.-[J].石油炼制与化工,1995,23(7).
  • 6陆恩锡 等.-[J].炼油设计,1998,(5).
  • 7[6]杨友麒,项曙光主编.化工过程模拟与优化[M].北京:化学工业出版社,2005:
  • 8[9]HUANG Zhi-guang,WANG Rong shun,GU An zhong,SHI Yu-mei.Modeling and Simulation of Skid-mounted LNG Plants Using HYSYS Software[J].Journal of Donghua University.Eng.Ed.2007,24(1)
  • 9[10]Ingunn Olsen,Guttorm Oiav Endrestol and Terje Sira.A Rigorous and Efficient Distillation Column Model for Engineering and Training Simulators[J].Computers and Chemical Engineering.1997,21(Sup):193-198
  • 10[11]Zalizawati Abdullah,Norashid Aziz and Zainal Abroad.Nonlinear Modeling Application in Distillation Column[J] Chemical Product and Process Modeling.2007,2(3):Article 12

共引文献45

同被引文献19

  • 1刘涛,张卫东,顾诞英.一类开环不稳定串级控制系统的解析设计[J].控制与决策,2004,19(8):872-876. 被引量:10
  • 2张鹏飞,张华伟,王聪,陈燕杰.催化裂化装置吸收稳定系统进料工艺分析[J].石油炼制与化工,2006,37(4):11-14. 被引量:9
  • 3张鹏飞,王申江,张华伟,池红卫.吸收稳定系统能耗分析及优化[J].化学工程,2006,34(11):75-77. 被引量:5
  • 4Mark L. Darby,Michael Nikolaou,James Jones,Doug Nicholson.RTO: An overview and assessment of current practice[J]. Journal of Process Control . 2011 (6)
  • 5Yingchun Zhong,Yan Luo.Comparative Study of Single-loop Control and Cascade Control of Third-order Object[J]. Procedia Engineering . 2011
  • 6Sebastian Engell.Feedback control for optimal process operation[J]. Journal of Process Control . 2006 (3)
  • 7José Luis Figueroa.Economic performance of variable structure control: a case study[J]. Computers and Chemical Engineering . 2000 (8)
  • 8Steinboeck, Andreas,Graichen, Knut,Kugi, Andreas.Dynamic optimization of a slab reheating furnace with consistent approximation of control variables. IEEE Transactions on Control Systems Technology . 2011
  • 9Henson, Michael A.,Seborg, Dale E.Input-output linearization of general nonlinear processes. American Institute of Chemical Engineers Journal . 1990
  • 10Abe N,Nakamura A.Learning to optimally schedule internet banneradvertisements. ICML . 1999

引证文献2

二级引证文献4

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部