Model reduction and control of reactor-heat exchanger networks

被引:23
作者
Baldea, M [1 ]
Daoutidis, P [1 ]
机构
[1] Univ Minnesota, Dept Chem Engn & Mat Sci, Minneapolis, MN 55455 USA
关键词
model reduction; nonlinear control; energy recycle; singular perturbations;
D O I
10.1016/j.jprocont.2005.06.007
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
This paper focuses on the dynamics and control of process networks consisting of a reactor connected with an external heat exchanger through a large material recycle stream that acts as an energy carrier. Using singular perturbation arguments, we show that such networks exhibit a dynamic behavior featuring two time scales: a fast one, in which the energy balance variables evolve, and a slow time scale that captures the evolution of the terms in the material balance equations. We present a procedure for deriving reduced-order, non-stiff models for the fast and slow dynamics, and a framework for rational control system design that accounts for the time scale separation exhibited by the system dynamics. The theoretical developments are illustrated with an example and numerical simulation results. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:265 / 274
页数:10
相关论文
共 28 条
[1]   Temperature control of ethylene to butene-1 dimerization reactor [J].
Ali, E ;
Al-humaizi, K .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (05) :1320-1329
[2]  
BALDEA M, IN PRESS P 16 IFAC W
[3]  
BALDEA M, 2004, ADCHEM 03, P645
[4]   Stability and multiplicity approach to the design of heat-integrated PFR [J].
Bildea, CS ;
Dimian, AC .
AICHE JOURNAL, 1998, 44 (12) :2703-2712
[5]   Design and control of heat-integrated reactors [J].
Chen, YH ;
Yu, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (12) :2791-2808
[6]   Temperature control of industrial gas phase polyethylene reactors [J].
Dadebo, SA ;
Bell, ML ;
McLellan, PJ ;
McAuley, KB .
JOURNAL OF PROCESS CONTROL, 1997, 7 (02) :83-95
[7]   DYNAMIC OUTPUT-FEEDBACK CONTROL OF MINIMUM-PHASE MULTIVARIABLE NONLINEAR PROCESSES [J].
DAOUTIDIS, P ;
KRAVARIS, C .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (04) :433-447
[8]   DYNAMIC OUTPUT-FEEDBACK CONTROL OF MINIMUM-PHASE NONLINEAR PROCESSES [J].
DAOUTIDIS, P ;
KRAVARIS, C .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (04) :837-849
[9]   Process systems and inventory control [J].
Farschman, CA ;
Viswanath, KP ;
Ydstie, BE .
AICHE JOURNAL, 1998, 44 (08) :1841-1857
[10]   TEMPERATURE CONTROL OF CONTINUOUS, BULK STYRENE POLYMERIZATION REACTORS AND THE INFLUENCE OF VISCOSITY - AN ANALYTICAL STUDY [J].
HENDERSON, LS ;
CORNEJO, RA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (11) :1644-1653