Control of a fluid catalytic cracking unit based on proportional-integral reduced order observers

被引:8
作者
Aguilar, R
González, J
Alvarez-Ramirez, J
Barrón, M
机构
[1] Univ Autonoma Metropolitana Azcapotzalco, Div Ciencias Basicas & Ingn, Mexico City 07300, DF, Mexico
[2] Dept Ingn Proc, Mexico City, DF, Mexico
关键词
FCC units; modeling error; PI2; compensators; control gains tuning;
D O I
10.1016/S1385-8947(99)00076-5
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The fluid catalytic cracking (FCC) unit is one of the most complex interactive processes in the refining industry, and is difficult to operate and control. This work deals with the regulative control law design for stabilization of the reactor and regenerator temperatures, considering that the kinetics terms are poorly known. The proposed control law makes use of on-line estimates of the input/output modeling errors, obtained from a proportional-integral reduced order observer. The structure of the proposed controller is similar to a proportional-double integral compensator (PI2) such that a new parameterization of the controllers gains is given in terms of the closed-loop and estimation time constants. The performance of the control scheme proposed here is analyzed via numerical simulations. (C) 1999 Elsevier Science S.A. All rights reserved.
引用
收藏
页码:77 / 85
页数:9
相关论文
共 22 条
[1]  
Aguilar R, 1997, J CHEM TECHNOL BIOT, V70, P209, DOI 10.1002/(SICI)1097-4660(199711)70:3<209::AID-JCTB749>3.3.CO
[2]  
2-U
[3]   Nonlinear model predictive control of industrial type IV fluid catalytic cracking (FCC) units for maximum gasoline yield [J].
Ali, EE ;
Elnashaie, SSEH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (02) :389-398
[4]   Robust regulation of temperature in reactor-regenerator fluid catalytic cracking units [J].
AlvarezRamirez, J ;
Aguilar, R ;
LopezIsunza, F .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (05) :1652-1659
[5]   Dynamics and control of fluidized catalytic crackers .4. The impact of design on partial control [J].
Arbel, A ;
Rinard, IH ;
Shinnar, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (03) :747-759
[6]   STATE-SPACE PREDICTIVE CONTROL (REPRINTED FROM CHEMICAL-ENGINEERING SCI, VOL 47, PG 787-807, 1992) [J].
BALCHEN, JG ;
LJUNGQUIST, D ;
STRAND, S .
MODELING IDENTIFICATION AND CONTROL, 1992, 13 (02) :77-112
[7]   A NEW CLASS OF STABILIZING CONTROLLERS FOR UNCERTAIN DYNAMICAL-SYSTEMS [J].
BARMISH, BR ;
CORLESS, M ;
LEITMANN, G .
SIAM JOURNAL ON CONTROL AND OPTIMIZATION, 1983, 21 (02) :246-255
[8]   Design of low-frequency compensators for improvement of plantwide regulatory performance [J].
Belanger, PW ;
Luyben, WL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (12) :5339-5347
[9]  
CADWELL JM, 1991, P 4 INT C CHEM P CON, P319
[10]   HIGH-GAIN ESTIMATION FOR NONLINEAR-SYSTEMS [J].
DEZA, F ;
BUSVELLE, E ;
GAUTHIER, JP ;
RAKOTOPARA, D .
SYSTEMS & CONTROL LETTERS, 1992, 18 (04) :295-299