Design procedure for nonlinear multivariable processes control

被引:0
|
作者
Ciprian, Lupu [1 ]
Dumitru, Popescu [1 ]
Andreea, Udrea [1 ]
Catalin, Dimon [1 ]
机构
[1] Univ Politehn Bucuresti, Automat & Comp Sci, 313 Splaiul Independentei,Sector 6, Bucharest, Romania
关键词
multivariable control; nonlinear process; real time system;
D O I
暂无
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 study presents comparative results of real time implementing of three methods for control a multivariable process with nonlinear static characteristics. The first two methods are classic and are based on decentralized control and respectively, oil static decoupling procedures. The third proposed method is developed using a combined feedforward and feedback control scheme with nonlinear compensators. The use of this last structure imposes solving some specific problems, like process's static characteristic determination, construction of a nonlinear compensator or robust control law design. The applicability of the proposed method and of the two classic methods is proved using a real-time structure based on RST control algorithms. In the end, its software implementation and the obtained results are also shown.
引用
收藏
页码:362 / +
页数:2
相关论文
共 50 条
  • [1] Solutions for nonlinear multivariable processes control
    Ciprian, Lupu
    Dumitru, Popescu
    Andreea, Udrea
    Catalin, Dimon
    WSEAS Transactions on Systems and Control, 2008, 3 (06): : 597 - 606
  • [2] Nonlinear adaptive control for multivariable chemical processes
    Guo, BJ
    Jiang, AP
    Hua, XM
    Jutan, A
    CHEMICAL ENGINEERING SCIENCE, 2001, 56 (23) : 6781 - 6791
  • [3] JASON PROCEDURE FOR DESIGN OF MULTIVARIABLE CONTROL SYSTEMS
    ELSEY, JI
    BRULEY, DF
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (04): : 431 - &
  • [4] Design procedure for inverse model command: Control method for nonlinear processes
    Lupu, Ciprian
    Petrescu, Catalin
    Ticlea, Alexandru
    Dimon, Catalin
    Udrea, Andreea
    Irimia, Bogdan
    UPB Scientific Bulletin, Series C: Electrical Engineering, 2008, 70 (03): : 87 - 100
  • [5] DESIGN PROCEDURE FOR INVERSE MODEL COMMAND: CONTROL METHOD FOR NONLINEAR PROCESSES
    Lupu, Ciprian
    Petrescu, Catalin
    Ticlea, Alexandru
    Dimon, Catalin
    Udrea, Andreea
    Irimia, Bogdan
    UNIVERSITY POLITEHNICA OF BUCHAREST SCIENTIFIC BULLETIN SERIES C-ELECTRICAL ENGINEERING AND COMPUTER SCIENCE, 2008, 70 (03): : 87 - 100
  • [6] FEEDFORWARD FEEDBACK-CONTROL OF MULTIVARIABLE NONLINEAR PROCESSES
    DAOUTIDIS, P
    SOROUSH, M
    KRAVARIS, C
    AICHE JOURNAL, 1990, 36 (10) : 1471 - 1484
  • [7] STRUCTURAL EVALUATION OF CONTROL CONFIGURATIONS FOR MULTIVARIABLE NONLINEAR PROCESSES
    DAOUTIDIS, P
    KRAVARIS, C
    CHEMICAL ENGINEERING SCIENCE, 1992, 47 (05) : 1091 - 1107
  • [8] Bounded robust control of constrained multivariable nonlinear processes
    El-Farra, NH
    Christofides, PD
    CHEMICAL ENGINEERING SCIENCE, 2003, 58 (13) : 3025 - 3047
  • [9] Nonlinear controller design for input-constrained, multivariable processes
    Kanter, JM
    Soroush, M
    Seider, WD
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (16) : 3735 - 3744