CONTROL AND ESTIMATION FOR PERTURBED NONLINEAR PROCESSES WITH DEADTIME

REFERENCES

• Alvarez , J. , Alvarez , J. , and Gonzalez , E. , “ Global Nonlinear Control of a Continuous Stirred Tank Reactor .” Chem. Eng. Sci. , 44 , 1147 – 1160 ( 1989 ).
   Web of Science ®Google Scholar
• Bequette , B.W. , “ Nonlinear Control of Chemical Processes A Review .” Ind. Eng. Chem. Research , 30 , 1391 – 1413 ( 1991 ).
   Web of Science ®Google Scholar
• Brockett , R.W. , Millman , R.S. , and Sussmann , H.J. , Differential Geometric Control Theory , Birkhäuser , Boston ( 1983 ).
   Google Scholar
• Calvet , J.-P. , and Arkun , Y. , “ Feedforward and Feedback Linearization of Nonlinear Systems with Disturbances .” Int. J. Control , 48 , 1551 – 1559 ( 1988 a).
   Web of Science ®Google Scholar
• Calvet , J.-P. , and Arkun , Y. , “ Feedforward and Feedback Linearization of Nonlinear Systems and Its Implementation Using Internal Model Control (IMC). ” Ind. Eng. Chem. Research , 27 , 1822 – 1831 ( 1988 b).
   Web of Science ®Google Scholar
• Daoutidis , P. , and Kravaris , C. , “ Synthesis of Feedforward/State Feedback Controllers for Nonlinear Processes .” AIChEJ. , 35 , 1602 – 1616 ( 1989 ).
   Web of Science ®Google Scholar
• Daoutidis , P. , Soroush , M. , and Kravaris , C. , “ Feedforward/Feedback Control of Multivariate Nonlinear Processes .” AIChEJ. , 36 , 1471 – 1484 ( 1990 ).
   Web of Science ®Google Scholar
• Henson , M.A. , and Seborg , D.E. , “ Critique of Exact Linearization Strategies for Process Control .” J. Proc. Control , 1 , 122 – 139 ( 1991 ).
   Google Scholar
• Herman , R. , and Krener , A.J. , “ Nonlinear Controllability and Observability .” IEEE Trans. Autom. Control , AC-22 , 728 – 740 ( 1977 ).
   Web of Science ®Google Scholar
• Hoo , K.A. , and Kantor , J.C. , “ An Exothermic Continuous Stirred Tank Reactor is Feedback Equivalent to a Linear System .” Chem. Eng. Common. , 37 , 1 - 10 ( 1985 ).
   Web of Science ®Google Scholar
• Hoo , K.A. , and Kantor , J.C. , “ Linear Feedback Equivalence and Control of an Unstable Biological Reactor .” Chem. Eng. Commun. , 46 , 385 – 399 ( 1986 ).
   Web of Science ®Google Scholar
• Huang , H.P. , and Chao , Y.C. , “ Parameter Identification and the Self-Tuning Adaptive Control by a Sensitivity Approach .” Chem. Eng. Commun. , 6 , 313 – 331 ( 1980 ).
   Google Scholar
• Huang , H.P. , Chao , Y.C. , and Shiau , S.L. , “ Modeling and Identification of Deterministic Models from Closed-Loop Data .” J. CMChE , 13 , 183 – 190 ( 1982 ).
   Google Scholar
• Huang , HP. , Chen , C.L. , Chao , Y.C. , and Chen , PL. , “ A Modified Smith Predictor with an Approximate Inverse of Dead Time .” AIChE J. , 36 , 1025 – 1031 ( 1990 ).
   Web of Science ®Google Scholar
• Huang , H.P. , and Wang , G.B. , “ Deadtime Compensation for Nonlinear Processes with Disturbances .” Int. J. Systems Sci. , in press ( 1992 ).
   Web of Science ®Google Scholar
• Hunt , L.R. , Su , R. , and Meyer , G. , “ Global Transformations of Nonlinear Systems .” IEEE Trans. Autom. Control , AC-28 , 24 – 31 ( 1983 ).
   Web of Science ®Google Scholar
• Isidori , A. , Nonlinear Control Systems An Introduction , 2nd Ed. , Springer-Verlag , New York ( 1989 ).
   Google Scholar
• Kantor , J.C. , “ An Overview of Nonlinear Geometrical Methods for Process Control .” In The Shell Process Control Workshop ( Edited by D.M. Prett and M. Morari ), pp. 225 – 250 . Butterworths , Boston , MA ( 1987 ).
   Google Scholar
• Kantor , J.C. , “ A Finite Dimensional Nonlinear Observer for an Exothermic Stirred-Tank Reactor .” Chem. Eng. Sci. , 44 , 1503 – 1510 ( 1989 ).
   Web of Science ®Google Scholar
• Kravaris , C. , and Chung , C.B. , “ Nonlinear State Feedback Synthesis by Global Input/Output Linearization .” AIChE J. , 33 , 592 – 603 ( 1987 ).
   Web of Science ®Google Scholar
• Kravaris , C , and Kantor , J.C. , “ Geometric Methods for Nonlinear Process Control. 1. Background .” Ind. Eng. Chem. Research , 29 , 2295 – 2310 ( 1990 a).
   Web of Science ®Google Scholar
• Kravaris , C. , and Kantor , J.C. , “ Geometric Methods for Nonlinear Process Control. 2. Controller Synthesis .” Ind. Eng. Chem. Research , 29 , 2310 – 2323 ( 1990 b).
   Web of Science ®Google Scholar
• Kravaris , C. , and Wright , R.A. , “ Deadtime Compensation for Nonlinear Processes .” AIChE J. , 35 , 1535 – 1542 ( 1989 ).
   Web of Science ®Google Scholar
• Kravaris , C. , and Soroush , M. , “ Synthesis of Multivariate Nonlinear Controllers by Input/Output Linearization .” AIChEJ. , 36 , 249 – 264 ( 1990 ).
   Web of Science ®Google Scholar
• Limqueco , L.C. , and Kantor , J.C. , “ Nonlinear Output Feedback Control of an Exothermic Reactor .” Comput. Chem. Eng. , 14 , 427 – 437 ( 1990 ).
   Web of Science ®Google Scholar
• McLellan , P.J. , Harris , T.J. , and Bacon , D.W. , “ Error Trajectory Descriptions of Nonlinear Controller Designs .” Chem. Eng. Sci. , 45 , 3017 – 3034 ( 1990 ).
   Web of Science ®Google Scholar
• Morari , M. , and Zafiriou , E. , Robust Process Control , Prentice-Hall , Englewood Cliffs , NJ ( 1989 ).
   Google Scholar
• Shinskey , F.G. , Process Control Systems , 3rd Ed. , McGraw-Hill , New York ( 1988 ).
   Google Scholar
• Smith , O.J.M. , “ Closer Control of Loops with Dead Time .” Chem. Eng. Prog. , 53 , 217 – 219 ( 1957 ).
   Google Scholar
• Su , R. , “ On the Linear Equivalents of Nonlinear Systems .” Syst. Control Lett. , 2 , 48 – 52 ( 1982 ).
   Web of Science ®Google Scholar
• Uppal , A. , Ray , W.H. , and Poore , A.B. , “ On the Dynamic Behaviour of Continuous Stirred Tank Reactors .” Chem. Eng. Sci. , 29 , 967 – 985 ( 1974 ).
   Web of Science ®Google Scholar
• Watanabe , K. , Ishiyama , Y. , and Ito , M. , “ Modified Smith Predictor Control for Multivariable Systems with Delays and Unmeasurable Step Disturbances .” Int. J. Control , 37 , 959 – 973 ( 1983 ).
   Web of Science ®Google Scholar