Optimal non‐linear control with application to level control system

References

• Bequette , B.W. 1991 . “Nonlinear Control of Chemical Processes; A Review,” . Industrial & Engineering Chemistry Research , 30 : 1391 – 1413 .
   Web of Science ®Google Scholar
• Brockett , R.W. 1976 . “Nonlinear Systems and Differential Geometry,” . Proceedings of the IEEE , 64 : 61 – 72 .
   Web of Science ®Google Scholar
• Gilbert , E. and Ha , I.J. 1984 . “An Approach to Nonlinear Feedback Control with Applications to Robotics,” . IEEE Transactions on Systems, Man and Cybernetics , 14 : 879
   Web of Science ®Google Scholar
• Henson , M.A. and Seborg , D.E. 1991 . “Critique of Exact Linearization Strategies for Process Control,” . Journal of Process Control , 1 : 122 – 139 .
   Google Scholar
• Hoo , K.A. and Kantor , J.C. 1985 . “An Exothermic Continuous Stirred Tank Reactor Is Feedback Equivalent to a Linear System,” . Chemical Engineering Communication , 37 : 1 – 10 .
   Web of Science ®Google Scholar
• Hoo , K.A. and Kantor , J.C. 1986 . “Linear Feedback Equivalence and Control of an Unstable Biological Reactor,” . Chemical Engineering Communication , 46 : 385 – 399 .
   Web of Science ®Google Scholar
• Huang , H.P. and Wang , G.B. 1992 . “Control and Estimation for Perturbed Nonlinear Processes with Deadtime,” . Chemical Engineering Communication , 117 : 117 – 141 .
   Web of Science ®Google Scholar
• Hunt , L.R. , Su , R. and Meyer , G. 1983 . “Global Transformations of Nonlinear Systems,” . IEEE Transactions on Automatic Control , 28 : 24 – 30 .
   Web of Science ®Google Scholar
• Kravaris , C. 1988 . “Input/Output Linearization : A Nonlinear Analog of Placing Poles at Process Zeros,” . AIChE. Journal , 34 ( 11 ) : 1803 – 1812 .
   Google Scholar
• Kravaris , C. and Chung , C.B. 1987 . “Nonlinear State Feedback Synthesis by Global Input/Output Linearization,” . AIChE. Journal , 33 ( 4 ) : 592 – 603 .
   Web of Science ®Google Scholar
• Kravaris , C. and Kantor , J.C. 1990 . “Geometric Methods for Nonlinear Process Control. 1. Background . Industrial & Engineering Chemistry Research , 29 : 2295 – 2310 .
   Web of Science ®Google Scholar
• Kravaris , C. and Kantor , J.C. 1990 . “Geometric Methods for Nonlinear Process Control 2. Controller Synthesis,” . Industrial & Engineering Chemistry Research , 29 : 2310 – 2323 .
   Web of Science ®Google Scholar
• Limqueco , L.C. and Kantor , J.C. 1990 . “Nonlinear Output Feedback Control of an Exothermic Reactor,” . Computer & Chemical Engineering , 14 : 427 – 437 .
   Web of Science ®Google Scholar
• Liou , C.T. and Hsiue , T.H. 1995 . “Controller Design for Nonlinear Systems via Different Transformations,” . Journal of the Chinese Institute of Chemical Engineers , 26 ( 4 ) : 203 – 212 .
   Google Scholar
• Liou , C.T. and Hsiue , T.H. 1995 . “Exact Linearization and Control of a Continuous Stirred Tank Reactor,” . Journal of the Chinese Institute of Engineers , 18 ( 6 ) : 825 – 833 .
   Web of Science ®Google Scholar
• Liou , C.T. and Hsiue , T.H. 1995 . “Linearization and Control of a Non‐linear Systems via Reaction Curve Method,” . Journal of the Chinese Institute of Chemical Engineers , 26 ( 5 ) : 281 – 292 .
   Google Scholar
• McLellan , P.J. , Harris , T.J. and Bacon , D.W. 1990 . “Error Trajectory Descriptions of Nonlinear Controller Designs,” . Chemical Engineering Science , 5 : 3017 – 3034 .
   Web of Science ®Google Scholar
• Ogunnaike , B.A. 1986 . “Controller Design for Nonlinear Process System via Variable Transformation,” . Industrial & Engineering Chemical Process Design Developement , 25 : 241 – 248 .
   Google Scholar
• Sage , A.P. and White , C.C. III . 1977 . Optimum Systems Control, , 2nd ed. , New Jersey : Prentice‐Hall .
   Google Scholar
• Su , R. 1982 . “On the Linear Equivalents of Nonlinear Systems,” . System & Control Letters , 2 : 48 – 52 .
   Web of Science ®Google Scholar
• Correspondence addressee
   Google Scholar