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- W4200408174 abstract "One of the methods that has gained popularity in controller design for nonlinear systems is to find some global transformations which converts the nonlinear model in the original variable into an exact linear model in a different set of variables. Linear controller design methods can then be easily applied on the equivalent linear system with a back transformation to the original variables for implementation purposes. Consequent upon this, two types i.e. Type I and Type II of global linearizing transformations for a single, isothermal continuous stirred tank reactor (CSTR) used for ethylene hydrogenation are derived using literature techniques for first-order nonlinear systems. These are then used to carry out alternate nonlinear control designs for the set point and regulatory control of the exit concentration of an isothermal CSTR used for ethylene hydrogenation which exhibits multiplicity of steady-states. For set point change control, simulation results show that the nominal performance of the Type II variable transformation controller is better than that of the Type I variable transformation controller while the latter seemed to have better regulatory control performance. However, simulation results of the sensitivity/robustness of the nonlinear controllers to modeling errors and measurement noise investigated showed the Type I variable transformation controller to be better than the Type II for both set point change over a wide operating span, and regulatory control at an unstable steady-state point." @default.
- W4200408174 created "2021-12-31" @default.
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- W4200408174 date "2021-01-01" @default.
- W4200408174 modified "2023-10-18" @default.
- W4200408174 title "Performance and Robustness of Alternate Nonlinear Control System Designs for a Nonlinear Isothermal CSTR" @default.
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- W4200408174 doi "https://doi.org/10.1016/j.ifacol.2021.12.022" @default.
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