The reversed frame normalizing design technique of Y.S. Hung and A.G.F. Mac Farlane (1982) is modified to yield decentralized controllers. This modified technique is applied to a binary distillation control problem. It results in a simple decentralized control law that proves to be superior to conventionally designed PI-controllers and no worse than higher-order decentralized controllers based on constrained H/sub 2/minimization. The basic ideas of this linear multivariable design method are summarized. Then, modifications necessary to achieve (block) diagonal controller transfer-function matrices are outlined. Implications for achievable closed-loop performance are discussed. They are seen to follow directly from the theory of optimal matr...
The problem of controlling binary distillation column effluents by manipulating the reflux and vapor...
ABSTRACT: This work addresses the systematic tuning of proportional−integral (PI) controllers for di...
Abstract: Identification process of the distillation column is the first step for design and impleme...
This dissertation presents three decentralized control systems for the three distillation systems in...
In this dissertation, the design procedures of four typical decentralized PI/PID controller design m...
A robust nonlinear control law is designed to reject unknown feed composition disturbances with over...
The work of S. Skogestad et al. (1988) has generated some interest in controller design for ill-cond...
The authors introduce a novel design procedure for two-degree-of-freedom controllers. The technique ...
Design of robust multivariable nonlinear feddback controllers for dual composition control in a dist...
Reports on experiences with the application of H∞-controller H∞-design methods to distillation proce...
© 2017, Association of Chemists and Chemical Engineers of Serbia. All rights reserved. This paper co...
Utilizing experimental transient data, of a ten-plate pilot plant binary distillation column, report...
The purpose of a multivariable control involves maintaining various control variables at independent...
Control of reactive distillation columns is a challenging task due to the complex dynamics arising f...
In this paper, we report our experience with the design of linear multivariable controllers for a st...
The problem of controlling binary distillation column effluents by manipulating the reflux and vapor...
ABSTRACT: This work addresses the systematic tuning of proportional−integral (PI) controllers for di...
Abstract: Identification process of the distillation column is the first step for design and impleme...
This dissertation presents three decentralized control systems for the three distillation systems in...
In this dissertation, the design procedures of four typical decentralized PI/PID controller design m...
A robust nonlinear control law is designed to reject unknown feed composition disturbances with over...
The work of S. Skogestad et al. (1988) has generated some interest in controller design for ill-cond...
The authors introduce a novel design procedure for two-degree-of-freedom controllers. The technique ...
Design of robust multivariable nonlinear feddback controllers for dual composition control in a dist...
Reports on experiences with the application of H∞-controller H∞-design methods to distillation proce...
© 2017, Association of Chemists and Chemical Engineers of Serbia. All rights reserved. This paper co...
Utilizing experimental transient data, of a ten-plate pilot plant binary distillation column, report...
The purpose of a multivariable control involves maintaining various control variables at independent...
Control of reactive distillation columns is a challenging task due to the complex dynamics arising f...
In this paper, we report our experience with the design of linear multivariable controllers for a st...
The problem of controlling binary distillation column effluents by manipulating the reflux and vapor...
ABSTRACT: This work addresses the systematic tuning of proportional−integral (PI) controllers for di...
Abstract: Identification process of the distillation column is the first step for design and impleme...