ABSTRACT Three-tank benchmark system is a nonlinear multivariable process that is a good prototype of chemical industrial processes. The open loop process is unstable inherently, thus a proper controller must be applied to stabilize the system as well as reaching good dynamic response. In this paper, several controllers have been proposed using pole-placement with integral control. Then, the best controller is selected considering deterministic and stochastic performances. Deterministic performance was evaluated using step test on closed loop. Minimum variance (MV) index was used for stochastic performance assessment. Multivariate time series (MTS) is cached from sampled outputs of the simulated system in closed loop. Then, maxlikelihood m...
A nonlinear version of the Generalized Minimum Variance (GMV) multivariable control law has been rec...
444-449This paper discusses the control of non-linear multivariable process named as Completely Mo...
Several of the practical industrial control processes are multivariable processes. Due to the relati...
Three-tank benchmark system is a nonlinear multivariable process that is a good prototype of chemica...
Abstract: The main concern of this thesis is to assess control loop performance using minimum varian...
A complex system usually comprises numerous loops that are controlled by local SISO controllers. The...
A minimum-variance control problem is defined that involves the minimisation of the integral of esti...
Control loop performance assessment analyses routine operating data to identify poorly performing co...
Modeling and designing a suitable controller for a process plays a crucial role in deciding the e...
This paper proposes to study the potential of use a three-tank system in laboratory scale to teach h...
With the advancement of control system, Model Predictive Control has taken over the mainstream PID c...
A three-tank process has difficulty in controller design because of nonlinear flow and interactions ...
The important part of a process industry is the analysis of chemical processes and controlling proce...
Process control and performance analysis are the key features of any industry. This report provides ...
The use of the generalised minimum variance control law for control loop performance assessment and ...
A nonlinear version of the Generalized Minimum Variance (GMV) multivariable control law has been rec...
444-449This paper discusses the control of non-linear multivariable process named as Completely Mo...
Several of the practical industrial control processes are multivariable processes. Due to the relati...
Three-tank benchmark system is a nonlinear multivariable process that is a good prototype of chemica...
Abstract: The main concern of this thesis is to assess control loop performance using minimum varian...
A complex system usually comprises numerous loops that are controlled by local SISO controllers. The...
A minimum-variance control problem is defined that involves the minimisation of the integral of esti...
Control loop performance assessment analyses routine operating data to identify poorly performing co...
Modeling and designing a suitable controller for a process plays a crucial role in deciding the e...
This paper proposes to study the potential of use a three-tank system in laboratory scale to teach h...
With the advancement of control system, Model Predictive Control has taken over the mainstream PID c...
A three-tank process has difficulty in controller design because of nonlinear flow and interactions ...
The important part of a process industry is the analysis of chemical processes and controlling proce...
Process control and performance analysis are the key features of any industry. This report provides ...
The use of the generalised minimum variance control law for control loop performance assessment and ...
A nonlinear version of the Generalized Minimum Variance (GMV) multivariable control law has been rec...
444-449This paper discusses the control of non-linear multivariable process named as Completely Mo...
Several of the practical industrial control processes are multivariable processes. Due to the relati...