This paper studies the performance assessment of linear controllers in univariate feedback control loops, where the processes to be controlled can be approximated by first-order plus dead time models, and the set points are subject to ramp or step changes. The lower bound of the total variation (TV) of control signals is established. Taking the lower bound of TV and that of integrated absolute error (IAE) as benchmarks, an IAE-TV-based performance index is proposed. Four industrial linear control schemes are investigated to find out the conditions simultaneously achieving satisfactory performances in terms of input load disturbance rejection and set point tracking subject to a constraint on the robustness. A novel performance assessment met...
The high seasonality and variability of electricity production from renewable sources has enormous ...
The thesis contains two parts, dead-time compensation and performance monitoring. The first part on ...
Proportional-integral (PI) or proportional-integral-derivative (PID) controllers are still by far th...
This paper studies the design and performance assessment of setpoint feedforward controllers in univ...
This paper assesses the performance of feedforward controllers for disturbance rejection in univaria...
This paper aims at assessing the setpoint tracking performance of PID control loops, under certain c...
Assessment of performance in tracking set-point changes for single loop systems is presented. In con...
The purpose of this paper is to contribute with some refinements to recent methods of analysis of co...
This paper studies the performance assessment of proportional-integral (PI) control loops in terms o...
In industrial feedback control loops, setpoint changes are often in the form of step, ramp or other ...
Abstract: The main concern of this thesis is to assess control loop performance using minimum varian...
Performance assessment tools are very useful in providing information about the control loop perfor...
Assessing the quality of industrial control loops is an important auditing task for the control engi...
Abstract: In this paper, a new local measure of linear controller performance is introduced for line...
Industrial practice in process control shows a very wide gap with respect to the theory, as usually ...
The high seasonality and variability of electricity production from renewable sources has enormous ...
The thesis contains two parts, dead-time compensation and performance monitoring. The first part on ...
Proportional-integral (PI) or proportional-integral-derivative (PID) controllers are still by far th...
This paper studies the design and performance assessment of setpoint feedforward controllers in univ...
This paper assesses the performance of feedforward controllers for disturbance rejection in univaria...
This paper aims at assessing the setpoint tracking performance of PID control loops, under certain c...
Assessment of performance in tracking set-point changes for single loop systems is presented. In con...
The purpose of this paper is to contribute with some refinements to recent methods of analysis of co...
This paper studies the performance assessment of proportional-integral (PI) control loops in terms o...
In industrial feedback control loops, setpoint changes are often in the form of step, ramp or other ...
Abstract: The main concern of this thesis is to assess control loop performance using minimum varian...
Performance assessment tools are very useful in providing information about the control loop perfor...
Assessing the quality of industrial control loops is an important auditing task for the control engi...
Abstract: In this paper, a new local measure of linear controller performance is introduced for line...
Industrial practice in process control shows a very wide gap with respect to the theory, as usually ...
The high seasonality and variability of electricity production from renewable sources has enormous ...
The thesis contains two parts, dead-time compensation and performance monitoring. The first part on ...
Proportional-integral (PI) or proportional-integral-derivative (PID) controllers are still by far th...