This paper presents the result of an investigation into the Proportional Integral Plus (PIP) control of nitrate in the second zone of an activated sludge benchmark. A data-based reduced order model is used as the control model and identified using the Simplified Refined Instrumental Variable (SRIV) identification and estimation algorithm. The PIP control design is based on the Non Minimum State Space (NMSS) form and State Variable Feedback (SVF) methodology. The PIP controller is tested against dynamic load disturbances and compared with the response of a well-tuned PI controller
Wastewater Treatment Plant (WWTP) is highly complex with the nonlinearity of control parameters and ...
More stringent requirements on nitrogen removal from wastewater are the motivation for this thesis. ...
A reduced order dynamic model for an activated sludge process performing carbonaceous removal, nitri...
In this research, the decentralized control of an Activated Sludge Process (ASP) with the modern Pro...
This paper investigates the application of multivariable PID (MPID) controllers to wastewater treatm...
Proportional-integral-plus (PIP) controllers exploit the full power of optimal state variable feedba...
In this study, a self-tuning Proportional-Integral-Derivative (PID) controller is applied to a multi...
This paper is concerned with long-range adaptive predictive control of the biological nitrogen remov...
In this paper, a feedforward-cascade controller for dissolved oxygen concentration in an activated s...
The aim of this paper is to present a reduced model of an industrial activated sludge process which ...
In this paper, an optimal Proportional-Integral-Plus (PIP) controller based on State-Dependent Param...
Wastewater treatment plant is a large-scale system and highly known with the nonlinearity of the par...
The aim of this paper is to evaluate several multivariable model-based control algorithms for contro...
In wastewater treatment plants (WWTPs) with biological nitrogen removal it is commonthat large amoun...
Wastewater Treatment Plant (WWTP) is highly complex with the nonlinearity of control parameters and ...
Wastewater Treatment Plant (WWTP) is highly complex with the nonlinearity of control parameters and ...
More stringent requirements on nitrogen removal from wastewater are the motivation for this thesis. ...
A reduced order dynamic model for an activated sludge process performing carbonaceous removal, nitri...
In this research, the decentralized control of an Activated Sludge Process (ASP) with the modern Pro...
This paper investigates the application of multivariable PID (MPID) controllers to wastewater treatm...
Proportional-integral-plus (PIP) controllers exploit the full power of optimal state variable feedba...
In this study, a self-tuning Proportional-Integral-Derivative (PID) controller is applied to a multi...
This paper is concerned with long-range adaptive predictive control of the biological nitrogen remov...
In this paper, a feedforward-cascade controller for dissolved oxygen concentration in an activated s...
The aim of this paper is to present a reduced model of an industrial activated sludge process which ...
In this paper, an optimal Proportional-Integral-Plus (PIP) controller based on State-Dependent Param...
Wastewater treatment plant is a large-scale system and highly known with the nonlinearity of the par...
The aim of this paper is to evaluate several multivariable model-based control algorithms for contro...
In wastewater treatment plants (WWTPs) with biological nitrogen removal it is commonthat large amoun...
Wastewater Treatment Plant (WWTP) is highly complex with the nonlinearity of control parameters and ...
Wastewater Treatment Plant (WWTP) is highly complex with the nonlinearity of control parameters and ...
More stringent requirements on nitrogen removal from wastewater are the motivation for this thesis. ...
A reduced order dynamic model for an activated sludge process performing carbonaceous removal, nitri...