This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Concentration in a stirred laboratory-scale bioreactor. The controller manipulates the airflow and agitation speed in the reactor. Departing from a mechanistic model that relates the manipulated variables and the oxygen transfer coefficient, linearized local models of the process are obtained. It is observed that there is high variability in the process behavior with the operating point. Then, a Gain-Scheduled controller is proposed. The strategy varies the agitation speed employing a PI control law and varies the air flow according to a switching law that detects saturations in the manipulated variables. The proposed strategy is evaluated in simu...
In this paper, we propose a new strategy to control the yield and productivity of the fermentation p...
The paper presents a fed-batch fermentation technique for bioreactors operating close to their maxim...
In the present work, the results of a complete dynamical analysis of open- and closed-loop continuou...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This report discusses control of dissolved oxygen in a bioreactor where the oxygen supply is manipul...
An adaptive control system for the set-point control and disturbance rejection of biotechnological-p...
Abstract This report discusses control of dissolved oxygen in a biore actor where the oxygen supply ...
The dynamic behavior of open- and closed-loop continuous bioreactors for cultures of substrate-inhib...
The dynamic behavior of open- and closed-loop continuous bioreactors for cultures of substrate-inhib...
The dynamic behavior of open- and closed-loop continuous bioreactors for cultures of substrate-inhib...
In this study, microbial kinetic and oxygen transfer modelling coupled with energy analysis was appl...
In this study, microbial kinetic and oxygen transfer modelling coupled with energy analysis was appl...
In this paper, we propose a new strategy to control the yield and productivity of the fermentation p...
The paper presents a fed-batch fermentation technique for bioreactors operating close to their maxim...
In the present work, the results of a complete dynamical analysis of open- and closed-loop continuou...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This article presents a multi-variable control strategy for the regulation of Dissolved Oxygen Conce...
This report discusses control of dissolved oxygen in a bioreactor where the oxygen supply is manipul...
An adaptive control system for the set-point control and disturbance rejection of biotechnological-p...
Abstract This report discusses control of dissolved oxygen in a biore actor where the oxygen supply ...
The dynamic behavior of open- and closed-loop continuous bioreactors for cultures of substrate-inhib...
The dynamic behavior of open- and closed-loop continuous bioreactors for cultures of substrate-inhib...
The dynamic behavior of open- and closed-loop continuous bioreactors for cultures of substrate-inhib...
In this study, microbial kinetic and oxygen transfer modelling coupled with energy analysis was appl...
In this study, microbial kinetic and oxygen transfer modelling coupled with energy analysis was appl...
In this paper, we propose a new strategy to control the yield and productivity of the fermentation p...
The paper presents a fed-batch fermentation technique for bioreactors operating close to their maxim...
In the present work, the results of a complete dynamical analysis of open- and closed-loop continuou...