The selection of suitable control structures has an important influence on the economic performance of process systems in the presence of disturbances. Economics has been incorporated in the control structure selection problem using different formulations based on different criteria. The back-off approach is based on the idea of minimizing the economic loss that results from the need to back off from the active constraints to avoid violating them in the presence of disturbances. On the other hand, self-optimizing control schemes aim at selecting controlled variables and constant setpoint values, such that the economic loss with respect to optimal operation is minimized in the presence of disturbances. This paper presents a comprehensive stu...
Optimal operation is important to improve productivity to be more competitive, and therefore, increa...
Plantwide control is concerned with the structural decisions involved in the control system design o...
In order to operate continuous processes near the economically optimal steady-state operating point,...
In industrial chemical plants, the selection of controlled variables, manipulated variables, and set...
Chemical processes are usually designed to work at a specified set of conditions, fixed by a combina...
One of the key components in the operation of chemical plants is the ability to operate over a range...
Increased competition in the process industries requires optimal operation and better utilization of...
Increased competition in the process industries requires optimal operation and better utilization of...
Optimal operating conditions in chemical plants are characterized by operation on a number of active...
The ultimate goal in the operation of chemical plants is to work at the possible optimal conditions....
Self-optimizing control is a strategy for selecting controlled variables. It is distinguished by the...
Abstract Rules for control structure design for industrial processes have been extensively proposed ...
Plantwide control is concerned with the structural decisions involved in the control system design o...
Plantwide control is concerned with the structural decisions involved in the control system design o...
Economic optimal operation typically involves operating as close as possible to the active constrain...
Optimal operation is important to improve productivity to be more competitive, and therefore, increa...
Plantwide control is concerned with the structural decisions involved in the control system design o...
In order to operate continuous processes near the economically optimal steady-state operating point,...
In industrial chemical plants, the selection of controlled variables, manipulated variables, and set...
Chemical processes are usually designed to work at a specified set of conditions, fixed by a combina...
One of the key components in the operation of chemical plants is the ability to operate over a range...
Increased competition in the process industries requires optimal operation and better utilization of...
Increased competition in the process industries requires optimal operation and better utilization of...
Optimal operating conditions in chemical plants are characterized by operation on a number of active...
The ultimate goal in the operation of chemical plants is to work at the possible optimal conditions....
Self-optimizing control is a strategy for selecting controlled variables. It is distinguished by the...
Abstract Rules for control structure design for industrial processes have been extensively proposed ...
Plantwide control is concerned with the structural decisions involved in the control system design o...
Plantwide control is concerned with the structural decisions involved in the control system design o...
Economic optimal operation typically involves operating as close as possible to the active constrain...
Optimal operation is important to improve productivity to be more competitive, and therefore, increa...
Plantwide control is concerned with the structural decisions involved in the control system design o...
In order to operate continuous processes near the economically optimal steady-state operating point,...