1
artículo
Publicado 2014
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Experimental results are presented adaptive control with reference model of a plant according to your previously made identification can be represented as a first order system. Is chosen as the reference model also one of the first order with unity gain. Adaptive controller analysis is performed, justifying its performance in closed loop depends on the proper choice of a scale parameter adjustable. The controller is implemented and temporary plant responses to step inputs for different kinds of adjustable parameter values are recorded.
2
artículo
Publicado 2010
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This paper presents a methodology for designing a strategy proportional integral controller (PI) given that the policy will be implemented in an industrial process controller. The design considers the modeling of the plant through analog techniques of system identifi cation. It is used in controller design algorithm discrete digital PI controller that is running the process controller used. Considered for the design specifi cations of closed loop time response primarily to obtain a settling time line that you can be met without exceeding the range of the control signal that can deliver the process controller used. Implement the control system to verify the behavior of the closed loop system in relation to the specifi ed control objective.
3
artículo
This paper presents a study of the effect of delay in the performance of closed loop systems control plants that can be modeled as second order sobreamortiguadas, in which were not considered the delay in the controller design. They choose the types of plants representative of the second order and are designed for each driver to the classic controller as proportional integral derivative (PID). Experienced with test plants which are conducted previously analog and identification procedures are then controlled by the PID incorporating delays corresponding to plants is not considered in the design. Tests are performed to obtain the corresponding closed-loop performance parameters measured dynamic response to the output of the plant.
4
artículo
Publicado 2010
Enlace
Enlace
This paper presents a methodology for designing a strategy proportional integral controller (PI) given that the policy will be implemented in an industrial process controller. The design considers the modeling of the plant through analog techniques of system identifi cation. It is used in controller design algorithm discrete digital PI controller that is running the process controller used. Considered for the design specifi cations of closed loop time response primarily to obtain a settling time line that you can be met without exceeding the range of the control signal that can deliver the process controller used. Implement the control system to verify the behavior of the closed loop system in relation to the specifi ed control objective.
5
artículo
This paper presents a study of the effect of delay in the performance of closed loop systems control plants that can be modeled as second order sobreamortiguadas, in which were not considered the delay in the controller design. They choose the types of plants representative of the second order and are designed for each driver to the classic controller as proportional integral derivative (PID). Experienced with test plants which are conducted previously analog and identification procedures are then controlled by the PID incorporating delays corresponding to plants is not considered in the design. Tests are performed to obtain the corresponding closed-loop performance parameters measured dynamic response to the output of the plant.
6
artículo
Publicado 2014
Enlace
Enlace
Experimental results are presented adaptive control with reference model of a plant according to your previously made identification can be represented as a first order system. Is chosen as the reference model also one of the first order with unity gain. Adaptive controller analysis is performed, justifying its performance in closed loop depends on the proper choice of a scale parameter adjustable. The controller is implemented and temporary plant responses to step inputs for different kinds of adjustable parameter values are recorded.