2011
DOI: 10.1049/iet-cta.2009.0156
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Non-linear and adaptive control of a refrigeration system

Abstract: In a refrigeration process heat is absorbed in an evaporator by evaporating a flow of liquid refrigerant at low pressure and temperature. Controlling the evaporator inlet valve and the compressor in such a way that a high degree of liquid filling in the evaporator is obtained at all compressor capacities ensures a high energy efficiency. The level of liquid filling is indirectly measured by the superheat. Introduction of variable speed compressors and electronic expansion valves enables the use of more sophist… Show more

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Cited by 41 publications
(9 citation statements)
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“…La diferencia en el desempeño temporal de estos controladores sería inapreciable. (14), respectivamente, para un mayor número de frecuencias que (16). Para cada lazo, se representan las magnitudes de las respuestas frecuenciales para todas las plantas del dominio de incertidumbre y la cota de especificación.…”
Section: Control Robusto Qftunclassified
See 1 more Smart Citation
“…La diferencia en el desempeño temporal de estos controladores sería inapreciable. (14), respectivamente, para un mayor número de frecuencias que (16). Para cada lazo, se representan las magnitudes de las respuestas frecuenciales para todas las plantas del dominio de incertidumbre y la cota de especificación.…”
Section: Control Robusto Qftunclassified
“…Por otro lado, el enfoque del problema no ha de ser necesariamente multivariable, sino que las características particulares de la planta de refrigeración pueden simplificar mucho la estrategia de diseño de los controladores. Se partirá de un modelo de simulación [8][9] de un sistema de refrigeración por compresión de vapor de una etapa, de validez contrastada [4][5][14] [16], y que se corresponde con un sistema real. Se mostrará cómo para este caso el empleo de un control descentralizado más un desacoplador en una sola dirección es suficiente para cumplir los objetivos.…”
Section: Introductionunclassified
“…Some authors (Perez et a l, 2004) suggest that the evaporators are complex systems that are required to be linearized in the equilibrium point to control the process. Another work in the control of heat exchangers is presented in Rasmussen and Larsen (2011), in this work a low order non linear model of the evaporator is developed and used in a backstepping design of a nonlinear adaptive controller. The proposed m ethod allows work in a wide range of operating points.…”
Section: Introductionmentioning
confidence: 99%
“…Similarly, a low-order nonlinear evaporator model was developed for backstepping design of a nonlinear adaptive controller [15]. A model predictive control algorithm was applied to compute an optimal command profile of each actuator by formulating a multiple criterion including cycle efficiency and technological constraints [16], based on a low order nonlinear model of a vapor compression cycle proposed in [17].…”
Section: Introductionmentioning
confidence: 99%