2002
DOI: 10.1016/s0959-1524(01)00051-8
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Disturbance modeling for offset-free linear model predictive control

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Cited by 403 publications
(281 citation statements)
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“…In order to study the tracking performance of the adaptive decoupling switching controller, the product density is changed from 1429.4 to 1435 kg/m 3 at t = 0-2 h. For comparison, the linear GPC control strategy is adopted in this process. The product density is changed from 1435 to 1440 kg/m 3 at t = 2-5 h, and the effect of changes of the specific heat of the liquor are simulated during the process, the specific heat of the liquor is varied from 3.61 to 3.63 kJ/(kg· kJ/(kg·°C) at t = 3 h. The offset-free MPC [28], [29] strategy is adopted for the comparison. Effect of the external disturbance are simulated during t = 5−7 h, where a random bounded disturbance is added to the feed flow rate and the feed density at t = 5, the ranges of the feed flow rate and the feed density are 76-84 m 3 /h and 1361-1369 kg/m 3 , respectively.…”
Section: Simulation Resultsmentioning
confidence: 99%
“…In order to study the tracking performance of the adaptive decoupling switching controller, the product density is changed from 1429.4 to 1435 kg/m 3 at t = 0-2 h. For comparison, the linear GPC control strategy is adopted in this process. The product density is changed from 1435 to 1440 kg/m 3 at t = 2-5 h, and the effect of changes of the specific heat of the liquor are simulated during the process, the specific heat of the liquor is varied from 3.61 to 3.63 kJ/(kg· kJ/(kg·°C) at t = 3 h. The offset-free MPC [28], [29] strategy is adopted for the comparison. Effect of the external disturbance are simulated during t = 5−7 h, where a random bounded disturbance is added to the feed flow rate and the feed density at t = 5, the ranges of the feed flow rate and the feed density are 76-84 m 3 /h and 1361-1369 kg/m 3 , respectively.…”
Section: Simulation Resultsmentioning
confidence: 99%
“…In this work, we will keep the same actuators and sensors in all our analysis. states as outputs [18,19]. Based on the augmented system description an ordinary Kalman filter can be designed and an MPC controller synthesised based on the following performance cost function (6) Where h represents the prediction and control horizon, y sp are reference signals for the controlled outputs, y, and the matrices Q and R give relative weights to the contributions from the individual tracking errors and on the speed of the individual actuators respectively.…”
Section: Control Designmentioning
confidence: 99%
“…But it is also possible to use formulations where the disturbance enters the plant in input, output, state or a combination mixed disturbance models. For all of those model types, properties for detectablity are given in (Muske and Badgwellb, 2002). An alternative disturbance modeling scheme is shown in (Pannocchia and Rawlings, 2001) where a mixed model is used for input and output disturbance where the disturbance state is estimated via a standard Kalman filter using such an augmentation of the system and the prediction model (4) it is possible to minimize cost (7) under constraints 2 2 min s.t.…”
Section: Nominal Mpc With (Mixed) Disturbance Model (Md-mpc)mentioning
confidence: 99%