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Assessment and Future Directions of Nonlinear Model Predictive ...

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Receding-Horizon Estimation <strong>and</strong> Control <strong>of</strong> Ball Mill Circuits 4914 Numerical ResultsIn this section, the combined scheme (s<strong>of</strong>tware sensor + NMPC) is evaluated insimulation, using a typical test run corresponding to a setpoint change. Point1 in Figure 2 (where y =[0.86 0.35] T ) is the initial operating condition, <strong>and</strong>point 2 (with y =[0.90 0.31] T ) represents the target (this point correspondsto a higher product fineness <strong>and</strong> near maximum product flow rate). The samplingperiod T s = 5 min <strong>and</strong> the prediction horizon is 80 min (Np = 16). Twomanipulated variable moves are used (Nu = 2) <strong>and</strong> the weighting matrix Q i ischosen as a constant identity matrix. Amplitude saturations are qCmax<strong>and</strong> Reg max = 100. Limits for the rates <strong>of</strong> change are ∆qCmax<strong>and</strong> ∆Reg max = 80. Limits on the mill flow rate are q min=60 tonhour= 15 tonhourtonM = 60hour<strong>and</strong>qMmax ton=90hour. The observer parameters are defined in Section 3.2.It is first assumed that the process model is accurate <strong>and</strong> that the measurementsare noise free. Figure 4 shows the controlled <strong>and</strong> the manipulated variables (solidlines). The performance is satisfactory, the controlled variables reach the setpointafter about 20 min <strong>and</strong> the steady state is obtained after 70 min. Moreover, constraintsare active in the first 5 min (first sample), as the maximum register displacement<strong>and</strong> the maximum rate <strong>of</strong> change <strong>of</strong> the input flow rate are required.The performance <strong>of</strong> the control scheme is then tested when measurementsare subject to a noise with a maximum absolute error <strong>of</strong> 0.02 tonm(around a 5%maximum relative error). The s<strong>of</strong>tware sensor can efficiently take these stochasticdisturbances into account, <strong>and</strong> the performance <strong>of</strong> the control scheme remainsquite satisfactory.Finally, the influence <strong>of</strong> parametric uncertainties (plant-model mismatch dueto errors at the identification stage) is investigated. A parametric sensitivityanalysis is performed, <strong>and</strong> Figure 5 shows step responses corresponding to eitheran accurate model or to a −10% error in the fragmentation rate or the transportvelocity. Clearly, fragmentation parameters (which represents material hardness0.920.315w P;30.910.90.890.880.870.86w M;20.310.850 20 40 60 80 1000.3050 20 40 60 80 100100408035Reg (%)60q C(t/h)304025200 20 40 60 80 100time (min)200 20 40 60 80 100time (min)Fig. 4. NMPC <strong>and</strong> state observer; solid: noise-free measurements, dashed: measurementscorrupted by white noise

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