Page 270 - Distributed model predictive control for plant-wide systems
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244                           Distributed Model Predictive Control for Plant-Wide Systems



                                              Communicator
                                                                   ˆ x
                                             …         …
                             MPC 1    MPC 2     Predictor  MPC N   EKF
                                u 1      u 2                 u N
                                                           N
                                       2
                             u →F 1   u →F 2              u →F N
                              1
                                F        F                   F N
                        FT       1        2                          CT
                               PI       PI   …    PI    …   PI






                           Figure 11.3  The structure of DMPC framework for HSLC



             However, for this large-scale, nonlinear, and relatively fast system, the online implementa-
           tion of centralized MPC is impractical due to the large computation. To decrease the compu-
           tational burden and guarantee the performance of overall system at the same time, a DMPC
           framework based on neighborhood optimization and successive linearization is therefore
           proposed for HSLC.


           11.3   Control Strategy of HSLC
           Since the major obstacle of accurate online control of HSLC is the large-scale, nonlinear char-
           acteristics, the DPMC framework is adopted. The whole system is divided into N subsystems
           (the sth subsystem ranges from l s − 1  to l [s = 1, 2, … , N] as shown in Figure 11.2), and each
                                            s
           subsystem is controlled by a local MPC controller as shown in Figure 11.3. Since the strip
           temperature can only be measured at a few positions inside the cooling section due to the
           hard ambient conditions, an EKF is employed to estimate the distribution of strip temperature.
           Each local MPC calculates the set-point of PI controller based on the current strip temperature
           estimated by EKF and the future states of its neighbors. Each PI controller regulates water
           flux to be consistent with the set-point calculated by local MPC. Since there are no manipu-
           lated variables in the subsystems with closed header group, a predictor is substituted for local
           MPC. The predictor estimates the future states of corresponding subsystem and broadcasts
           the estimations to its neighbors. In this way, the EKF, MPCs and predictors, as well as the PI
           controllers work together through network information to control the HSLC.



           11.3.1   State Space Model of Subsystems

           Since it is not easy for MPC to predict the future states using model (11.1), the state space
           representation of model (11.1) for each subsystem is deduced first in this subsection. Using
           two-dimensional finite volumes scheme, model (11.1) can be reduced into a finite-dimensional
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