(545g) Distributed and Multiple Model Predictive Control for Rapid Load-Following Operation of Supercritical Pulverized Coal Power Plants
AIChE Annual Meeting
2022
2022 Annual Meeting
Computing and Systems Technology Division
Networked, Decentralized, and Distributed Control
Wednesday, November 16, 2022 - 5:24pm to 5:43pm
A high-fidelity model of an SCPC plant that is validated with the industrial data is used for developing and evaluating the control algorithms. The MMPC approach partitions the desired operating range of 40% to 100% into multiple regions optimally selected based on the nonlinearity of the region and operating conditions. Linear or simple nonlinear models are optimally identified for each of these ranges. Model weights for an operating region are estimated from Bayesian statistics, updated recursively, based on the model residuals [5]. In the DMPC approach, the main control objectives such as the load control, steam temperature control, pressure control, etc. are split into multiple sub-MPCâs with an efficient communication strategy of their respective states and inputs at desired intervals. This approach is not only computationally easier to solve and implement [6], but also facilitates difference in execution time of the underlying sub-MPCS.
Results are presented to validate the performance of the controllers for disturbance rejection at the nominal load, followed by studies of their relative performance under load-following at different ramp rates across the whole range. During rapid load-following, the magnitude of temperature excursion constrains the rate of change as large temperature excursions can lead to low efficiencies and equipment damage. In this work, the adverse effect of temperature is quantified in terms of evolving thermal stress on boiler components, available through the high-fidelity boiler model that is incorporated into the dynamic model [7]. One of the issues with the DMPC is that they can lead to suboptimal performance. Therefore, in this work, we also investigate synergistic and coordinated control using both MMPC and DMPC to take advantage of both control approaches. The efficacy of the proposed approaches is evaluated by comparing their performances in terms of optimality, constraint satisfaction, convergence characteristics, and computational expense with the industry-standard coordinated control systems.
References:
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[5] M. Kuure-Kinsey, B. Bequette, âMultiple Model Predictive Control Strategy for Disturbance Rejection,â Industrial and Engineering Chemistry Research, Vol. 49, Pages 7983-7989, (2010).
[6] P.D. Christofides, R. Scattolini, D. Muñoz de la Peña, J. Liu, âDistributed Model Predictive Control: A Tutorial Review and Future Research Directions,â Computer & Chemical Engineering, Vol. 51, Pages 21-41, (2013).
[7] K. Hedrick, E. Hedrick, B. Omell, S.E. Zitney, and D. Bhattacharyya, âDynamic Modeling, Parameter Estimation, and Data Reconciliation of a Supercritical Pulverized Coal-Fired Boiler,â Manuscript under Review