2017 Annual Meeting
(756d) Design and Implementation of MPC Strategies for Supercritical Pulverized Coal-Fired Power Plant Cycling with Carbon Capture
In this work, the design and implementation of linear and nonlinear model predictive control (MPC) strategies are performed for base-load and cycling scenarios. The application system is a supercritical pulverized coal-fired (SCPC) power plant with post-combustion carbon capture. The linear MPC control strategy is based on the dynamic matrix control (DMC) method. For this method, a multiple-input-multiple-output dynamic matrix is obtained by performing step response tests in the SCPC plant. The proposed nonlinear MPC strategy is an extension of NLMPC, which is based on the direct transcription method [3, 4]. For the NLMPC implementation, the nonlinear programming (NLP) solver IPOPT is employed, which is an efficient interior point-based large-scale nonlinear optimization algorithm [5]. Also, an open-source automatic differentiation package ADOL-C is used for improving the accuracy and calculation speed of system derivatives [6]. For the extended nonlinear MPC strategy, sequential quadratic programming (SQP) algorithms are analyzed for potential computational improvements when solving the posed NLP problem related to the large-scale power plant application.
In this presentation, a number of scenarios for the SCPC power plant will be discussed including: (i) trajectory tracking associated with power generation demands according to cycling starting from the original power generation setpoint; (ii) disturbance rejection for maintaining the carbon capture rate. In this case, the power generation should be kept at the original setpoint while potential disturbances affect the system, such as the carbon content in the coal is changed; and (iii) combination of both setpoint tracking and disturbance rejection cases. Preliminary results on the implementation of the DMC strategy for the carbon capture sub-system show that the controller can successfully keep the carbon capture rate at the specified 90% setpoint when the fluegas flowrate entering the system acts as step and ramp disturbances. Results on the closed-loop responses for different scenarios related to the SCPC plant will be compared and analyzed considering the advanced linear and nonlinear MPC strategies.
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