DocumentCode :
2909259
Title :
Nonlinear model predictive control of IGCC plants with membrane reactors for carbon capture
Author :
Lima, F.V. ; Amrit, Rishi ; Tsapatsis, Michael ; Daoutidis, Prodromos
Author_Institution :
Dept. of Chem. Eng. & Mater. Sci., Univ. of Minnesota, Minneapolis, MN, USA
fYear :
2013
fDate :
17-19 June 2013
Firstpage :
3747
Lastpage :
3752
Abstract :
This paper focuses on the application of a nonlinear model predictive control (MPC) method to coal-based integrated gasification combined cycle (IGCC) plants with water gas shift membrane reactors (WGS-MR) for pre-combustion capture of CO2. A systems-level nonlinear model of the integrated IGCC-MR process is introduced. The simulation results for a steady-state design used as a starting point for the control studies are presented. For such studies, a centralized nonlinear MPC strategy using a collocation-based algorithm is formulated to control power generation according to the demand. This strategy is successfully implemented to address scenarios that consider power load transitions (setpoint tracking) and variability in coal/slurry feed composition (disturbance rejection). The closed-loop simulation results show that power control is attained without violating process constraints related to target specifications and regulations imposed in stream temperatures and purities, including the carbon capture goal of 90% recommended by the U.S. Department of Energy (DOE).
Keywords :
carbon capture and storage; chemical reactors; combined cycle power stations; control system synthesis; nonlinear control systems; power control; power generation control; predictive control; water gas shift; CO2; IGCC plants; MPC method; WGS-MR; carbon capture; centralized nonlinear MPC strategy; closed-loop simulation; coal-based integrated gasification combined cycle plants; coal-slurry feed composition; collocation-based algorithm; integrated IGCC-MR process; nonlinear model predictive control method; power control; power generation control; steady-state design; stream temperatures; systems-level nonlinear model; water gas shift membrane reactors; Carbon; Feeds; Mathematical model; Power generation; Process control; Slurries; Steady-state;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
American Control Conference (ACC), 2013
Conference_Location :
Washington, DC
ISSN :
0743-1619
Print_ISBN :
978-1-4799-0177-7
Type :
conf
DOI :
10.1109/ACC.2013.6580410
Filename :
6580410
Link To Document :
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