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Simplified schematic view of a coal-fired subcritical boiler-turbine (B-T) unit.

Simplified schematic view of a coal-fired subcritical boiler-turbine (B-T) unit.

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Article
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This paper proposes a nonlinear model predictive control (NMPC) strategy based on a local model network (LMN) and a heuristic optimization method to solve the control problem for a nonlinear boiler–turbine unit. First, the LMN model of the boiler–turbine unit is identified by using a data-driven modeling method and converted into a time-varying glo...

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Context 1
... schematic of a typical coal-fired subcritical drum-type boiler-turbine unit is shown in Figure 1. The boiler transfers the chemical energy of fuel into the thermal energy of steam, which is directly fed to the turbine where the thermal energy is converted into mechanical energy and the generator is driven to generate electricity. ...
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... schematic of a typical coal-fired subcritical drum-type boiler-turbine unit is shown in Figure 1. The boiler transfers the chemical energy of fuel into the thermal energy of steam, which is directly fed to the turbine where the thermal energy is converted into mechanical energy and the generator is driven to generate electricity. ...
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... model accuracy was verified by the field data. The model is in the form of Figure 1. Simplified schematic view of a coal-fired subcritical boiler-turbine (B-T) unit. ...
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... LMN model of the 500 MW coal-fired B-T unit shown in Figure 1 is identified to provide the prediction mode for the proposed nonlinear predictive control method. In order to fully stimulate the nonlinearity of the B-T unit under different load conditions, two uncorrelated modified pseudo-random sequences are respectively applied to the two manipulated variables u B and u T to generate identification data, as shown in Figure 7. ...
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... time t = 400 s, the setpoint of output power N E is increased by 20 MW, and at time t = 1200 s, the setpoint of N E is decreased by 20 MW and returned to 450 MW, while the main steam pressure P T is kept unchanged. The responses of outputs N E and P T as well as the control inputs u B and u T are shown in Figure 10. The similar test is also carried out under 60% load condition (N E = 300 MW,P T = 11.69 ...
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... similar test is also carried out under 60% load condition (N E = 300 MW,P T = 11.69 MPa), and the results are shown in Figure 11. ...
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... can be seen from Figures 10 and 11 that, for the NMPC, no matter whether under high-load or low-load condition, under the premise of satisfying the constraints on the control action, the output power can be quickly tracked to its setpoint without overshoot, and the fluctuation of main steam pressure is small. The setting time is no more than 250 s and the maximum deviation of main steam pressure is less than 0.3 MPa. ...
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... 2: The second case is designed to test the tracking capability of the proposed control strategy under wide-range operation, which simulates the automatic generation control (AGC) operation. As shown in Figure 12, the unit is operating in variable-steam-pressure mode; the setpoint of the output power is first increased linearly from 400 (80% load condition) to 500 MW (100% load condition) at a rate of 2% maximum continuous rating/min, then the setpoint is decreased to 250 MW (50% load condition) at the same rate, and finally ramped back to 400 MW. Meanwhile, the setpoint of the main steam pressure is changed in proportion to the load. ...
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... can be observed from Figure 12 that good tracking behavior of the power and main steam pressure is obtained by using the proposed NMPC. The performance of LMPC is worse than the NMPC, especially in the main steam pressure, where a huge control offset occurred under low-load conditions, which is due to the significant modeling mismatch caused by the nonlinearity of the B-T unit. ...
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... indicates the dynamic behavior of the unit has changed significantly; and the setpoints of output power and main steam pressure are changed the same as in Case 2. The responses of the NMPC system under wide-range operation are shown in Figure 13. It can be seen that both the output power and main steam pressure can track the change of their setpoints rapidly and steadily even if the dynamic behavior of the B-T unit has changed significantly, which indicates that the nonlinear predictive control based on an LMN and IGA has strong robustness. ...
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... can be seen that both the output power and main steam pressure can track the change of their setpoints rapidly and steadily even if the dynamic behavior of the B-T unit has changed significantly, which indicates that the nonlinear predictive control based on an LMN and IGA has strong robustness. Since the control performances of LMPC and PI are very poor in this severe situation, they are not shown in Figure 13. operation. As shown in Figure 12, the unit is operating in variable-steam-pressure mode; the setpoint of the output power is first increased linearly from 400 (80% load condition) to 500 MW (100% load condition) at a rate of 2% maximum continuous rating/min, then the setpoint is decreased to 250 MW (50% load condition) at the same rate, and finally ramped back to 400 MW. ...
Context 12
... As shown in Figure 12, the unit is operating in variable-steam-pressure mode; the setpoint of the output power is first increased linearly from 400 (80% load condition) to 500 MW (100% load condition) at a rate of 2% maximum continuous rating/min, then the setpoint is decreased to 250 MW (50% load condition) at the same rate, and finally ramped back to 400 MW. Meanwhile, the setpoint of the main steam pressure is changed in proportion to the load. ...
Context 13
... can be observed from Figure 12 that good tracking behavior of the power and main steam pressure is obtained by using the proposed NMPC. The performance of LMPC is worse than the NMPC, especially in the main steam pressure, where a huge control offset occurred under low-load conditions, which is due to the significant modeling mismatch caused by the nonlinearity of the B-T unit. ...
Context 14
... PI control shows the worst performance and is completely unable to deal with the rapidly changing operating conditions. which indicates the dynamic behavior of the unit has changed significantly; and the setpoints of output power and main steam pressure are changed the same as in Case 2. The responses of the NMPC system under wide-range operation are shown in Figure 13. It can be seen that both the output power and main steam pressure can track the change of their setpoints rapidly and steadily even if the dynamic behavior of the B-T unit has changed significantly, which indicates that the nonlinear predictive control based on an LMN and IGA has strong robustness. ...
Context 15
... can be seen that both the output power and main steam pressure can track the change of their setpoints rapidly and steadily even if the dynamic behavior of the B-T unit has changed significantly, which indicates that the nonlinear predictive control based on an LMN and IGA has strong robustness. Since the control performances of LMPC and PI are very poor in this severe situation, they are not shown in Figure 13. ...
Context 16
... taking the identified local model network of the nonlinear system as the prediction model, a nonlinear predictive control strategy based on an immune genetic algorithm (IGA) optimization is proposed in this paper to improve the control performance of the boiler-turbine (B-T) unit, because of its ability in dealing with the control constraints and nonlinearity. An accurate local model Figure 13. Case 3: Output responses and control inputs of the system under wide-range operation in the presence of model mismatch. ...

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... The boiler combustion efficiency can be efficiently controlled by the model predictive control algorithm, and the average simulation error is about 5%. Zhu et al. (2019) developed a nonlinear model predictive control technique based on a local model network and a heuristic optimization method to address the control issue of a nonlinear boiler-turbine unit, and the results show limited tracking capacity. To control the steam temperature of a power plant boiler, Tavoosi and Mohammadzadeh (2021) introduced RBF network-based model predictive control. ...
... To address this, Hyatt et al. [11] propose a parallelized GA implementation that can solve NMPC problems in real-time by evaluating multiple candidate control inputs simultaneously on a GPU. Additionally, in [12], [13], a specially designed GA is used to solve the nonlinearly constrained optimization problem for predictive control in an online setting. ...
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... Moreover, a nonlinear model predictive control strategy based on a local model network is used to deal with the control problem of a 500 MW boiler-turbine unit. As a result, a good tracking behavior of the power and the main steam pressure was obtained [9]. However, the above scheme is restricted by the safety of coal-fired units, where an intelligent control algorithm increases the complexity of the control system. ...
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