Optimal scheduling and its Lyapunov stability for advanced load-following energy plants with CO2 capture

被引:16
作者
Bankole, Temitayo [1 ]
Jones, Dustin [2 ]
Bhattacharyya, Debangsu [1 ]
Turton, Richard [1 ]
Zitney, Stephen E. [1 ,3 ]
机构
[1] West Virginia Univ, Dept Chem & Biomed Engn, Morgantown, WV 26506 USA
[2] Foxboro Inc, Schneider Elect, Foxboro, MA 02035 USA
[3] US DOE, Natl Energy Technol Lab, Morgantown, WV 26507 USA
关键词
CO2; capture; Scheduling; Predictive control; Lyapunov stability; Load-following; IGCC; MODEL-PREDICTIVE CONTROL; CONTROLLED VARIABLE SELECTION; FLEXIBLE OPERATION; POWER-PLANT; SYSTEMS; DESIGN; PATTERNS;
D O I
10.1016/j.compchemeng.2017.10.025
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
In this study, a two-level control methodology consisting of an upper-level scheduler and a lower-level supervisory controller is proposed for an advanced load-following energy plant with CO2 capture. With the use of an economic objective function that considers fluctuation in electricity demand and price at the upper level, optimal scheduling of energy plant electricity production and carbon capture with respect to several carbon tax scenarios is implemented. The optimal operational profiles are then passed down to corresponding lower-level supervisory controllers designed using a methodological approach that balances control complexity with performance. Finally, it is shown how optimal carbon capture and electricity production rate profiles for an energy plant such as the integrated gasification combined cycle (IGCC) plant are affected by electricity demand and price fluctuations under different carbon tax scenarios. The paper also presents a Lyapunov stability analysis of the proposed scheme. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:30 / 47
页数:18
相关论文
共 39 条
  • [1] [Anonymous], 1984, P 16 ANN ACM S THEOR
  • [2] REPRESENTATION OF PROCESS TRENDS .4. INDUCTION OF REAL-TIME PATTERNS FROM OPERATING DATA FOR DIAGNOSIS AND SUPERVISORY CONTROL
    BAKSHI, BR
    STEPHANOPOULOS, G
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 (04) : 303 - 332
  • [3] BANERJEE P, 1992, PROCEEDINGS OF THE 31ST IEEE CONFERENCE ON DECISION AND CONTROL, VOLS 1-4, P3233, DOI 10.1109/CDC.1992.371232
  • [4] Steady-State Simulation and Optimization of an Integrated Gasification Combined Cycle Power Plant with CO2 Capture
    Bhattacharyya, Debangsu
    Turton, Richard
    Zitney, Stephen E.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (03) : 1674 - 1690
  • [5] Birk W., 2003, EUROPEAN CONTROL C E, P2625, DOI [10.23919/ECC.2003.7086437, DOI 10.23919/ECC.2003.7086437]
  • [6] Valuing flexible operation of power plants with CO2 capture
    Chalmers, Hannah
    Leach, Matt
    Lucquiaud, Mathieu
    Gibbins, Jon
    [J]. GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01): : 4289 - 4296
  • [7] CO2 control technology effects on IGCC plant performance and cost
    Chen, Chao
    Rubin, Edward S.
    [J]. ENERGY POLICY, 2009, 37 (03) : 915 - 924
  • [8] Turning CO2 Capture On and Off in Response to Electric Grid Demand: A Baseline Analysis of Emissions and Economics
    Cohen, Stuart M.
    Rochelle, Gary T.
    Webber, Michael E.
    [J]. JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2010, 132 (02): : 0210031 - 0210038
  • [9] Conley A, 2000, IEEE DECIS CONTR P, P5020, DOI 10.1109/CDC.2001.914730
  • [10] A Lyapunov Function for Economic Optimizing Model Predictive Control
    Diehl, Moritz
    Amrit, Rishi
    Rawlings, James B.
    [J]. IEEE TRANSACTIONS ON AUTOMATIC CONTROL, 2011, 56 (03) : 703 - 707