Maximizing coal-fired power plant efficiency with integration of amine-based CO2 capture in greenfield and retrofit scenarios

被引:17
作者
Van Wagener, David H. [1 ]
Liebenthal, Ulrich [2 ]
Plaza, Jorge M. [1 ]
Kather, Alfons [2 ]
Rochelle, Gary T. [1 ]
机构
[1] Univ Texas Austin, McKetta Dept Chem Engn, Austin, TX 78712 USA
[2] Hamburg Univ Technol, Inst Energy Syst, D-21073 Hamburg, Germany
关键词
CO2; capture; Integration; Retrofit; Greenfield; CONFIGURATIONS; OPTIMIZATION; TECHNOLOGY; PIPERAZINE; SOLUBILITY; DERIVATION; EVALUATE; IMPACT;
D O I
10.1016/j.energy.2014.04.117
中图分类号
O414.1 [热力学];
学科分类号
摘要
A modeling study was performed to investigate the direct impact of amine CO2 scrubbing on the efficiency of a coal-fired power plant. The full scope of the capture process was simulated with 8 m PZ (piperazine) to estimate the steam, electricity, and cooling water requirements. The steam cycle was simulated for applications of the capture technology to both retrofit and greenfield (optimized new build) coal-fired power plants. The reboiler duty of the stripping column had an optimal molar L/G (liquid to gas ratio) of 4.9 in the absorber and the maximum reboiler temperature of 150 degrees C. Integration of this CO2 capture with a greenfield coal plant yielded an identical optimal L/G, but the optimal reboiler temperature was 140 degrees C, and the decrease in power plant efficiency was 73%. The retrofit case resulted in an optimum case with an L/G of 5.9, a reboiler temperature of 120 degrees C, and a decrease in plant efficiency of 7.0%. When running at the optimal L/G, the optimization sensitivity to the reboiler temperature was low. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:824 / 831
页数:8
相关论文
共 33 条
[1]   Process configuration studies of the amine capture process for coal-fired power plants [J].
Ahn, Hyungwoong ;
Luberti, Mauro ;
Liu, Zhengyi ;
Brandani, Stefano .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2013, 16 :29-40
[2]  
[Anonymous], 2012, FRESH PLAZA
[3]  
Chen E., 2007, THESIS U TEXAS AUSTI
[4]  
Dugas R.E., 2009, CO2 Absorption, Desorption, and Diffusion in Aqueous PZ and MEA
[5]   Solubility of carbon dioxide in aqueous solutions of piperazine in the low gas loading region [J].
Ermatchkov, Viktor ;
Kamps, Alvaro Perez-Salado ;
Speyer, Dirk ;
Maurer, Gerd .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (05) :1788-1796
[6]   Modeling piperazine thermodynamics [J].
Frailie, Peter ;
Plaza, Jorge ;
Van Wagener, David ;
Rochelle, Gary T. .
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 :35-42
[7]   Carbon dioxide capture with concentrated, aqueous piperazine [J].
Freeman, Stephanie A. ;
Dugas, Ross ;
Van Wagener, David H. ;
Nguyen, Thu ;
Rochelle, Gary T. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2010, 4 (02) :119-124
[8]   A review of efficiency penalty in a coal-fired power plant with post-combustion CO2 capture [J].
Goto, Kazuya ;
Yogo, Katsunori ;
Higashii, Takayuki .
APPLIED ENERGY, 2013, 111 :710-720
[9]   Using multi-objective optimisation in the design of CO2 capture systems for retrofit to coal power stations [J].
Harkin, Trent ;
Hoadley, Andrew ;
Hooper, Barry .
ENERGY, 2012, 41 (01) :228-235
[10]  
Hilliard M., 2008, A predictive thermodynamic model for an aqueous blend of potassium carbonate, piperazine, and monoethanolamine for carbon dioxide capture from flue gas