Optimisation of power stations with carbon capture plants - the trade-off between costs and net power

被引:58
作者
Harkin, Trent [1 ,2 ]
Hoadley, Andrew [1 ,2 ]
Hooper, Barry [1 ]
机构
[1] Univ Melbourne, Cooperat Res Ctr Greenhouse Gas Technol CO2CRC, Melbourne, Vic 3010, Australia
[2] Monash Univ, Dept Chem Engn, Clayton, Vic 3800, Australia
关键词
CCS; Potassium carbonate; Heat integration; Power; Cost estimation; Optimisation; CO2; CAPTURE; CONFIGURATIONS; INTEGRATION; HEAT; FUEL;
D O I
10.1016/j.jclepro.2011.12.032
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The addition of carbon capture and storage to a power station will impact the net power generated and increase the cost of electricity produced from the power stations. A method is presented to help design the carbon capture and compression process retrofitted to the power station. It combines simulation, automated heat integration and multi-objective optimisation. The methodology is applied to a coal fired power station combined with potassium carbonate based solvent absorption. To capture 90% of the CO2 emissions the energy penalty, the ratio of the change in efficiency of the power station due to the addition of carbon capture and storage relative to the efficiency of the original power station, can be reduced from 38% to 14% using this method. However to minimise the cost of electricity, more modest reductions in energy penalty of 25%-30% are recommended. Crown Copyright (C) 2012 Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:98 / 109
页数:12
相关论文
共 49 条
[11]  
Davidson RM., 2007, POSTCOMBUSTION CARBO
[12]   A fast and elitist multiobjective genetic algorithm: NSGA-II [J].
Deb, K ;
Pratap, A ;
Agarwal, S ;
Meyarivan, T .
IEEE TRANSACTIONS ON EVOLUTIONARY COMPUTATION, 2002, 6 (02) :182-197
[13]   Performance modelling of a carbon dioxide removal system for power plants [J].
Desideri, U ;
Paolucci, A .
ENERGY CONVERSION AND MANAGEMENT, 1999, 40 (18) :1899-1915
[14]   TOTAL SITE TARGETS FOR FUEL, COGENERATION, EMISSIONS, AND COOLING [J].
DHOLE, VR ;
LINNHOFF, B .
COMPUTERS & CHEMICAL ENGINEERING, 1993, 17 :S101-S109
[15]   Towards large scale CCS [J].
Dreher, Trina ;
Dugan, Craig ;
Harkin, Trent ;
Hooper, Barry .
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 :5549-5556
[16]   The effect of boric acid on the vapour liquid equilibrium of aqueous potassium carbonate [J].
Endo, Kohei ;
Nguyen, Que S. ;
Kentish, Sandra E. ;
Stevens, Geoffrey W. .
FLUID PHASE EQUILIBRIA, 2011, 309 (02) :109-113
[17]  
Gas Processors Suppliers Association, 1998, ENG DAT BOOK
[18]   Absorption of carbon dioxide into aqueous potassium carbonate promoted by boric acid [J].
Ghosh, Ujjal K. ;
Kentish, Sandra E. ;
Stevens, Geoff W. .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :1075-1081
[19]   On the use of process integration techniques to generate optimal steam cycle configurations for the power plant industry [J].
Girardin, Luc ;
Bolliger, Raffaele ;
Marechal, Francois .
PRES'09: 12TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2009, 18 :171-176
[20]   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