Techno-economic comparison of three technologies for precombustion CO2 capture from a lignite-fired IGCC

被引:18
作者
Roussanaly, Simon [1 ]
Vitvarova, Monika [2 ]
Anantharaman, Rahul [1 ]
Berstad, David [1 ]
Hagen, Brede [1 ]
Jakobsen, Jana [1 ]
Novotny, Vaclav [2 ]
Skaugen, Geir [1 ]
机构
[1] SINTEF Energy Res, NO-7465 Trondheim, Norway
[2] Czech Tech Univ, Fac Mech Engn, Prague 16607 6, Czech Republic
关键词
carbon capture and storage (CCS); technoeconomic comparison; pre-combustion capture; physical solvent; low-temperature capture; CO2-SELECTIVE MEMBRANES; POWER-PLANT; HYDROGEN-PRODUCTION; PROCESS SIMULATION; COAL; TRANSPORT; PERFORMANCE; SELECTION; SYSTEMS; CCS;
D O I
10.1007/s11705-019-1870-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper compares the techno-economic performances of three technologies for CO2 capture from a lignite-based IGCC power plant located in the Czech Republic: (1) Physical absorption with a Rectisol-based process; (2) Polymeric CO2-selective membrane-based capture; (3) Low-temperature capture. The evaluations show that the IGCC plant with CO2 capture leads to costs of electricity between 91 and 120 euro center dot MWh(-1), depending on the capture technology employed, compared to 65 euro center dot MWh(-1) for the power plant without capture. This results in CO2 avoidance costs ranging from 42 to 84 euro center dot tCO2,avoidedmainly linked to the losses in net power output. From both energy and cost points of view, the low-temperature and Rectisol based CO2 capture processes are the most efficient capture technologies. Furthermore, partial CO2 capture appears as a good mean to ensure early implementation due to the limited increase in CO2 avoidance cost when considering partial capture. To go beyond the two specific CO2-selective membranes considered, a cost/membrane property map for CO2-selective membranes was developed. This map emphasise the need to develop high performance membrane to compete with solvent technology. Finally, the cost of the whole CCS chain was estimated at 54 euro center dot tCO2,avoidedonce pipeline transport and storage are taken into consideration.
引用
收藏
页码:436 / 452
页数:17
相关论文
共 61 条
[1]   Hydrogen selective membranes: A review of palladium-based dense metal membranes [J].
Al-Mufachi, N. A. ;
Rees, N. V. ;
Steinberger-Wilkens, R. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2015, 47 :540-551
[2]   Selection of optimal CO2 capture plant capacity for better investment decisions [J].
Anantharaman, R. ;
Roussanaly, S. ;
Westman, S. F. ;
Husebye, J. .
GHGT-11, 2013, 37 :7039-7045
[3]  
Anantharaman R, 2011, DI 4 3 EUROPEAN BEST
[4]   Techno-economic performance of a hybrid membrane - liquefaction process for post-combustion CO2 capture [J].
Anantharaman, Rahul ;
Berstad, David ;
Roussanaly, Simon .
INTERNATIONAL CONFERENCE ON APPLIED ENERGY, ICAE2014, 2014, 61 :1244-1247
[5]  
[Anonymous], 2012, QUAL GUID EN SYST ST
[6]  
[Anonymous], 2013, IHS CERA EUR POW CAP
[7]  
[Anonymous], 2011, COSTS CO2 CAPT TRANS
[8]  
[Anonymous], 2021, IEAGHG technical report 2021-05
[9]  
[Anonymous], 2016, CO2 CAPT NAT GAS PRO
[10]  
[Anonymous], 2007, COST FACT LOC MAN