The role of CO2 purification and transport networks in carbon capture and storage cost reduction

被引:81
作者
Kolster, Clea [1 ,2 ,3 ]
Mechleri, E. [2 ,3 ]
Krevor, Sam [4 ]
Mac Dowell, Niall [2 ,3 ]
机构
[1] Imperial Coll London, SSCP DTP, Grantham Inst Climate Change & Environm, London SW7 2AZ, England
[2] Imperial Coll London, Ctr Environm Policy, London SW7 1NA, England
[3] Imperial Coll London, Ctr Proc Syst Engn, London SW7 2AZ, England
[4] Imperial Coll London, Dept Earth Sci & Engn, London SW7 2AZ, England
基金
英国自然环境研究理事会; 英国工程与自然科学研究理事会;
关键词
Multi-scale modelling; CCS; Oxy-combustion; FOR; CO2; transport; SIMULATION; COMBUSTION; DESIGN;
D O I
10.1016/j.ijggc.2017.01.014
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A number of Carbon Capture and Storage projects (CCS) are under way around the world, but the technology's high capital and operational costs act as a disincentive to large-scale deployment. In the case of both oxy-combustion and post-combustion CO2 capture, the CO2 compression and purification units (CO2CPU) are vital, but costly, process elements needed to bring the raw CO2 product to a quality that is adequate for transport and storage. Four variants of the CO2CPU were modelled in Aspen HYSYS each of which provide different CO2 product purities at different capital and operating costs. For each unit, a price of CO2 is calculated by assuming that it is an independent entity in which to invest and the internal rate of return (IRR) must be greater or equal to the minimum rate of return on investment. In this study, we test the hypothesis that, owing to the fact that CO2 will likely be transported in multi-source networks, not all CO2 streams will need to be of high purity, and that it may be possible to combine several sources of varying purity to obtain an end-product that is suitable for storage. We find that, when considering study generated costs for an example network in the UK, optimally combining these different sources into one multi-source transport network subject to a minimum CO2 purity of 96% can reduce the price of captured CO2 by 17%. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:127 / 141
页数:15
相关论文
共 55 条
[1]   Multiscale design and analysis of CO2 capture, transport and storage networks [J].
Alhajaj, Ahmed ;
Mac Dowell, Niall ;
Shah, Nilay .
GHGT-11, 2013, 37 :2552-2561
[2]  
Angus V.S., 1977, CHEM INGENIEUR TECHN, V3, P594
[3]  
[Anonymous], 2016, GREENH GAS R D PROGR
[4]  
[Anonymous], 2009, TECHNICAL REPORT
[5]  
Aspen Capital Cost Estimator, 2012, ASP CAP COST EST US
[6]  
Aspen Tech, 2014, ASP EC EV FAM
[7]  
Benton D., 2015, TECHNICAL REPORT
[8]  
Binci F., IN PRESS
[9]   Carbon capture and storage update [J].
Boot-Handford, M. E. ;
Abanades, J. C. ;
Anthony, E. J. ;
Blunt, M. J. ;
Brandani, S. ;
Mac Dowell, N. ;
Fernandez, J. R. ;
Ferrari, M. -C. ;
Gross, R. ;
Hallett, J. P. ;
Haszeldine, R. S. ;
Heptonstall, P. ;
Lyngfelt, A. ;
Makuch, Z. ;
Mangano, E. ;
Porter, R. T. J. ;
Pourkashanian, M. ;
Rochelle, G. T. ;
Shah, N. ;
Yao, J. G. ;
Fennell, P. S. .
ENERGY & ENVIRONMENTAL SCIENCE, 2014, 7 (01) :130-189
[10]  
Campbell R.J., 2013, Increasing the Efficiency of Existing Coal-Fired Power Plants