Simulation-based techno-economic evaluation for optimal design of CO2 transport pipeline network

Applied Energy

Volumn 132, Issue , 2014, Pages 610-620

  Luo, Xiaobo ^a   Wang, Meihong ^a   Oko, Eni ^a   Okezue, Chima ^a  

^a UNIVERSITY OF HULL   (United Kingdom)

Author keywords

CCS; Economic evaluation; Pipeline transport; Process simulation

Indexed keywords

EID: 84907335800     PISSN: 03062619     EISSN: 18729118     Source Type: Journal    
DOI: 10.1016/j.apenergy.2014.07.063     Document Type: Article

References (59)

1. 2 Proc Inst Mech Eng, Part A: J Power Energy 217 1 2003 1 7
2. 2 capture with chemical absorption: a state-of-the-art review Chem Eng Res Des 89 9 2011 1609 1624
3. IEA. Technology roadmap: carbon capture and storage. Paris, France: International Energy Agency; 2013.
4. 2 - application to carbon capture and storage Energy Convers Manage 45 15-16 2004 2343 2353
5. IPCC. Carbon dioxide capture and storage. UK2005. p. 431.
6. IEA. Energy technology perspectives 2012. Paris: International Energy Agency; 2012.
7. US-DOE. Interagency task force on carbon capture and storage. Washington, DC, USA 2010.
8. 2 transport pipeline network design for Humber region in the UK Proc Inst Mech Eng, Part E: J Process Mech Eng 2013 43
9. 2 sequestration Energy Convers Manage 47 6 2006 702 715
10. 2 with application to carbon capture and storage Int J Greenhouse Gas Control 2 2 2008 219 229
11. 2 capture and storage system Appl Energy 86 2 2009 202 213
12. 2 transport process. ASME Turbo Expo 2006: Power for Land, Sea, and Air 8-11.05.06, Barcelona, Spain; 2006.
13. 2 pipeline specification: defining tolerance limits for impurities J Pipeline Eng 11 3 2012 p173
14. 2 pipelines. In: 2008 7th International Pipeline Conference; Calgary, Alberta, Canada: International Petroleum Technology Institute and the Pipeline Division; 2008.
15. A. Chapoy, R. Burgass, B. Tohidi, J. Michael Austell, and C. Eickhoff Effect of common impurities on the phase behavior of carbon-dioxide-rich systems: minimizing the risk of hydrate formation and two-phase flow SPE Journal 16 4 2011 921 930
16. 2 solubility for hydrate formation from carbon dioxide containing water and other impurities Phys Chem Chem Phys 16 18 2014 8623 8638
17. 2 capture and transport Int J Greenhouse Gas Control 1 3 2007 343 354
18. 3 in the European Union Atmos Environ 44 11 2010 1369 1385
19. 2 process- and transport chain in CCS systems - examination of transport and storage processes Chem Erde 70 2010 185 192
20. S. Liljemark, K. Arvidsson, M.T.P. Mc Cann, H. Tummescheit, and S. Velut Dynamic simulation of a carbon dioxide transfer pipeline for analysis of normal operation and failure modes Energy Procedia 4 2011 3040 3047
21. 2-rich mixtures for carbon capture and storage Int J Greenhouse Gas Control 9 2012 446 456
22. 2 transport through use of a trunk pipeline Energy Convers Manage 51 12 2010 2825 2834
23. 2 storage infrastructure using a GIS based linear optimization energy model Environ Model Software 25 12 2010 1754 1768
24. 2 storage 2003. p. 1-115. [cited 06.02.14]. Available from: < http://sequestration.mit.edu/pdf/LFEE_2003-003_RP.pdf>.
25. 2 pipeline infrastructure: an analysis of global challenges and opportunities 2010. [cited 2014 02/06]. Available from: http://www.ccsassociation.org.uk/docs/2010/IEA%20Pipeline%20final%20report%20270410.pdf.
26. 2 transportation: case study in China Energy Procedia 4 2011 5974 5981
27. 2 and energy. Transmission study report. IEA GHG; 2002. p. 1-140.
28. 2 storage cost curve and analysis of the potential for large scale carbon dioxide capture and storage in the people's Republic of China. 2009 Contract No.: PNNL-19091. [cited 2014 02/06]. Available from: < http://www.pnl.gov/main/publications/external/technical_reports/PNNL-19091.pdf>.
29. McCollum DL, Ogden JM. Techno-economic models for carbon dioxide compression, transport, and storage & correlations for estimating carbon dioxide density and viscosity. 2006. p. 1-87. [cited 2014 02/06]. Available from: < http://www.its.ucdavis.edu/research/publication/publication-detail/?pub_id=1047>.
30. GCCSI. Economic assessment of carbon capture and storage technologies: GCCSI; 2011. [cited 2014 02/06]. Available from: < http://www.globalccsinstitute.com/publications/economic-assessment-carbon-capture-and-storage-technologies-2011-update>.
31. Ogden JM, Yang C, Johnson N, Ni J, Johnson J. Conceptual design of optimized fossil energy systems with capture and sequestration of carbon dioxide. 2004 Contract No.: DE-FC26-02NT41623. [cited 2014 02/06]. Available from: < http://www.osti.gov/scitech/biblio/829538>.
32. 2 storage. Part 2: European sector; 2004. p. 1-162. [cited 2014 02/06]. Available from: < http://cdn.globalccsinstitute.com/sites/default/files/publications/95736/building-cost-curves-co2-storage-european-sector.pdf>.
33. 2 pipeline transport Int J Greenhouse Gas Control 16 2013 241 270
34. 2Co Energy. Don Valley CCS Project 2013 [cited 2014 02/06]. Available from: < http://www.2coenergy.com/don_valley_power_project.html>.
35. CPL. About the White Rose CCS Project: Capture Power Limited; 2013 [cited 2014 02/06]. Available from: < http://www.whiteroseccs.co.uk/about-white-rose>.
36. Grid N. Yorkshire and Humber CCS Project 2014 [cited 2014 02/06]. Available from: http://www.ccshumber.co.uk/.
37. G. Soave Equilibrium constants for modified Redlich-Kwong equation of state Chem Eng Sci 27 1972 1196 1203
38. D.Y. Peng, and D.B. Robinson A new two-constant equation of state Ind Eng Chem Fundam 15 1 1976 59 64
39. 2 capture and storage processes Appl Energy 86 6 2009 826 836
40. B.I. Lee, and M.G. Kesler Generalized thermodynamic correlation based on three-parameter corresponding states AIChE J 21 3 1975 510 527
41. M.S. Wertheim Fluids with highly directional attractive forces. I. Statistical thermodynamics J Stat Phys 35 1-2 1984 19 34
42. M.S. Wertheim Fluids with highly directional attractive forces. IV. Equilibrium polymerization J Stat Phys 42 3-4 1986 477 492
43. R. Span, and W. Wagner A new equation of state for carbon dioxide covering the fluid region from the triple-point temperature to 1100 K at pressures up to 800 MPa J Phys Chem Ref Data 25 6 1996 1509 1596
44. O. Kunz, and W. Wagner The GERG-2008 wide-range equation of state for natural gases and other mixtures: an expansion of GERG-2004 J Chem Eng Data 57 11 2012 3032 3091
45. 2 mixtures with other gases Ind Eng Chem Res 2013 10.1021/ie303248q:130227083947003
46. Y. Kim Equation of state for carbon dioxide J Mech Sci Technol 21 5 2007 799 803
47. N. Mac Dowell, F.E. Pereira, F. Llovell, F.J. Blas, C.S. Adjiman, and G. Jackson Transferable SAFT-VR models for the calculation of the fluid phase equilibria in reactive mixtures of carbon dioxide, water, and n-alkylamines in the context of carbon capture J Phys Chem B 115 25 2011 8155 8168
48. N. Mac Dowell, F. Llovell, C.S. Adjiman, G. Jackson, and A. Galindo Modeling the fluid phase behavior of carbon dioxide in aqueous solutions of monoethanolamine using transferable parameters with the SAFT-VR approach Ind Eng Chem Res 49 4 2009 1883 1899
49. 2 capture, transport and storage: review of available experimental data and theoretical models Appl Energy 88 11 2011 3567 3579
50. 2 pipeline rupture. Hazards XX - Process Safety and Environmental Protection Harnessing Knowledge - Challenging Complacency, Manchester, United Kingdom, 14 April 2008 through 17 April 2008, Code 74089.
51. 2 mixtures in the applications of CO2 capture and storage (CCS) processes Appl Energy 86 12 2009 2760 2770
52. Foster NR, Bezanehtak K, Dehghani F. Modeling of phase equilibria for binary and ternary mixture of carbon dioxide, hydrogen and methanol. [cited 2014 02/06]. Available from: http://www.isasf.net/fileadmin/files/Docs/Versailles/Papers/PTs15.pdf.
53. E.ON. 6.23 Equation of state prediction of carbon dioxide properties. Kingsnorth Carbon Capture & Storage Project; 2010. [cited 2014 02/06]. Available from: < http://webarchive.nationalarchives.gov.uk/20111209170139/https:/www.decc.gov.uk/en/content/cms/emissions/ccs/demo_prog/feed/e_on_feed_/transport/transport.aspx>.
54. Whiteside J, editor Increasing project performance using Aspen Kbase. AspenTech Worldwide User Meeting; 2005; Houston. USA.
55. Aspen-Tech. Aspen Icarus Reference Guide: Icarus Evaluation Engine (IEE) V8.0. Burlington, USA: Aspen Technology, Inc.; 2012.
56. 2 sequestration. Thermodynamics and safety problems Energy Convers Manage 76 2013 665 673
57. 2 capture and storage project in the APEC regions: a training manual for policy makers and practitioners; 2005.
58. K. Piessens, B. Laenen, W. Nijs, P. Mathieu, J.M. Baele, and C. Hendriks Policy Support Syst Carbon Capture Storage 45 2008 1 269
59. 2 transport technologies for a group of various size industries Int J Greenhouse Gas Control 12 2013 341 350