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| Titel |
Techno-economic analysis of integrated onshore and offshore UCG-CCS systems to produce electricity, SNG and urea |
| VerfasserIn |
Natalie Nakaten, Krzysztof Kapusta, Dorota Burchart-Korol, Thomas Kempka |
| Konferenz |
EGU General Assembly 2017
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| Medientyp |
Artikel
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| Sprache |
en
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| Digitales Dokument |
PDF |
| Erschienen |
In: GRA - Volume 19 (2017) |
| Datensatznummer |
250150435
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| Publikation (Nr.) |
 EGU/EGU2017-14899.pdf |
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| Zusammenfassung |
| Underground coal gasification (UCG) enables the utilization of coal reserves that are economically not exploitable because of complex geological boundary conditions. In the present study, we investigate site-specific commercial-scale onshore and offshore UCG-systems combined with carbon capture and storage (CCS) in line with electricity, synthetic natural gas (SNG) and fertilizer (urea) production based on data of in-situ trail undertaken at the Wieczorek coal mine (Silesian Basin, Poland) [1] and ex-situ tests on different Polish coals. Hereby, techno-economic modeling approaches according to Kempka et al. [2] and Nakaten et al. [3] have been applied to determine onshore and offshore levelized end-use product costs as well as cost bandwidths resulting from economical, technical and geological uncertainties.
Our analysis results show that the investigated onshore UCG end-use options are by 3 % (SNG), 27 % (electricity) and 47 % (urea) lower than the according market prices, and thus competitive on the Polish energy market. However, due to high costs for the offshore platform and the related infrastructure, offshore UCG end-use products are not economic in view of the EU raw materials and energy market. For UCG-CCS systems, a relevant approach to decrease production costs is a precise management of the oxidizer composition: an oxygen ratio below 30 % by volume and a high UCG-to-syngas conversion efficiency favor the economics of electricity and SNG production, whereby cost-effective urea production under the given boundary conditions is characterized by high CO2 and H2 ratios in the synthesis gas composition. As drilling costs have a limited share on total levelized production costs of 3 % in maximum, uncertainties related to model input parameters affected by drilling costs, e.g., UCG reactor width, are negligible.
From our techno-economic modeling results, we conclude that competitiveness of the investigated onshore UCG-CCS end-use options will be even more profitable in view of the expected future development of natural gas prices.
[1] Stanczyk, K., Howaniec, N., Smolinski, A., Swiadrowski, J., Kapusta, K., Wiatowski, M., Grabowski, J., Rogut, J. (2011): Gasification of lignite and hard coal with air and oxygen enriched air in a pilot scale ex-situ reactor for underground gasification. Fuel, 90, p. 1953-1962, doi:10.1016/j.fuel.2010.12.007.
[2] Kempka, T., Schlüter, R., Hamann, J., Deowan, S., Azzam, R. (2011): Carbon dioxide utilisation for carbamide production by application of the coupled UCG-Urea process. Energy Procedia, 4, p. 2200-2205, doi.org/10.1016/j.egypro.2011.02.107.
[3] Nakaten, N.C., Schlüter, R., Azzam, R. and Kempka, T. (2014): Development of a techno-economic model for dynamic calculation of COE, energy demand and CO2 emissions of an integrated UCG-CCS process. Energy, 66, p. 779-790, doi: 10.1016/j.energy.2014.01.014. |
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