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- In relation to this article, we declare that there is no conflict of interest.
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Received March 22, 2011
Accepted August 18, 2011
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Effects of burner type on a bench-scale entrained flow gasifier and conceptual modeling of the system with Aspen Plus
Power Generation Lab., KEPCO Research Institute, 65 Munji-ro, Yuseong-gu, Daejeon 305-760, Korea
joongwonlee@kepco.co.kr
Korean Journal of Chemical Engineering, May 2012, 29(5), 574-582(9), 10.1007/s11814-011-0217-z
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Abstract
The integrated gasification combined cycle (IGCC) system is well known for its high efficiency compared with that of other coal fueled power generating systems. In this study, gasification using different types of burners with different oxygen supply angles in a bench-scale entrained flow gasifier was investigated. The effects of the oxygen gas supply angle of the coal burner and resulting oxygen supply location in the gasifier on the syngas composition and temperature of the gasifier were experimentally examined. These changes had a significant influence on the syngas_x000D_
composition of the final stream, carbon conversion, and efficiencies. According to the experimental results, the models using the Aspen Plus process simulator were positioned to define the effects of the experimental parameters and to find the optimum operating conditions in the bench gasifier facility.
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Wen CY, Chaung TZ, Ind. Eng. Chem. Process Des. Dev., 18, 684 (1979)
Govind R, Shah J, AIChE J., 30(1), 79 (1984)
Higman C, Van der Burgt M, 2nd Ed., Elsevier (2003)
Frey CH, Akunuri N, http://www4.ncsu.edu/~frey/reports/Frey_akunuri_2001.pdf (2001)
Martinez E, Vicente W, Salinas Vazquez M, Information Technology., 6, 141 (2006)
Nathen SV, Kirkpatrick RD, Young BR, Energy Fuels, 22(4), 2687 (2008)
Chen CX, Horio M, Kojima T, Chem. Eng. Sci., 55(18), 3861 (2000)
Brown D, Fuchino T, Marechal F, Elsevier, 1661 (2005)
Valero A, Uson S, Energy., 28, 7433 (2003)
Petersen I, Werther J, Chem. Eng. Sci., 44, 717 (2005)
Robinson PJ, Luyben WL, Ind. Eng. Chem. Res., 47(20), 7784 (2008)
Biagini E, Bardi A, Pannocchia G, Tognotti L, Ind. Eng. Chem. Res., 48(19), 9028 (2009)
Perez-Fortes M, Bojarski AD, Velo E, Nougues JM, Puigjaner L, Energy, 34(10), 1721 (2009)
Lee JW, Kim MY, Chi JH, Kim SM, Park SI, Trans. of the Korean Hydrogen and New Energy Society., 21, 425 (2010)
Park SI, Lee JW, Seo HK, Transactions of the Korean Hydrogen and New Energy Society., 21, 470 (2010)
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Aspen Technology, Inc. Aspen Plus Model for Entrained Flow Coal Gasifier, V7.2, http://support.aspentech.com.