Numerical Study the NOx Emission Characteristics of 600MW Opposed Swirling Coal-Fired Utility Boiler

Article Preview

Abstract:

In this paper, a computational fluid dynamics (CFD) model of a 600 MW opposed swirling coal-fired utility boiler has been established to numerically study the NOx emission characteristics under different ratios of over fire air (OFA) and modes of in-service burner layers. The current CFD model had adopted a chemical percolation devolatilization (CPD) model and been validated by comparing the simulated results with the experimental data. The numerical simulation results show that, with increasing the ratio of OFA, the carbon content in fly-ash increase somewhat linearly and the NOx emission reduce significantly, and the OFA ratio of 30% is optimal with higher burnout of pulverized coal and lower NOx emission. The different in-service burner layer modes have different influences on the residence time of the pulverized-coal particles, effect of air staging in the burner region and flue gas temperature at the exit of the lower furnace. Stopping the upper burner layers can increases the residence time of the pulverized-coal particles, resulting in the reduction of the carbon content in the fly ash and the increase of the pulverized-coal burnout. The flue gas temperature at the exit of the lower furnace can also decrease, which would be helpful to reducing the slagging tendency on the surfaces of the platen superheaters.

You might also be interested in these eBooks

Info:

Periodical:

Advanced Materials Research (Volumes 1010-1012)

Pages:

847-855

Citation:

Online since:

August 2014

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2014 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] X. F. Fan, Z. L. Zhang and S. H. Wu, Design and technological characteristics of the first China-made ultra-supercritical boiler, Journal of Power Engineering, 28(2008) 497-501. In Chinese.

Google Scholar

[2] Z. H. Hu, X. S. Yang and G. J. Wang, Combustion optimization of 1000 MW ultra-supercritical once-through boiler, Boiler Technology, 39(2008) 42-46. In Chinese.

Google Scholar

[3] M. H. Xu, J. L. T. Azevedo and M. G. Carvalho, Modeling of the combustion process and NOx emission in a utility boiler, Fuel, 79(2000) 1611-1619.

DOI: 10.1016/s0016-2361(00)00019-3

Google Scholar

[4] L. B. Thomas, C. Francisco, and C. Sebastien, Coal combustion modelling of large power plant for NOx abatement, Fuel, 86(2007) 2213-2220.

DOI: 10.1016/j.fuel.2007.05.054

Google Scholar

[5] S. Belosevic, M. Sijercic, and P. Stefanovic, A numerical study of pulverized coal ignition by means of plasma torches in air-coal dust mixture ducts of utility boiler furnaces, Int. J. Heat Mass Trans., 51(2008) 1970-(1978).

DOI: 10.1016/j.ijheatmasstransfer.2007.06.003

Google Scholar

[6] L. L. Zhao, Q. T. Zhou, and C. S. Zhao, Flame characteristics in a novel petal swirl burner, Combust. Flame, 155(2008) 277-288.

DOI: 10.1016/j.combustflame.2008.04.012

Google Scholar

[7] Korytnyi, R. Saveliev, M. Perelman, and B. Chudnovsky, Computational fluid dynamic simulations of coal-fired utility boilers: An engineering tool, Fuel, 88(2009) 9-18.

DOI: 10.1016/j.fuel.2008.08.010

Google Scholar

[8] Y. S. Shen, B. Y. Guo, A. B. Yu, and P. Zulli, A three-dimensional numerical study of the combustion of coal blends in blast furnace, Fuel, 99(2009) 255-263.

DOI: 10.1016/j.fuel.2008.08.013

Google Scholar

[9] L. Ma, J. M. Jones, and M. Pourkashanian, Modelling the combustion of pulverized biomass in an industrial combustion test furnace, Fuel, 86(2007) 1959-(1965).

DOI: 10.1016/j.fuel.2006.12.019

Google Scholar

[10] C. G. Yin, L. Rosendahl, and S. K. Kær, Mathematical modeling and experimental study of biomass combustion in a thermal 108 MW grate-fired boiler, Energy Fuels, 22(2008) 1380-1390.

DOI: 10.1021/ef700689r

Google Scholar

[11] K. D. Tiggesa, F. Klaukea, and K. Busekrus, Conversion of existing coal-fired power plants to oxyfuel combustion: case study with experimental results and CFD simulations, Energy Procedia, 1(2009) 549-556.

DOI: 10.1016/j.egypro.2009.01.073

Google Scholar

[12] D. Toporov, P. Bocian, and A. Kellermann, Detailed investigation of a pulverized fuel swirl flame in CO2/O2 atmosphere, Combust. Flame, 155(2006) 605-618.

DOI: 10.1016/j.combustflame.2008.05.008

Google Scholar

[13] C. M. Shen, R. Sun, and S. H. Wu, Numerical simulation of pulverized coal combustion in a 1GW dual circle tangential firing single chamber boiler, Proceedings of the CSEE, 26(2006) 51-56. In Chinese.

Google Scholar

[14] W. G. Zhang, Numerical simulation of air-staged combustion in utility boiler, Power System Engineering, 24(2008) 9-12. In Chinese.

Google Scholar

[15] L. D. Smoot and P. J. Smith, Coal Combustion and Gasification, New York: Plenum Press, (1989).

Google Scholar

[16] S. C. Hill and L. D. Smoot, Modeling of nitrogen oxides formation and destruction in combustion systems, Prog. Energ. Combust., 26(2000) 417-458.

DOI: 10.1016/s0360-1285(00)00011-3

Google Scholar

[17] G. De Soete, Overall reaction rates of NO and N2 formation from fuel nitrogen. 15th Symposium (international) on Combustion, Pittsburgh, PA. 1975, pp.1093-1102.

DOI: 10.1016/s0082-0784(75)80374-2

Google Scholar

[18] D. Genetti and T. H. Fletcher, Modeling nitrogen release during devolatilization on the basis of chemical structure of coal, Energy Fuels, 13(1999)1082-1091.

DOI: 10.1021/ef990056i

Google Scholar

[19] S. T. Perry and T. H. Fletcher, Modeling nitrogen evolution during coal pyrolysis based on a global free-radical mechanism, Energy Fuels, 14(2000)1094-1102.

DOI: 10.1021/ef000061i

Google Scholar