CLC number: TK224.1
On-line Access: 2020-03-17
Received: 2019-07-31
Revision Accepted: 2020-01-13
Crosschecked: 2020-02-10
Cited: 0
Clicked: 3578
Citations: Bibtex RefMan EndNote GB/T7714
Xiao-qiang Xie, Jian-guo Yang, Chao-yang Zhu, Chuan-huai Liu, Hong Zhao, Zhi-hua Wang. Numerical analysis of reasons for the CO distribution in an opposite-wall-firing furnace[J]. Journal of Zhejiang University Science A, 2020, 21(3): 193-208.
@article{title="Numerical analysis of reasons for the CO distribution in an opposite-wall-firing furnace",
author="Xiao-qiang Xie, Jian-guo Yang, Chao-yang Zhu, Chuan-huai Liu, Hong Zhao, Zhi-hua Wang",
journal="Journal of Zhejiang University Science A",
volume="21",
number="3",
pages="193-208",
year="2020",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.A1900363"
}
%0 Journal Article
%T Numerical analysis of reasons for the CO distribution in an opposite-wall-firing furnace
%A Xiao-qiang Xie
%A Jian-guo Yang
%A Chao-yang Zhu
%A Chuan-huai Liu
%A Hong Zhao
%A Zhi-hua Wang
%J Journal of Zhejiang University SCIENCE A
%V 21
%N 3
%P 193-208
%@ 1673-565X
%D 2020
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.A1900363
TY - JOUR
T1 - Numerical analysis of reasons for the CO distribution in an opposite-wall-firing furnace
A1 - Xiao-qiang Xie
A1 - Jian-guo Yang
A1 - Chao-yang Zhu
A1 - Chuan-huai Liu
A1 - Hong Zhao
A1 - Zhi-hua Wang
J0 - Journal of Zhejiang University Science A
VL - 21
IS - 3
SP - 193
EP - 208
%@ 1673-565X
Y1 - 2020
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.A1900363
Abstract: In practical operations, the carbon monoxide (CO) distribution in an opposite-wall-firing furnace (OWFF) is characterized by a high concentration near the side walls and a low concentration in the center, accompanied by a series of combustion-related issues. To find the reasons for the CO distribution, a numerical study was conducted on a 660 MWe OWFF. The CO concentration profiles, distribution coefficients of coal and air, mixing coefficients, and the aerodynamic characteristics were extracted for analysis. The CO distribution within the furnace greatly depends on the mixing of coal and air. A mismatch between the aerodynamic behaviors of coal and air causes the non-uniform distribution of CO. Taking into consideration that distinctive flow patterns exist within the different regions, the formation mechanisms of the CO distribution can be divided into two components: (1) In the burner region, the collision of opposite flows leads to the migration of gas and particles toward the side wall which, together with the vortexes formed at furnace corners, is responsible for unburned particles concentrated and oxygenized from the furnace center to the side wall. Thus, high CO concentrations appear in these areas. (2) As the over-fire air (OFA) jet is injected into the furnace, it occupies the central region of furnace and pushes the gas from the burner region outward to the side wall, which is disadvantageous for the mixing effect in the side wall region. As a consequence, a U-shaped distribution of CO concentration is formed. Our results contribute to a theoretical basis for facilitating the control of variation in CO concentration within the furnace.
The paper addresses an important issue such as the uneven distribution of CO in a full size pulverized coal burner. It correctly identifies the reason in the slip flow between particles and gas in presence of high acceleration zones.
[1]Bar-Ziv E, Saveliev R, Korytnyi E, et al., 2014. Evaluation of performance of Anglo-Mafube bituminous South African coal in 550 MW opposite-wall and 575 MW tangential-fired utility boilers. Fuel Processing Technology, 123: 92-106.
[2]Baum MM, Street PJ, 1971. Predicting the combustion behaviour of coal particles. Combustion Science and Technology, 3(5):231-243.
[3]Chen XD, Kong LX, Bai J, et al., 2017. Study on fusibility of coal ash rich in sodium and sulfur by synthetic ash under different atmospheres. Fuel, 202:175-183.
[4]Chen ZC, Li ZQ, Jing JP, et al., 2008. The influence of fuel bias in the primary air duct on the gas/particle flow characteristics near the swirl burner region. Fuel Processing Technology, 89(10):958-965.
[5]Chen ZC, Li ZQ, Zhu QY, et al., 2011. Gas/particle flow and combustion characteristics and NOx emissions of a new swirl coal burner. Energy, 36(2):709-723.
[6]Cheng P, 1964. Two-dimensional radiating gas flow by a moment method. AIAA Journal, 2(9):1662-1664.
[7]Choi CR, Kim CN, 2009. Numerical investigation on the flow, combustion and NOx emission characteristics in a 500 MWe tangentially fired pulverized-coal boiler. Fuel, 88(9):1720-1731.
[8]Costa M, Azevedo JLT, 2007. Experimental characterization of an industrial pulverized coal-fired furnace under deep staging conditions. Combustion Science and Technology, 179(9):1923-1935.
[9]Drosatos P, Nikolopoulos N, Agraniotis M, et al., 2016. Numerical investigation of firing concepts for a flexible Greek lignite-fired power plant. Fuel Processing Technology, 142:370-395.
[10]Fan JR, Sun P, Zheng YQ, et al., 1999. Numerical and experimental investigation on the reduction of NOx emission in a 600 MW utility furnace by using OFA. Fuel, 78(12):1387-1394.
[11]Fan WD, Li YY, Lin ZC, et al., 2010. PDA research on a novel pulverized coal combustion technology for a large utility boiler. Energy, 35(5):2141-2148.
[12]Field MA, 1969. Rate of combustion of size-graded fractions of char from a low-rank coal between 1200 K and 2000 K. Combustion and Flame, 13(3):237-252.
[13]He BS, Chen MQ, Liu SM, et al., 2005. Measured vorticity distributions in a model of tangentially fired furnace. Experimental Thermal and Fluid Science, 29(5):537-554.
[14]Hong R, Shen Y, Zhao Z, 2012. Emission characteristics of CO and NOx from opposed firing boiler in a 600 MW supercritical unit. Journal of Chinese Society of Power Engineering, 32(12):922-927.
[15]Huang LK, Li ZQ, Sun R, et al., 2006. Numerical study on the effect of the over-fire-air to the air flow and coal combustion in a 670 t/h wall-fired boiler. Fuel Processing Technology, 87(4):363-371.
[16]Karampinis E, Nikolopoulos N, Nikolopoulos A, et al., 2012. Numerical investigation Greek lignite/cardoon co-firing in a tangentially fired furnace. Applied Energy, 97:514-524.
[17]Kobayashi H, Howard JB, Sarofim AF, 1977. Coal devolatilization at high temperatures. Symposium (International) on Combustion, 16(1):411-425.
[18]Li ZQ, Sun R, Chen LZ, et al., 2002. Effect of primary air flow types on particle distributions in the near swirl burner region. Fuel, 81(6):829-835.
[19]Li ZQ, Jing JP, Chen ZC, et al., 2008. Combustion characteristics and NOx emissions of two kinds of swirl burners in a 300-MWe wall-fired pulverized-coal utility boiler. Combustion Science and Technology, 180(7):1370-1394.
[20]Li ZQ, Li S, Zhu QY, et al., 2014. Effects of particle concentration variation in the primary air duct on combustion characteristics and NOx emissions in a 0.5-MW test facility with pulverized coal swirl burners. Applied Thermal Engineering, 73(1):859-868.
[21]Liu C, Zhao H, Yang WY, et al., 2018. Chemical kinetics simulation of semi-dry dechlorination in coal-fired flue gas. Journal of Zhejiang University-SCIENCE A (Applied Physics & Engineering), 19(2):148-157.
[22]Liu H, Liu YH, Yi GZ, et al., 2013. Effects of air staging conditions on the combustion and NOx emission characteristics in a 600 MW wall fired utility boiler using lean coal. Energy & Fuels, 27(10):5831-5840.
[23]Luo R, Fu JP, Li N, et al., 2015. Combined control of secondary air flaring angle of burner and air distribution for opposed-firing coal combustion. Applied Thermal Engineering, 79:44-53.
[24]Park S, Kim JA, Ryu C, et al., 2013. Combustion and heat transfer characteristics of oxy-coal combustion in a 100 MWe front-wall-fired furnace. Fuel, 106:718-729.
[25]Purimetla A, Cui J, 2009. CFD studies on burner secondary airflow. Applied Mathematical Modelling, 33(2):1126-1140.
[26]Rosin P, Rammler E, 1933. The laws governing the fineness of powdered coal. Journal of the Institute of Fuel, 7:29-36.
[27]Shih TH, Liou WW, Shabbir A, et al., 1995. A new k-ϵ eddy viscosity model for high Reynolds number turbulent flows. Computers & Fluids, 24(3):227-238.
[28]Sivathanu YR, Faeth GM, 1990. Generalized state relationships for scalar properties in nonpremixed hydrocarbon/ air flames. Combustion and Flame, 82(2):211-230.
[29]Smith TF, Shen ZF, Friedman JN, 1982. Evaluation of coefficients for the weighted sum of gray gases model. Journal of Heat Transfer, 104(4):602-608.
[30]Szuhánszki J, Black S, Pranzitelli A, et al., 2013. Evaluation of the performance of a power plant boiler firing coal, biomass and a blend under oxy-fuel conditions as a CO2 capture technique. Energy Procedia, 37:1413-1422.
[31]van der Lans RP, Glarborg P, Dam-Johansen K, 1997. Influence of process parameters on nitrogen oxide formation in pulverized coal burners. Progress in Energy and Combustion Science, 23(4):349-377.
[32]Vikhansky A, Bar-Ziv E, Chudnovsky B, et al., 2004. Measurements and numerical simulations for optimization of the combustion process in a utility boiler. International Journal of Energy Research, 28(5):391-401.
[33]Vuthaluru R, Vuthaluru HB, 2006. Modelling of a wall fired furnace for different operating conditions using FLUENT. Fuel Processing Technology, 87(7):633-639.
[34]Xie XQ, Yang JG, Zhu CY, et al., 2019. Effect of bowl-shaped secondary air distribution on combustion efficiency and NOx mass concentration. Journal of Zhejiang University (Engineering Science), 53(2):220-227 (in Chinese).
[35]Xu MH, Yuan JW, Ding SF, et al., 1998. Simulation of the gas temperature deviation in large-scale tangential coal fired utility boilers. Computer Methods in Applied Mechanics and Engineering, 155(3-4):369-380.
[36]Yang JH, Kim JEA, Hong J, et al., 2015. Effects of detailed operating parameters on combustion in two 500-MWe coal-fired boilers of an identical design. Fuel, 144:145-156.
[37]Yang WJ, You RZ, Wang ZH, et al., 2017. Effects of near-wall air application in a pulverized-coal 300 MWe utility boiler on combustion and corrosive gases. Energy & Fuels, 31(9):10075-10081.
[38]Zhou H, Yang Y, Dong K, et al., 2014. Influence of the gas particle flow characteristics of a low-NOx swirl burner on the formation of high temperature corrosion. Fuel, 134: 595-602.
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