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Frontiers in Energy

ISSN 2095-1701

ISSN 2095-1698(Online)

CN 11-6017/TK

Postal Subscription Code 80-972

2018 Impact Factor: 1.701

Front. Energy    2021, Vol. 15 Issue (1) : 132-142    https://doi.org/10.1007/s11708-020-0803-z
RESEARCH ARTICLE
Industrial-scale investigations on effects of tertiary-air declination angle on combustion and steam temperature characteristics in a 350-MW supercritical down-fired boiler
Xiaoguang LI1, Lingyan ZENG1(), Hongye LIU1, Yao LI2, Yifu LI2, Yunlong ZHAO3, Bo JIAO3, Minhang SONG1, Shaofeng ZHANG1, Zhichao CHEN1, Zhengqi LI1
1. School of Energy Science and Engineering, Harbin Institute of Technology, Harbin 150001, China
2. Guizhou Wanfeng Electric Power Co., Ltd., Xingyi 562400, China
3. Guizhou Xingyi Project Department, Huadian United (Beijing) Power Engineering Co., Ltd., Xingyi 562400, China
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Abstract

Industrial-scale experiments were conducted to study the effects of tertiary air declination angle (TDA) on the coal combustion and steam temperature characteristics in the first 350-MW supercritical down-fired boiler in China with the multiple-injection and multiple-staging combustion (MIMSC) technology at medium and high loads. The experimental results indicated that as the TDA increased from 0° to 15°, the overall gas temperature in the lower furnace rose and the symmetry of temperature field was enhanced. The ignition distance of the fuel-rich coal/air flow decreased. In near-burner region, the concentration of O2 decreased while the concentrations of CO and NO increased. The concentration of NO decreased in near-tertiary-air region. The carbon in fly ash decreased significantly from 8.40% to 6.45% at a load of 260 MW. At a TDA of 15°, the ignition distances were the shortest (2.07 m and 1.73 m) at a load of 210 MW and 260 MW, respectively. The main and reheat steam temperatures were the highest (557.2°C and 559.4°C at a load of 210 MW, 558.4°C and 560.3°C at a load of 260 MW). The carbon in fly ash was the lowest (4.83%) at a load of 210 MW. On changing the TDA from 15° to 25°, the flame kernel was found to move downward and the main and reheat steam temperatures dropped obviously. The change of TDA has little effect on NOx emissions(660–681 mg/m3 at 6% O2). In comprehensive consideration of the pulverized coal combustion characteristics and the unit economic performance, an optimal TDA of 15° is recommended.

Keywords supercritical down-fired boiler      industrial-scale experiment      tertiary air declination angle      coal combustion      steam temperature     
Corresponding Author(s): Lingyan ZENG   
Online First Date: 26 March 2020    Issue Date: 19 March 2021
 Cite this article:   
Xiaoguang LI,Lingyan ZENG,Hongye LIU, et al. Industrial-scale investigations on effects of tertiary-air declination angle on combustion and steam temperature characteristics in a 350-MW supercritical down-fired boiler[J]. Front. Energy, 2021, 15(1): 132-142.
 URL:  
https://academic.hep.com.cn/fie/EN/10.1007/s11708-020-0803-z
https://academic.hep.com.cn/fie/EN/Y2021/V15/I1/132
Case (Load) Design parameter (350 MW) Operating parameter
212 MW 210 MW 213 MW 259 MW 261 MW 262 MW
TDA/(° ) 0 0 15 25 0 15 25
Flow rate of the main steam/(t·h–1) 1117 669 670 675 880 880 908
Pressure of the main steam/MPa 25.4 20.1 20.2 20.2 22.5 22.1 23.1
Total flux of the primary air/(t·h–1) 241 253 259 255 249 255 252
Temperature of the secondary air/° C 120 115 113 114 101 98 99
Total flux of the secondary air/(t·h–1) 1007 714 718 721 1088 1072 1091
Temperature of the secondary air/°C 356 320 322 319 318 319 317
Damper opening of secondary air/% 100 35 35 35 60 60 60
Damper opening of tertiary air/% 100 50 50 50 60 60 60
Damper opening of OFA/% 100 20 20 20 15 15 15
Temperature of main steam/°C 571.0 555.1 557.2 551.2 557.8 558.4 546.1
Temperature of reheat steam/°C 569.0 557.1 559.4 553.1 555.6 560.3 545.1
Superheat degree/°C 21.8 23.5 23.9 22.3 24.9 21.0
Tab.1  Design and main operating parameters at different TDAs
Case Proximate analysis, wt.% (as received) Net heating value/(MJ·kg−1)
Volatile matter Ash Moisture Fixed carbon
Design coal 5.29 32.98 8.00 53.73 19.45
Actual coal (210 MW) 6.37 38.04 9.38 45.85 16.30
Actual coal (260 MW) 6.75 36.14 9.56 47.54 17.16
Tab.2  Characteristics of coal
Fig.1  Combustion system of the down-fired 350 MWe supercritical boiler with MIMSC technology/mm.
Fig.2  Locations of measuring points/mm.
Floor Front side Rear side Whole floor
0 ° 15 ° 25 ° 0 ° 15 ° 25 ° 0 ° 15 ° 25 °
1st 1075 1124 1014 957 1085 1005 1016 1104 1010
2nd 1126 1155 1104 1032 1115 1064 1079 1135 1084
3rd 1272 1239 1150 1160 1186 1168 1216 1213 1159
4th 1198 1154 1167 1119 1152 1155 1158 1153 1161
5th 1105 1135 1154 1053 1118 1165 1079 1127 1160
Tab.3  Mean temperature of each floor of measuring ports
Fig.3  Gas temperature distributions in lower furnace/°C.
Fig.4  Heating process of fuel-rich coal/air flow.
Fig.5  Characteristics of front/rear water wall temperature.
Fig.6  Concentrations of gas species in the region near the wing wall of the inspection.
Fig.7  Experimental results of the parameters at the furnace exit.
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