MILD-Oxy Combustion Characteristics of Pulverized Coal Affected by Oxidizer O2 Concentrations under Dry and Wet Recycle Modes

被引:5
|
作者
Zhao, Zhenghong [1 ]
Zhang, Zewu [1 ]
Zha, Xiaojian [1 ]
Gao, Ge [1 ]
Li, Xiaoshan [1 ]
Wu, Fan [1 ]
Luo, Cong [1 ]
Zhang, Liqi [1 ]
机构
[1] Huazhong Univ Sci & Technol, Sch Energy & Power Engn, State Key Lab Coal Combust, Wuhan 430074, Peoples R China
关键词
EDDY DISSIPATION CONCEPT; FLAMELESS COMBUSTION; DILUTION COMBUSTION; FUEL COMBUSTION; MODERATE; GASIFICATION; O-2/CO2; STEAM; H2O; CO2;
D O I
10.1021/acs.energyfuels.3c01658
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Moderate or intense low-oxy dilution oxy-fuel (MILD-oxy)combustioncan synergistically reduce the emissions of CO2 and NO x , and its industrial implementation is carriedout under dry and wet recycle modes. In this work, a series of numericalsimulations on pulverized coal MILD-oxy combustion under the typicaldry and wet recycle modes are performed, aiming at fully evaluatingthe combustion behaviors affected by the oxidizer O-2 concentration(21-30%) under different recycle modes. The results show thatincreasing O-2 concentration weakens the in-furnace fluegas recirculation and promotes the combustion intensity, while a moreuniform temperature distribution is obtained under dry recycle modethan under wet recycle mode. The diffusion/kinetics-controlled MILDregime is realized as the O-2 concentration increases. Nevertheless,the diffusion effect is enhanced due to the accelerated reaction rateunder a high O-2 level. The gasification reaction is strengthenedwith the increased O-2 concentration. Compared with wetrecycle mode, the burnout of coal char is slowed down under dry recyclemode because of the lower burnout rate. The fuel-NO conversion ratiois significantly reduced with the increased O-2 concentration,while wet recycle mode shows more potential in achieving low NO x emission than dry recycle mode. This workis expected to provide new insights into the comprehensive understandingof MILD-oxy combustion.
引用
收藏
页码:12259 / 12273
页数:15
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