燃烧
氨
煤
氧气
化学
极限氧浓度
热力学
分析化学(期刊)
环境化学
材料科学
有机化学
物理
作者
Guanglei Wang,Chuanjin Zhao,Junxiang Xu,Bin Zhang,Hai Zhang,Kunmin Wu,Xiangxin Han,Weidong Fan
标识
DOI:10.1080/00102202.2025.2536216
摘要
Ammonia-coal co-combustion is a promising approach for coal decarbonization. However, the introduction of NH₃ tends to increase NO emissions. Therefore, understanding the formation characteristics and the associated reaction mechanisms of NO in ammonia-coal co-combustion mode is essential for its industrialized development. In this study, a high-temperature tubular furnace and CHEMKIN simulation are employed to investigate NO formation and its underlying mechanisms over a wide range of ammonia blending ratios, O₂ concentrations, and temperatures. Experimental results show that during the co-combustion of ammonia with either volatiles or char, NO peak values increase with rising O₂ concentration at low ammonia blending ratios (R = 10). However, at higher blending ratios (R ≥ 20), a reduction in NO peaks is observed in the high-temperature region. CHEMKIN simulations further reveal that at low temperature (1100°C), increasing O₂ concentration suppresses the reaction of NH2 with NO at a low blending ratio (R = 10). In contrast, at a high blending ratio (R = 40), the conversion of HNO to NO is enhanced, and the reduction of NO by HO₂ radicals is also promoted. At high temperature (1400°C), increasing O₂ concentration at R = 10 mainly intensifies the competition between NO₂ reduction to NO and NO oxidation to NO₂. Under high blending conditions (R = 40), the conversion of HNO to NO is weakened, while multiple competing pathways between NO and NO₂ emerge.
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