烟气脱硫
烟气
二氧化硫
臭氧
氨
燃烧
化学
废气
废物管理
氮氧化物
硫黄
选择性催化还原
化学工程
材料科学
催化作用
氮气
无机化学
导管(解剖学)
石膏
化石燃料燃烧烟气排放
氮氧化物
冷却塔
吸收(声学)
氮氧化物
环境科学
胺气处理
制浆造纸工业
二氧化氮
作者
Takeru Itagaki,Taiga Tanaka,Tomoyuki Kuroki,H. Yamasaki,Hashira Yamamoto,Masanori Hattori,Masaaki Okubo
标识
DOI:10.1016/j.rineng.2026.108965
摘要
Ammonia-coal co-firing for thermal power generation has recently attracted considerable attention as a game-changer for decarbonization. However, its combustion with a 20% or higher ammonia (NH 3 ) ratio emits higher amounts of nitrogen oxides (NO x ) than coal-fired combustion, surpassing the denitration capabilities of existing selective catalytic reduction (SCR) systems, resulting in excessing the regulation value determined by agreements on environmental conservation. To eliminate the NO x remaining after SCR, we propose a plasma-chemical hybrid process (PCHP) as a NO x treatment technology that can be easily retrofitted into existing exhaust gas treatment equipment. PCHP consists of NO oxidation using plasma ozonizers and NO 2 reduction by existing desulfurization equipment. Assuming the ozone injection in the flue gas duct between the SCR and desulfurization equipment, we conducted NO oxidation and the simultaneous removal of NO x and sulfur oxides (SO x ) for a simulated flue gas comprising low-concentration NO and high-concentration sulfur dioxide (SO 2 ). This was achieved using an ozone injection tower that simulated the flue gas duct and a calcium carbonate-slurry based SO 2 absorption tower that simulated the desulfurization equipment. The results show that even under conditions containing SO 2 at a concentration 46-fold higher than that of NO, the NO oxidation by O 3 was achieved without the effect of SO 2 . When the SO 2 removal efficiency reached 99%, which is equivalent to that of an actual facility, an NO x removal efficiency of 45% was attained. Therefore, an NO x removal efficiency of 45% can be also expected for an actual facility, contributing to further reductions in NO x .
科研通智能强力驱动
Strongly Powered by AbleSci AI