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During the operation of selective catalytic reduction (SCR) flue gas denitration system of coal-fired units, NH₃ and SO₃ in the flue gas generate liquid ammonium bisulfate (ABS) at a specific temperature, which is viscous and easy to cause catalyst deactivation at 0~40% low load due to micropore plugging and aggravate the fly ash blockage of heat exchange elements at the cold end of air preheater. Alkali powder injection to remove SO₃ from flue gas is an important method to control ABS. However, the existing grid type multi-nozzle device has problems of uneven injection and low SO₃ removal efficiency. A vertical gas-solid fluidization mixing and distribution injection device is developed to improve the uniformity of absorbent powder injection in the flue section. The pilot test results show that, the SO₃ removal efficiency at upstream of the SCR denitration system reaches 55.6%, the condensation temperature of the catalyst ABS decreases by 8.6 ℃, and the minimum operation temperature decreases by 11.9 ℃, which can expand the lower limit of the catalyst operation temperature and reduce the restriction on the lower limit of the peak load of the unit. The SO₃ removal efficiency at upstream of the air preheater reaches 84.3%, and the ABS deposition influence coefficient decreases by 86.9%, which can delay the ABS ash blockage at the cold end of the air preheater. The SO₃ emission mass concentration from the chimney is 2.5~3.4 mg/m³, which can eliminate blue smoke.

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燃煤机组选择性催化还原（SCR）烟气脱硝系统在运行过程中，烟气中的NH₃与SO₃在特定温度下生成液态硫酸氢铵（ABS），易在0~40%低负荷造成脱硝催化剂ABS失活和加剧空气预热器冷端换热元件ABS灰垢堵塞。碱粉喷射脱除SO₃是控制ABS的重要方法，但现有的格栅式多喷嘴装置存在喷射不均、SO₃脱除效率低等问题。研发了立式气固流态化混合分配装置，改善了烟道截面的粉体喷射均匀性。中试试验结果显示：SCR脱硝系统上游烟气中的SO₃脱除效率达到55.6%，催化剂ABS结露温度降低8.6 ℃，最低连续喷氨运行温度降低11.9 ℃，可拓展催化剂安全运行温度下限，并减轻对机组调峰负荷下限的制约；空气预热器上游SO₃脱除效率达到84.3%，ABS沉积影响系数降低86.9%，可延缓空气预热器冷端的ABS灰垢堵塞；烟囱SO₃排放浓度约为2.5~3.4 mg/m³，可消除蓝色烟羽。

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宋玉宝（1972），男，博士，研究员，主要研究方向为燃煤锅炉氮氧化物协同控制技术，sybyuyu@126.com。

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宋玉宝（1972），男，博士，研究员，主要研究方向为燃煤锅炉氮氧化物协同控制技术，sybyuyu@126.com。

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