首页|催化裂化装置余锅运行优化与调整

催化裂化装置余锅运行优化与调整

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清江石化催化装置余锅排烟温度逐步上升,检查时发现余锅后部蒸发段和省煤段压降也在上升,而且余锅出口烟气中氮氧化物含量上升明显。为保证烟气中氮氧化物达标排放,只有不断提高注氨量,而高的注氨量会造成氨逃逸,从而引起省煤段翅片管结晶,以上问题也更加严重。针对此问题,决定将再生器改加强化脱硝助剂,优化操作,降低床温,控制烟气低含氧量操作,同时优化余锅激波吹灰运行等措施后,余锅压降、排烟温度得到有效控制,注氨量大幅下降,保证装置长周期运行。
Operation Optimization and Adjustment of Residual Boiler in Catalytic Cracking Unit
The exhaust temperature of the residual boiler in the catalytic unit of Qingjiang Petrochemical is gradually increasing.During inspection,it is found that the pressure drop in the evaporation section and coal saving section at the rear of the residual boiler is also increasing,and the nitrogen oxide content in the exhaust gas at the outlet of the residual boiler is significantly increasing.To ensure the emission of nitrogen oxides in flue gas meet the standard,the only solution is to continuously increase the ammonia injection rate.However,high ammonia injection rates can cause ammonia escape,leading to crystallization of the finned tubes in the coal saving section,and the above problems are even more serious.In response to this issue,it was decided to add enhanced denitrification agents to the regenerator,optimize operation,reduce bed temperature,control low oxygen content in flue gas,and optimize shock wave soot blowing operation in the residual boiler.As a result,the pressure drop and exhaust temperature of the residual boiler were effectively controlled,and the ammonia injection rate was significantly reduced to ensure long-term operation of the device.

exhaust temperaturepressure dropammonia injection rateSCRenhanced denitrification agentlow bed temperature

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中国石化淮安清江石油化工有限责任公司,江苏 淮安 223002

排烟温度 压降 注氨量 SCR 强化脱硝剂 低床温

2025

广州化工
广州市化工行业协会 广州市化学化工学会 广州市化学工业研究所

广州化工

影响因子:0.358
ISSN:1001-9677
年,卷(期):2025.53(1)