石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (9): 130-135.
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黄波林,安士新,吕增
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摘要: 某石化企业3号催化裂化装置烟气脱硫塔出现烟气中颗粒物浓度升高的问题。经过多角度分析,发现烟气脱硫塔出口颗粒物浓度升高的主要原因是脱尘效率下降。通过减少反应-再生系统催化剂藏量、降低第一再生器料位、增加三级旋风分离器细粉储罐卸剂时长、提高烟气脱硫塔外排水流量等关键参数,烟气中颗粒物质量浓度稳定控制在20 mg/m3左右,满足相关指标要求。
关键词: 催化裂化, 烟气脱硫塔, 颗粒物浓度
Abstract: A petrochemical enterprise encountered an issue of elevated particulate matter concentration in the flue gas of desulfurization tower of No.3 catalytic cracking unit. Through multi-angle analysis, it was identified that the primary cause of the increased particulate matter concentration at the desulfurization tower outlet was a decline in dust removal efficiency. By adjusting key parameters such as reducing the catalyst inventory in the reaction-regeneration system,lowering the bed level of the first regenerator,increasing the discharge duration of the third-stage cyclone fine powder storage tank, and raising the external drainage flow rate of the desulfurization tower, the particulate matter concentration in the flue gas was stabilized at approximately 20 mg/m3, meeting the relevant regulatory requirements.
Key words: catalytic cracking, flue gas desulfurization, concentration of particulate matter
黄波林 安士新 吕增. 催化裂化装置烟气脱硫塔出口颗粒物浓度升高原因分析及应对措施[J]. 石油炼制与化工, 2026, 57(9): 130-135.
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