石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (3): 27-31.
• 催化剂 • 上一篇 下一篇
刘淼1,李勃呈1,何承臻1,郭靖2
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摘要: 某石化企业2.2 Mt/a催化裂化装置受上游常减压蒸馏装置回炼污油影响,原料油铁质量分数达8.2 μg/g;催化剂平衡剂铁质量分数超过0.6%,催化剂活性下降;表现出催化剂铁污染现象:如催化剂表面形成“铁瘤”,剂耗增加,催化剂比表面积降低至102 m2/g,平均粒径增大至78 μm,同时反应-再生系统流化效果变差,产品收率降低。为解决催化剂铁污染问题,选择使用抗铁助剂,加入抗铁助剂后,抗铁助剂凹槽处孔隙均被“铁瘤”覆盖,铁质量分数高达13.22%,有效缓解了催化剂铁污染情况。
关键词: MIP-CGP, 催化裂化, 铁污染, 抗铁助剂, 扫描电子显微镜
Abstract: The mass fraction of iron in the raw material in the 2.2Mt/a catalytic cracking unit using MIP-CGP process in a petrochemical company reached 8.2μg/g due to the influence of the upstream atmospheric and vacuum distillation unit. The activity of catalyst decrease and the iron mass fraction of equilibrium catalyst exceeded 0.6%. The catalyst system showed the phenomenon of iron contamination of the catalyst: such as the formation of "iron nodules" on the surface of the catalyst, the catalyst consumption increase, the specific surface area of the catalyst was reduced to 102 m2/g, the average particle size was increased to 78 μm, the fluidization effect of the reaction-regeneration system was worse, and the product yield was reduced. In order to solve the problem of iron contamination in the catalyst, anti-iron additives were used. After the addition of anti-iron additives, the pores at the grooves of the anti-iron additives were covered by "iron nodules", in which the iron mass fraction was as high as 13.22%, which could effectively alleviate the iron contamination of the catalyst.
Key words: MIP-CGP, fluid catalytic cracking, iron contamination, anti-iron additives, scanning electron microscope
刘淼 李勃呈 何承臻 郭靖. MIP-CGP装置催化剂铁污染及抗铁助剂使用情况分析[J]. 石油炼制与化工, 2025, 56(3): 27-31.
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