石油炼制与化工 ›› 2026, Vol. 58 ›› Issue (7): 25-31.

• 加工工艺 • 上一篇    下一篇

催化裂化装置面对原料劣质化加剧和产品结构调整的应对策略及其应用效果

周桦,丁亮   

  1. 中国石化扬子石油化工有限公司
  • 收稿日期:2025-12-16 修回日期:2026-03-11 出版日期:2026-07-12 发布日期:2026-06-29
  • 通讯作者: 周桦 E-mail:zhouhua.yzsh@sinopec.com

MEASURES AND APPLICATION EFFECTS CATALYTIC CRACKING UNITS IN RESPONSE TO INCREASING FEEDSTOCK DEGRADATION AND PRODUCT STRUCTURE ADJUSTMENT

  • Received:2025-12-16 Revised:2026-03-11 Online:2026-07-12 Published:2026-06-29

摘要: 作为炼油结构调整的主要生产装置,某公司2.80 Mt/a MIP-CGP工艺催化裂化装置面临原料劣质化程度加剧、原料性质多变的情况,以及根据需求减产柴油、增产汽油或液化气,确保汽油烯烃和苯含量合格等难题。通过采用提高第一反应区出口温度、进料预热温度、汽提蒸汽量,调整平衡剂活性和催化剂配方,LTAG喷嘴加工来自渣油加氢装置柴油及轻循环油,使用催化裂解助剂等优化措施,保证了(汽油+液化气)收率稳定在64%左右,显著高于设计值;同时,柴油产量大幅降低,汽油研究法辛烷值大于92.5;优化后装置效益增加约10538万元/a。

关键词: 催化裂化, SYC催化裂解助剂, MIP-CGP工艺, 柴油, 汽油

Abstract: A company's 2.80 Mt/a MIP-CGP catalytic cracking unit serves as the primary production unit for refining structure adjustment. Since its startup, the unit has faced challenges such as intensified feedstock deterioration and frequent variations in feedstock properties. Meanwhile, it is required to reduce diesel production based on operational demands while increasing gasoline or liquefied gas (LPG) output, ensuring that gasoline olefin and benzene content meet quality standards. By implementing measures such as increasing the outlet temperature of the first reaction zone, raising the feed preheating temperature, optimizing the stripping steam flow rate, adjusting balancing agent activity and catalyst formulation, processing diesel and light cycle oil from the residue hydrotreating unit using the LTAG nozzle, and employing deep catalytic cracking additives, the combined yield of gasoline and LPG was stabilized at around 64%, significantly exceeding the design value. Diesel production was substantially reduced, and the research octane number of gasoline remained consistently above 92.5. Following optimization, the unit's annual economic benefit increased by about 105.38 million yuan.

Key words: catalytic cracking, SYC deep catalytic cracking additive, MIP-CGP process, diesel, gasoline