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    • 8. 发明授权
    • Catalytic cracking processes
    • 催化裂化过程
    • US4663025A
    • 1987-05-05
    • US896490
    • 1986-08-14
    • Chia-Min Fu
    • Chia-Min Fu
    • C10G11/00B01J29/08B01J29/18C10G11/05
    • B01J29/08B01J29/18C10G11/05B01J2229/16
    • Hydrocarbon-containing feed streams (preferably heavy gas oils and hydrotreated residua) having an initial boiling point of at least 400.degree. F. are catalytically cracked in the presence of a cracking catalyst comprising a faujasite-type zeolite having a unit cell size of about 24.28-24.48 A and an an alkali metal content of less than about 0.5 weight percent and being substantially free of iron ions. Preferably, the faujasite-type zeolite has an atomic Si:Al ratio in the crystalline framework of about 8:1 to 21:1 and has been partially dealuminated by a process comprising steam treatment followed by acid leaching.
    • 初始沸点为至少400°F的含烃进料流(优选重瓦斯油和加氢处理的残渣)在含有单元电池尺寸约24.28的八面沸石型沸石的裂化催化剂存在下被催化裂化 -24.48A,碱金属含量小于约0.5重量%,基本上不含铁离子。 优选地,八面沸石型沸石在晶体框架中具有约8:1至21:1的原子Si:Al比,并且通过包括蒸汽处理随后酸浸的方法部分脱铝。