CATALYTIC SYSTEM AND ADDITIVE FOR MAXIMISATION OF LIGHT OLEFINS IN FLUID CATALYTIC CRACKING UNITS IN OPERATIONS OF LOW SEVERITY
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    发明申请
    CATALYTIC SYSTEM AND ADDITIVE FOR MAXIMISATION OF LIGHT OLEFINS IN FLUID CATALYTIC CRACKING UNITS IN OPERATIONS OF LOW SEVERITY 审中-公开
    催化体系和添加剂在液体催化裂化装置中在低严重运行中最大化烯烃

    公开(公告)号:US20090107885A1

    公开(公告)日:2009-04-30

    申请号:US12260181

    申请日:2008-10-29

    摘要: The present invention concerns the field of fluid catalytic cracking (FCC) processes. The invention provides a process increasing production of LPG and propene in FCC units operating under conditions of maximisation of middle distillates of low aromaticity, such that they may be incorporated into the diesel oil pool. The invention also relates to the preparation and employment of additives based on zeolites having small pores, such as ferrierite (FER), in catalytic systems for FCC units, wherein conditions of low severity are adopted with a view to increasing yields of LPG and light olefins whilst improving stability of petrol. The invention also provides an original catalytic system, being more efficient than catalytic systems known in the state of the art, to increase the yield of LPG and propene without prejudicing the yield and quality of LCO. Furthermore it provides a method of preparation of an additive for said process employing the zeolite ferrierite.

    摘要翻译: 本发明涉及流化催化裂化(FCC)方法领域。 本发明提供一种加工生产液化石油气和丙烯的方法,其中FCC装置在低芳烃中间馏分最大化的条件下运行,使得它们可以并入柴油池中。 本发明还涉及在FCC单元的催化体系中制备和使用基于具有小孔的沸石的添加剂,例如镁碱沸石(FER),其中采用低严重性的条件以提高LPG和轻质烯烃的产率 同时提高汽油的稳定性。 本发明还提供了比现有技术中已知的催化体系更有效的原始催化体系,以增加LPG和丙烯的产率而不损害LCO的产率和质量。 此外,它提供了使用沸石镁碱沸石的所述方法的添加剂的制备方法。