FLUIDIZED CATALYTIC CRACKING PROCESS
    2.
    发明申请
    FLUIDIZED CATALYTIC CRACKING PROCESS 审中-公开
    流化催化裂化工艺

    公开(公告)号:US20120024748A1

    公开(公告)日:2012-02-02

    申请号:US13260919

    申请日:2010-03-29

    IPC分类号: C10G1/00 C10G11/02

    摘要: The present invention relates to a fluidized catalytic cracking process for cracking hydrocarbon feed having organo-sulfur compound as an impurity, said process comprising: adding a heavy metal poisoned spent catalyst to an equilibrium catalyst to obtain a composite circulating catalyst, wherein the heavy metal poisoned spent catalyst is added in an amount to maintain the activity of the circulating catalyst; and obtaining a fluidized catalytic cracked product.The present invention further relates to fluidized catalytic cracked product obtained by the process of the present invention. The sulfur content of the fluidized catalytic cracked product mainly gasoline which is boiling in the range of C5-250° C. reduced by more than 20% (wt/wt). And Research Octane number of the fluidized catalytic cracked product is increased by more than 1 unit.

    摘要翻译: 本发明涉及一种用于裂化具有有机硫化合物作为杂质的烃进料的流化催化裂化方法,所述方法包括:向沉淀催化剂中加入重金属中毒废催化剂以得到复合循环催化剂,其中重金属中毒 添加废催化剂以维持循环催化剂的活性; 得到流化催化裂化产物。 本发明还涉及通过本发明的方法获得的流化催化裂化产物。 主要是在C5-250℃范围内沸腾的汽油的流化催化裂化产物的硫含量降低了20%(wt / wt)。 研究表明,流化催化裂化产物的辛烷值增加了1个以上。