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    Method for Upgrading Hydrocarbon Using C4, C5 and C6 Streams
    2.
    发明申请
    Method for Upgrading Hydrocarbon Using C4, C5 and C6 Streams 审中-公开
    使用C4，C5和C6流升级烃的方法

    公开(公告)号：US20160115093A1

    公开(公告)日：2016-04-28

    申请号：US14887929

    申请日：2015-10-20

    申请人： SK Innovation Co., Ltd. ,  SK Energy Co., Ltd.

    发明人： Hee-Jung Jeon ,  Yong-Woo Kim

    IPC分类号： C07C2/12 ,  C07C2/66

    CPC分类号： C07C2/12 ,  C07C2/66 ,  C07C2/72 ,  C07C2529/06 ,  C10G11/18 ,  C10G29/205 ,  C10G35/00 ,  C10G50/00 ,  C10G57/005 ,  C10G57/02 ,  C10G2300/1088 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/304

    摘要： The present disclosure relates to a method for upgrading hydrocarbon using C4, C5 and C6 streams, and more specifically, to a method for upgrading hydrocarbons using C4, C5 and C6 streams. The method includes the steps of: preparing C4, C5 and C6 streams, which are the products of naphtha catalytic cracking (NCC) process, heavy oil upgrading process, thermal cracking process, or fluidized catalytic cracking (FCC or RFCC) process; oligomerizing the C4, C5 and C6 streams with a catalyst to produce branched unsaturated hydrocarbons; and fractional distillating the branched unsaturated hydrocarbons to separate into C14-18 products or C32-40 products.

    摘要翻译： 本公开涉及使用C4，C5和C6流改质烃的方法，更具体地说，涉及一种使用C4，C5和C6流改质烃的方法。 该方法包括以下步骤：制备石脑油催化裂化（NCC）工艺，重油改质工艺，热裂解工艺或流化催化裂化（FCC或RFCC）工艺的C4，C5和C6流。 用催化剂使C4，C5和C6物流低聚以产生支链不饱和烃; 并分批蒸馏支链不饱和烃以分离成C14-18产物或C32-40产物。

    RFCC Process with Maximized Diesel Yields
    5.
    发明申请
    RFCC Process with Maximized Diesel Yields 审中-公开
    最大化柴油产量的RFCC过程

    公开(公告)号：US20150337219A1

    公开(公告)日：2015-11-26

    申请号：US14721212

    申请日：2015-05-26

    申请人： SK Innovation Co., Ltd.

    发明人： Hee-Jung Jeon ,  Yong-Woo Kim

    IPC分类号： C10G11/02

    CPC分类号： C10G11/02 ,  B01J23/75 ,  B01J23/755 ,  B01J23/8472 ,  B01J35/1061 ,  B01J35/108 ,  B01J37/0203 ,  C10G11/18 ,  C10G2300/701 ,  C10L1/08

    摘要： The present invention relates to a RFCC process. More specifically, the present invention relates to a RFCC process with maximized diesel yield which includes catalytically reacting a catalytic cracking catalyst in which zeolite has been selectively removed, with a petroleum feedstock in a reaction zone of a fluidized bed catalytic cracking unit to thereby obtain a product stream, an unreacted petroleum feedstock and a mixture of the used catalysts, and separating and collecting the product stream from the used catalyst and the unreacted petroleum feedstock.

    摘要翻译： 本发明涉及RFCC方法。 更具体地说，本发明涉及一种具有最大柴油产率的RFCC方法，其包括使已经选择性除去沸石的催化裂化催化剂与流化床催化裂化装置的反应区中的石油原料催化反应，由此获得 产物流，未反应的石油原料和所用催化剂的混合物，并从所用催化剂和未反应的石油原料中分离和收集产物流。