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    • 13. 发明申请
    • PROCESS FOR AROMATIC HYDROGENATION AND CETANE VALUE INCREASE OF MIDDLE-DISTILLATE FEEDSTOCKS
    • 芳烃加氢方法和中等离子交换剂的增值价格
    • US20110303585A1
    • 2011-12-15
    • US13139451
    • 2009-12-11
    • Jean-Pierre DathSander Van DonkGiacomo GrassoFrans PlantengaJan Nieman
    • Jean-Pierre DathSander Van DonkGiacomo GrassoFrans PlantengaJan Nieman
    • C10G45/50C10G45/52C10G45/46
    • C10G45/52B01J23/44B01J23/63B01J23/652B01J23/89B01J35/0066B01J35/1019B01J35/1042C10G45/04C10G45/08C10G65/08
    • The instant invention pertains to a process for treating a feed, for example a Light Cycle Oil (LCO), having a high content of S and/or N impurities and/or a high content of aromatics, comprising the following steps, in particular in such an order a step of desulphurisation (HDS) and denitrification (HDN) of a feed, in particular LCO, is passed in presence of hydrogen over a catalyst, containing metals of the group VI B and VIII, leading to an effluent, optionally a step of stripping of the effluent, at least a subsequent step for dearomatization (HDA) in which at least a portion of the effluent, optionally stripped, is passed in presence of hydrogen over a catalyst comprising a combination of platinum and palladium supported on a carrier comprising silica-alumina dispersed in an alumina binder wherein the amount of alumina binder is 5-50 wt. % based on the total weight of the silica-alumina and alumina binder present in the carrier and wherein the silica-alumina comprises 5-50 wt. % of alumina based on the weight of the silica-alumina, and recovering the final load obtained, the use of a specific catalyst and a process for preparing diesel comprising the step of mixing the final effluent obtained by a process of the invention.
    • 本发明涉及用于处理具有高含量的S和/或N杂质和/或高含量芳族化合物的进料例如轻循环油(LCO)的方法,其包括以下步骤,特别是在 进料的脱硫(HDS)和脱氮(HDN),特别是LCO的步骤在氢气存在下通过含有VIB和VIII族的金属的催化剂,导致流出物,任选地 至少后续的脱气步骤(HDA),其中至少一部分流出物(任选地被汽提)在氢气存在下通过催化剂,所述催化剂包含负载在载体上的铂和钯的组合 包括分散在氧化铝粘合剂中的二氧化硅 - 氧化铝,其中氧化铝粘合剂的量为5-50wt。 基于存在于载体中的二氧化硅 - 氧化铝和氧化铝粘合剂的总重量,其中二氧化硅 - 氧化铝包含5-50wt。 基于二氧化硅 - 氧化铝的重量的氧化铝的百分比,并且回收所获得的最终载荷,使用特定催化剂和制备柴油的方法,包括混合通过本发明的方法获得的最终流出物的步骤。