RESIDUE HYDROTREATMENT CATALYST COMPRISING VANADIUM, AND ITS USE IN A RESIDUE HYDROCONVERSION PROCESS
    1.
    发明申请
    RESIDUE HYDROTREATMENT CATALYST COMPRISING VANADIUM, AND ITS USE IN A RESIDUE HYDROCONVERSION PROCESS 审中-公开
    包含VANADIUM的残留加氢催化剂及其在残留加氢过程中的应用

    公开(公告)号:US20140166540A1

    公开(公告)日:2014-06-19

    申请号:US14105211

    申请日:2013-12-13

    Abstract: A catalyst containing a group VIB element; a group VIII element; phosphorus in a quantity of 0.1% to 9% by weight of phosphorus pentoxide with respect to the total catalyst mass; vanadium in a quantity of 0.25% to 7% by weight of vanadium pentoxide with respect to the total catalyst mass; a porous refractory oxide support;which catalyst has: a total pore volume of 0.3 mL/g or more; a macropore volume of 40% or less of the total pore volume; a median diameter of the mesopores in the range 5 nm to 36 nm; a BET surface area of at least 120 m2/g, and a process for the hydrotreatment of heavy residue type hydrocarbon feeds, in a fixed bed and/or ebullated bed, by said catalyst.

    Abstract translation: 含有VIB族元素的催化剂; 第八组元素; 相对于总催化剂质量为0.1〜9重量%的五氧化二磷的磷; 相对于总催化剂质量,钒的五氧化二钒的量为0.25重量%〜7重量%的钒; 多孔难熔氧化物载体; 该催化剂的总孔体积为0.3mL / g以上; 大孔体积为总孔体积的40%以下; 介孔的中值直径在5nm至36nm的范围内; 至少120m 2 / g的BET表面积,以及通过所述催化剂在固定床和/或沸腾床中加氢处理重残渣型烃进料的方法。

    PROCESS FOR REFINING A HEAVY HYDROCARBON FEED USING A SELECTIVE DEASPHALTING STEP
    2.
    发明申请
    PROCESS FOR REFINING A HEAVY HYDROCARBON FEED USING A SELECTIVE DEASPHALTING STEP 有权
    使用选择性去除步骤精炼重油加料的方法

    公开(公告)号:US20150337223A1

    公开(公告)日:2015-11-26

    申请号:US14652813

    申请日:2013-12-03

    Abstract: The invention concerns a process for refining a heavy hydrocarbon feed, comprising the following steps: a) a step for selective deasphalting of the heavy hydrocarbon feed by single-step liquid/liquid extraction in an extraction medium, said extraction being carried out using a mixture of at least one polar solvent and at least one apolar solvent, in order to obtain an asphalt phase and a deasphalted oil phase DAO, the proportions of said polar solvent and said apolar solvent in the solvent mixture being adjusted as a function of the properties of the feed and the desired asphalt yield, said deasphalting step being carried out under subcritical conditions for the solvent mixture; b) a step for hydrotreatment of at least a portion of the deasphalted oil phase DAO obtained from step a); c) optionally, a step for catalytic cracking of at least a portion of the effluent obtained from step b).

    Abstract translation: 本发明涉及一种用于精制重烃进料的方法,包括以下步骤:a)通过在萃取介质中单步液/液萃取来选择性脱沥青重质烃进料的步骤,所述萃取使用混合物 的至少一种极性溶剂和至少一种非极性溶剂,为了获得沥青相和脱沥青油相DAO,所述极性溶剂和所述非极性溶剂在溶剂混合物中的比例作为 所述进料和所需的沥青产量,所述脱沥青步骤在所述溶剂混合物的亚临界条件下进行; b)用于加氢处理从步骤a)得到的脱沥青油相DAO的至少一部分的步骤; c)任选地,用于对从步骤b)获得的至少一部分流出物进行催化裂化的步骤。

Patent Agency Ranking