RESIDUE CONVERSION PROCESS THAT INCLUDES A DEASPHALTING STAGE AND A HYDROCONVERSION STAGE
    3.
    发明申请
    RESIDUE CONVERSION PROCESS THAT INCLUDES A DEASPHALTING STAGE AND A HYDROCONVERSION STAGE 有权
    残留转换过程包括去除阶段和降解阶段

    公开(公告)号:US20120061293A1

    公开(公告)日:2012-03-15

    申请号:US13226626

    申请日:2011-09-07

    IPC分类号: C10G67/04

    摘要: Conversion of a heavy hydrocarbon fraction that is obtained either from a crude oil or from the distillation of a crude oil and that has an initial boiling point of at least 300° C. by hydroconversion of at least one portion of heavy hydrocarbon fraction in the presence of hydrogen in at least one three-phase reactor containing at least one hydroconversion catalyst, separation of the effluent to obtain a light liquid fraction that boils at a temperature that is less than 300° C. and a heavy liquid fraction that boils at a temperature that is greater than 300° C., and a deasphalting of at least one portion of the heavy liquid fraction that boils at a temperature that is greater than 300° C.

    摘要翻译: 在原油中或通过原油蒸馏得到的重质烃馏分的转化,其初始沸点为至少300℃,通过在存在下加氢转化至少一部分重质烃馏分 在含有至少一种加氢转化催化剂的至少一个三相反应器中的氢气分离出流出物以获得在低于300℃的温度下沸腾的轻质液体馏分和在温度下沸腾的重质液体馏分 大于300℃,并且至少一部分重质液体馏分在大于300℃的温度下沸腾的脱沥青。

    METHOD FOR THE VALORIZATION OF HEAVY CHARGES BY BUBBLING-BED DEASPHALTING AND HYDROCRACKING
    6.
    发明申请
    METHOD FOR THE VALORIZATION OF HEAVY CHARGES BY BUBBLING-BED DEASPHALTING AND HYDROCRACKING 有权
    通过泡沫床除磷和水解加工重金属的方法

    公开(公告)号:US20110062055A1

    公开(公告)日:2011-03-17

    申请号:US12900987

    申请日:2010-10-08

    IPC分类号: C10G69/04

    CPC分类号: C10G69/04 C10G2300/107

    摘要: The invention relates to a method for treating a hydrocarbons charge comprising the following stages, in which: a) the charge is brought into contact with a solvent in order to obtain a deasphalted effluent having a content of asphaltenes below 3000 ppm by weight, b) the deasphalted effluent is cracked in the presence of hydrogen and a hydrocracking catalyst, in a bubbling-bed reactor, so as to convert at least 50 wt. % of the fraction of the deasphalted effluent boiling above 500° C. to compounds having a boiling point below 500° C., c) the effluent from stage b) is fractionated to recover gasolines, kerosene, gas oils and a first residue, and d) at least a portion of this first residue is cracked so as to obtain an effluent comprising gasolines, kerosene, gas oils and a second residue.

    摘要翻译: 本发明涉及一种用于处理包括以下阶段的烃装料的方法,其中:a)使电荷与溶剂接触,以获得沥青质含量低于3000重量ppm的脱沥青流出物,b) 在氢气和加氢裂化催化剂的存在下,在鼓泡床反应器中将脱沥青的流出物裂化,以便将至少50wt。 沸点高于500℃的脱沥青流出物的百分比达到沸点低于500℃的化合物,c)将来自阶段b)的流出物分馏以回收汽油,煤油,瓦斯油和第一残渣,以及 d)该第一残留物的至少一部分被裂化,以获得包含汽油,煤油,瓦斯油和第二残余物的流出物。