PROCESS FOR PRODUCING DISTILLATE FUELS AND ANODE GRADE COKE FROM VACUUM RESID
    21.
    发明申请
    PROCESS FOR PRODUCING DISTILLATE FUELS AND ANODE GRADE COKE FROM VACUUM RESID 有权
    生产蒸馏燃料和阳离子色料的方法

    公开(公告)号:US20140275676A1

    公开(公告)日:2014-09-18

    申请号:US14184099

    申请日:2014-02-19

    CPC classification number: C07C4/06 C10G9/005 C10G69/06 C10G2300/202

    Abstract: A process for upgrading residuum hydrocarbon feedstocks that may include: contacting a residuum hydrocarbon and hydrogen with a hydroconversion catalyst in a residuum hydroconversion reactor system; recovering an effluent from the residuum hydroconversion reactor system; separating the effluent to recover two or more hydrocarbon fractions including at least a vacuum residuum fraction and a heavy vacuum gas oil fraction; combining at least a portion of the heavy vacuum gas oil fraction and at least a portion of the vacuum residuum fraction to form a mixed heavy hydrocarbon fraction; feeding at least a portion of the mixed heavy hydrocarbon fraction to a coker; operating the coker at conditions to produce anode grade green coke and distillate hydrocarbons; recovering the distillate hydrocarbons from the coker; fractionating the distillate hydrocarbons to recover hydrocarbon fractions including a light distillates fraction, a heavy coker gas oil fraction, and a coker recycle fraction.

    Abstract translation: 一种用于升级残油烃原料的方法,其可以包括:在残渣加氢转化反应器系统中使残油烃和氢与加氢转化催化剂接触; 从渣油加氢转化反应器系统回收污水; 分离出流出物以回收两个或多个烃馏分,包括至少一个真空渣油馏分和一个重质真空瓦斯油馏分; 将至少一部分重质减压瓦斯油馏分和至少一部分真空残渣馏分组合以形成混合的重质烃馏分; 将至少一部分混合的重质烃部分进料至焦化器; 在生产阳极级绿色焦炭和馏出物烃的条件下操作焦化器; 从焦化器回收馏出物烃; 馏分馏分烃以回收烃馏分,包括轻馏分馏分,重焦油瓦斯油馏分和焦化循环馏分。

    INTEGRATION OF RESIDUE HYDROCRACKING AND SOLVENT DEASPHALTING
    22.
    发明申请
    INTEGRATION OF RESIDUE HYDROCRACKING AND SOLVENT DEASPHALTING 审中-公开
    残留水解和溶剂去除的综合

    公开(公告)号:US20140221709A1

    公开(公告)日:2014-08-07

    申请号:US13758554

    申请日:2013-02-04

    Abstract: A process for upgrading residuum hydrocarbons is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a first hydroconversion catalyst in a first ebullated bed hydroconversion reactor system; recovering a first effluent from the first ebullated bed hydroconversion reactor system; solvent deasphalting a vacuum residuum fraction to produce a deasphalted oil fraction and an asphalt fraction; contacting the deasphalted oil fraction and hydrogen with a second hydroconversion catalyst in a second hydroconversion reactor system; recovering a second effluent from the second hydroconversion reactor system; and fractionating the first effluent from the first ebullated bed hydroconversion reactor system and the second effluent from the second hydroconversion reactor system to recover one or more hydrocarbon fractions and the vacuum residuum fraction in a common fractionation system.

    Abstract translation: 公开了一种用于升级残油烃的方法。 该方法可以包括:在第一沸腾床加氢转化反应器系统中使残油烃馏分和氢与第一加氢转化催化剂接触; 从第一沸腾床加氢转化反应器系统回收第一流出物; 溶剂脱沥青真空残渣馏分以产生脱沥青油馏分和沥青馏分; 在第二加氢转化反应器系统中使脱沥青油馏分和氢气与第二加氢转化催化剂接触; 从第二加氢转化反应器系统回收第二流出物; 并将来自第一沸腾床加氢转化反应器系统的第一流出物和来自第二加氢转化反应器系统的第二流出物分馏,以在普通分馏系统中回收一种或多种烃馏分和真空残渣馏分。

    CONVERSION OF ALCOHOLS TO DISTILLATE FUELS
    23.
    发明申请
    CONVERSION OF ALCOHOLS TO DISTILLATE FUELS 有权
    酒精转化燃料

    公开(公告)号:US20140114101A1

    公开(公告)日:2014-04-24

    申请号:US14052972

    申请日:2013-10-14

    Abstract: A process for the production of jet and other heavy fuels from alcohols and mixture of alcohols is disclosed. The process may include contacting in a reaction zone at least one C2 to C11 alcohol with a solid catalyst having activity for the simultaneous dehydration of the alcohols to form olefins, isomerization of the olefins to form internal olefins, and oligomerization of the olefins produced in situ via the dehydration reaction to form an effluent comprising mono-olefinic hydrocarbons. Preferably, the alcohol feed is a mixture of alcohols, such as C2 to C7 alcohols or C4 and C6 alcohols, enabling the production of a mixture of branched hydrocarbons that may be used directly as a jet fuel without blending.

    Abstract translation: 公开了一种从醇和醇的混合物生产射流和其它重质燃料的方法。 该方法可以包括在反应区中使至少一种C 2至C 11醇与固体催化剂接触,所述固体催化剂具有用于同时脱水醇形成烯烃的活性,烯烃异构化以形成内烯烃,以及原位生产的烯烃的低聚 通过脱水反应形成包含单烯烃的流出物。 优选地,醇进料是醇,例如C 2至C 7醇或C 4和C 6醇的混合物,使得能够生产可直接用作喷气燃料而不混合的支链烃混合物。

    SYSTEM FOR UPGRADING RESIDUUM HYDROCARBONS
    26.
    发明申请

    公开(公告)号:US20180119027A1

    公开(公告)日:2018-05-03

    申请号:US15848666

    申请日:2017-12-20

    Abstract: A process for upgrading residuum hydrocarbons is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a first hydroconversion catalyst in a first ebullated bed hydroconversion reactor system; recovering a first effluent from the first ebullated bed hydroconversion reactor system; solvent deasphalting a vacuum residuum fraction to produce a deasphalted oil fraction and an asphalt fraction; contacting the deasphalted oil fraction and hydrogen with a second hydroconversion catalyst in a second hydroconversion reactor system; recovering a second effluent from the second hydroconversion reactor system; and fractionating the first effluent from the first ebullated bed hydroconversion reactor system and the second effluent from the second hydroconversion reactor system to recover one or more hydrocarbon fractions and the vacuum residuum fraction in a common fractionation system.

    Process for producing distillate fuels and anode grade coke from vacuum resid
    30.
    发明授权
    Process for producing distillate fuels and anode grade coke from vacuum resid 有权
    从真空渣油生产馏出燃料和阳极级焦炭的方法

    公开(公告)号:US09452955B2

    公开(公告)日:2016-09-27

    申请号:US14184099

    申请日:2014-02-19

    CPC classification number: C07C4/06 C10G9/005 C10G69/06 C10G2300/202

    Abstract: A process for upgrading residuum hydrocarbon feedstocks that may include: contacting a residuum hydrocarbon and hydrogen with a hydroconversion catalyst in a residuum hydroconversion reactor system; recovering an effluent from the residuum hydroconversion reactor system; separating the effluent to recover two or more hydrocarbon fractions including at least a vacuum residuum fraction and a heavy vacuum gas oil fraction; combining at least a portion of the heavy vacuum gas oil fraction and at least a portion of the vacuum residuum fraction to form a mixed heavy hydrocarbon fraction; feeding at least a portion of the mixed heavy hydrocarbon fraction to a coker; operating the coker at conditions to produce anode grade green coke and distillate hydrocarbons; recovering the distillate hydrocarbons from the coker; fractionating the distillate hydrocarbons to recover hydrocarbon fractions including a light distillates fraction, a heavy coker gas oil fraction, and a coker recycle fraction.

    Abstract translation: 一种用于升级残油烃原料的方法,其可以包括:在残渣加氢转化反应器系统中使残油烃和氢与加氢转化催化剂接触; 从渣油加氢转化反应器系统回收污水; 分离出流出物以回收两个或多个烃馏分,包括至少一个真空渣油馏分和一个重质真空瓦斯油馏分; 将至少一部分重质减压瓦斯油馏分和至少一部分真空残渣馏分组合以形成混合的重质烃馏分; 将至少一部分混合的重质烃部分进料至焦化器; 在生产阳极级绿色焦炭和馏出物烃的条件下操作焦化器; 从焦化器回收馏出物烃; 馏分馏分烃以回收烃馏分,包括轻馏分馏分,重焦油瓦斯油馏分和焦化循环馏分。

Patent Agency Ranking