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    Three stage cocurrent liquid and vapor hydroprocessing
    1.
    发明授权
    Three stage cocurrent liquid and vapor hydroprocessing 失效
    三级并流液相加氢处理

    公开(公告)号：US6054041A

    公开(公告)日：2000-04-25

    申请号：US73412

    申请日：1998-05-06

    申请人： Edward S. Ellis ,  William Ernest Lewis ,  David C. Dankworth ,  Ramesh Gupta

    发明人： Edward S. Ellis ,  William Ernest Lewis ,  David C. Dankworth ,  Ramesh Gupta

    IPC分类号： C10G65/04 ,  C10G45/02 ,  C10G65/00 ,  C10G65/02 ,  C10G45/00

    CPC分类号： C10G65/00

    摘要： A hydroprocessing process includes two cocurrent flow liquid reaction stages and one vapor stage, in which feed components are catalytically hydroprocessed by reacting with hydrogen. The liquid stages both produce a liquid and a hydrogen-rich vapor effluent, with most of the hydroprocessing accomplished in the first stage. The first stage vapor is also hydroprocessed. The hydroprocessed vapor and second stage vapor are cooled to condense and recover additional product liquid and produce an uncondensed hydrogen-rich vapor. After cleanup to remove contaminants, the hydrogen-rich vapor is recycled back into the first stage as treat gas. Fresh hydrogen is introduced into the second stage. This is useful for hydrotreating heteroatom-containing hydrocarbons.

    摘要翻译： 加氢处理方法包括两个并流流动液体反应阶段和一个蒸气阶段，其中进料组分通过与氢反应催化加氢处理。 液相都产生液体和富氢蒸汽流出物，大部分加氢处理在第一阶段完成。 第一级蒸气也被加氢处理。 将加氢蒸气和第二级蒸气冷却以冷凝并回收另外的产物液体并产生未冷凝的富氢蒸汽。 净化后清除污染物，富氢蒸汽再循环回第一阶段作为处理气体。 新鲜氢气被引入第二阶段。 这对于加氢处理含杂原子的烃是有用的。

    Hydroprocessing of petroleum fractions with a dual catalyst system
    2.
    发明授权
    Hydroprocessing of petroleum fractions with a dual catalyst system 失效
    用双重催化剂体系对石油馏分进行加氢处理

    公开(公告)号：US5871635A

    公开(公告)日：1999-02-16

    申请号：US753857

    申请日：1996-12-03

    申请人： Ramesh Gupta ,  Edward S. Ellis ,  William Ernest Lewis

    发明人： Ramesh Gupta ,  Edward S. Ellis ,  William Ernest Lewis

    IPC分类号： C10G45/00 ,  C10G45/04 ,  C10G45/12 ,  C10G47/00 ,  C10G47/16

    CPC分类号： C10G45/12 ,  C10G45/00 ,  C10G45/04 ,  C10G47/00 ,  C10G47/16

    摘要： Hydrocarbonaceous feedstocks admixed with a flow-through catalyst and hydrogen are hydroprocessed in a hydroprocessing reactor containing a captive hydroprocessing catalyst. The flow-through catalyst is continually withdrawn with the hydroprocessed feed from the hydroprocessing reactor. The flow-through catalyst may be an FCC, hydrocracking, isomerization or ring-opening catalyst. In a preferred embodiment, the captive hydroprocessing catalyst contains Co, Ni and/or Mo on an alumina base and the flow-through catalyst is an FCC zeolitic catalyst which is withdrawn with the hydroprocessed feed from the hydroprocessing reactor and then sent to an FCC unit.

    摘要翻译： 与流通催化剂和氢气混合的烃类原料在含有捕获加氢处理催化剂的加氢处理反应器中进行加氢处理。 使用加氢处理反应器的加氢进料连续抽出流通催化剂。 流通催化剂可以是FCC，加氢裂化，异构化或开环催化剂。 在优选的实施方案中，捕获加氢处理催化剂在氧化铝基底上含有Co，Ni和/或Mo，并且流通催化剂是FCC沸石催化剂，其由来自加氢处理反应器的加氢处理进料排出，然后送至FCC装置 。

    High pressure revamp of low pressure distillate hydrotreating process units
    10.
    发明申请
    High pressure revamp of low pressure distillate hydrotreating process units 有权
    低压馏分加氢处理装置的高压改造

    公开(公告)号：US20100263185A1

    公开(公告)日：2010-10-21

    申请号：US12798973

    申请日：2010-04-15

    申请人： William Ernest Lewis ,  William M. Gregory

    发明人： William Ernest Lewis ,  William M. Gregory

    IPC分类号： B23P17/00

    CPC分类号： C10G45/02 ,  C10G49/00 ,  C10G2300/4012 ,  C10G2300/4056 ,  Y10T29/49238 ,  Y10T29/49716

    摘要： A cost effective method for revamping a low pressure distillate hydrotreating process unit to a high pressure distillate hydrotreating process unit. A high pressure hot-feed pump is added, the furnace is retubed for higher pressures, the low pressure reactor is replaced with a high pressure reactor, a high pressure let-down valve is added at the reactor outlet, and the low pressure recycle compressor is replaced with a high pressure recycle compressor.

    摘要翻译： 将低压馏出物加氢处理装置改造成高压馏出物加氢处理装置的成本有效的方法。 加入高压热水泵，将炉子再压入高压，低压反应器用高压反应器代替，在反应器出口加入高压降压阀，低压循环压缩机 用高压循环压缩机代替。