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    Control methodology for desulfurization process
    102.
    发明申请
    Control methodology for desulfurization process 有权
    脱硫工艺控制方法

    公开(公告)号：US20060151358A1

    公开(公告)日：2006-07-13

    申请号：US11034796

    申请日：2005-01-13

    申请人： Ronald Brown ,  Warren Ewert

    发明人： Ronald Brown ,  Warren Ewert

    IPC分类号： C10G45/00

    CPC分类号： C10G45/22 ,  C10G25/00

    摘要： A desulfurization system is operated in a manner which optimizes sulfur removal and octane retention. When the desulfurization reactor is operated at a specific ratio of total pressure to hydrogen partial pressure (PT/PH) and/or within a specific temperature range, optimum sulfur removal and octane retention are realized. The desulfurization reactor can be maintained at these optimized operating conditions by automatically adjusting one or more operating parameters of the desulfurization reactor in order to maintain a substantially constant hydrogen partial pressure (PH) in the reactor. Maintaining a relatively constant hydrogen partial pressure (PH) in the desulfurization reactor helps ensure a relatively consistent degree of desulfurization.

    摘要翻译： 脱硫系统以优化除硫和辛烷值保持的方式运行。 当脱硫反应器以总压力与氢气分压的特定比例和/或在特定温度范围内操作时，最佳除硫 并实现辛烷保留。 通过自动调节脱硫反应器的一个或多个操作参数以便在反应器中保持基本上恒定的氢分压（P H H H），可将脱硫反应器保持在这些优化的操作条件下。 在脱硫反应器中保持相对恒定的氢分压有助于确保相对一致的脱硫程度。

    Two phase hydroprocessing
    103.
    发明申请
    Two phase hydroprocessing 有权
    两相加氢处理

    公开(公告)号：US20050082202A1

    公开(公告)日：2005-04-21

    申请号：US11007846

    申请日：2004-12-09

    申请人： Michael Ackerson ,  Michael Byars

    发明人： Michael Ackerson ,  Michael Byars

    IPC分类号： C10G45/22 ,  C10G47/00 ,  C10G65/08 ,  C10G45/02 ,  C10G65/02

    CPC分类号： C10G45/22 ,  C10G47/00 ,  C10G65/08

    摘要： A process where the need to circulate hydrogen through the catalyst is eliminated is provided. This is accomplished by mixing and/or flashing the hydrogen and the oil to be treated in the presence of a solvent or diluent in which the hydrogen solubility is “high” relative to the feed. The type and amount of diluent added, as well as the reactor conditions, can be set so that all of the hydrogen required in the hydroprocessing reactions may be available in solution. The oil/diluent/hydrogen solution can then be fed to a plug flow reactor packed with catalyst where the oil and hydrogen react. No additional hydrogen is required, therefore, hydrogen recirculation is avoided and trickle bed operation of the reactors is avoided. Therefore, the large trickle bed reactors can be replaced by much smaller tubular reactor.

    摘要翻译： 提供了通过催化剂循环氢气的过程。 这是通过在相对于进料的氢溶解度“高”的溶剂或稀释剂的存在下混合和/或闪蒸待处理的氢气和油。 添加的稀释剂的类型和量以及反应器条件可以设定为使得加氢处理反应中所需要的氢都可以在溶液中得到。 然后将油/稀释剂/氢溶液进料到填充有油和氢反应的催化剂的活塞流反应器中。 不需要额外的氢气，因此避免了氢再循环，避免了反应器的滴流床操作。 因此，大型滴流床反应器可以被更小的管状反应器代替。