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71. 发明申请

US20090321319A1 Multi-Staged Hydroprocessing Process And System 有权
标题翻译：多级加氢处理和系统
公开(公告)号：US20090321319A1
公开(公告)日：2009-12-31
申请号：US12165522
申请日：2008-06-30
申请人： Peter Kokayeff , Charles P. Luebke , John Anthony Petri
发明人： Peter Kokayeff , Charles P. Luebke , John Anthony Petri
IPC分类号： C10G45/00 , B01J19/00
CPC分类号： C10G65/00 , C10G65/12
摘要： Methods and systems of processing a hydrocarbonaceous feed stock flows are provided. In one aspect, the method includes providing two or more hydroprocessing stages disposed in sequence, each hydroprocessing stage having a hydroprocessing reaction zone with a hydrogen requirement and each stage in fluid communication with the preceding stage. A hydrogen source is provided substantially free of hydrogen from a hydrogen recycle compressor. The hydrocarbonaceous feed stock flow is separated into an portions of fresh feed for each hydroprocessing stage, and then supplying the first portion of fresh feed with hydrogen from the hydrogen source in an amount satisfying substantially all of the hydrogen requirements of the hydroprocessing stages to a first hydroprocessing zone.
摘要翻译：提供了处理含烃原料流的方法和系统。一方面，该方法包括提供依次设置的两个或多个加氢处理阶段，每个加氢处理阶段具有氢需求的加氢处理反应区，每个阶段与前一阶段流体连通。从氢循环压缩机中提供基本上不含氢气的氢源。将烃类原料流分离成每个加氢处理阶段的新鲜进料的一部分，然后将来自氢源的新鲜进料的第一部分以满足加氢处理阶段的基本上所有氢气需求的量供应到第一加氢处理区。

72. 发明申请

US20090095652A1 Hydrocarbon Conversion Process To Decrease Polyaromatics 有权
标题翻译：烃转化过程降低多元芳烃
公开(公告)号：US20090095652A1
公开(公告)日：2009-04-16
申请号：US11872140
申请日：2007-10-15
申请人： Peter Kokayeff , Laura Elise Leonard , Michael Roy Smith
发明人： Peter Kokayeff , Laura Elise Leonard , Michael Roy Smith
IPC分类号： C10G69/02
CPC分类号： C10G65/12 , C10G2400/04
摘要： A process is provided for producing low sulfur diesel having a reduced poly-aromatic level where at least a portion of the poly-aromatics are converted to mono-aromatics. In one aspect, the process separates the temperature and pressure requirements for obtaining low levels of sulfur from the temperature and pressure requirements to saturate poly-aromatics to mono-aromatics. By one approach, the process first converts a diesel boiling range hydrocarbon stream in a hydrotreating zone at conditions effective to produce a hydrotreating zone effluent having a reduced concentration of sulfur with minimal saturation of poly-aromatics. Hydrogen is then admixed in the hydrotreating zone effluent or at least a portion thereof, which is then reacted in a substantially liquid-phase continuous reaction zone to effect saturation of poly-aromatics to provide a liquid-phase continuous reaction zone effluent having a reduced level of poly-aromatics relative to the diesel feed.
摘要翻译：提供了一种制备具有降低的聚芳族水平的低硫柴油的方法，其中至少一部分多芳族化合物转化为单芳族化合物。在一个方面，该方法将温度和压力要求从温度和压力要求中分离出来以获得低水平的硫，从而将多芳族化合物饱和至单芳族化合物。通过一种方法，该方法首先将加氢处理区中的柴油沸程烃流转化成有效地产生具有降低的硫浓度并且具有最小的多芳族化合物饱和度的加氢处理区流出物的条件。然后将氢混合在加氢处理区流出物或其至少一部分中，然后将其在基本上液相的连续反应区中反应以实现多芳族化合物的饱和，以提供具有降低水平的液相连续反应区流出物的多芳烃相对于柴油进料。

73. 发明申请

US20080159928A1 Hydrocarbon Conversion Process 审中-公开
标题翻译：烃转化过程
公开(公告)号：US20080159928A1
公开(公告)日：2008-07-03
申请号：US11618623
申请日：2006-12-29
申请人： Peter Kokayeff , Laura E. Leonard , Michael R. Smith
发明人： Peter Kokayeff , Laura E. Leonard , Michael R. Smith
IPC分类号： C10G47/02
CPC分类号： C10G45/22 , C10G65/04 , C10G65/12 , C10G2300/1048 , C10G2300/202 , C10G2300/307 , C10G2300/42 , C10G2400/04
摘要： A process is provided to produce an ultra low sulfur diesel with less than about 10 ppm sulfur using a two-phase or liquid-phase continuous reaction zone to convert a diesel boiling range distillate preferably obtained from a mild hydrocracking unit. In one aspect, the diesel boiling range distillate is introduced to the liquid-phase continuous reaction zone over-saturated with hydrogen in an amount effective so that the liquid phase remains substantially saturated with hydrogen throughout the reaction zone as the reactions proceed.
摘要翻译：提供了一种使用两相或液相连续反应区产生具有小于约10ppm硫的超低硫柴油以转化优选从温和加氢裂化装置获得的柴油沸程馏出物的方法。在一个方面，柴油沸程馏出物被引入到氢过饱和的液相连续反应区中，其量是有效的，使得当反应进行时液相在整个反应区中基本上被氢饱和。

74. 发明申请

US20080023372A1 Hydrocracking Process 审中-公开
标题翻译：加氢裂化工艺
公开(公告)号：US20080023372A1
公开(公告)日：2008-01-31
申请号：US11460307
申请日：2006-07-27
申请人： Laura E. Leonard , Peter Kokayeff
发明人： Laura E. Leonard , Peter Kokayeff
IPC分类号： C10G11/00
CPC分类号： C10G65/12 , C10G2300/1011 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/207 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4081 , Y02P30/20
摘要： A catalytic hydrocracking process wherein a liquid phase stream comprising a hydrocarbonaceous feedstock, a liquid phase effluent from a hydrocracking zone, and a sufficiently low hydrogen concentration to maintain a liquid phase continuous system is fed into a hydrotreating zone to produce a first hydrocarbonaceous stream comprising hydrocarbons having a reduced level of sulfur and nitrogen. The resulting hydrocarbons having a reduced level of sulfur and nitrogen are introduced into a hydrocracking zone with a sufficiently low hydrogen concentration to maintain a liquid phase continuous system to produce a hydrocracking zone effluent which provides lower boiling range hydrocarbons.
摘要翻译：催化加氢裂化方法，其中将包含烃原料，来自加氢裂化区的液相流出物和足够低的氢气浓度以保持液相连续系统的液相料流进料到加氢处理区中，以产生包含烃的第一烃流具有降低的硫和氮水平。将具有降低的硫和氮水平的所得烃引入到具有足够低氢浓度的加氢裂化区中，以保持液相连续系统以产生提供较低沸点烃的加氢裂化区流出物。

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