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公开(公告)号：US08816141B2
公开(公告)日：2014-08-26
申请号：US12861173
申请日：2010-08-23
IPC分类号： C07C1/00
CPC分类号： C10G3/45 , C10G3/44 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/52 , C10G3/60 , C10G45/02 , C10G45/58 , C10G2300/1011 , C10G2300/1014 , C10G2300/1055 , C10G2300/4018 , C10G2300/4081 , C10G2300/42 , C10G2400/04 , C10L1/08 , Y02P30/20
摘要： Processes are provided for deoxygenation of a biocomponent feedstock with reduced hydrogen consumption. The biocomponent feedstock can be processed under relatively low hydrogen partial pressures and at a relatively low treat gas ratio compared to the hydrogen need of the feedstock. The relatively low pressure, relatively low treat gas ratio hydroprocessing can result in reduced production of water and carbon monoxide and in increased production of carbon dioxide compared to relatively higher pressure process conditions.
摘要翻译： 为生物组分原料脱氧提供了减少氢消耗的方法。 生物组分原料可以在相对低的氢分压下以相对较低的处理气体比例与原料的氢气需求相比进行处理。 相对低压，相对较低的处理气体比例加氢处理可以导致水和一氧化碳的产生减少，并且与相对较高的压力过程条件相比，二氧化碳的产生增加。
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公开(公告)号：US20110054230A1
公开(公告)日：2011-03-03
申请号：US12861173
申请日：2010-08-23
IPC分类号： C07C1/207
CPC分类号： C10G3/45 , C10G3/44 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/52 , C10G3/60 , C10G45/02 , C10G45/58 , C10G2300/1011 , C10G2300/1014 , C10G2300/1055 , C10G2300/4018 , C10G2300/4081 , C10G2300/42 , C10G2400/04 , C10L1/08 , Y02P30/20
摘要： Processes are provided for deoxygenation of a biocomponent feedstock with reduced hydrogen consumption. The biocomponent feedstock can be processed under relatively low hydrogen partial pressures and at a relatively low treat gas ratio compared to the hydrogen need of the feedstock. The relatively low pressure, relatively low treat gas ratio hydroprocessing can result in reduced production of water and carbon monoxide and in increased production of carbon dioxide compared to relatively higher pressure process conditions.
摘要翻译： 为生物组分原料脱氧提供了减少氢消耗的方法。 生物组分原料可以在相对低的氢分压下以相对较低的处理气体比例与原料的氢气需求相比进行处理。 相对低压，相对较低的处理气体比例加氢处理可以导致水和一氧化碳的产生减少，并且与相对较高的压力过程条件相比，二氧化碳的产生增加。
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3.发明申请PROCESS FOR PREPARING DIESEL FUELS USING VEGETABLE OILS OR FATTY ACID DERIVATIVES 有权使用蔬菜油或脂肪酸衍生物制备柴油的方法公开(公告)号：US20100331586A1
公开(公告)日：2010-12-30
申请号：US12794253
申请日：2010-06-04
IPC分类号： C10G1/00
CPC分类号： C10G49/00 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/54 , C10G49/04 , C10G65/02 , C10G2300/1007 , C10G2300/1014 , C10G2300/1018 , C10G2300/1048 , C10G2300/1074 , C10G2300/304 , C10G2300/4018 , C10G2400/04 , C10L1/08 , C10L1/19 , Y02E50/13 , Y02P30/20 , Y02T50/678
摘要： A process for preparing fuels, such as diesel fuels or jet fuels, by hydrotreating vegetable oils or fatty acid derivatives that may be applied to existing equipment for treating fossil fuels. The process comprises feeding hydrotreating a combined oxygenate feed stream, such as FAME, and a hydrocarbon feed stream until not more than 86 wt % of the esters in the oxygenate feed stream are converted to hydrocarbons, and optionally further hydrotreating the product stream within at least a second hydrotreatment reaction zone until at least 90 wt % of the esters in the oxygenate feed stream are converted to hydrocarbons, before removing and separating a hydrocarbon stream suitable for use as fuel.
摘要翻译： 通过加氢处理可用于处理化石燃料的现有设备的植物油或脂肪酸衍生物来制备燃料例如柴油燃料或喷气燃料的方法。 该方法包括进料加氢处理组合的含氧化合物进料流（例如FAME）和烃进料流，直到含氧化合物进料流中的不超过86重量％的酯转化为烃，并且任选地进一步加氢处理产物流至少 第二加氢处理反应区，直到在除去和分离适合用作燃料的烃流之前，将含氧化合物进料流中的至少90重量％的酯转化为烃。
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4.发明授权Process for preparing diesel fuels using vegetable oils or fatty acid derivatives 有权使用植物油或脂肪酸衍生物制备柴油燃料的方法公开(公告)号：US08686203B2
公开(公告)日：2014-04-01
申请号：US12794253
申请日：2010-06-04
CPC分类号： C10G49/00 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/54 , C10G49/04 , C10G65/02 , C10G2300/1007 , C10G2300/1014 , C10G2300/1018 , C10G2300/1048 , C10G2300/1074 , C10G2300/304 , C10G2300/4018 , C10G2400/04 , C10L1/08 , C10L1/19 , Y02E50/13 , Y02P30/20 , Y02T50/678
摘要： A process for preparing fuels, such as diesel fuels or jet fuels, by hydrotreating vegetable oils or fatty acid derivatives that may be applied to existing equipment for treating fossil fuels. The process comprises feeding hydrotreating a combined oxygenate feed stream, such as FAME, and a hydrocarbon feed stream until not more than 86 wt % of the esters in the oxygenate feed stream are converted to hydrocarbons, and optionally further hydrotreating the product stream within at least a second hydrotreatment reaction zone until at least 90 wt % of the esters in the oxygenate feed stream are converted to hydrocarbons, before removing and separating a hydrocarbon stream suitable for use as fuel.
摘要翻译： 通过加氢处理可用于处理化石燃料的现有设备的植物油或脂肪酸衍生物来制备燃料例如柴油燃料或喷气燃料的方法。 该方法包括进料加氢处理组合的含氧化合物进料流（例如FAME）和烃进料流，直到含氧化合物进料流中的不超过86重量％的酯转化为烃，并且任选地进一步加氢处理产物流至少 第二加氢处理反应区，直到在除去和分离适合用作燃料的烃流之前，将含氧化合物进料流中的至少90重量％的酯转化为烃。
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公开(公告)号：US08580108B2
公开(公告)日：2013-11-12
申请号：US12960833
申请日：2010-12-06
IPC分类号： C10G21/16
CPC分类号： C10G65/16 , B01J23/002 , B01J23/8885 , B01J37/031 , C10G3/46 , C10G3/48 , C10G3/50 , C10G65/04 , C10G65/08 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2300/301 , C10G2300/308 , C10G2300/4018 , C10G2400/04 , Y02P30/20
摘要： Methods are provided for hydrotreating high nitrogen feeds with improved results for nitrogen removal, aromatic saturation, and/or sulfur removal. The method includes hydrotreating the feed with a supported hydrotreating catalyst followed by a bulk metal catalyst, the hydrotreated effluent of which can be suitable for use as a feed to an FCC reactor.
摘要翻译： 提供了用于加氢处理高氮进料的方法，其具有除氮，芳烃饱和和/或硫去除的改进结果。 该方法包括用负载的加氢处理催化剂和随后的本体金属催化剂加氢处理进料，其加氢处理流出物可适用于FCC反应器的进料。
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公开(公告)号：US09267084B2
公开(公告)日：2016-02-23
申请号：US14058803
申请日：2013-10-21
CPC分类号： C10G65/16 , B01J23/002 , B01J23/8885 , B01J37/031 , C10G3/46 , C10G3/48 , C10G3/50 , C10G65/04 , C10G65/08 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2300/301 , C10G2300/308 , C10G2300/4018 , C10G2400/04 , Y02P30/20
摘要： Methods are provided for hydrotreating high nitrogen feeds with improved results for nitrogen removal, aromatic saturation, and/or sulfur removal. The method includes hydrotreating the feed with a supported hydrotreating catalyst followed by a bulk metal catalyst, the hydrotreated effluent of which can be suitable for use as a feed to an FCC reactor.
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公开(公告)号：US20110163009A1
公开(公告)日：2011-07-07
申请号：US12960833
申请日：2010-12-06
CPC分类号： C10G65/16 , B01J23/002 , B01J23/8885 , B01J37/031 , C10G3/46 , C10G3/48 , C10G3/50 , C10G65/04 , C10G65/08 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2300/301 , C10G2300/308 , C10G2300/4018 , C10G2400/04 , Y02P30/20
摘要： Methods are provided for hydrotreating high nitrogen feeds with improved results for nitrogen removal, aromatic saturation, and/or sulfur removal. The method includes hydrotreating the feed with a supported hydrotreating catalyst followed by a bulk metal catalyst, the hydrotreated effluent of which can be suitable for use as a feed to an FCC reactor.
摘要翻译： 提供了用于加氢处理高氮进料的方法，其具有除氮，芳烃饱和和/或硫去除的改进结果。 该方法包括用负载的加氢处理催化剂和随后的本体金属催化剂加氢处理进料，其加氢处理流出物可适用于FCC反应器的进料。
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公开(公告)号：US20140179976A1
公开(公告)日：2014-06-26
申请号：US14097582
申请日：2013-12-05
IPC分类号： C10G45/08
摘要： Methods are provided herein for co-processing of biocomponent feeds as well processing of mineral feeds in a reaction system at hydrogen partial pressures of about 500 psig (3.4 MPag) or less. The methods include using stacked beds of both CoMo and NiMo catalysts. The stacked catalyst beds provided unexpectedly high catalyst activity as the input feed to a reaction system was switched between a mineral feed and a feed containing both mineral and biocomponent portions. Additionally, use of stacked catalyst beds can allow for maintenance of the activity for the catalyst system in a reaction system while still achieving a desired activity for both types of feeds.
摘要翻译： 本文提供了用于共生处理生物组分进料的方法以及在约500psig（3.4Mag）或更低的氢分压下在反应体系中处理矿物进料。 这些方法包括使用CoMo和NiMo催化剂的堆叠床。 堆叠的催化剂床提供意想不到的高催化剂活性，因为反应体系的输入进料在矿物进料和含有矿物和生物组分部分的进料之间切换。 此外，使用堆叠的催化剂床可以维持反应体系中的催化剂体系的活性，同时仍然实现两种类型的进料所需的活性。
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公开(公告)号：US20120004479A1
公开(公告)日：2012-01-05
申请号：US13168115
申请日：2011-06-24
申请人： Patrick L. Hanks , William E. Lewis
发明人： Patrick L. Hanks , William E. Lewis
CPC分类号： C10G65/04 , B01J23/882 , B01J29/7461 , C10G3/42 , C10G3/45 , C10G3/46 , C10G3/47 , C10G3/49 , C10G3/50 , C10G3/60 , C10G45/58 , C10G65/02 , C10G65/043 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , Y02E50/13 , Y02P30/20
摘要： Diesel fuel is produced from a feedstock that is at least partially biocomponent in origin. A feedstock is treated in a reactor including one or more hydrotreating zones having a continuous gas phase. The liquid effluent from the hydrotreating zones is then hydroprocessed in a hydroprocessing zone having a continuous liquid phase, such as a hydroprocessing zone in the same reactor. The hydroprocessing zone can be operated under effective catalytic dewaxing conditions.
摘要翻译： 柴油由原料至少部分生物成分生产。 原料在包括一个或多个具有连续气相的加氢处理区的反应器中处理。 然后将来自加氢处理区的液体流出物在具有连续液相的加氢处理区中加氢处理，例如在同一反应器中的加氢处理区。 加氢处理区可以在有效的催化脱蜡条件下运行。
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公开(公告)号：US09523046B2
公开(公告)日：2016-12-20
申请号：US14097582
申请日：2013-12-05
摘要： Methods are provided herein for co-processing of biocomponent feeds as well processing of mineral feeds in a reaction system at hydrogen partial pressures of about 500 psig (3.4 MPag) or less. The methods include using stacked beds of both CoMo and NiMo catalysts. The stacked catalyst beds provided unexpectedly high catalyst activity as the input feed to a reaction system was switched between a mineral feed and a feed containing both mineral and biocomponent portions. Additionally, use of stacked catalyst beds can allow for maintenance of the activity for the catalyst system in a reaction system while still achieving a desired activity for both types of feeds.
摘要翻译： 本文提供了用于共生处理生物组分进料的方法以及在约500psig（3.4Mag）或更低的氢分压下在反应体系中处理矿物进料。 这些方法包括使用CoMo和NiMo催化剂的堆叠床。 堆叠的催化剂床提供意想不到的高催化剂活性，因为反应体系的输入进料在矿物进料和含有矿物和生物组分部分的进料之间切换。 此外，使用堆叠的催化剂床可以维持反应体系中的催化剂体系的活性，同时仍然实现两种类型的进料所需的活性。
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