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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:US20110219671A1
公开(公告)日:2011-09-15
申请号:US13043804
申请日:2011-03-09
IPC分类号: C10L1/02
CPC分类号: C10G3/49 , C10G3/46 , C10G3/47 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , C10G2300/1055 , C10G2300/202 , C10G2300/207 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: Feeds containing a hydrotreated biocomponent portion, and optionally a mineral portion, can be processed under catalytic conditions for isomerization and/or dewaxing. The sulfur content of the feed for dewaxing can be selected based on the hydrogenation metal used for the catalyst. Diesel fuel products with improved cold flow properties can be produced.
摘要翻译: 含有加氢处理的生物组分部分和任选的矿物部分的进料可在用于异构化和/或脱蜡的催化条件下加工。 用于脱蜡的进料的硫含量可以基于用于催化剂的氢化金属来选择。 可以生产具有改善的冷流特性的柴油燃料产品。
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公开(公告)号:US20110219669A1
公开(公告)日:2011-09-15
申请号:US12932893
申请日:2011-03-09
IPC分类号: C10L1/02
CPC分类号: C10G3/49 , C10G3/46 , C10G3/47 , C10G3/50 , C10G45/64 , C10G65/04 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/304 , C10G2300/4018 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: Non-hydrotreated biocomponent feeds can be mixed with mineral feeds and processed under catalytic isomerization/dewaxing conditions. The catalytic isomerization/dewaxing conditions can be selected to advantageously also substantially deoxygenate the mixed feed. Diesel fuel products with improved cold flow properties can be produced.
摘要翻译: 非加氢处理的生物组分饲料可与矿物饲料混合并在催化异构化/脱蜡条件下加工。 可以选择催化异构化/脱蜡条件以有利地也基本上使混合进料脱氧。 可以生产具有改善的冷流特性的柴油燃料产品。
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公开(公告)号:US08729330B2
公开(公告)日:2014-05-20
申请号:US12932893
申请日:2011-03-09
IPC分类号: C10L1/02
CPC分类号: C10G3/49 , C10G3/46 , C10G3/47 , C10G3/50 , C10G45/64 , C10G65/04 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/304 , C10G2300/4018 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: Non-hydrotreated biocomponent feeds can be mixed with mineral feeds and processed under catalytic isomerization/dewaxing conditions. The catalytic isomerization/dewaxing conditions can be selected to advantageously also substantially deoxygenate the mixed feed. Diesel fuel products with improved cold flow properties can be produced.
摘要翻译: 非加氢处理的生物组分饲料可与矿物饲料混合并在催化异构化/脱蜡条件下加工。 可以选择催化异构化/脱蜡条件以有利地也基本上使混合进料脱氧。 可以生产具有改善的冷流特性的柴油燃料产品。
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公开(公告)号:US20110219672A1
公开(公告)日:2011-09-15
申请号:US13127875
申请日:2008-11-06
IPC分类号: C10L1/02
CPC分类号: C10L1/08 , C10G45/64 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/307 , C10G2300/4018 , C10G2400/04 , C10L1/026 , C10L2200/0469 , C10L2270/026 , C10L2290/06 , C10L2290/54 , Y02E50/13 , Y02P30/20
摘要: A method for producing diesel fuel from biocomponent feeds includes hydrotreating the feed followed by catalytic dewaxing with a ZSM-48 containing catalyst. The hydrotreated feed may be cascaded directly to the dewaxing step, or the hydrotreated feed can undergo intermediate separation. The diesel fuel resulting from processing of the biocomponent feed exhibits superior cetane values.
摘要翻译: 从生物组分进料生产柴油燃料的方法包括用含ZSM-48的催化剂加氢处理进料,然后进行催化脱蜡。 加氢处理的进料可以直接级联到脱蜡步骤,或加氢处理的进料可以进行中间分离。 由生物组分进料加工产生的柴油表现出优异的十六烷值。
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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:US08674160B2
公开(公告)日:2014-03-18
申请号:US13043804
申请日:2011-03-09
IPC分类号: C10L1/02
CPC分类号: C10G3/49 , C10G3/46 , C10G3/47 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , C10G2300/1055 , C10G2300/202 , C10G2300/207 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要: Feeds containing a hydrotreated biocomponent portion, and optionally a mineral portion, can be processed under catalytic conditions for isomerization and/or dewaxing. The sulfur content of the feed for dewaxing can be selected based on the hydrogenation metal used for the catalyst. Diesel fuel products with improved cold flow properties can be produced.
摘要翻译: 含有加氢处理的生物组分部分和任选的矿物部分的进料可在用于异构化和/或脱蜡的催化条件下加工。 用于脱蜡的进料的硫含量可以基于用于催化剂的氢化金属来选择。 可以生产具有改善的冷流特性的柴油燃料产品。
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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:US20110056869A1
公开(公告)日:2011-03-10
申请号:US12875165
申请日:2010-09-03
CPC分类号: C10L1/026 , C10G3/45 , C10G3/46 , C10G3/48 , C10G3/50 , C10G45/58 , C10G65/043 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/301 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要: This invention relates to the production of dewaxed and/or hydroisomerized fuel composition that includes a step of hydrotreating a feedstock containing the lipidic material. The fuel compositions are high quality fuel compositions in which the fuel can be ultimately tailored for a variety of end uses such as jet fuel or diesel fuel.
摘要翻译: 本发明涉及脱蜡和/或加氢异构化的燃料组合物的生产,其包括加氢处理含有脂质材料的原料的步骤。 燃料组合物是高质量的燃料组合物,其中燃料可以最终定制用于各种最终用途,例如喷气燃料或柴油燃料。
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公开(公告)号:US09719034B2
公开(公告)日:2017-08-01
申请号:US14546565
申请日:2014-11-18
申请人: Stuart S. Shih , Gary P. Schleicher , Michael B. Carroll , Timothy L. Hilbert , Stephen J. McCarthy , William J. Novak
发明人: Stuart S. Shih , Gary P. Schleicher , Michael B. Carroll , Timothy L. Hilbert , Stephen J. McCarthy , William J. Novak
IPC分类号: C10G45/64 , C10G69/02 , C10M103/06 , B01J35/10 , C10G65/04 , C10G65/12 , B01J23/883 , B01J23/888 , B01J29/78
CPC分类号: C10G69/02 , B01J23/883 , B01J23/888 , B01J29/78 , B01J29/7846 , B01J29/7861 , B01J29/7884 , B01J29/7892 , B01J35/1014 , B01J2229/186 , B01J2229/20 , B01J2229/42 , C10G65/043 , C10G65/12 , C10G2300/1048 , C10G2300/203 , C10G2300/301 , C10G2300/302 , C10G2300/307 , C10G2400/04 , C10G2400/10 , C10M103/06
摘要: Methods are provided for processing a gas oil boiling range feedstock, such as a vacuum gas oil, in a single reaction stage and/or without performing intermediate separations. The methods are suitable for forming lubricants and distillate fuels while reducing or minimizing the production of lower boiling products such as naphtha and light ends. The methods can provide desirable yields of distillate fuels and lubricant base oils without requiring separate catalyst beds or stages for dewaxing and hydrocracking. The methods are based in part on use of a dewaxing catalyst that is tolerant of sour processing environments while still providing desirable levels of activity for both feed conversion and feed isomerization.
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