公开(公告)号：US20150045597A1

公开(公告)日：2015-02-12

申请号：US14260784

申请日：2014-04-24

申请人： UOP LLC

发明人： Gregory A. Funk ,  Steven T. Arakawa

IPC分类号： C10G69/14 ,  C10G63/08 ,  C10G63/06 ,  C10G61/08

CPC分类号： C10G69/14 ,  C10G59/02 ,  C10G61/04 ,  C10G61/06 ,  C10G61/08 ,  C10G61/10 ,  C10G63/06 ,  C10G63/08 ,  C10G67/00 ,  C10G67/0409

摘要： A process for increasing the yields of hydrocarbon components to gasoline blending pools from a hydrocarbon feedstock is presented. The process includes separating a naphtha feedstock to components to a first stream that are more readily processed in a cracking unit and to components in a second stream that are more readily processed in a reforming unit.The process includes the ability to convert components from the cracking stream to the reforming stream.

摘要翻译： 提出了一种从烃原料提高烃组分对汽油混合池产率的方法。 该方法包括将石脑油原料与组分分离成在裂化装置中更容易加工的第一流和在重整单元中更容易加工的第二流中的组分。 该方法包括将组分从裂化流转化为重整流的能力。

公开(公告)号：US20150044107A1

公开(公告)日：2015-02-12

申请号：US14521171

申请日：2014-10-22

申请人： KiOR, Inc.

发明人： Maria Magdalena Ramirez Corredores ,  Vicente Sanchez Iglesias

IPC分类号： C10L1/00

CPC分类号： C10L1/00 ,  C10B49/22 ,  C10B53/02 ,  C10G3/42 ,  C10G3/50 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/302 ,  C10L1/02 ,  C10L1/04 ,  C10L1/1817 ,  C10L2200/0469 ,  C10L2290/543 ,  Y02E50/14 ,  Y02P30/20

摘要： Renewable fuels are produced in commercial quantities and with enhanced efficiency by integrating a bio-oil production system with a conventional petroleum refinery so that the bio-oil is co-processed with a petroleum-derived stream in the refinery. The techniques used to integrate the bio-oil production system and conventional petroleum refineries are selected based on the quality of the bio-oil and the desired product slate from the refinery.

摘要翻译： 通过将生物油生产系统与传统的炼油厂相结合，可再生燃料以商业数量生产并提高效率，使生物油与炼油厂的石油衍生物流共同加工。 用于整合生物油生产系统和传统炼油厂的技术是根据生物油的质量和来自炼油厂的期望产品板岩来选择的。

公开(公告)号：US20140374314A1

公开(公告)日：2014-12-25

申请号：US14308905

申请日：2014-06-19

申请人： Ramanathan SUNDARARAMAN ,  Thomas Francis DEGNAN, JR. ,  Rustom Merwan BILLIMORIA ,  Natalie Ann FASSBENDER ,  Manuel A. FRANCISCO ,  Anjaneya Sarma KOVVALI ,  Randolph J. SMILEY ,  John Peter GREELEY ,  William Ernest LEWIS ,  Roby BEARDEN, JR.

发明人： Ramanathan SUNDARARAMAN ,  Thomas Francis DEGNAN, JR. ,  Rustom Merwan BILLIMORIA ,  Natalie Ann FASSBENDER ,  Manuel A. FRANCISCO ,  Anjaneya Sarma KOVVALI ,  Randolph J. SMILEY ,  John Peter GREELEY ,  William Ernest LEWIS ,  Roby BEARDEN, JR.

IPC分类号： C10G49/12 ,  C10G49/06 ,  C10G69/14

CPC分类号： C10G49/12 ,  C10G9/005 ,  C10G49/04 ,  C10G49/06 ,  C10G69/06 ,  C10G69/14

摘要： Systems and methods are provided for slurry hydroconversion of a heavy oil feed, such as an atmospheric or vacuum resid. The systems and methods allow for slurry hydroconversion using catalysts with enhanced activity and/or catalysts that can be recycled as a side product from a complementary refinery process.

摘要翻译： 提供了用于重油进料（例如大气压或真空渣油）的浆料加氢转化的系统和方法。 这些系统和方法允许使用具有增强活性的催化剂和/或催化剂进行浆料加氢转化，所述催化剂可以作为辅助炼油方法的副产物回收。

公开(公告)号：US20140357914A1

公开(公告)日：2014-12-04

申请号：US14271399

申请日：2014-05-06

申请人： UOP LLC

发明人： Gregory A. Funk ,  Mary Jo Wier

IPC分类号： C10G69/10

CPC分类号： C10G69/10 ,  C10G51/023 ,  C10G61/06 ,  C10G61/08 ,  C10G61/10 ,  C10G67/00 ,  C10G67/06 ,  C10G67/16 ,  C10G69/00 ,  C10G69/06 ,  C10G69/14 ,  C10G2400/20

摘要： A process for increasing the yields of light olefins and the yields of aromatics from a hydrocarbon stream is presented. The process includes a first separation to direct the light components that are not reformable to a cracking unit, with the remainder passed to a second separation unit. The second separation unit extracts normal components from the hydrocarbon stream to pass to the cracking unit. The resulting hydrocarbon stream with reduced light ends and reduced normals is passed to a reforming unit.

摘要翻译： 提出了一种从碳氢化合物流中提高轻质烯烃产率和芳族化合物收率的方法。 该方法包括将不可重整的轻组分引导至裂化装置的第一分离，其余部分通入第二分离单元。 第二分离单元从烃流中提取正常组分以通过裂解装置。 所得到的具有减少的光端和减少的法线的烃流被传送到重整单元。

公开(公告)号：US20140275673A1

公开(公告)日：2014-09-18

申请号：US14292945

申请日：2014-06-02

申请人： CHINA PETROLEUM CHEMICAL CORPORATION ,  RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC

发明人： Jun LONG ,  Zhijian DA ,  Dadong LI ,  Xieqing WANG ,  Xingtian SHU ,  Jiushun ZHANG ,  Hong NIE ,  Chaogang XIE ,  Zhigang ZHANG ,  Wei WANG

IPC分类号： C07C5/11 ,  C07C5/05 ,  C07C4/06

CPC分类号： C10G69/04 ,  C07C4/06 ,  C07C5/05 ,  C07C5/11 ,  C10G11/18 ,  C10G69/02 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4018 ,  C10G2300/4093 ,  C10G2300/44 ,  C10G2300/807 ,  C10G2400/20 ,  C10G2400/30

摘要： A process for producing light olefins and aromatics, which comprises reacting a feedstock by contacting with a catalytic cracking catalyst in at least two reaction zones, wherein the reaction temperature of at least one reaction zone among the reaction zones downstream of the first reaction zone is higher than that of the first reaction zone and its weight hourly space velocity is lower than that of the first reaction zone, separating the spent catalyst from the reaction product vapor, regenerating the separated spent catalyst and returning the regenerated catalyst to the reactor, and separating the reaction product vapor to obtain the desired products, light olefins and aromatics. This process produces maximum light olefins such as propylene, ethylene, etc from heavy feedstocks, wherein the yield of propylene exceeds 20% by weight, and produces aromatics such as toluene, xylene, etc at the same time.

摘要翻译： 一种用于生产轻质烯烃和芳族化合物的方法，其包括使原料与至少两个反应区中的催化裂化催化剂接触反应，其中第一反应区下游的反应区中的至少一个反应区的反应温度较高 比第一反应区的重量小时空速低于第一反应区，将废催化剂与反应产物蒸气分离，再生分离的废催化剂并将再生催化剂返回反应器，并将 反应产物蒸气得到所需产物，轻质烯烃和芳族化合物。 该方法从重质原料中产生最大的轻质烯烃，例如丙烯，乙烯等，其中丙烯的产率超过20重量％，同时产生芳烃如甲苯，二甲苯等。

公开(公告)号：US08546629B2

公开(公告)日：2013-10-01

申请号：US13242833

申请日：2011-09-23

申请人： Andrea G. Bozzano ,  Matthew James Griffiths ,  Amarendra Anumakonda

发明人： Andrea G. Bozzano ,  Matthew James Griffiths ,  Amarendra Anumakonda

IPC分类号： C07C2/64 ,  C07C5/22

CPC分类号： C07C2/66 ,  C01B3/26 ,  C10G3/00 ,  C10G3/50 ,  C10G9/00 ,  C10G29/205 ,  C10G45/32 ,  C10G57/005 ,  C10G69/00 ,  C10G69/123 ,  C10G69/126 ,  C10G69/14 ,  C10G2300/1014 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20 ,  C07C15/107

摘要： Embodiments of methods for co-production of linear alkylbenzene and biofuel from a natural oil are provided. A method comprises the step of deoxygenating the natural oils to form a stream comprising paraffins. A first portion of the paraffins are dehydrogenated to provide mono-olefins. Then, benzene is alkylated with the mono-olefins under alkylation conditions to provide an alkylation effluent comprising alkylbenzenes and benzene. Thereafter, the alkylbenzenes are isolated to provide the alkylbenzene product. A second portion of the paraffins is processed to form biofuel.

摘要翻译： 提供了从天然油共生产直链烷基苯和生物燃料的方法的实施方案。 一种方法包括使天然油脱氧以形成包含石蜡的物流的步骤。 将第一部分链烷烃脱氢以提供单烯烃。 然后，在烷基化条件下用单烯烃烷基化苯以提供包含烷基苯和苯的烷基化流出物。 此后，分离烷基苯以提供烷基苯产物。 处理第二部分石蜡以形成生物燃料。

公开(公告)号：US20130079573A1

公开(公告)日：2013-03-28

申请号：US13242833

申请日：2011-09-23

申请人： Andrea G. Bozzano ,  Matthew James Griffiths ,  Amarendra Anumakonda

发明人： Andrea G. Bozzano ,  Matthew James Griffiths ,  Amarendra Anumakonda

IPC分类号： C07C1/207

CPC分类号： C07C2/66 ,  C01B3/26 ,  C10G3/00 ,  C10G3/50 ,  C10G9/00 ,  C10G29/205 ,  C10G45/32 ,  C10G57/005 ,  C10G69/00 ,  C10G69/123 ,  C10G69/126 ,  C10G69/14 ,  C10G2300/1014 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20 ,  C07C15/107

摘要： Embodiments of methods for co-production of linear alkylbenzene and biofuel from a natural oil are provided. A method comprises the step of deoxygenating the natural oils to form a stream comprising paraffins. A first portion of the paraffins are dehydrogenated to provide mono-olefins. Then, benzene is alkylated with the mono-olefins under alkylation conditions to provide an alkylation effluent comprising alkylbenzenes and benzene. Thereafter, the alkylbenzenes are isolated to provide the alkylbenzene product. A second portion of the paraffins is processed to form biofuel.

摘要翻译： 提供了从天然油共生产直链烷基苯和生物燃料的方法的实施方案。 一种方法包括使天然油脱氧以形成包含石蜡的流的步骤。 将第一部分链烷烃脱氢以提供单烯烃。 然后，在烷基化条件下用单烯烃烷基化苯以提供包含烷基苯和苯的烷基化流出物。 此后，分离烷基苯以提供烷基苯产物。 处理第二部分石蜡以形成生物燃料。

公开(公告)号：US07947166B2

公开(公告)日：2011-05-24

申请号：US12047631

申请日：2008-03-13

申请人： Florent Picard ,  Quentin Debuisschert ,  Annick Pucci

发明人： Florent Picard ,  Quentin Debuisschert ,  Annick Pucci

IPC分类号： C10G45/00

CPC分类号： C10G69/123 ,  C10G29/205 ,  C10G45/32 ,  C10G45/40 ,  C10G69/14 ,  C10G2400/02

摘要： The present invention relates to a method for treating a feed corresponding to a pyrolysis gasoline, comprising: a) at least one stage of selective hydrogenation of the feed, referred to as HD1, b) fractionating in one or more distillation columns the effluent from stage a) in order to produce at least one light C5 cut, an intermediate C6 or C6-C7 or C6-C8 cut intended for aromatics production, a heavy C7+ or C8+ or C9+ cut intended for gasoline production, c) at least one stage of hydrodesulfurization and deep hydrogenation of the intermediate cut, referred to as HD2, d) at least one stage of alkylation of the heavy C7+, C8+ or C9+ cut consisting of a treatment on an acid catalyst allowing weighting of the sulfur compounds, e) at least one stage of distillation of the effluent from stage d), intended to produce a light fraction that can be directly used as a low-sulfur gasoline base, and a heavy C11+ or C12+ fraction rich in sulfur compounds, used as middle distillate or fuel oil.

摘要翻译： 本发明涉及用于处理对应于热解汽油的进料的方法，其包括：a）进料的至少一个阶段选择性氢化，称为HD1，b）在一个或多个蒸馏塔中分馏出来自阶段 a）为了产生至少一个轻C5切割，用于芳烃生产的中间体C6或C6-C7或C6-C8切割，用于汽油生产的重C 7 +或C 8 +或C 9 +切割，c）至少一个阶段 中间切片的加氢脱硫和深氢化，称为HD2，d）重酸C7 +，C8 +或C9 +切割的至少一个阶段的烷基化，由在酸催化剂上进行处理，允许加权硫化合物，e）至少 用于产生可以直接用作低硫汽油基质的轻馏分的一级阶段d）中的流出物的蒸馏，以及用作中间馏分或燃料油的富含硫化合物的重C11 +或C12 +馏分 。

公开(公告)号：US20090253947A1

公开(公告)日：2009-10-08

申请号：US12418986

申请日：2009-04-06

申请人： Timothy A. Brandvold ,  Joseph A. Kocal ,  Michael J. McCall

发明人： Timothy A. Brandvold ,  Joseph A. Kocal ,  Michael J. McCall

IPC分类号： C07C2/04 ,  C10L1/16

CPC分类号： C10L1/04 ,  C10B53/02 ,  C10G3/46 ,  C10G3/47 ,  C10G3/49 ,  C10G3/50 ,  C10G50/00 ,  C10G65/00 ,  C10G65/02 ,  C10G65/14 ,  C10G69/00 ,  C10G69/02 ,  C10G69/08 ,  C10G69/126 ,  C10G69/14 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/1037 ,  C10G2300/80 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10J3/00 ,  C10J2300/0916 ,  C10J2300/1659 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/42 ,  Y02T50/678

摘要： A process for producing a blended fuel from a paraffin rich component and a cyclic rich component, where each of the components are generated from a renewable feedstock, is presented. The paraffin rich component is generated from a first renewable feedstock comprising at least one component selected from the group consisting of glycerides, free fatty acids, biomass, lignocellulose, free sugars, and combinations thereof. The cyclic rich component is generated from a second renewable feedstock comprising at least one component selected from the group consisting of glycerides, free fatty acids, free fatty alkyl esters, biomass, lignocellulose, free sugars, and combinations thereof. The blended fuel may a gasoline boiling point range blended fuel, a diesel boiling point range blended fuel, an aviation boiling point range blended fuel, any combination thereof, or any mixture thereof.

摘要翻译： 本发明提供了一种从富含链烷烃的组分和富含循环的组分制备混合燃料的方法，其中每种组分均由可再生原料生成。 富含链烷烃的组分由包含至少一种选自甘油酯，游离脂肪酸，生物质，木质纤维素，游离糖及其组合的组分的第一可再生原料产生。 循环富含组分由第二可再生原料生成，其包含至少一种选自甘油酯，游离脂肪酸，游离脂肪烷基酯，生物质，木质纤维素，游离糖及其组合的组分。 混合燃料可以是汽油沸点范围混合燃料，柴油沸点范围混合燃料，航空沸点范围混合燃料，其任何组合，或其任何混合物。

公开(公告)号：US20080223753A1

公开(公告)日：2008-09-18

申请号：US12047631

申请日：2008-03-13

申请人： Florent Picard ,  Quentin Debuisschert ,  Annick Pucci

发明人： Florent Picard ,  Quentin Debuisschert ,  Annick Pucci

IPC分类号： C10G45/32

CPC分类号： C10G69/123 ,  C10G29/205 ,  C10G45/32 ,  C10G45/40 ,  C10G69/14 ,  C10G2400/02

摘要： The present invention relates to a method for treating a feed corresponding to a pyrolysis gasoline, comprising: a) at least one stage of selective hydrogenation of the feed, referred to as HD1, b) fractionating in one or more distillation columns the effluent from stage a) in order to produce at least one light C5 cut, an intermediate C6 or C6-C7 or C6-C8 cut intended for aromatics production, a heavy C7+ or C8+ or C9+ cut intended for gasoline production, c) at least one stage of hydrodesulfurization and deep hydrogenation of the intermediate cut, referred to as HD2, d) at least one stage of alkylation of the heavy C7+, C8+ or C9+ cut consisting of a treatment on an acid catalyst allowing weighting of the sulfur compounds, e) at least one stage of distillation of the effluent from stage d), intended to produce a light fraction that can be directly used as a low-sulfur gasoline base, and a heavy C11+ or C12+ fraction rich in sulfur compounds, used as middle distillate or fuel oil.

摘要翻译： 本发明涉及用于处理对应于热解汽油的进料的方法，其包括：a）进料的至少一个阶段选择性氢化，称为HD1，b）在一个或多个蒸馏塔中分馏出来自阶段 a）为了产生至少一个轻C5切割，用于芳烃生产的中间体C6或C6-C7或C6-C8切割，用于汽油生产的重C 7 +或C 8 +或C 9 +切割，c）至少一个阶段 中间切片的加氢脱硫和深氢化，称为HD2，d）重酸C7 +，C8 +或C9 +切割的至少一个阶段的烷基化，由在酸催化剂上进行处理，允许加权硫化合物，e）至少 用于产生可以直接用作低硫汽油基质的轻馏分的一级阶段d）中的流出物的蒸馏，以及用作中间馏分或燃料油的富含硫化合物的重C11 +或C12 +馏分 。