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公开(公告)号：US20160145509A1
公开(公告)日：2016-05-26
申请号：US14550384
申请日：2014-11-21
Applicant: Lummus Technology Inc.
Inventor： Ujjal K. Mukherjee , Mario C. Baldassari , Marvin I. Greene
CPC classification number: C10G67/049 , C10G7/06 , C10G21/003 , C10G47/00 , C10G65/14 , C10G67/00 , C10G67/0454 , C10G2300/1077 , C10G2300/206 , C10J3/00 , C10J2200/00
Abstract: Processes for upgrading partially converted vacuum residua hydrocarbon feeds are disclosed. The upgrading processes may include: steam stripping the partially converted vacuum residua to generate a first distillate and a first residuum; solvent deasphalting the first residuum stream to generate a deasphalted oil and an asphaltenes fraction; vacuum fractionating the deasphalted oil to recover a deasphalted gas oil distillate and a heavy deasphalted residuum; contacting the first distillate and the deasphalted gas oil distillate and hydrogen in the presence of a first hydroconversion catalyst to produce a product; contacting the heavy deasphalted residuum stream and hydrogen in the presence of a second hydroconversion catalyst to produce an effluent; and fractionating the effluent to recover a hydrocracked atmospheric residua and a hydrocracked atmospheric distillate
Abstract translation: 公开了用于升级部分转化的真空残余烃进料的方法。 升级过程可以包括：蒸汽汽提部分转化的真空残渣以产生第一馏出物和第一残渣; 溶剂脱沥青第一残渣流以产生脱沥青油和沥青质馏分; 真空分馏脱沥青油，以回收脱沥青瓦斯油馏出物和重质脱沥青渣; 在第一加氢转化催化剂的存在下使第一馏出物和脱沥青瓦斯油馏出物和氢接触以产生产物; 在第二加氢转化催化剂的存在下使沉重的脱沥青残渣物流和氢气接触以产生流出物; 并将流出物分馏以回收加氢裂化的大气残留物和加氢裂化的大气馏出物
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32.发明申请CONVERSION OF ASPHALTENIC PITCH WITHIN AN EBULLATED BED RESIDUUM HYDROCRACKING PROCESS 审中-公开浸渍床残留水解过程中的ASPHALTENIC PITCH的转化公开(公告)号：US20150217251A1
公开(公告)日：2015-08-06
申请号：US14685798
申请日：2015-04-14
Applicant: Lummus Technology Inc.
Inventor： Ujjal K. Mukherjee , Mario C. Baldassari , Marvin I. Greene
CPC classification number: B01J8/18 , B01J19/245 , B01J2208/00796 , B01J2219/24 , C10G1/08 , C10G1/086 , C10G47/26 , C10G65/10 , C10G65/12 , C10G67/02 , C10G67/049 , C10G2300/701
Abstract: A process for upgrading residuum hydrocarbons including: feeding pitch, hydrogen, and a partially spent catalyst recovered from a hydrocracking reactor to an ebullated bed pitch hydrocracking reactor; contacting the pitch, hydrogen, and the catalyst in the ebullated bed pitch hydrocracking reactor at reaction conditions of temperature and pressure sufficient to convert at least a portion of the pitch to distillate hydrocarbons; and separating the distillate hydrocarbons from the catalyst. In some embodiments, the process may include selecting the ebullated bed pitch hydrocracking reactor reaction conditions to be at or below the level where sediment formation would otherwise become excessive and prevent continuity of operations.
Abstract translation: 一种用于升级残油烃的方法，包括：将沥青，氢气和从加氢裂化反应器回收的部分废催化剂进料到沸腾床沥青加氢裂化反应器; 在沸腾床沥青加氢裂化反应器中的沥青，氢气和催化剂在足以将至少一部分沥青转化成馏出物烃的温度和压力的反应条件下接触; 并将馏出物烃与催化剂分离。 在一些实施方案中，该方法可以包括选择沸腾床沥青加氢裂化反应器反应条件处于或低于沉淀物形成否则将变得过大并防止操作连续性的水平。
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公开(公告)号：US09080113B2
公开(公告)日：2015-07-14
申请号：US13757203
申请日：2013-02-01
Applicant: Lummus Technology Inc.
Inventor： Marvin I. Greene , Ujjal K. Mukherjee , Arun Arora
IPC: C10G51/06 , C10G65/12 , C10G45/00 , C10G45/02 , C10G45/32 , C10G45/38 , C10G45/44 , C10G45/50 , C10G45/54 , C10G65/00 , C10G65/08 , C10G1/00
CPC classification number: C10G63/02 , B01J19/245 , B01J2219/24 , C10G1/002 , C10G45/00 , C10G45/02 , C10G45/32 , C10G45/38 , C10G45/44 , C10G45/50 , C10G45/54 , C10G65/00 , C10G65/08 , C10G65/12 , C10G2400/02 , C10G2400/04 , C10G2400/08
Abstract: Integrated processes for upgrading crude shale-derived oils, such as those produced by oil shale retorting or by in situ extraction or combinations thereof. Processes disclosed provide for a split-flow processing scheme to upgrade whole shale oil. The split flow concepts described herein, i.e., naphtha and kerosene hydrotreating in one or more stages and gas oil hydrotreating in one or more stages, requires additional equipment as compared to the alternative approach of whole oil hydrotreating. While contrary to conventional wisdom as requiring more capital equipment to achieve the same final product specifications, the operating efficiency vis a vis on-stream time efficiency and product quality resulting from the split flow concept far exceed in value the somewhat incrementally higher capital expenditure costs.
Abstract translation: 用于改进粗页岩衍生油的综合方法，例如通过油页岩蒸煮或原位萃取或其组合生产的那些。 所公开的方法提供了用于升级整个页岩油的分流处理方案。 本文所述的分流流动概念，即在一个或多个阶段中加氢处理的石脑油和煤油，以及一个或多个阶段加氢处理的瓦斯油，与全油加氢处理的替代方法相比，需要额外的设备。 虽然与传统智慧相反，要求更多的资本设备实现相同的最终产品规格，但是由分拆流程概念导致的运行效率和产品质量的运营效率远远超过了价值上的一些逐渐增加的资本支出成本。
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公开(公告)号：US09024096B2
公开(公告)日：2015-05-05
申请号：US13711140
申请日：2012-12-11
Applicant: Lummus Technology Inc.
Inventor： Marvin I. Greene
IPC: C10G3/00
CPC classification number: B01J19/24 , B01J8/02 , B01J2208/027 , B01J2219/00103 , B01J2219/24 , C10G3/40 , C10G3/50 , C10G45/00 , C10G45/06 , C10G45/08 , C10G45/10 , C10G65/12 , C10G69/06 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , Y02P30/20
Abstract: A process for converting triacylglycerides-containing oils into crude oil precursors and/or distillate hydrocarbon fuels is disclosed. The process may include reacting a triacylglycerides-containing oil-carbon dioxide mixture at a temperature in the range from about 250° C. to about 525° C. and a pressure greater than about 75 bar to convert at least a portion of the triacylglycerides to a hydrocarbon or mixture of hydrocarbons comprising one or more of isoolefins, isoparaffins, cycloolefins, cycloparaffins, and aromatics.
Abstract translation: 公开了一种将含三酰基甘油酯的油转化为原油前体和/或馏出烃燃料的方法。 该方法可以包括在约250℃至约525℃的温度和大于约75巴的压力下使含三酰基甘油酯的油 - 二氧化碳混合物反应，以将至少一部分三酰基甘油酯转化为 包含一种或多种异烯烃，异链烷烃，环烯烃，环烷烃和芳烃的烃或烃混合物。
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公开(公告)号：US10208261B2
公开(公告)日：2019-02-19
申请号：US14179083
申请日：2014-02-12
Applicant: Lummus Technology Inc.
Inventor： Arun Arora , Marvin I. Greene
Abstract: A process for upgrading vacuum residuum and vacuum gas oil hydrocarbons is disclosed. The process may include: contacting a heavy distillate hydrocarbon fraction and hydrogen with a zeolite selective hydrocracking catalyst in a first ebullated bed hydrocracking reaction zone to convert at least a portion of the vacuum gas oil to lighter hydrocarbons. Contacting a residuum hydrocarbon fraction and hydrogen with a non-zeolite base metal hydroconversion catalyst in a second ebullated bed hydroconversion reaction zone may produce a vapor stream containing unconverted hydrogen, acid gases and volatilized hydrocarbons which may be fed along with the vacuum gas oil in the first ebullated bed hydrocracking zone.
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Patent Agency Ranking
公开(公告)号：US09650312B2
公开(公告)日：2017-05-16
申请号：US14185237
申请日：2014-02-20
Applicant: Lummus Technology Inc.
Inventor： Mario C. Baldassari , Ujjal K. Mukherjee , Ann-Marie Olsen , Marvin I. Greene
CPC classification number: C07C4/06 , C10G65/12 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/4081
Abstract: A process for upgrading residuum hydrocarbons is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a first hydroconversion catalyst in a first ebullated bed hydroconversion reactor system; recovering a first effluent from the first ebullated bed hydroconversion reactor system; solvent deasphalting a vacuum residuum fraction to produce a deasphalted oil fraction and an asphalt fraction; contacting the deasphalted oil fraction and hydrogen with a second hydroconversion catalyst in a second hydroconversion reactor system; recovering a second effluent from the second hydroconversion reactor system; and fractionating the first effluent from the first ebullated bed hydroconversion reactor system and the second effluent from the second hydroconversion reactor system to recover one or more hydrocarbon fractions and the vacuum residuum fraction in a common fractionation system.
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公开(公告)号：US09440894B2
公开(公告)日：2016-09-13
申请号：US14197969
申请日：2014-03-05
Applicant: Lummus Technology Inc.
Inventor： Mario C. Baldassari , Ujjal K. Mukherjee , Ann-Marie Olsen , Marvin I. Greene
CPC classification number: C07C4/06 , C10G65/12 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/4081
Abstract: A process for upgrading residuum hydrocarbons is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a first hydroconversion catalyst in a first ebullated bed hydroconversion reactor system; recovering a first effluent from the first ebullated bed hydroconversion reactor system; solvent deasphalting a vacuum residuum fraction to produce a deasphalted oil fraction and an asphalt fraction; contacting the deasphalted oil fraction and hydrogen with a second hydroconversion catalyst in a second hydroconversion reactor system; recovering a second effluent from the second hydroconversion reactor system; and fractionating the first effluent from the first ebullated bed hydroconversion reactor system and the second effluent from the second hydroconversion reactor system to recover one or more hydrocarbon fractions and the vacuum residuum fraction in a common fractionation system.
Abstract translation: 公开了一种用于升级残油烃的方法。 该方法可以包括：在第一沸腾床加氢转化反应器系统中使残油烃馏分和氢与第一加氢转化催化剂接触; 从第一沸腾床加氢转化反应器系统回收第一流出物; 溶剂脱沥青真空残渣馏分以产生脱沥青油馏分和沥青馏分; 在第二加氢转化反应器系统中使脱沥青油馏分和氢气与第二加氢转化催化剂接触; 从第二加氢转化反应器系统回收第二流出物; 并将来自第一沸腾床加氢转化反应器系统的第一流出物和来自第二加氢转化反应器系统的第二流出物分馏，以在普通分馏系统中回收一种或多种烃馏分和真空残渣馏分。
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38.发明申请PROCESSING VACUUM RESIDUUM AND VACUUM GAS OIL IN EBULLATED BED REACTOR SYSTEMS 审中-公开在EBULLED BED反应器系统中处理真空残留物和真空油公开(公告)号：US20150225657A1
公开(公告)日：2015-08-13
申请号：US14179083
申请日：2014-02-12
Applicant: Lummus Technology Inc.
Inventor： Arun Arora , Marvin I. Greene
CPC classification number: C10G65/12 , C10G1/002 , C10G3/49 , C10G47/14 , C10G47/20 , C10G65/10 , C10G2300/1003 , C10G2300/1011 , C10G2300/1074 , C10G2300/1077 , C10G2300/205 , C10G2300/301 , Y02P30/20
Abstract: A process for upgrading vacuum residuum and vacuum gas oil hydrocarbons is disclosed. The process may include: contacting a heavy distillate hydrocarbon fraction and hydrogen with a zeolite selective hydrocracking catalyst in a first ebullated bed hydrocracking reaction zone to convert at least a portion of the vacuum gas oil to lighter hydrocarbons. Contacting a residuum hydrocarbon fraction and hydrogen with a non-zeolite base metal hydroconversion catalyst in a second ebullated bed hydroconversion reaction zone may produce a vapor stream containing unconverted hydrogen, acid gases and volatilized hydrocarbons which may be fed along with the vacuum gas oil in the first ebullated bed hydrocracking zone.
Abstract translation: 公开了一种用于提升真空渣油和减压瓦斯油烃的方法。 该方法可以包括：在第一沸腾床加氢裂化反应区中使重质馏分烃馏分和氢与沸石选择性加氢裂化催化剂接触，以将至少一部分真空瓦斯油转化为轻质烃。 在第二沸腾床加氢转化反应区中将残渣烃馏分和氢与非沸石母金属加氢转化催化剂接触可产生含有未转化的氢气，酸性气体和挥发的烃的蒸气流，其可以与真空瓦斯油一起进料 第一沸腾床加氢裂化区。
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公开(公告)号：US20150217265A1
公开(公告)日：2015-08-06
申请号：US14685781
申请日：2015-04-14
Applicant: Lummus Technology Inc.
Inventor： Marvin I. Greene
CPC classification number: B01J19/24 , B01J8/02 , B01J2208/027 , B01J2219/00103 , B01J2219/24 , C10G3/40 , C10G3/50 , C10G45/00 , C10G45/06 , C10G45/08 , C10G45/10 , C10G65/12 , C10G69/06 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , Y02P30/20
Abstract: A process for converting triacylglycerides-containing oils into crude oil precursors and/or distillate hydrocarbon fuels is disclosed. The process may include reacting a triacylglycerides-containing oil-carbon dioxide mixture at a temperature in the range from about 250° C. to about 525° C. and a pressure greater than about 75 bar to convert at least a portion of the triacylglycerides to a hydrocarbon or mixture of hydrocarbons comprising one or more of isoolefins, isoparaffins, cycloolefins, cycloparaffins, and aromatics.
Abstract translation: 公开了一种将含三酰基甘油酯的油转化为原油前体和/或馏出烃燃料的方法。 该方法可以包括在约250℃至约525℃的温度和大于约75巴的压力下使含三酰基甘油酯的油 - 二氧化碳混合物反应，以将至少一部分三酰基甘油酯转化为 包含一种或多种异烯烃，异链烷烃，环烯烃，环烷烃和芳烃的烃或烃混合物。
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40.发明申请CO-CURRENT ADIABATIC REACTION SYSTEM FOR CONVERSION OF TRIACYLGLYCERIDES RICH FEEDSTOCKS 审中-公开用于转化三聚氰胺的CO-电流ADIABATIC反应系统公开(公告)号：US20150152336A1
公开(公告)日：2015-06-04
申请号：US14096763
申请日：2013-12-04
Applicant: Lummus Technology Inc.
Inventor： Marvin I. Greene
IPC: C10G3/00
Abstract: A process for converting triacylglycerides-containing oils into crude oil precursors and/or distillate hydrocarbon fuels is disclosed. The process may include: reacting a triacylglycerides-containing oil-water-hydrogen mixture in a single reactor at a temperature in the range from about 250° C. to about 650° C. and a pressure greater than about 75 bar to convert at least a portion of the triacylglycerides via homogeneously catalyzed hydrothermolysis and heterogeneously catalyzed hydrotreatment.
Abstract translation: 公开了一种将含三酰基甘油酯的油转化为原油前体和/或馏出烃燃料的方法。 该方法可以包括：在单一反应器中在约250℃至约650℃的温度和大于约75巴的压力下使含三酰基甘油酯的油 - 水 - 氢混合物反应，以至少转化 通过均匀催化的水热解和非均相催化的加氢处理，一部分三酰甘油酯。
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