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1. 发明授权

US06835301B1 Production of low sulfur/low aromatics distillates 有权
标题翻译：生产低硫/低芳烃馏分
公开(公告)号：US06835301B1
公开(公告)日：2004-12-28
申请号：US09457434
申请日：1999-12-07
申请人： Edward S. Ellis , Henry Jung , William E. Lewis
发明人： Edward S. Ellis , Henry Jung , William E. Lewis
IPC分类号： C10G6512
CPC分类号： C10G65/12
摘要： A process for hydroprocessing a hydrotreated liquid distillate stream to produce a stream exceptionally low in sulfur as well as aromatics. A hydrotreated distillate stream is further hydrotreated in a co-current reaction zone wherein the reaction product is passed to a separation drum wherein a vapor product is collected overhead and a liquid product is passed to a aromatics saturation zone countercurrent to the flow of hydrogen treat gas.
摘要翻译：加氢加工处理的液体馏出物流以产生特别低的硫以及芳族化合物的方法。加氢处理的馏出物流在并流反应区中进一步加氢处理，其中将反应产物通入分离鼓，其中蒸气产物在塔顶馏出，液体产物通过与氢处理气体流逆流的芳烃饱和区。

2. 发明授权

US06702935B2 Hydrocracking process to maximize diesel with improved aromatic saturation 失效
标题翻译：加氢裂化过程使柴油最大化，提高芳族饱和度
公开(公告)号：US06702935B2
公开(公告)日：2004-03-09
申请号：US10028557
申请日：2001-12-19
申请人： Dennis R. Cash , Arthur J. Dahlberg
发明人： Dennis R. Cash , Arthur J. Dahlberg
IPC分类号： C10G6512
CPC分类号： C10G65/12
摘要： A VGO stream is initially hydrocracked in a hydrocracking reaction zone within an integrated hydroconversion process. Effluent from the hydrocracking reaction zone is combined with a light aromatic-containing feed stream, and the blended stream hydrotreated in a hydrotreating reaction zone. Heat exchange occurs between the hydrocracking reaction zone and the hydrotreating reaction zone, permitting the temperature control of the initial hydrocracking zone. The integrated reaction system provides a single hydrogen supply and recirculation system for use in two reaction processes.
摘要翻译： VGO流最初在加氢裂化反应区内进行加氢裂化，在一个集成的加氢转化过程中。将来自加氢裂化反应区的流出物与含轻芳香族的进料流混合，并将混合物流在加氢处理反应区中加氢处理。在加氢裂化反应区和加氢处理反应区之间发生热交换，允许初始加氢裂化区的温度控制。综合反应系统提供了单个氢气供应和再循环系统，用于两个反应过程。

3. 发明授权

US06183627B2 Process and apparatus for upgrading hydrocarbon feeds containing sulfur, metals, and asphaltenes 失效
标题翻译：用于升级含硫，金属和沥青质的烃进料的方法和装置
公开(公告)号：US06183627B2
公开(公告)日：2001-02-06
申请号：US09261157
申请日：1999-03-03
申请人： J. Robert Friday , Philip B. Rettger , Randall S. Goldstein
发明人： J. Robert Friday , Philip B. Rettger , Randall S. Goldstein
IPC分类号： C10G6512
CPC分类号： C10G67/049 , C10G47/34 , Y10S585/921
摘要： Upgrading of a hydrocarbon feed containing sulfur, metals, and asphaltenes involves applying the feed to a distillation column for producing a substantially asphaltene-free, and metal-free distillate fraction and a non-distilled fraction containing sulfur, asphaltenes, and metals. At least some of the substantially asphaltene-free, and metal-free distillate fraction is converted to a hydrogen donor diluent. The non-distilled fraction is processed in a solvent deasphalting unit for producing a deasphalted oil stream and an asphaltene stream. After a combined stream is formed from the hydrogen donor diluent and the deasphalted oil stream, the combined stream is thermally cracked forming a thermally cracked stream that is applied to the distillation column.
摘要翻译：包含硫，金属和沥青质的烃进料的升级包括将进料施加到蒸馏塔，用于生产基本上不含沥青质的，不含金属的馏出物馏分和含有硫，沥青质和金属的非蒸馏馏分。将至少一些基本上不含沥青质的无金属馏分馏分转化为氢供体稀释剂。未蒸馏的馏分在溶剂脱沥青装置中进行处理，用于生产脱沥青油料流和沥青质料流。在由氢供体稀释剂和脱沥青油流形成合并的流体之后，组合的料流被热裂化，形成施加到蒸馏塔的热裂化流。

4. 发明授权

US06602402B1 Flexible process for producing base stock and distillates by conversion-hydroisomerisation using a catalyst with low dispersion followed by catalytic dewaxing 失效
标题翻译：通过使用低分散体催化脱蜡的催化剂通过转化 - 加氢异构化生产基础油料和馏出物的柔性方法
公开(公告)号：US06602402B1
公开(公告)日：2003-08-05
申请号：US09562286
申请日：2000-05-01
申请人： Eric Benazzi , Nathalie Marchal-George , Tivadar Cseri , Pierre Marion , Christophe Gueret , Slavik Kasztelan
发明人： Eric Benazzi , Nathalie Marchal-George , Tivadar Cseri , Pierre Marion , Christophe Gueret , Slavik Kasztelan
IPC分类号： C10G6512
CPC分类号： C10G65/12 , B01J21/12 , B01J23/40 , B01J23/42 , B01J23/44 , B01J29/064 , B01J29/076 , B01J29/67 , B01J29/7446 , B01J29/7484 , B01J35/006 , B01J35/0066 , B01J35/023 , C10G45/62 , C10G65/043
摘要： An improved process for producing very high quality base stock and for simultaneous production of high quality middle distallates, comprising successive hydroisomerisation and catalystic dewaxing steps wherein hydroisomerisation is carried out in the presence of a catalyst containing at least one noble metal deposited on an amorphous acidic support, the dispersion of the metal being less than 20%. The support is preferably an amorphous silica-alumina. Catalytic dewaxing is carried out in the presence of a catalyst containing at least one hydrodehydrogenating element (group VIII) and at least one molecular sieve (preferably zeolite). The sieve is preferable selected from NU-10, EU-1, EU-13, zeolite and ferrierite.
摘要翻译：一种用于生产非常高质量的基础油料和用于同时生产高质量中间蒸馏物的改进方法，其包括连续加氢异构化和催化脱蜡步骤，其中加氢异构化在含有至少一种沉积在无定形酸性载体上的贵金属的催化剂存在下进行，金属的分散度小于20％。载体优选为无定形二氧化硅 - 氧化铝。催化脱蜡在含有至少一种氢化脱氢元素（VIII族）和至少一种分子筛（优选沸石）的催化剂存在下进行。筛子优选选自NU-10，EU-1，EU-13，沸石和镁碱沸石。

5. 发明授权

US06361683B1 Hydrocracking process 失效
标题翻译：加氢裂化过程
公开(公告)号：US06361683B1
公开(公告)日：2002-03-26
申请号：US09507660
申请日：2000-02-22
申请人： Tom N. Kalnes
发明人： Tom N. Kalnes
IPC分类号： C10G6512
CPC分类号： C10G65/12
摘要： A catalytic hydrocracking process wherein a hydrocarbonaceous feedstock and a liquid recycle stream having a temperature greater than about 500° F. and saturated with hydrogen is contacted with hydrogen in a hydrocracking reaction zone at elevated temperature and pressure to obtain conversion to lower boiling hydrocarbons. The resulting hot, uncooled effluent from the hydrocracking reaction zone is hot hydrogen stripped in a stripping zone maintained at essentially the same pressure as the hydrocracking zone to produce a first gaseous hydrocarbonaceous stream and a first liquid hydrocarbonaceous stream. The first gaseous hydrocarbonaceous stream is passed through a post-treat hydrogenation zone to saturate aromatic compounds and at least partially condensed to produce a second liquid hydrocarbonaceous stream and a second hydrogen-rich gaseous stream.
摘要翻译：催化加氢裂化方法，其中在高温和高压下，在加氢裂化反应区中将烃原料和温度大于约500°F并用氢饱和的液体再循环料与氢气接触，以获得转化为低沸点烃。所得到的来自加氢裂化反应区的热的未冷却流出物是在与加氢裂化区保持基本相同的压力的汽提区中汽提的氢气，以产生第一气态烃流和第一液体烃流。第一气态烃物流通过后处理氢化区以使芳族化合物饱和并至少部分冷凝以产生第二液态烃流和第二富氢气流。

6. 发明授权

US06337010B1 Process scheme for producing lubricating base oil with low pressure dewaxing and high pressure hydrofinishing 失效
标题翻译：用低压脱蜡和高压加氢精制生产润滑油基础油的工艺方案
公开(公告)号：US06337010B1
公开(公告)日：2002-01-08
申请号：US09366037
申请日：1999-08-02
申请人： Kevin L. Hofer
发明人： Kevin L. Hofer
IPC分类号： C10G6512
CPC分类号： C10G65/12 , C10G2400/10
摘要： A process for the production of a UV stable lubricating base oil from a waxy hydrocarbon feedstock comprising the steps of hydrocracking the feedstock; dewaxing the intermediate feedstock from the hydrocracking zone under low pressure; and stabilizing the dewaxed lubricating base oil under high pressure in a hydrofinishing zone.
摘要翻译：一种从蜡质烃原料生产UV稳定的润滑基础油的方法，包括加氢裂化原料的步骤; 在低压下从加氢裂化区脱蜡中间原料; 并且在加氢精制区域中在高压下稳定脱蜡润滑油基础油。

7. 发明授权

US06190535B1 Hydrocracking process 有权
标题翻译：加氢裂化过程
公开(公告)号：US06190535B1
公开(公告)日：2001-02-20
申请号：US09377410
申请日：1999-08-20
申请人： Tom N. Kalnes , Richard K. Hoehn
发明人： Tom N. Kalnes , Richard K. Hoehn
IPC分类号： C10G6512
CPC分类号： C10G65/12
摘要： A catalytic hydrocracking process wherein a denitrification and desulfurization reaction zone effluent is heat-exchanged with a hydrogen-rich gaseous stream and introduced into a hydrocracking zone. The resulting effluent from the hydrocracking zone is passed directly without cooling into a hot, high-pressure stripper utilizing a hot, hydrogen-rich gaseous stream at least a portion of which is heated during the heat exchange with the denitrification and desulfurization reaction zone effluent. The stripper overhead is partially condensed to produce a hydrogen-rich gaseous stream and a liquid stream containing hydrocracked hydrocarbon compounds. At least a portion of the stripper bottoms is recycled to the denitrification and desulfurization reaction zone.
摘要翻译：催化加氢裂化方法，其中脱氮和脱硫反应区流出物与富氢气流进行热交换并引入加氢裂化区。来自加氢裂化区的所得流出物直接通过，而不用冷却至热的高压汽提器，利用热的富氢气流，其中至少一部分气流在与脱氮和脱硫反应区流出物进行热交换期间被加热。汽提器顶部部分冷凝以产生富氢气流和含有加氢裂化烃化合物的液体流。至少部分汽提塔底部物料再循环到脱氮和脱硫反应区。

8. 发明授权

US06814856B1 Method for improving a gas oil fraction cetane index 失效
$Method for improving a gas oil fraction cetane index$
标题翻译：提高瓦斯油馏分十六烷指数的方法
公开(公告)号：US06814856B1
公开(公告)日：2004-11-09
申请号：US09445573
申请日：2000-05-04
申请人： Marcel Aussillous , Alain Billion , Patrick Briot , Christophe Gueret , Slavik Kasztelan , Narhalie Marchal , Pierre Marion
发明人： Marcel Aussillous , Alain Billion , Patrick Briot , Christophe Gueret , Slavik Kasztelan , Narhalie Marchal , Pierre Marion
IPC分类号： C10G6512
CPC分类号： C10G65/12 , C10G2400/04
摘要： A process for transforming a gas oil cut from a conversion process or from an aromatic crude is described, the aim of the process being to improve the cetane number of said cut. The process comprises at least one hydrogenation step in which said gas oil cut is passed, in the presence of hydrogen, over a catalyst comprising an amorphous mineral support, at least one compound of a group VIB metal, at least one compound of a non noble group VIII metal and at least phosphorous or a compound of phosphorous, the process then comprising a hydrocracking step in which the hydrogenated feed is passed, in the presence of hydrogen, over a catalyst comprising an acidic support, at least one compound of a group VIB metal and at least one compound of a non noble group VIII metal.

9. 发明授权

US06630066B2 Hydrocracking and hydrotreating separate refinery streams 有权
标题翻译：加氢裂化和加氢处理分离炼油厂流
公开(公告)号：US06630066B2
公开(公告)日：2003-10-07
申请号：US09808671
申请日：2001-03-14
申请人： Dennis R. Cash , Arthur J. Dahlberg
发明人： Dennis R. Cash , Arthur J. Dahlberg
IPC分类号： C10G6512
CPC分类号： C10G65/12
摘要： This invention is directed to middle distillate production (e.g., diesel and kerosene products) by means of a reactor hydroprocessing system using two or more reactors (or a single reactor vessel having two or more stages, each stage containing one or more reaction zones). Hydrocracking is preferably performed in the initial reactor, and hydrotreating (and/or further hydrocracking) is preferably performed in the subsequent reactor vessel or stages within a single vessel. Reaction stages are effectively segregated to avoid recracking of products, to dramatically reduce hydrogen consumption in saturating the bottoms product and to carry out aromatic saturation of middle distillates in a clean low-temperature environment.
摘要翻译：本发明涉及通过使用两个或多个反应器的反应器加氢处理系统（或具有两个或多个阶段的单个反应器容器，每个阶段包含一个或多个反应区域）的中间馏分生产（例如柴油和煤油产品）。加氢裂化优选在初始反应器中进行，并且加氢处理（和/或进一步加氢裂化）优选在随后的反应器容器或单个容器内的阶段中进行。反应阶段被有效地分离以避免产物重新产生，从而显着降低饱和塔底产物中的氢消耗，并在干净的低温环境中进行中间馏分的芳族饱和。

10. 发明授权

US06623623B2 Simultaneous hydroprocessing of two feedstocks 有权
标题翻译：同时加氢处理两种原料
公开(公告)号：US06623623B2
公开(公告)日：2003-09-23
申请号：US09894500
申请日：2001-06-28
申请人： Tom N. Kalnes
发明人： Tom N. Kalnes
IPC分类号： C10G6512
CPC分类号： C10G65/12 , C10G65/00
摘要： A catalytic hydrocracking process which simultaneously hydroprocesses two feedstocks to provide higher liquid product yields and increase the quality of the liquid products. A first feedstock is passed to a denitrification and desulfurization reaction zone to produce a stream which is in turn passed to a hot, high pressure stripper utilizing a hot, hydrogen-rich stripping gas to produce a first vapor stream and a first liquid stream. At least a portion of the first liquid stream is passed to a hydrocracking zone. A second feedstock having an average boiling point lower than the first feedstock in one embodiment is passed into an upper end of the hot, high pressure stripper to serve as reflux and in another embodiment is passed to an intermediate location in the denitrification and desulfurization reaction zone to serve as quench.
摘要翻译：同时加氢处理两种原料以提供更高液体产物的催化加氢裂化方法产生并提高液体产品的质量。将第一原料通入脱氮和脱硫反应区，以产生一种物流，该物流又通过热的富含氢气的汽提气体传递到热的高压汽提器，以产生第一蒸气流和第一液体流。至少一部分第一液体流被传送到加氢裂化区。在一个实施方案中，平均沸点低于第一原料的第二原料进入热高压汽提塔的上端，作为回流，在另一个实施方案中，通入脱氮和脱硫反应区的中间位置作为淬火。

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