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公开(公告)号：US06517705B1
公开(公告)日：2003-02-11
申请号：US09813557
申请日：2001-03-21
申请人： Tom N. Kalnes , Vasant P. Thakkar
发明人： Tom N. Kalnes , Vasant P. Thakkar
IPC分类号： C10G4700
摘要： A catalytic hydrocracking process for the production of lube base oil wherein a hydrocarbonaceous feedstock is contacted with hydrogen and a metal promoted hydrocracking catalyst in a hydrocracking reaction zone at elevated temperature and pressure to obtain conversion to higher hydrogen-content hydrocarbons including lube base oil. The resulting hot, uncooled effluent from the hydrocracking reaction zone is hydrogen stripped in a hot, high pressure 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. At least a portion of the first gaseous hydrocarbonaceous stream is condensed to produce a second liquid hydrocarbonaceous stream and a second hydrogen-rich gaseous stream. The first liquid hydrocarbonaceous stream is preferably separated at a pressure greater than atmospheric pressure to provide at least one lube base oil product stream.
摘要翻译： 用于生产润滑油基础油的催化加氢裂化方法，其中烃原料在升高的温度和压力下在加氢裂化反应区中与氢和金属促进的加氢裂化催化剂接触，以获得转化为更高含氢烃的烃，包括润滑油基础油。 所得到的来自加氢裂化反应区的热的未冷却流出物在与加氢裂化区保持基本相同的压力的热的高压汽提区中被汽提，以产生第一气态烃流和第一液体烃流。 第一气态烃流的至少一部分被冷凝以产生第二液态烃流和第二富氢气流。 优选在大于大气压的压力下分离第一液体烃流，以提供至少一种润滑油基础油产品流。
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公开(公告)号：US06106694A
公开(公告)日：2000-08-22
申请号：US163156
申请日：1998-09-29
申请人： Tom N. Kalnes , Vasant P. Thakkar
发明人： Tom N. Kalnes , Vasant P. Thakkar
CPC分类号： C10G65/00
摘要： A hydrocracking process wherein a hydrocarbonaceous feedstock and a hot hydrocracking zone effluent containing hydrogen is passed to a denitrification and desulfurization reaction zone to produce hydrogen sulfide and ammonia to thereby clean up the fresh feedstock. The resulting hot, uncooled effluent from the denitrification and desulfurization zone is hydrogen stripped in a stripping zone maintained at essentially the same pressure as the preceding reaction zone with a hydrogen-rich gaseous stream to produce a vapor stream comprising hydrogen, hydrocarbonaceous compounds boiling at a temperature below the boiling range of the fresh feedstock, hydrogen sulfide and ammonia, and a liquid hydrocarbonaceous stream.
摘要翻译： 加氢裂化方法，其中含烃原料和含氢气的热加氢裂化区流出物通入脱氮和脱硫反应区以产生硫化氢和氨，从而清洁新鲜原料。 所得到的来自脱氮和脱硫区的热未冷却流出物在汽提区中被氢气汽提，在汽提区中与富氧气流保持与前述反应区基本相同的压力，以产生包含氢气的蒸气流， 温度低于新鲜原料的沸程，硫化氢和氨，以及液体烃流。
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公开(公告)号：US5885440A
公开(公告)日：1999-03-23
申请号：US918436
申请日：1997-08-26
CPC分类号： C10G65/12
摘要： The invention is a hydrocracking process which employs a small reactor-containing hydrotreating catalyst to reduce the recombinant mercaptan content and/or smoke point of a product recovered from the effluent of the hydrocracking reactor. The entire effluent of the hydrocracking reactor is first cooled by indirect heat exchange and then passed through the hydrotreating catalyst. The effluent of the hydrotreating catalyst then continues throughout the customary cooling and separation steps employed in the product recovery system.
摘要翻译： 本发明是加氢裂化方法，其使用含有反应器的小型加氢处理催化剂来减少从加氢裂化反应器的流出物中回收的产物的重组硫醇含量和/或烟点。 首先通过间接热交换冷却加氢裂化反应器的全部流出物，然后通过加氢处理催化剂。 然后加氢处理催化剂的流出物在产品回收系统中采用的常规冷却和分离步骤中继续进行。
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公开(公告)号：US07803334B1
公开(公告)日：2010-09-28
申请号：US11456732
申请日：2006-07-11
申请人： Richard K. Hoehn , Vasant P. Thakkar , Vedula K. Murty , Douglas W. Kocher-Cowan , Jennifer L. Anderson
发明人： Richard K. Hoehn , Vasant P. Thakkar , Vedula K. Murty , Douglas W. Kocher-Cowan , Jennifer L. Anderson
CPC分类号： C10G47/00 , B01J8/0453 , B01J8/0492 , B01J2208/00274 , B01J2208/025
摘要： A hydrocracking process and apparatus wherein the feedstock is hydrotreated and the liquid and gaseous effluent from the hydrotreater is directly introduced into the upper end of a hydrocracking vessel which provides a liquid seal to prevent the passage of the gaseous stream containing hydrogen sulfide and ammonia from the hydrotreater to enter the hydrocracking zone containing hydrocracking catalyst. Fresh hydrogen is then introduced into the hydrocracking zone.
摘要翻译： 加氢裂化方法和装置，其中原料被加氢处理，并且来自加氢处理器的液态和气态流出物被直接引入加氢裂化容器的上端，该加氢裂化容器提供液体密封，以防止含有硫化氢和氨的气流从 加氢处理器进入含有加氢裂化催化剂的加氢裂化区。 然后将新鲜氢气引入加氢裂化区。
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公开(公告)号：US07419582B1
公开(公告)日：2008-09-02
申请号：US11456728
申请日：2006-07-11
申请人： Richard K. Hoehn , Vasant P. Thakkar , Vedula K. Murty , Douglas W. Kocher-Cowan , Jennifer L. Anderson
发明人： Richard K. Hoehn , Vasant P. Thakkar , Vedula K. Murty , Douglas W. Kocher-Cowan , Jennifer L. Anderson
摘要： A hydrocracking process wherein the feedstock is hydrotreated and the liquid and gaseous effluent from the hydrotreater is directly introduced into the upper end of a hydrocracking vessel which provides a liquid seal to prevent the passage of the gaseous stream containing hydrogen sulfide and ammonia from the hydrotreater to enter the hydrocracking zone containing hydrocracking catalyst. Fresh hydrogen is then introduced into the hydrocracking zone. An apparatus for hydrocracking a hydrocarbon feedstock is also disclosed.
摘要翻译： 加氢裂化方法，其中原料被加氢处理，来自加氢处理器的液态和气态流出物被直接引入加氢裂化容器的上端，该加氢裂化容器提供液体密封以防止含有硫化氢和氨的气态物流从加氢处理器通到 进入含有加氢裂化催化剂的加氢裂化区。 然后将新鲜氢气引入加氢裂化区。 还公开了用于加氢裂化烃原料的装置。
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16.发明授权
公开(公告)号：US5985132A
公开(公告)日：1999-11-16
申请号：US957236
申请日：1997-10-24
CPC分类号： C10G65/00 , C10G2400/10
摘要： A process for the simultaneous production of lubricating blending stocks by means of hydrocracking a hydrocarbon feedstock in a first hydrocracking zone to convert at least a portion of the heavy hydrocarbon feedstock to produce an effluent stream containing lube oil boiling range hydrocarbons. One portion of the effluent stream is directly removed from the first hydrocracking zone to produce high quality lube oil blending stocks. Another portion of the effluent stream from the first hydrocracking zone is directly introduced into a second hydrocracking zone without intermediate separation. The second hydrocracking zone is utilized to further crack the feed to produce motor fuel.
摘要翻译： 一种通过在第一加氢裂化区中加氢裂解烃原料同时生产润滑共混料的方法，以转化至少一部分重质烃原料以产生含有润滑油沸程烃的流出物流。 排出物流的一部分从第一加氢裂化区直接除去，以产生高品质的润滑油混合料。 来自第一加氢裂化区的流出物流的另一部分被直接引入第二加氢裂化区而没有中间分离。 第二个加氢裂化区用于进一步裂化进料以产生电动机燃料。
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17.发明授权公开(公告)号：US07384542B1
公开(公告)日：2008-06-10
申请号：US10862731
申请日：2004-06-07
CPC分类号： C10G65/14 , C10G2400/02 , C10G2400/04
摘要： A process for the production of low sulfur diesel and high octane naphtha.
摘要翻译： 一种生产低硫柴油和高辛烷值的石脑油的方法。
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公开(公告)号：US07547386B1
公开(公告)日：2009-06-16
申请号：US11049542
申请日：2005-02-02
CPC分类号： C10G65/14 , C10G45/02 , C10G47/00 , C10G69/14 , C10G70/043
摘要： An integrated process for the hydroprocessing of multiple feedstreams including vacuum gas oil and light cycle oil. The light cycle oil is reacted with hydrogen in a hydrocracking zone and the hydrocarbon feedstream comprising vacuum gas oil is reacted with hydrogen in a hydrodesulfurization reaction zone. The hydrotreated vacuum gas oil is good FCC feedstock. Naphtha and ultra low sulfur diesel are recovered in a common fractionation column.
摘要翻译： 用于加氢处理多种进料流的综合方法，包括减压瓦斯油和轻循环油。 光循环油在加氢裂化区与氢反应，含有真空瓦斯油的烃进料流与加氢脱硫反应区中的氢反应。 加氢处理的真空瓦斯油是良好的FCC原料。 石脑油和超低硫柴油在普通分馏塔中回收。
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19.发明授权Combination of mild hydrotreating and hydrocracking for making low sulfur diesel and high octane naphtha 有权结合轻度加氢处理和加氢裂化制备低硫柴油和高辛烷值的石脑油公开(公告)号：US08404103B2
公开(公告)日：2013-03-26
申请号：US13286769
申请日：2011-11-01
申请人： Bart Dziabala , Vasant P. Thakkar , Suheil F. Abdo
发明人： Bart Dziabala , Vasant P. Thakkar , Suheil F. Abdo
CPC分类号： C10G65/12 , C10G2300/1037 , C10G2300/202 , C10G2300/301 , C10G2300/305 , C10G2300/4018 , C10G2400/02 , C10G2400/04
摘要： Methods are disclosed for the hydrotreating and hydrocracking of highly aromatic distillate feeds such as light cycle oil (LCO) to produce ultra low sulfur gasoline and diesel fuel. Optimization of hydrotreater severity improves the octane quality of the gasoline or naphtha fraction. In particular, the operation of the hydrotreater at reduced severity to allow at least about 20 ppm by weight of organic nitrogen into the hydrocracker feed is shown to lead to these important benefits. Post-treating of the hydrocracker effluent over an additional hydrotreating catalyst bed may be desired to meet specifications for ultra low sulfur fuel components.
摘要翻译： 公开了用于加氢处理和加氢裂解高芳烃馏出物如轻循环油（LCO）以产生超低硫汽油和柴油燃料的方法。 加氢处理剂严重性的优化提高了汽油或石脑油馏分的辛烷值。 特别地，加氢处理器以较低的苛刻度运行，使至少约20ppm重量的有机氮进入加氢裂化器进料显示出这些重要的益处。 在另外的加氢处理催化剂床上后处理加氢裂化器流出物可能需要满足超低硫燃料组分的规格。
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公开(公告)号：US07686941B2
公开(公告)日：2010-03-30
申请号：US11530637
申请日：2006-09-11
IPC分类号： C10G45/00
摘要： A process for simultaneously hydrocracking multiple feedstocks wherein a first feedstock is hydrotreated in a hydrotreating zone to produce a hydrotreating zone effluent which is separated to provide a first vaporous hydrocarbonaceous stream and a first liquid hydrocarbonaceous stream. The second feedstock and the first vaporous hydrocarbonaceous stream are hydroprocessed in a hydroprocessing zone to produce a hydroprocessing zone effluent. A third feedstock and the first liquid hydrocarbonaceous stream are hydrocracked in a hydrocracking zone to produce a hydrocracking zone effluent. The hydrocracking zone effluent and the hydroprocessing zone effluent are separated to recover hydrocracked hydrocarbons.
摘要翻译： 一种同时加氢裂化多种原料的方法，其中第一原料在加氢处理区中加氢处理以产生加氢处理区流出物，其被分离以提供第一气态烃流和第一液体烃流。 将第二原料和第一气相烃流在加氢处理区中加氢处理以产生加氢处理区流出物。 将第三原料和第一液体烃流在加氢裂化区中加氢裂化以产生加氢裂化区流出物。 加氢裂化区流出物和加氢处理区流出物被分离以回收加氢裂化烃。
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