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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：US07097760B1
公开(公告)日：2006-08-29
申请号：US10141228
申请日：2002-05-07
CPC分类号： C10G45/02 , C10G47/00 , C10G65/12 , C10G2400/04
摘要： A catalytic hydrocracking process for the production of ultra low sulfur diesel wherein a hydrocarbonaceous feedstock is hydrocracked at elevated temperature and pressure to obtain conversion to diesel boiling range hydrocarbons. The resulting hydrocracking zone effluent is 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 containing diesel boiling range hydrocarbons is introduced into a desulfurization zone and subsequently partially condensed to produce a hydrogen-rich gaseous stream and a second liquid hydrocarbonaceous stream containing diesel boiling range hydrocarbons. The first liquid stream is separated to produce a third liquid hydrocarbonaceous stream containing diesel boiling range hydrocarbons which is also introduced into the desulfurization zone. An ultra low sulfur diesel product stream is recovered.
摘要翻译： 用于生产超低硫柴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加氢裂化以获得转化为柴油沸程烃。 所得到的加氢裂化区流出物在汽提区中被汽提，保持在与加氢裂化区基本相同的压力，以产生第一气态烃流和第一液体烃流。 将含有柴油沸程烃的第一气态烃流引入脱硫区，随后部分冷凝以产生富含氢的气态物流和含有柴油沸程烃的第二液体烃物流。 分离第一液体流以产生含有柴油沸程烃的第三液体烃流，其也被引入脱硫区。 回收超低硫柴油产品流。
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3.发明授权公开(公告)号：US06379533B1
公开(公告)日：2002-04-30
申请号：US09738452
申请日：2000-12-18
IPC分类号： C10G6500
CPC分类号： C10G65/12
摘要： A catalytic hydrocracking process which provides for the simultaneous production of LPG and distillate hydrocarbons. The feedstock is introduced into a denitrification and desulfurization zone and then passed directly to a hot, high pressure stripper utilizing a hot, hydrogen-rich stripping gas to produce a first liquid stream boiling in the range of the feedstock and a first vapor stream comprising hydrocarbonaceous compounds boiling at a temperature below the boiling range of the feedstock. The first liquid stream is hydrocracked in a first hydrocracking zone and then passed to the denitrification and desulfurization zone. At least a portion of the first vapor stream is condensed to produce a second liquid stream comprising hydrocarbonaceous compounds boiling at a temperature below the boiling range of the feedstock. At least a portion of the second liquid stream is hydrocracked in a second hydrocracking zone containing a second hydrocracking catalyst to produce LPG boiling range hydrocarbonaceous compounds.
摘要翻译： 催化加氢裂化方法，提供同时生产液化石油气和馏出烃。 将原料引入反硝化和脱硫区，然后通过热的富含氢气的汽提器直接通入热的高压汽提器，以产生在原料范围内沸腾的第一液体物流和含有烃的第一蒸气流 在低于原料沸点范围的温度下沸腾的化合物。 将第一液流在第一加氢裂化区中加氢裂化，然后通入脱氮脱硫区。 第一蒸气流的至少一部分被冷凝以产生包含在低于原料的沸程的温度下沸腾的含烃化合物的第二液流。 在含有第二加氢裂化催化剂的第二加氢裂化区中将至少一部分第二液体物流加氢裂解，以产生LPG沸程烃类化合物。
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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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6.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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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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公开(公告)号：US06638418B1
公开(公告)日：2003-10-28
申请号：US10045285
申请日：2001-11-07
IPC分类号： C10G4500
CPC分类号： C10G65/12 , C10G2400/04
摘要： A dual recycle catalytic hydrocracking process for the production of ultra low sulfur diesel while simultaneously processing two feedstocks. One preferred feedstock boils in the temperature range of diesel and the second preferred feedstock boils in the temperature range above that of diesel.
摘要翻译： 双重循环催化加氢裂化方法，用于生产超低硫柴油，同时处理两种原料。 一种优选的原料在柴油的温度范围内沸腾，第二种优选的原料在高于柴油的温度范围内沸腾。
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10.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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