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51. 发明授权

US07938955B2 Method for producing super-low sulfur gas oil blending component or super-low sulfur gas oil composition, and super-low sulfur gas oil composition 失效
标题翻译：生产超低硫含硫油混合成分或超低硫含硫油组合物的方法，以及超低硫瓦斯油组合物
公开(公告)号：US07938955B2
公开(公告)日：2011-05-10
申请号：US11793209
申请日：2005-12-21
申请人： Yasuhiro Araki , Katsuaki Ishida
发明人： Yasuhiro Araki , Katsuaki Ishida
IPC分类号： C10G45/04 , C07C7/12
CPC分类号： C10G25/00 , B01J23/88 , B01J23/882 , B01J23/883 , B01J35/0006 , C10G45/08 , C10G2300/1059 , C10G2300/202 , C10G2300/308 , C10G2400/06
摘要： Provided are a method for producing a super-low sulfur gas oil blending component or a super-low sulfur gas oil composition having a sulfur content of less than 5 mass ppm, under relatively mild conditions, without greatly increasing the hydrogen consumption and without remarkably decreasing the aromatic content; and a super-low sulfur gas oil composition having a sulfur content of less than 5 mass ppm which exhibits a high heating value, is excellent in fuel economy and output power, and is free from an adverse effect on a sealing rubber member or the like used in the fuel injection system and thus does not cause the leakage of a fuel. A method for producing a super-low sulfur gas oil blending component or a super-low sulfur gas oil composition having a sulfur content of less than 5 mass ppm is also disclosed.
摘要翻译：提供一种在相对温和的条件下生产硫含量小于5质量ppm的超低硫油混合组分或超低硫油组合物的方法，而不会大大增加氢消耗并且不显着降低芳香含量; 硫含量低于5质量ppm的超低硫磺油组合物，具有高的发热量，燃料经济性和输出功率优异，并且对密封橡胶构件等没有不利影响在燃料喷射系统中使用，因此不会导致燃料泄漏。还公开了一种硫含量小于5质量ppm的超低硫油混合组分或超低硫含硫油组合物的制备方法。

52. 发明申请

US20110087059A1 PROCESS FOR HYDROTREATMENT AND HYDROISOMERIZATION OF FEEDSTOCKS OBTAINED FROM A RENEWABLE SOURCE IMPLEMENTING A MODIFIED ZEOLITE 审中-公开
标题翻译：从可再生来源获得的进料的水解和水解过程实施改性沸石
公开(公告)号：US20110087059A1
公开(公告)日：2011-04-14
申请号：US12903690
申请日：2010-10-13
申请人： Laurent SIMON , Antoine DAUDIN
发明人： Laurent SIMON , Antoine DAUDIN
IPC分类号： C10G1/00
CPC分类号： B01J29/166 , B01J23/883 , B01J29/084 , B01J29/72 , B01J29/7261 , B01J29/78 , B01J29/7861 , B01J37/20 , B01J2229/16 , B01J2229/20 , B01J2229/32 , B01J2229/42 , C10G3/46 , C10G3/47 , C10G3/50 , C10G3/54 , C10G45/64 , C10G2300/1014 , C10G2300/1018 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/06 , C10G2400/08 , Y02P30/20
摘要： This invention describes a process for treatment of feedstocks obtained from a renewable source implementing a catalyst that comprises at least one hydro-dehydrogenating metal that is selected from the group that is formed by the metals of group VIB and group VIII of the periodic table and a substrate that comprises at least one zeolite that has at least one series of channels whose opening is defined by a ring with 8 oxygen atoms modified by a) at least one stage for introducing at least one alkaline cation that belongs to group IA or IIA of the periodic table, b) a stage for treating said zeolite in the presence of at least one molecular compound that contains at least one silicon atom, c) at least one stage of partial exchange of said alkaline cations by NH4+ cations, and d) at least one heat treatment stage.
摘要翻译：本发明描述了一种处理从可再生原料获得的原料的方法，该方法包括至少一种选自由元素周期表第ⅥB族和Ⅷ族金属形成的基团的至少一种氢化脱氢金属的催化剂，以及底物，其包含至少一种沸石，其具有至少一个通道系列，其开口由具有8个氧原子的环限定，所述环具有由a）至少一个阶段修饰，用于引入至少一种碱性阳离子，所述碱性阳离子属于周期表，b）在至少一种含有至少一个硅原子的分子化合物存在下处理所述沸石的阶段，c）至少一个阶段由NH 4 +阳离子部分交换所述碱性阳离子，和d）至少一个热处理阶段。

53. 发明授权

US07923593B2 Process for producing a middle distillate 有权
标题翻译：生产中间馏分的方法
公开(公告)号：US07923593B2
公开(公告)日：2011-04-12
申请号：US12184069
申请日：2008-07-31
申请人： Sven Ivar Hommeltoft , Stephen J. Miller , Ajit Pradhan
发明人： Sven Ivar Hommeltoft , Stephen J. Miller , Ajit Pradhan
IPC分类号： C07C2/60 , C07C2/62
CPC分类号： C10G29/205 , C10G17/09 , C10G2300/1022 , C10G2300/1033 , C10G2300/1081 , C10G2300/1088 , C10G2300/301 , C10G2300/4025 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08
摘要： A process for producing a middle distillate or a middle distillate blending component, comprising contacting a feed comprising an olefin, an isoparaffin, and less than 5 wt % oligomerized olefin, in an ionic liquid alkylation zone with an acidic haloaluminate ionic liquid, at alkylation conditions; and recovering an effluent comprising an alkylated product that has greater than 35 vol % C10+ and less than 1 vol % C55+. Also processes for producing a middle distillate by alkylating isobutane and butene in the presence of defined chloroaluminate ionic liquid catalysts, wherein a separating step separates the middle distillate and wherein the middle distillate is from 20 wt % or higher of the total alkylate product. Also a process for producing middle distillate with FC cracker feed comprising olefins. A separated middle distillate has greater than 30 vol % C10+, less than 1 vol % C55+, and a cloud point less than −50° C.
摘要翻译：一种制备中间馏分或中间馏分共混组分的方法，包括在烷基化条件下使包含烯烃，异链烷烃和少于5重量％的低聚烯烃的进料在离子液体烷基化区与酸性卤化铝离子液体接触 ; 并回收含有大于35体积％C 10+且小于1体积％C 55+的烷基化产物的流出物。还有在定义的氯铝酸盐离子液体催化剂的存在下，通过烷基化异丁烷和丁烯生产中间馏分的方法，其中分离步骤分离中间馏分，其中中间馏分为总烷基化产物的20重量％或更高。还有一种生产含有烯烃的FC裂化器进料的中间馏分的方法。分离的中间馏分具有大于30体积％的C10 +，小于1体积％的C55 +和浊点小于-50℃。

54. 发明申请

US20110036755A1 Operating Method for Hydrodenitrogenation 有权
标题翻译：加氢脱氮的操作方法
公开(公告)号：US20110036755A1
公开(公告)日：2011-02-17
申请号：US12856234
申请日：2010-08-13
申请人： Teh C. Ho , Stuart L. Soled , Kuangnan Qian , Stephen J. McCarthy , Andrew C. Moreland
发明人： Teh C. Ho , Stuart L. Soled , Kuangnan Qian , Stephen J. McCarthy , Andrew C. Moreland
IPC分类号： C10G35/04
CPC分类号： C10G45/08 , C10G2400/06
摘要： The present invention relates to a catalytic process for removing organonitrogen species from hydrocarbon mixtures such as refinery process feedstreams. More particularly, this invention relates to a new operating and catalyst loading strategies based on organonitrogen concentration, composition, and structure.
摘要翻译：本发明涉及一种用于从烃混合物如炼油工艺进料流中除去有机氮物质的催化方法。更具体地，本发明涉及基于有机氮浓度，组成和结构的新的操作和催化剂加载策略。

55. 发明申请

US20090124711A1 Fischer-tropsch process and reactor assembly 有权
标题翻译：费 - 托法和反应器组装
公开(公告)号：US20090124711A1
公开(公告)日：2009-05-14
申请号：US11988970
申请日：2006-07-14
申请人： Arend Hoek , Hans Michiel Huisman
发明人： Arend Hoek , Hans Michiel Huisman
IPC分类号： C10G2/00 , B01J19/00
CPC分类号： C10G2/32 , B01J8/0278 , B01J8/065 , B01J8/067 , B01J8/22 , B01J2219/00038 , B01J2219/00202 , B01J2219/00211 , B01J2219/00231 , B01J2219/00238 , C10G2/34 , C10G2400/02 , C10G2400/06 , C10G2400/08 , C10G2400/10 , C10G2400/18
摘要： A method of accommodating a reduction in production capacity of one or more reactors in a multi-reactor assembly adapted for the production of hydrocarbon products from syngas, the syngas being provided by a syngas manufacturing facility and provided to an entry stream system providing syngas to each of the reactors, and having an exit stream system taking at least hydrocarbon products from the reactors, wherein the method comprises the steps of: redistributing the syngas from the one or more said reactors to one or more other reactors, and increasing the temperature in the said one or more other reactors to at least partially take over the reduction in production capacity of the one or more reactors.
摘要翻译：一种在适合从合成气生产碳氢化合物产品的多反应器组合中容纳一个或多个反应器的生产能力降低的方法，合成气由合成气制造设施提供并提供给进入流系统，其将合成气提供给每个的反应器，并且具有至少从反应器中取出烃产物的出口流系统，其中所述方法包括以下步骤：将来自所述一个或多个所述反应器的合成气重新分配到一个或多个其它反应器，并且增加所述反应器中的温度所述一个或多个其它反应器至少部分地承担一个或多个反应器的生产能力的降低。

56. 发明申请

US20080017551A1 Catalyst for Hydrotreating Hydrocarbon Oil, Process for Producing the Same, and Method for Hydrotreating Hydrocarbon Oil 有权
标题翻译：用于加氢处理烃油的催化剂，其制备方法和加氢处理烃油的方法
公开(公告)号：US20080017551A1
公开(公告)日：2008-01-24
申请号：US10594451
申请日：2005-03-22
申请人： Kazuyuki Kiriyama , Takashi Fujikawa , Masahiro Kato , Minoru Hashimoto
发明人： Kazuyuki Kiriyama , Takashi Fujikawa , Masahiro Kato , Minoru Hashimoto
IPC分类号： B01J27/19 , B01J29/16 , C10G45/04 , C10G45/08 , C10G45/12
CPC分类号： C10G45/12 , B01J21/12 , B01J27/1853 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1066 , C10G45/06 , C10G45/08 , C10G2300/4018 , C10G2400/02 , C10G2400/06 , C10G2400/08
摘要： There is provided a catalyst for hydrotreating a hydrocarbon oil, which comprises an inorganic oxide support containing a certain amount of phosphorus oxide having provided thereon: at least one selected from metals in the Group 6 of the periodic table, at least one selected from metals in the Group 8 of the periodic table, and carbon, and which has a certain specific surface area, pore volume, and mean pore diameter, a process for producing the same, and a method for hydrotreating a hydrocarbon oil using the same. Thereby, the catalyst can be produced in a simple and convenient manner and sulfur compounds in the hydrocarbon oil can be exceedingly highly desulfurized and simultaneously nitrogen compounds can be diminished without necessitating severe operating conditions.
摘要翻译：提供了一种用于加氢处理烃油的催化剂，其包含含有一定量的在其上提供的一定量的氧化磷的无机氧化物载体：选自元素周期表第6族金属中的至少一种，选自金属中的至少一种周期表第8族和碳，并且其具有一定的比表面积，孔体积和平均孔径，其制造方法以及使用其的烃油加氢处理方法。因此，催化剂可以以简单方便的方式制造，烃油中的硫化合物可以极度高度脱硫，同时氮化合物可以减少而不需要严苛的操作条件。

57. 发明申请

US20070261994A1 Method For Producing Super-Low Sulfur Gas Oil Blending Component Or Super-Low Sulfur Gas Oil Composition, and Super-Low Sulfur Gas Oil Composition 失效
标题翻译：超低硫磺油混合组分或超低硫磺油组合物和超低硫磺油组合物的生产方法
公开(公告)号：US20070261994A1
公开(公告)日：2007-11-15
申请号：US11793209
申请日：2005-12-21
申请人： Yasuhiro Araki , Katsuaki Ishida
发明人： Yasuhiro Araki , Katsuaki Ishida
IPC分类号： C10G45/60
CPC分类号： C10G25/00 , B01J23/88 , B01J23/882 , B01J23/883 , B01J35/0006 , C10G45/08 , C10G2300/1059 , C10G2300/202 , C10G2300/308 , C10G2400/06
摘要： Provided are a method for producing a super-low sulfur gas oil blending component or a super-low sulfur gas oil composition having a sulfur content of less than 5 mass ppm, under relatively mild conditions, without greatly increasing the hydrogen consumption and without remarkably decreasing the aromatic content; and a super-low sulfur gas oil composition having a sulfur content of less than 5 mass ppm which exhibits a high heating value, is excellent in fuel economy and output power, and is free from an adverse effect on a sealing rubber member or the like used in the fuel injection system and thus does not cause the leakage of a fuel. A method for producing a super-low sulfur gas oil blending component or a super-low sulfur gas oil composition having a sulfur content of less than 5 mass ppm is also disclosed.
摘要翻译：提供一种在相对温和的条件下生产硫含量小于5质量ppm的超低硫油混合组分或超低硫油组合物的方法，而不会大大增加氢消耗并且不显着降低芳香含量; 硫含量低于5质量ppm的超低硫磺油组合物，具有高的发热量，燃料经济性和输出功率优异，并且对密封橡胶构件等没有不利影响在燃料喷射系统中使用，因此不会导致燃料泄漏。还公开了一种硫含量小于5质量ppm的超低硫油混合组分或超低硫含硫油组合物的制备方法。

58. 发明授权

US07285693B2 Process to prepare a catalytically dewaxed gas oil or gas oil blending component 有权
标题翻译：制备催化脱蜡瓦斯油或瓦斯油混合组分的方法
公开(公告)号：US07285693B2
公开(公告)日：2007-10-23
申请号：US10505670
申请日：2003-02-25
申请人： Richard Hugh Clark
发明人： Richard Hugh Clark
IPC分类号： C10L1/00 , C10G65/12
CPC分类号： C10L1/08 , C10G2300/1022 , C10G2300/1059 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/80 , C10G2400/06 , C10G2400/10 , C10L1/04 , Y10S208/95
摘要： A process to prepare a catalytically dewaxed gas oil or gas oil blending component by performing the following steps:(a) hydrocracking/hydroisomerizing a Fischer-Tropsch product;(b) separating the product of step (a) into at least one or more fuel fractions and a gas oil precursor fraction;(c) catalytically dewaxing the gas oil precursor fraction obtained in step (b); and,(d) isolating the catalytically dewaxed gas oil or gas oil blending component from the product of step (c) by means of distillation.
摘要翻译：一种通过以下步骤制备催化脱蜡瓦斯油或瓦斯油混合组分的方法：（a）费 - 托产物的加氢裂化/加氢异构化; （b）将步骤（a）的产物分离成至少一种或多种燃料馏分和瓦斯油前体馏分; （c）催化脱蜡步骤（b）中获得的瓦斯油前体馏分; 和（d）通过蒸馏从步骤（c）的产物中分离催化脱蜡的瓦斯油或瓦斯油混合组分。

59. 发明授权

US07276150B2 Method of desulfurizing gas oil fraction, desulfurized gas oil, and desulfurizer for gas oil fraction 失效
$Method of desulfurizing gas oil fraction, desulfurized gas oil, and desulfurizer for gas oil fraction$
标题翻译：粗柴油馏分脱硫方法，脱硫瓦斯油，瓦斯油馏分脱硫剂
公开(公告)号：US07276150B2
公开(公告)日：2007-10-02
申请号：US10275038
申请日：2001-11-16
申请人： Shigeki Nagamatsu , Jun Abe , Akira Sugimoto , Makoto Inomata , Tetsuya Watanabe
发明人： Shigeki Nagamatsu , Jun Abe , Akira Sugimoto , Makoto Inomata , Tetsuya Watanabe
IPC分类号： C10L1/00 , C10G45/00
CPC分类号： C10G65/16 , B01J23/882 , C10G2300/1059 , C10G2300/202 , C10G2300/207 , C10G2400/06
摘要： The process for desulfurizing a gas oil fraction according to the invention comprises a low-boiling gas oil fraction hydrodesulfurization step (I) wherein a low-boiling gas oil fraction is desulsurized under the condition of a H2/Oil ratio of 70 to 200 Nm3/kl to obtain a treated oil, a high-boiling gas oil fraction hydrodesulfurization step (II) wherein a high-boiling gas oil fraction is desulsurized under the condition of a H2Oil ratio of 200 to 800 Nm3/kl to obtain a treated oil, and a step (III) wherein the treated oil obtained in the step (I) is mixed with the treated oil obtained in the step (II), and in this process, at least a part of a gas containing unreacted hydrogen in the step (II) is used for the hydrodesulfurization of the step (I).
摘要翻译：根据本发明的粗柴油馏分的脱硫方法包括低沸点瓦斯油馏分加氢脱硫步骤（I），其中低沸点瓦斯油馏分在H 2 N 2 / 油比为70〜200Nm 3 / kl，得到处理油，高沸点瓦斯油馏分加氢脱硫工序（II），其中高沸点瓦斯油馏分在条件下脱硫 H 2油比为200〜800Nm 3 / kl，得到处理油，和步骤（III），其中步骤（I）中得到的处理油为与步骤（II）中获得的处理油混合，并且在该方法中，将步骤（II）中的至少一部分含有未反应的氢的气体用于步骤（I）的加氢脱硫。

60. 发明申请

US20070213414A1 PROCESS TO PREPARE A FISCHER-TROPSCH SYNTHESIS PRODUCT 有权
标题翻译：制备FISCHER-TROPSCH SYNTHESIS产品的方法
公开(公告)号：US20070213414A1
公开(公告)日：2007-09-13
申请号：US11682351
申请日：2007-03-06
申请人： Jacobus Eilers , Robert Schouwenaar
发明人： Jacobus Eilers , Robert Schouwenaar
IPC分类号： C07C27/06
CPC分类号： C10G2/00 , C01B3/36 , C01B3/382 , C01B3/52 , C01B2203/0216 , C01B2203/0255 , C01B2203/0415 , C01B2203/0485 , C01B2203/062 , C01B2203/0827 , C01B2203/1241 , C01B2203/142 , C01B2203/148 , C01B2203/1614 , C01B2203/169 , C10G2300/1022 , C10G2300/4081 , C10G2400/06
摘要： The invention provides a process to prepare a Fischer-Tropsch synthesis product from a gaseous mixture of hydrocarbons comprising methane, ethane and optional higher carbon number hydrocarbons comprising the steps of: (a) pre-reforming the hydrocarbon mixture adiabatically, (b) heating the gaseous mixture obtained in step (a) to a temperature greater than 650° C., (c) performing a non-catalyzed partial oxidation by contacting the heated mixture of step (b) yielding a reactor effluent having a temperature of between 1100 and 1500 ° C., (d) performing a Fischer-Tropsch synthesis using the hydrogen- and carbon monoxide-containing gas as obtained in step (c) as feedstock and (e) wherein from the synthesis product obtained in step (d) a relatively light stream is separated and wherein a first part of the light stream is recycled to step (a) to be subjected to pre-reforming and wherein a second part of the light stream is recycled to the burner of step (c) to be subjected to partial oxidation and wherein the temperature in step (a) is controlled by the adjusting the amount of light stream that is recycled to step (a).
摘要翻译：本发明提供了一种从包含甲烷，乙烷和任选的较高碳数烃的烃的气体混合物制备费 - 托合成产物的方法，包括以下步骤：（a）绝热地预先重整烃混合物，（b）步骤（a）中获得的气态混合物至大于650℃的温度，（c）通过使加热的步骤（b）的混合物接触而进行非催化部分氧化，产生温度为1100至1500℃的反应器流出物 ℃，（d）使用步骤（c）中获得的含氢和一氧化碳的气体作为原料进行费 - 托合成，（e）其中从步骤（d）中获得的合成产物相对较轻流分离，并且其中轻流的第一部分被再循环到步骤（a）以进行预重整，并且其中轻流的第二部分被再循环到步骤（c）的燃烧器以进行部分氧化物离子，并且其中步骤（a）中的温度通过调节再循环到步骤（a）的轻质流量来控制。

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