公开(公告)号：US20120074042A1

公开(公告)日：2012-03-29

申请号：US12889715

申请日：2010-09-24

申请人： Shabbir Husain ,  Lin Li ,  Zhen Zhou ,  Alexander E. Kuperman ,  Zunqing He ,  Huping Luo

发明人： Shabbir Husain ,  Lin Li ,  Zhen Zhou ,  Alexander E. Kuperman ,  Zunqing He ,  Huping Luo

IPC分类号： C10G29/04

CPC分类号： C10G29/00 ,  C10G29/04 ,  C10G29/06 ,  C10G2300/1011 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/203 ,  C10G2300/4018 ,  Y02P30/20

摘要： Disclosed are embodiments relating to a process for reducing the total acid number of a hydrocarbon feed by contacting the feed with a metal titanate catalyst having an MTiO3 structure wherein M is a metal having a valence of 2+, resulting in a hydrocarbon product having a final total acid number lower than the initial total acid number of the feed. The process is useful for pretreating high acid crudes prior to further processing thus avoiding corrosion of equipment used in refining operations. The process can be integrated into conventional refining operations in order to treat various refinery streams. In one embodiment, a process is provided for refining a low acid crude oil and a high acid crude oil by separately introducing a relatively low acid crude oil feed and a relatively high acid crude oil feed to an atmospheric distillation column, wherein the relatively high acid crude oil feed is contacted with a metal titanate catalyst prior to introduction to the atmospheric distillation column.

摘要翻译： 公开了通过使进料与具有MTiO 3结构的金属钛酸酯催化剂接触来降低烃进料的总酸值的方法的实施方案，其中M是具有2+价数的金属，导致烃产物具有最终的 总酸值低于进料的初始总酸值。 该方法可用于在进一步加工之前预处理高酸性原油，从而避免在精炼操作中使用的设备的腐蚀。 该方法可以集成到常规的精炼操作中，以便处理各种炼油流。 在一个实施方案中，提供了通过将相对低的酸性原油进料和相对高的酸性原油进料单独引入常压蒸馏塔来提炼低酸原油和高酸性原油的方法，其中相对高的酸 原油进料在引入常压蒸馏塔之前与钛酸金属催化剂接触。

公开(公告)号：US08142527B2

公开(公告)日：2012-03-27

申请号：US11378322

申请日：2006-03-20

申请人： Mordechay Herskowitz ,  Miron Landau ,  Iehudit Reizner ,  Mark Kaliya

发明人： Mordechay Herskowitz ,  Miron Landau ,  Iehudit Reizner ,  Mark Kaliya

IPC分类号： C10G3/00 ,  C10L1/04

CPC分类号： C10G3/50 ,  C10G3/47 ,  C10G3/49 ,  C10G3/54 ,  C10G45/64 ,  C10G49/007 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/20 ,  C10G2300/202 ,  C10G2300/307 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/405 ,  C10G2300/4081 ,  C10G2300/42 ,  C10G2400/02 ,  C10G2400/04 ,  C10L1/026 ,  C10L1/04 ,  C10L1/08 ,  Y02P30/20

摘要： A process for producing a fuel composition from vegetable and/or animal oil comprises hydrodeoxygenating and hydroisomerizing the oil in a single step. The fuel composition has acceptable lubricity and comprises a mixture of C14 to C18 paraffins having a ratio of iso to normal paraffins of 2 to 8 and less than 5 ppm sulfur.

摘要翻译： 用于从植物油和/或动物油生产燃料组合物的方法包括在一个步骤中加氢脱氧和油加氢异构化。 燃料组合物具有可接受的润滑性，并且包含C14至C18烷烃的混合物，其具有2至8和小于5ppm硫的异链烷烃与正常链烷烃的比例。

公开(公告)号：US20120043257A1

公开(公告)日：2012-02-23

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

IPC分类号： C10G69/02

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。

公开(公告)号：US08119552B2

公开(公告)日：2012-02-21

申请号：US12091706

申请日：2006-10-26

申请人： Götz Burgfels ,  Stephan Wellach ,  Josef Schönlinner ,  Friedrich Schmidt ,  Volker Kurth ,  Vebjorn Knut Grande ,  Jorunn Steinsland Rosvoll ,  Per Aksel Skjølsvik

发明人： Götz Burgfels ,  Stephan Wellach ,  Josef Schönlinner ,  Friedrich Schmidt ,  Volker Kurth ,  Vebjorn Knut Grande ,  Jorunn Steinsland Rosvoll ,  Per Aksel Skjølsvik

IPC分类号： C10G47/00

CPC分类号： C10G47/20 ,  B01J29/166 ,  B01J29/78 ,  B01J29/80 ,  B01J37/0009 ,  B01J2229/20 ,  B01J2229/42 ,  C10G45/64 ,  C10G65/12 ,  C10G2300/1059 ,  C10G2300/1074 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/307 ,  C10G2300/308 ,  C10G2300/4018 ,  C10G2400/04

摘要： The present invention relates to a catalyst composition for the reaction of hydrocarbons comprising a zeolite with has a faujasite structure and a fibrous zeolite which comprises essentially non-crossing one-dimensional channels. Further, the catalyst composition comprises in a preferred embodiment a metal component selected from metals of the group VIB and VIII of the periodic table of elements and their compounds. The invention relates further to a process for the synthesis of such a catalyst composition and to a process for hydrocracking hydrocarbon feedstocks by using said catalyst composition.

摘要翻译： 本发明涉及包含具有八面沸石结构的沸石和包含基本上非交叉的一维通道的纤维状沸石的烃的反应用催化剂组合物。 此外，催化剂组合物在一个优选的实施方案中包括选自元素周期表第ⅥB族和第Ⅷ族金属及其化合物的金属组分。 本发明进一步涉及合成这种催化剂组合物的方法和通过使用所述催化剂组合物加氢裂解烃原料的方法。

公开(公告)号：US20120022224A1

公开(公告)日：2012-01-26

申请号：US13156824

申请日：2011-06-09

申请人： Geraldine Tosin ,  Marcel J. G. Janssen ,  Paul Hamilton ,  Georges M.K. Mathys

发明人： Geraldine Tosin ,  Marcel J. G. Janssen ,  Paul Hamilton ,  Georges M.K. Mathys

IPC分类号： C08F4/58 ,  B01J29/40 ,  C08F2/00

CPC分类号： C07C2/12 ,  B01J29/06 ,  B01J29/7026 ,  B01J35/023 ,  B01J35/026 ,  B01J35/08 ,  B01J37/0009 ,  B01J37/0063 ,  B01J2229/42 ,  C07C11/02 ,  C07C2529/40 ,  C07C2529/70 ,  C10G50/00 ,  C10G2300/1081 ,  C10G2300/1088 ,  C10G2300/1092 ,  C10G2300/4018 ,  C10G2400/22

摘要： Embodiments of an invention disclosed herein relate to particles made from zeolite catalysts and their use in oligomerization processes. In particular, shaped particles (for example, spheroid particles) are made from compositions including the contact product of at least one zeolite catalyst and at least one binder.

摘要翻译： 本文公开的发明的实施方案涉及由沸石催化剂制备的颗粒及其在低聚方法中的用途。 特别地，成形颗粒（例如，球状颗粒）由包括至少一种沸石催化剂和至少一种粘合剂的接触产物的组合物制成。

公开(公告)号：US20120000817A1

公开(公告)日：2012-01-05

申请号：US13169170

申请日：2011-06-27

申请人： Stuart S. Shih

发明人： Stuart S. Shih

IPC分类号： C10G49/00

CPC分类号： C10G65/04 ,  C10G45/10 ,  C10G45/12 ,  C10G2300/1048 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/4006 ,  C10G2300/4018 ,  C10G2400/04 ,  C10G2400/08

摘要： In a process for producing a low color diesel and/or kerosene fuel, a middle distillate feed can be supplied to a reactor having at least one first catalyst bed containing a first desulfurization and/or isomerization catalyst and at least one second catalyst bed containing a decolorization catalyst downstream from the first catalyst bed(s). The feed can be reacted with the hydrogen in the presence of the first catalyst at a temperature from about 290° C. to about 430° C. to produce a first liquid effluent, which can be cooled by about 10° C. to about 40° C. with a quench medium and cascaded to the at least one second catalyst bed. The cooled first liquid effluent can then be reacted with hydrogen in the presence of the decolorization catalyst at a temperature from about 280° C. to about 415° C. to produce a second effluent having an ASTM color less than 2.5.

摘要翻译： 在生产低色柴油和/或煤油燃料的方法中，中间馏分料可以供给至具有至少一个含有第一脱硫和/或异构化催化剂的第一催化剂床和至少一个含有 脱色催化剂从第一催化剂床下游。 在约290℃至约430℃的温度下，进料可以在第一催化剂存在下与氢反应，以产生第一液体流出物，其可被冷却约10℃至约40℃ ℃，并与骤冷介质并级联至至少一个第二催化剂床。 然后在约280℃至约415℃的温度下，将冷却的第一液体流出物在脱色催化剂存在下与氢气反应，以产生ASTM颜色小于2.5的第二流出物。

公开(公告)号：US08066867B2

公开(公告)日：2011-11-29

申请号：US12268048

申请日：2008-11-10

申请人： Bart Dziabala ,  Vasant P. Thakkar ,  Suheil F. Abdo

发明人： Bart Dziabala ,  Vasant P. Thakkar ,  Suheil F. Abdo

IPC分类号： C10G45/00 ,  C10G45/021

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。

公开(公告)号：US20110230688A1

公开(公告)日：2011-09-22

申请号：US13050136

申请日：2011-03-17

申请人： Nadege CHARON ,  Hugues Dulot ,  Alain Quignard ,  Wilfried Weiss

发明人： Nadege CHARON ,  Hugues Dulot ,  Alain Quignard ,  Wilfried Weiss

IPC分类号： C10G1/00 ,  C10G1/06 ,  C10L1/04 ,  C10G1/10

CPC分类号： C10G1/002 ,  C10G1/042 ,  C10G1/065 ,  C10G2300/1003 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/307 ,  C10G2300/308 ,  C10G2300/4018 ,  C10G2300/44 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/08 ,  Y02E50/32 ,  Y02P30/20

摘要： A process for the conversion of coal into fuel bases comprises two successive direct liquefaction stages in ebullated bed reactors followed by a fixed bed hydrocracking stage. This process can produce excellent quality fuel bases (kerosene and diesel).

摘要翻译： 将煤转化为燃料基的方法包括在沸腾床反应器中的两个连续的直接液化阶段，随后是固定床加氢裂化阶段。 这个过程可以生产优质的燃料基（煤油和柴油）。

公开(公告)号：US20110219672A1

公开(公告)日：2011-09-15

申请号：US13127875

申请日：2008-11-06

申请人： William J. Novak ,  Zhiguo Hou ,  William J. Tracy, III ,  Patrick L. Hanks ,  Timothy L. Hilbert

发明人： William J. Novak ,  Zhiguo Hou ,  William J. Tracy, III ,  Patrick L. Hanks ,  Timothy L. Hilbert

IPC分类号： C10L1/02

CPC分类号： C10L1/08 ,  C10G45/64 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/307 ,  C10G2300/4018 ,  C10G2400/04 ,  C10L1/026 ,  C10L2200/0469 ,  C10L2270/026 ,  C10L2290/06 ,  C10L2290/54 ,  Y02E50/13 ,  Y02P30/20

摘要： A method for producing diesel fuel from biocomponent feeds includes hydrotreating the feed followed by catalytic dewaxing with a ZSM-48 containing catalyst. The hydrotreated feed may be cascaded directly to the dewaxing step, or the hydrotreated feed can undergo intermediate separation. The diesel fuel resulting from processing of the biocomponent feed exhibits superior cetane values.

摘要翻译： 从生物组分进料生产柴油燃料的方法包括用含ZSM-48的催化剂加氢处理进料，然后进行催化脱蜡。 加氢处理的进料可以直接级联到脱蜡步骤，或加氢处理的进料可以进行中间分离。 由生物组分进料加工产生的柴油表现出优异的十六烷值。

公开(公告)号：US20110192765A1

公开(公告)日：2011-08-11

申请号：US13057781

申请日：2009-07-29

申请人： Emmanuelle Guillon ,  Laurent Simon

发明人： Emmanuelle Guillon ,  Laurent Simon

IPC分类号： C10G47/02 ,  B01J29/076 ,  B01J29/072 ,  C10G49/08 ,  C07C4/02 ,  C10G45/00 ,  C10G65/00 ,  C07C7/00

CPC分类号： B01J29/76 ,  B01J21/04 ,  B01J21/12 ,  B01J29/78 ,  B01J37/0009 ,  B01J37/20 ,  B01J2229/20 ,  B01J2229/42 ,  C01B39/48 ,  C10G47/16 ,  C10G47/20 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/4018

摘要： The present invention relates to a catalyst comprising at least one IZM-2 zeolite, at least one amorphous matrix, at least one hydro-dehydrogenating element selected from the group formed by the elements from group VIB and from group VIII of the periodic table and excluding platinum and palladium. The catalyst also optionally contains a controlled quantity of at least one doping element selected from phosphorus, boron and silicon, optionally at least one element from group VB of the periodic table of the elements, and optionally a group VIIA element. The invention also relates to hydrocracking and hydrotreatment processes implementing this catalyst.

摘要翻译： 本发明涉及包含至少一种IZM-2沸石，至少一种无定形基质，至少一种加氢脱氢元素的催化剂，所述至少一种加氢脱氢元件选自由元素周期表中VIB族和VIII族元素形成的基团，不包括 铂和钯。 催化剂还任选地含有受控量的至少一种选自磷，硼和硅的掺杂元素，任选地包含元素周期表第VB族中的至少一种元素，以及任选的第VIIA族元素。 本发明还涉及实施该催化剂的加氢裂化和加氢处理方法。