公开(公告)号：US11760947B2

公开(公告)日：2023-09-19

申请号：US17812803

申请日：2022-07-15

Applicant: LUMMUS TECHNOLOGY LLC ,  Saudi Aramco Technologies Company ,  Chevron Lummus Global LLC

Inventor： Kareemuddin Shaik ,  Ujjal Mukherjee ,  Essam Abdullah Al-Sayed ,  Pedro Santos ,  Theodorus Maesen ,  Mazin Tamimi ,  Julie Chabot ,  Ibrahim Abba ,  Kandasamy Sundaram ,  Sami Barnawi ,  Ronald M. Venner

IPC: C10G69/06 ,  C10G45/26 ,  C10G45/24 ,  C10G45/32 ,  B01J19/24 ,  C10L1/08 ,  C10G45/44 ,  C10G49/22 ,  C10G65/12 ,  C10G9/36 ,  C10G47/30 ,  C10G49/02 ,  C10G21/00 ,  C10G47/26 ,  C10G55/04 ,  B01D3/06 ,  B01D19/00

CPC classification number: C10G69/06 ,  B01J19/245 ,  C10G9/36 ,  C10G21/003 ,  C10G45/26 ,  C10G45/32 ,  C10G45/44 ,  C10G47/26 ,  C10G47/30 ,  C10G49/02 ,  C10G49/22 ,  C10G55/04 ,  C10G65/12 ,  C10L1/08 ,  B01D3/06 ,  B01D19/0057 ,  B01J2219/0004 ,  C10G2300/1044 ,  C10G2300/1048 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/308 ,  C10G2300/40 ,  C10G2300/4006 ,  C10G2300/4081 ,  C10G2300/807 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30

Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.

公开(公告)号：US20170348676A1

公开(公告)日：2017-12-07

申请号：US15536382

申请日：2015-12-18

Applicant: JOHNSON MATTHEY PUBLIC LIMITED COMPANY

Inventor： Duncan Roy COUPLAND ,  Jonathan PHILLIPS ,  Sophie WINFIELD

IPC: B01J23/83 ,  B01J37/02 ,  B01J35/10 ,  B01J35/00 ,  B01J23/40 ,  B01J29/06 ,  B01J23/74 ,  B01J23/72 ,  B01J37/04 ,  B01J35/04

CPC classification number: B01J23/83 ,  B01J23/40 ,  B01J23/72 ,  B01J23/74 ,  B01J23/76 ,  B01J23/89 ,  B01J29/06 ,  B01J35/002 ,  B01J35/0026 ,  B01J35/04 ,  B01J35/1038 ,  B01J35/1042 ,  B01J37/0018 ,  B01J37/0215 ,  B01J37/0219 ,  B01J37/0246 ,  B01J37/04 ,  B01J37/08 ,  C04B35/111 ,  C04B35/18 ,  C04B35/195 ,  C04B35/634 ,  C04B35/636 ,  C04B38/0096 ,  C04B2111/0081 ,  C04B2235/3206 ,  C04B2235/3208 ,  C04B2235/3232 ,  C04B2235/3281 ,  C04B2235/5212 ,  C04B2235/5409 ,  C04B2235/5436 ,  C04B2235/6026 ,  C04B2235/6567 ,  C04B2235/77 ,  C04B2235/96 ,  C10G49/02 ,  C10G70/042 ,  C10G2300/70 ,  C04B35/00 ,  C04B38/0006

Abstract: A method for producing a catalyst or catalyst precursor is described including: applying a slurry of a particulate catalyst compound in a carrier fluid to an additive layer manufactured support structure to form a slurry-impregnated support, and drying and optionally calcining the slurry-impregnated support to form a catalyst or catalyst precursor. The mean particle size (D50) of the particulate catalyst compound in the slurry is in the range 1-50 μm and the support structure has a porosity ≧0.02 ml/g.

公开(公告)号：US20170327754A1

公开(公告)日：2017-11-16

申请号：US15588024

申请日：2017-05-05

Applicant: Saudi Arabian Oil Company

Inventor： Lianhui Ding ,  Essam Al-Sayed ,  Duhaiman U. Al-Yami ,  Abdennour Bourane ,  Alberto Lozano Ballesteros ,  Ibrahim Abba

IPC: C10G69/06

CPC classification number: C10G69/06 ,  C07C4/04 ,  C10G9/36 ,  C10G49/02 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/308 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30

Abstract: Embodiments for an integrated hydrotreating and steam pyrolysis process for the processing of crude oil comprising recycling the higher boiling point fraction of the upgraded crude oil to increase the yield of petrochemicals such as olefins and aromatics.

公开(公告)号：US09663728B2

公开(公告)日：2017-05-30

申请号：US14525477

申请日：2014-10-28

Applicant: Pallassana S. Venkataraman ,  Gordon F. Stuntz ,  Jonathan Martin McConnachie ,  Faiz Pourarian

Inventor： Pallassana S. Venkataraman ,  Gordon F. Stuntz ,  Jonathan Martin McConnachie ,  Faiz Pourarian

IPC: B01J21/06 ,  B01J21/08 ,  B01J29/076 ,  C10G45/00 ,  C10G45/22 ,  C10L1/00 ,  C10G49/04 ,  B01J31/12 ,  C10G45/60 ,  C10G47/02 ,  C10G1/00 ,  C10G45/04 ,  C10G45/06 ,  C10G49/02

CPC classification number: C10G49/04 ,  B01J31/121 ,  B01J2231/64 ,  B01J2531/0222 ,  B01J2531/42 ,  B01J2531/48 ,  B01J2531/52 ,  B01J2531/56 ,  C10G1/002 ,  C10G45/04 ,  C10G45/06 ,  C10G45/60 ,  C10G47/02 ,  C10G49/02 ,  C10G2300/1011 ,  Y02E50/13 ,  Y02P30/20

Abstract: The present invention relates to the processing of hydrocarbon-containing feedstreams in the presence of an interstitial metal hydride comprised of at least one chemical element selected from Groups 3-11 (including the lanthanides, atomic numbers 58 to 71), and at least one chemical element selected from Groups 13-15 from the IUPAC Periodic Table of Elements. These interstitial metal hydrides, their catalysts and processes using these interstitial metal hydrides and catalysts of the present invention improve overall hydrogenation, product conversion, as well as sulfur reduction in hydrocarbon feedstreams.

公开(公告)号：US09534177B2

公开(公告)日：2017-01-03

申请号：US13172149

申请日：2011-06-29

Applicant: Scott Michael Babitz

Inventor： Scott Michael Babitz

IPC: B01J29/06 ,  B01J37/00 ,  C10G2/00 ,  B01D53/94 ,  B01J29/08 ,  C01B3/02 ,  C10G1/08 ,  C10G11/05 ,  C10G29/20 ,  C10G35/06 ,  C10G49/02 ,  B01J35/00

CPC classification number: C10G2/33 ,  B01D53/94 ,  B01J29/06 ,  B01J29/084 ,  B01J35/002 ,  B01J37/0045 ,  B01J2229/42 ,  C01B3/02 ,  C01B2203/1041 ,  C10G1/086 ,  C10G11/05 ,  C10G29/205 ,  C10G35/06 ,  C10G49/02

Abstract: Process for the preparation of a catalyst comprising the steps of (a) preparing a slurry comprising clay, zeolite, and quasi-crystalline boehmite, provided that the slurry does not comprise peptized quasi-crystalline boehmite, (b) adding a monovalent acid to the slurry, (c) adding a silicon source to the slurry, and (d) shaping the slurry to form particles. This process leads to a catalyst with high accessibility and high attrition resistance.

Abstract translation: 制备催化剂的方法包括以下步骤：（a）制备包含粘土，沸石和准结晶勃姆石的浆料，条件是浆料不包含胶溶的准晶勃姆石，（b）向 浆料，（c）向浆料中加入硅源，和（d）使浆料成形以形成颗粒。 该方法导致具有高可接近性和高抗磨性的催化剂。

公开(公告)号：US09347006B2

公开(公告)日：2016-05-24

申请号：US14149274

申请日：2014-01-07

Applicant: SAUDI ARABIAN OIL COMPANY ,  JGC CATALYSTS AND CHEMICALS LTD. ,  JAPAN COOPERATION CENTER, PETROLEUM

Inventor： Omer Refa Koseoglu ,  Adnan Al-Hajji ,  Hendrik Muller ,  Masaru Ushio ,  Koji Nakano

IPC: C10G47/12 ,  C10G47/14 ,  C10G47/16 ,  C10G47/18 ,  C10G47/20 ,  C10G65/02 ,  C10G65/12 ,  C10G45/04 ,  C10G45/06 ,  C10G45/10 ,  C10G45/12 ,  C10G45/32 ,  C10G45/44 ,  C10G47/02 ,  C10G49/00 ,  C10G49/02 ,  C10G49/04 ,  C10G49/06 ,  C10G49/08 ,  B01J35/00 ,  B01J23/882 ,  B01J23/883 ,  B01J29/08 ,  B01J29/16

CPC classification number: C10G65/12 ,  B01J23/882 ,  B01J23/883 ,  B01J29/084 ,  B01J29/166 ,  B01J35/0006 ,  C10G45/04 ,  C10G45/06 ,  C10G45/10 ,  C10G45/12 ,  C10G45/32 ,  C10G45/44 ,  C10G47/02 ,  C10G49/002 ,  C10G49/02 ,  C10G49/04 ,  C10G49/06 ,  C10G49/08 ,  C10G2300/1074 ,  C10G2300/202

Abstract: The invention relates to a method for optimizing layered catalytic processes. This is accomplished by testing various catalysts with a compound found in a feedstock to be tested, to determine the facility of the catalyst in hydrogenating, hydrosulfurizing, or hydrodenitrogenating the molecule, and hence the feedstock. In a preferred embodiment, the Double Bond Equivalence of the feedstock and molecule are determined, and catalysts are pre-selected based upon their known ability to work with materials of this DBE value.

Abstract translation: 本发明涉及一种用于优化分层催化过程的方法。 这是通过用待测试的原料中发现的化合物测试各种催化剂来实现的，以确定催化剂在分子氢化，加氢硫化或加氢脱氮中的设备，从而确定催化剂的原料。 在优选的实施方案中，确定原料和分子的双键等价性，并且基于其已知的与该DBE值的材料一起使用的能力预先选择催化剂。

公开(公告)号：US09206363B2

公开(公告)日：2015-12-08

申请号：US13597598

申请日：2012-08-29

Applicant: Hyung Suk Woo ,  Jane Chi-ya Cheng ,  Teh C. Ho ,  Stephen Harold Brown ,  Richard Charles Dougherty ,  David Thomas Ferrughelli ,  Federico Barrai

Inventor： Hyung Suk Woo ,  Jane Chi-ya Cheng ,  Teh C. Ho ,  Stephen Harold Brown ,  Richard Charles Dougherty ,  David Thomas Ferrughelli ,  Federico Barrai

IPC: C10G47/00 ,  C10G53/02 ,  C10G53/04 ,  C10G65/12 ,  C10G47/02 ,  C10G45/04 ,  C10G49/02 ,  C10G49/22 ,  C10G67/04 ,  B01J37/20 ,  B01J23/74 ,  B01J35/02 ,  B01J37/02 ,  B01J23/883 ,  B01J23/888 ,  B01J35/10

CPC classification number: C10G45/00 ,  B01J23/74 ,  B01J23/883 ,  B01J23/8885 ,  B01J35/023 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1061 ,  B01J37/0201 ,  B01J37/0207 ,  B01J37/20 ,  C10G45/02 ,  C10G45/04 ,  C10G45/32 ,  C10G45/44 ,  C10G45/58 ,  C10G47/00 ,  C10G47/02 ,  C10G49/02 ,  C10G49/22 ,  C10G67/0454 ,  C10G67/049 ,  C10G2300/1037 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4081 ,  C10G2300/44 ,  C10L1/04

Abstract: Heavy oil feeds are hydroprocessed in the presence of a solvent under conditions that provide a variety of benefits. The solvent can be an added solvent or a portion of the liquid effluent from hydroprocessing. The processes allow for lower pressure processing of heavy oil feeds for extended processing times or extended catalyst lifetimes be reducing or mitigating the amount of coke formation on the hydroprocessing catalyst.

Abstract translation: 在提供各种益处的条件下，在溶剂存在下将重油进料加氢处理。 溶剂可以是加氢处理的添加溶剂或一部分液体流出物。 该方法允许重油进料的较低压力处理用于延长的处理时间或延长的催化剂寿命来减少或减轻加氢处理催化剂上焦炭形成的量。

公开(公告)号：US20150045600A1

公开(公告)日：2015-02-12

申请号：US14525477

申请日：2014-10-28

Applicant: Pallassana S. Venkataraman ,  Gordon F. Stuntz ,  Jonathan Martin McConnachie ,  Faiz Pourarian

Inventor： Pallassana S. Venkataraman ,  Gordon F. Stuntz ,  Jonathan Martin McConnachie ,  Faiz Pourarian

IPC: C10G49/04 ,  C10G1/00 ,  C10G47/02 ,  C10G49/02 ,  C10G45/04 ,  C10G45/06

CPC classification number: C10G49/04 ,  B01J31/121 ,  B01J2231/64 ,  B01J2531/0222 ,  B01J2531/42 ,  B01J2531/48 ,  B01J2531/52 ,  B01J2531/56 ,  C10G1/002 ,  C10G45/04 ,  C10G45/06 ,  C10G45/60 ,  C10G47/02 ,  C10G49/02 ,  C10G2300/1011 ,  Y02E50/13 ,  Y02P30/20

Abstract: The present invention relates to the processing of hydrocarbon-containing feedstreams in the presence of an interstitial metal hydride comprised of at least one chemical element selected from Groups 3-11 (including the lanthanides, atomic numbers 58 to 71), and at least one chemical element selected from Groups 13-15 from the IUPAC Periodic Table of Elements. These interstitial metal hydrides, their catalysts and processes using these interstitial metal hydrides and catalysts of the present invention improve overall hydrogenation, product conversion, as well as sulfur reduction in hydrocarbon feedstreams.

Abstract translation: 本发明涉及在由选自组3-11（包括镧系元素，原子序数58至71）的至少一种化学元素组成的间隙金属氢化物存在下的含烃原料流的处理，以及至少一种化学 元素选自IUPAC元素周期表第13-15组元素。 这些间隙金属氢化物，它们的催化剂和使用这些间隙金属氢化物的方法和本发明的催化剂改进了烃进料流中的总体氢化，产物转化以及硫的还原。

公开(公告)号：US20140322087A1

公开(公告)日：2014-10-30

申请号：US14329592

申请日：2014-07-11

Applicant: PHILLIPS 66 COMPANY

Inventor： Jianhua YAO ,  Edward L. SUGHRUE, II ,  Ronald E. BROWN

IPC: B01J19/26

CPC classification number: B01J19/26 ,  C10G3/46 ,  C10G3/50 ,  C10G49/02 ,  C10G2300/1011 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  Y02E50/13 ,  Y02P30/20

Abstract: A method of hydrotreating liquefied biomass feedstock with diesel feedstock to produce alkanes is demonstrated that prevents damage to the reactor catalyst, reduces coke production, and converts nearly all of the polyols to alkanes. In order to mitigate the potential coking issue and to moderate the temperature of the catalyst bed while maintaining high conversion for sugar alcohol to hydrocarbon via a hydrotreating process, a diesel feedstock is fed over the reactor catalyst with multiple injections of polyol feedstock along the reactor.

Abstract translation: 证明了用柴油原料加氢处理液化生物质原料以生产烷烃的方法，其防止对反应器催化剂的损害，减少焦炭产生，并将几乎所有多元醇转化为烷烃。 为了减轻潜在的焦化问题并缓解催化剂床的温度，同时通过加氢处理方法保持糖醇与烃的高转化率，将柴油原料在反应器催化剂上沿反应器多次注入多元醇原料。

公开(公告)号：US20140171299A1

公开(公告)日：2014-06-19

申请号：US13715943

申请日：2012-12-14

Applicant: Julie Chabot ,  Bo Kou ,  Alexander Kuperman

Inventor： Julie Chabot ,  Bo Kou ,  Alexander Kuperman

IPC: B01J23/78 ,  B01J23/75 ,  B01J23/755 ,  B01J23/28 ,  B01J23/30

CPC classification number: B01J23/78 ,  B01J21/02 ,  B01J21/06 ,  B01J21/10 ,  B01J21/12 ,  B01J23/28 ,  B01J23/30 ,  B01J23/75 ,  B01J23/755 ,  B01J23/85 ,  B01J31/0205 ,  B01J31/0247 ,  B01J35/0006 ,  B01J35/023 ,  B01J37/0036 ,  B01J37/04 ,  C10G47/26 ,  C10G49/02 ,  C10G49/12

Abstract: A hydroprocessing co-catalyst composition may comprise in an embodiment a first component comprising co-catalyst particles and a liquid carrier, and a second component comprising a dispersant and a dispersant diluent. The co-catalyst particles may be in the micron size range, and the dispersant may promote dispersion of the co-catalyst particles in materials such as the liquid carrier, the dispersant diluent, and combinations thereof. Methods of introducing a hydroprocessing co-catalyst composition into a hydroprocessing system are also disclosed.

Abstract translation: 加氢处理助催化剂组合物可以在一个实施方案中包括包含助催化剂颗粒和液体载体的第一组分，和包含分散剂和分散剂稀释剂的第二组分。 助催化剂颗粒可以在微米尺寸范围内，并且分散剂可以促进助催化剂颗粒在诸如液体载体，分散剂稀释剂及其组合的材料中的分散。 还公开了将加氢助催化剂组合物引入加氢处理系统的方法。