公开(公告)号：US20190071609A1

公开(公告)日：2019-03-07

申请号：US16156393

申请日：2018-10-10

Applicant: Saudi Arabian Oil Company

Inventor： Omer Refa KOSEOGLU

IPC: C10G25/00 ,  C10G67/16 ,  C10G67/06 ,  C10G65/16 ,  C10G65/04 ,  C10G65/00 ,  C10G45/58 ,  C10G67/00

CPC classification number: C10G25/00 ,  C10G45/58 ,  C10G65/00 ,  C10G65/043 ,  C10G65/16 ,  C10G67/00 ,  C10G67/06 ,  C10G67/16 ,  C10G2300/1059 ,  C10G2300/202 ,  C10G2300/301

Abstract: Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by with an apparatus arranged for flashing the feed at a target cut point temperature to obtain two fractions. A low boiling temperature fraction contains refractory, sterically hindered sulfur-containing compounds, which have a boiling point at or above the target cut point temperature. A high boiling temperature fraction, having a boiling point below the target cut point temperature, is substantially free of refractory sulfur-containing compounds. The high boiling temperature fraction is contacted with isomerization catalyst, and the isomerized effluent and the low boiling temperature fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level.

公开(公告)号：US09969945B2

公开(公告)日：2018-05-15

申请号：US14799801

申请日：2015-07-15

Applicant: INSTITUTO MEXICANO DEL PETROLEO

Inventor： Jorge Ancheyta Juarez ,  Luis Carlos Castaneda Lopez ,  Jose Antonio D. Munoz Moya ,  Guillermo Centeno Nolasco ,  Gustavo Jesus Marroquin Sanchez ,  Sergio Ramirez Amador ,  Fernando Alonso Martinez

IPC: C10G67/00 ,  C10G65/00 ,  C10G45/04 ,  C10G45/06 ,  C10G45/08 ,  C10G45/10 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G47/04 ,  C10G47/06 ,  C10G5/06 ,  C10G7/02

CPC classification number: C10G67/00 ,  C10G5/06 ,  C10G7/02 ,  C10G45/04 ,  C10G45/06 ,  C10G45/08 ,  C10G45/10 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G47/04 ,  C10G47/06 ,  C10G65/00 ,  C10G2300/1033 ,  C10G2300/202 ,  C10G2300/302

Abstract: The present invention relates to a process for the partial upgrading of properties of heavy and/or extra-heavy crude oil by low severity catalytic hydrotreatment in only one reaction step. The process of the present invention is obtained upgraded oil with properties required for its transportation from offshore platforms either to maritime terminal or to refining centers. The process reduces the viscosity of heavy and/or extra-heavy crude oil, and decreases the concentration of impurities, such as sulfur, nitrogen, and metals, in such a way that heavy and/or extra-heavy crude oils can be transported to maritime terminals or to refining centers. The process increases the lifetime of the catalyst and decreased operating costs by reducing consumption of utilities because the operation of the process is carried out at lower severity. The partially upgraded oils obtained in this process can be transported directly to the maritime terminals or to existing refineries.

公开(公告)号：US09909074B2

公开(公告)日：2018-03-06

申请号：US14679495

申请日：2015-04-06

Applicant: Saudi Arabian Oil Company

Inventor： Omer Refa Koseoglu ,  Abdennour Bourane

IPC: C10G27/00 ,  C10G27/04 ,  C10G27/10 ,  C10G45/02 ,  C10G67/00 ,  C10G67/16 ,  C10G27/12 ,  C10G53/04 ,  C10G53/14 ,  C10G67/04 ,  B01J19/24 ,  C10G67/12

CPC classification number: C10G27/12 ,  B01J19/2445 ,  B01J19/245 ,  B01J2219/24 ,  C10G27/04 ,  C10G53/04 ,  C10G53/14 ,  C10G67/00 ,  C10G67/0418 ,  C10G67/12 ,  C10G67/16 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/4037

Abstract: An oxidative treatment process, e.g., oxidative desulfurization or denitrification, is provided in which the oxidant is produced in-situ using an aromatic-rich portion of the original liquid hydrocarbon feedstock. The process reduces or replaces the need for the separate introduction of liquid oxidants such as hydrogen peroxide, organic peroxide and organic hydroperoxide in an oxidative treatment process.

公开(公告)号：US20170145323A1

公开(公告)日：2017-05-25

申请号：US15402774

申请日：2017-01-10

Applicant: Saudi Arabian Oil Company

Inventor： Omer Refa KOSEOGLU

IPC: C10G69/02 ,  B01J19/24

CPC classification number: C10G69/02 ,  B01J19/245 ,  B01J2219/24 ,  C10G25/00 ,  C10G45/58 ,  C10G65/00 ,  C10G65/043 ,  C10G65/16 ,  C10G67/00 ,  C10G67/06 ,  C10G67/16 ,  C10G2300/1059 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/44

Abstract: Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by first subjecting the entire feed to an extraction zone to separate an aromatic-rich fraction containing a substantial amount of the aromatic refractory and sterically hindered sulfur-containing compounds and an aromatic-lean fraction containing a substantial amount of the labile sulfur-containing compounds. The aromatic-rich fraction is contacted with isomerization catalyst, and the isomerized aromatic-rich fraction and the aromatic-lean fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level.

公开(公告)号：US09441174B2

公开(公告)日：2016-09-13

申请号：US13491147

申请日：2012-06-07

Applicant: Mario C. Baldassari ,  Ujjal K. Mukherjee ,  Avinash Gupta

Inventor： Mario C. Baldassari ,  Ujjal K. Mukherjee ,  Avinash Gupta

IPC: C10G67/04 ,  C10G65/14 ,  C10G21/00 ,  C10G47/00 ,  C10G49/22

CPC classification number: C10G67/049 ,  C10G21/003 ,  C10G47/00 ,  C10G67/00 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/42

Abstract: Processes for upgrading resid hydrocarbon feeds are disclosed. The upgrading processes may include: hydrocracking a resid in a first reaction stage to form a first stage effluent; hydrocracking a deasphalted oil fraction in a second reaction stage to form a second stage effluent; fractionating the first stage effluent and the second stage effluent to recover at least one distillate hydrocarbon fraction and a resid hydrocarbon fraction; feeding the resid hydrocarbon fraction to a solvent deasphalting unit to provide an asphaltene fraction and the deasphalted oil fraction.

Abstract translation: 公开了用于升级残油烃进料的方法。 升级过程可以包括：在第一反应阶段加氢裂化残渣以形成第一级流出物; 在第二反应阶段加氢裂解脱沥青油馏分以形成第二阶段流出物; 分馏第一级流出物和第二级流出物以回收至少一种馏出物烃馏分和残留烃馏分; 将残余烃馏分进料到溶剂脱沥青单元以提供沥青质馏分和脱沥青油馏分。

公开(公告)号：US20160177202A1

公开(公告)日：2016-06-23

申请号：US14974313

申请日：2015-12-18

Applicant: AXENS

Inventor： Frederic MOREL ,  Jacinthe FECON

IPC: C10G67/04

CPC classification number: C10G67/049 ,  C10G65/10 ,  C10G65/12 ,  C10G67/00

Abstract: The invention concerns a process for the intense conversion of a heavy hydrocarbon feed, comprising the following steps: a) a first step for ebullated bed hydroconversion; b) a step for separating at least a portion of the hydroconverted liquid effluent obtained from step a); c) a step for hydrocracking at least a portion of the vacuum gas oil fraction obtained from step b); d) a step for fractionating at least a portion of the effluent obtained from step c); e) a step for recycling at least a portion of the unconverted vacuum gas oil fraction obtained from step d) to said first hydroconversion step a).

Abstract translation: 本发明涉及重质烃进料的强力转化的方法，包括以下步骤：a）用于沸腾床加氢转化的第一步骤; b）分离从步骤a）获得的至少一部分加氢转化的液体流出物的步骤; c）加氢裂化从步骤b）获得的至少一部分真空瓦斯油馏分的步骤; d）分离从步骤c）得到的至少一部分流出物的步骤; e）将从步骤d）获得的未转化的减压瓦斯油馏分的至少一部分再循环到所述第一加氢转化步骤a）的步骤。

公开(公告)号：US20160145509A1

公开(公告)日：2016-05-26

申请号：US14550384

申请日：2014-11-21

Applicant: Lummus Technology Inc.

Inventor： Ujjal K. Mukherjee ,  Mario C. Baldassari ,  Marvin I. Greene

IPC: C10G67/00 ,  B01J8/18 ,  C10J3/00

CPC classification number: C10G67/049 ,  C10G7/06 ,  C10G21/003 ,  C10G47/00 ,  C10G65/14 ,  C10G67/00 ,  C10G67/0454 ,  C10G2300/1077 ,  C10G2300/206 ,  C10J3/00 ,  C10J2200/00

Abstract: Processes for upgrading partially converted vacuum residua hydrocarbon feeds are disclosed. The upgrading processes may include: steam stripping the partially converted vacuum residua to generate a first distillate and a first residuum; solvent deasphalting the first residuum stream to generate a deasphalted oil and an asphaltenes fraction; vacuum fractionating the deasphalted oil to recover a deasphalted gas oil distillate and a heavy deasphalted residuum; contacting the first distillate and the deasphalted gas oil distillate and hydrogen in the presence of a first hydroconversion catalyst to produce a product; contacting the heavy deasphalted residuum stream and hydrogen in the presence of a second hydroconversion catalyst to produce an effluent; and fractionating the effluent to recover a hydrocracked atmospheric residua and a hydrocracked atmospheric distillate

Abstract translation: 公开了用于升级部分转化的真空残余烃进料的方法。 升级过程可以包括：蒸汽汽提部分转化的真空残渣以产生第一馏出物和第一残渣; 溶剂脱沥青第一残渣流以产生脱沥青油和沥青质馏分; 真空分馏脱沥青油，以回收脱沥青瓦斯油馏出物和重质脱沥青渣; 在第一加氢转化催化剂的存在下使第一馏出物和脱沥青瓦斯油馏出物和氢接触以产生产物; 在第二加氢转化催化剂的存在下使沉重的脱沥青残渣物流和氢气接触以产生流出物; 并将流出物分馏以回收加氢裂化的大气残留物和加氢裂化的大气馏出物

公开(公告)号：US20150045598A1

公开(公告)日：2015-02-12

申请号：US14260812

申请日：2014-04-24

Applicant: UOP LLC

Inventor： Gregory A. Funk ,  Steven T. Arakawa ,  Matthew Lippmann ,  Mary Jo Wier

IPC: C10G51/06 ,  C10G63/08 ,  C10G69/14

CPC classification number: C10G51/06 ,  C10G9/36 ,  C10G55/04 ,  C10G55/08 ,  C10G61/04 ,  C10G61/06 ,  C10G61/10 ,  C10G63/08 ,  C10G67/00 ,  C10G67/06 ,  C10G67/16 ,  C10G69/00 ,  C10G69/06 ,  C10G69/10 ,  C10G69/14 ,  C10G2400/02 ,  C10G2400/20

Abstract: A process for increasing the yields of light olefins or shifting to increase the hydrocarbon components to gasoline blending pools from a hydrocarbon feedstock is presented. The process includes separating a naphtha feedstock to components to a first stream that are more readily processed in a cracking unit and to components in a second stream that are more readily processed in a reforming unit. The process includes the ability to convert components from the cracking stream to the reforming stream, and to convert components from the reforming stream to the cracking stream.

Abstract translation: 提出了一种用于提高轻质烯烃的产率或转移以从烃原料将烃组分增加到汽油混合池的方法。 该方法包括将石脑油原料与组分分离成在裂解装置中更容易加工的第一流和在重整单元中更容易加工的第二流中的组分。 该方法包括将组分从裂化流转化为重整流并将组分从重整流转化为裂化流的能力。

公开(公告)号：US08940154B2

公开(公告)日：2015-01-27

申请号：US12682031

申请日：2008-11-06

Applicant: Ranfeng Ding

Inventor： Ranfeng Ding

IPC: C10G45/44 ,  C10G21/00 ,  C10G45/38 ,  C10G45/50 ,  C10G65/16 ,  C10G67/00 ,  C10G67/04 ,  C10L1/06

CPC classification number: C10G21/00 ,  C10G45/38 ,  C10G45/50 ,  C10G65/16 ,  C10G67/00 ,  C10G67/04 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/301 ,  C10G2400/02 ,  C10L1/06

Abstract: A system and process for the preparation of high quality gasoline through recombination of catalytic hydrocarbon includes fractionator and extractor. The upper part of the fractionator is equipped with light petrol pipeline, the lower part of the fractionator is equipped with heavy petrol pipeline, the middle part of the fractionator is equipped with medium petrol pipeline. The medium petrol pipeline is connected with a medium petrol extractor, the upper part of the medium petrol extractor is connected with the medium petrol raffinate oil hydrogenation unit through the pipeline, the lower part of the medium petrol extractor is connected with the medium petrol aromatic hydrocarbon hydrogenation unit through the pipeline. The medium petrol aromatic hydrocarbon hydrogenation unit is then connected with the light petrol pipeline in the upper part of the fractionator through the pipeline, the lower part of the heavy petrol extractor is connected with the medium petrol aromatic hydrocarbon hydrogenation unit through the pipeline, the upper part of the heavy petrol extractor is connected with the medium petrol raffinate oil hydrogenation unit through the pipeline.

Abstract translation: 通过催化烃的重组制备高质量汽油的系统和方法包括分馏塔和萃取器。 分馏塔上部配有轻质汽油管道，分馏塔下部配有重质汽油管道，分馏塔中部配有中型汽油管道。 中型汽油管道与中型汽油提取器连接，中部汽油提取器的上部通过管道与中型汽油萃取油加氢装置连接，中部汽油提取器的下部与中等汽油芳烃连接 氢化装置通过管道。 中等汽油芳烃加氢装置然后通过管道与分馏塔上部的轻质汽油管道连接，重质汽油提取器的下部通过管道与中等汽油芳烃氢化装置连接，上部 重质汽油提取器的一部分通过管道与中等汽油提余油加氢装置连接。

公开(公告)号：US08715595B2

公开(公告)日：2014-05-06

申请号：US13213225

申请日：2011-08-19

Applicant: Richard K. Hoehn ,  Vedula K. Murty

Inventor： Richard K. Hoehn ,  Vedula K. Murty

IPC: B01J8/00 ,  B01J19/00 ,  C10G45/00

CPC classification number: C10G67/00 ,  C10G7/00 ,  C10G67/16 ,  C10G69/04 ,  C10G2300/1055 ,  C10G2400/04

Abstract: An apparatus is disclosed for recovering hydroprocessing effluent from a hydroprocessing unit utilizing a hot stripper and a cold stripper. A net overhead stream from the hot stripper is forwarded to the cold stripper for further stripping. The invention is particularly suitable for hydrotreating residue feed streams. The hot stripped stream may be subjected to fluid catalytic cracking. The apparatus and process eliminates the need for a fired heater in the product recovery unit.

Abstract translation: 公开了一种利用热汽提器和冷汽提器从加氢处理装置回收加氢处理流出物的装置。 来自热汽提器的净顶部物流被送往冷汽提器以进一步汽提。 本发明特别适用于加氢处理残余物进料流。 热的汽提流可能经受流体催化裂化。 该设备和工艺消除了对产品回收单元中的燃烧加热器的需要。