公开(公告)号：US20170166819A1

公开(公告)日：2017-06-15

申请号：US15374295

申请日：2016-12-09

申请人： Saudi Arabian Oil Company

发明人： Ki-Hyouk Choi ,  Mohammad A. AlAbdullah ,  Emad N. Al-Shafei ,  Massad S. Alanzi ,  Bandar K. Alotaibi ,  Bandar Hussain Alsolami ,  Ali M. Alsomali

IPC分类号： C10B57/06 ,  C10B57/04 ,  C10B55/00

CPC分类号： C10G69/06 ,  B01D11/0403 ,  B01D11/0415 ,  B01D11/0488 ,  B01J3/008 ,  C10B55/00 ,  C10B57/045 ,  C10B57/06 ,  C10G9/005 ,  C10G21/003 ,  C10G21/14 ,  C10G31/06 ,  C10G31/08 ,  C10G31/10 ,  C10G45/26 ,  C10G47/32 ,  C10G49/007 ,  C10G49/18 ,  C10G55/04 ,  C10G67/0454 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/42 ,  C10L5/00 ,  C10L9/08

摘要： Embodiments of a process for producing high grade coke from crude oil residue include at least partially separating, in a solvent extraction unit, the crude oil residue into a deasphalted oil (DAO)-containing stream and an asphaltene containing-stream, producing a pressurized, heated DAO-containing stream, where the pressurized, heated DAO-containing stream, mixing a supercritical water stream with the pressurized, heated DAO-containing stream to create a combined feed stream, introducing the combined feed stream to an upgrading reactor system operating at supercritical temperature and pressure to yield one or more upgrading reactor output streams comprising upgraded product and a slurry mixture, where the slurry mixture comprises sulfur and one or more additional metals. The process also may include calcining the slurry mixture at a temperature of from 700° C. to 1900° C. to produce a product stream comprising the high grade coke.

公开(公告)号：US09657233B2

公开(公告)日：2017-05-23

申请号：US13879717

申请日：2011-12-09

申请人： Marc Bories ,  Patrick Leroy

发明人： Marc Bories ,  Patrick Leroy

IPC分类号： C10G11/20 ,  C10G11/14 ,  B01J8/00 ,  B01J8/18 ,  B01J8/30 ,  B01J8/34 ,  C10G11/18 ,  B01J8/24 ,  B01J8/26

CPC分类号： C10G11/20 ,  B01J8/0045 ,  B01J8/1827 ,  B01J8/24 ,  B01J8/26 ,  B01J8/30 ,  B01J8/34 ,  B01J2208/00017 ,  B01J2208/00557 ,  B01J2208/00991 ,  C10G11/182 ,  C10G11/187 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/1077 ,  C10G2300/1096 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/4081 ,  C10G2300/4093 ,  C10G2300/708 ,  Y02P30/20 ,  Y02P30/446

摘要： Process for the fluidized-bed catalytic cracking of a weakly coking feedstock having a Conradson carbon residue equal to or less than 0.1% by weight and a hydrogen content equal to or greater than 12.7% by weight, comprising at least a step of cracking the feedstock, a step of separating/stripping the effluents from the coked catalyst particles and a step of regenerating said particles, the process being characterized in that at least one coking, carbonaceous and/or hydrocarbonaceous effluent having a content of aromatic compounds of greater than 50% by weight, comprising more than 20% by weight of polyaromatic compounds, is recycled to homogeneously distributed and weakly coked catalyst, before regeneration, in order to adjust the delta coke of the process.

公开(公告)号：US20170029719A1

公开(公告)日：2017-02-02

申请号：US15101004

申请日：2014-11-27

申请人： IFP ENERGIES NOUVELLES

发明人： Isabelle MERDRIGNAC ,  Jerome MAJCHER

IPC分类号： C10G53/06 ,  C10G21/02 ,  C10G21/14 ,  C10G21/00

CPC分类号： C10G53/06 ,  C10G21/003 ,  C10G21/02 ,  C10G21/12 ,  C10G21/14 ,  C10G2300/1077 ,  C10G2300/201 ,  C10G2300/206

摘要： The invention describes a process for the deasphalting of a heavy feedstock by liquid/liquid extraction, said process comprising at least two stages of deasphalting in series carried out on the feedstock to be treated making it possible to separate at least one fraction of asphalt, at least one fraction of heavy deasphalted oil, referred to as heavy DAO and at least one fraction of light deasphalted oil, referred to as light DAO, at least one of said stages of deasphalting being carried out by means of a mixture of at least one polar solvent and at least one apolar solvent, said stages of deasphalting being implemented under the subcritical conditions of the mixture of solvents used.

摘要翻译： 本发明描述了一种通过液体/液体萃取对重质原料进行脱沥青的方法，所述方法包括至少两个阶段的脱沥青在待处理原料上进行，使得可以将至少一部分沥青分离在 称为重DAO的至少一部分重质脱沥青油，称为轻DAO的至少一部分轻质脱沥青油，至少一个脱沥青阶段是通过至少一种极性的 溶剂和至少一种非极性溶剂，所述脱沥青阶段在所用溶剂混合物的亚临界条件下实施。

公开(公告)号：US20170022433A1

公开(公告)日：2017-01-26

申请号：US15202732

申请日：2016-07-06

申请人： ExxonMobil Research and Engineering Company

发明人： Stephen H. BROWN ,  Warren B. AMES ,  Federico BARRAI

IPC分类号： C10G67/04 ,  C10G45/00 ,  C10G69/04 ,  C10G47/00

CPC分类号： C10G67/0454 ,  C10G45/00 ,  C10G47/00 ,  C10G49/002 ,  C10G67/0463 ,  C10G67/049 ,  C10G69/04 ,  C10G2300/1077 ,  C10G2300/206 ,  C10G2300/40

摘要： Systems and methods are provided for fixed bed hydroprocessing of deasphalter rock. Instead of attempting to process vacuum resid in a fixed bed processing unit, vacuum resid is deasphalted to form a deasphalted oil and deasphalter residue or rock. The rock can then be hydroprocessed in a fixed bed reaction zone, optionally after combining the rock with an aromatic co-feed and/or a hydroprocessing solvent. This can allow for improved conversion of the deasphalter rock and/or improved combined conversion of the deasphalter rock and deasphalted oil.

摘要翻译： 提供脱沥青岩固定床加氢的系统和方法。 除了试图在固定床处理单元中处理真空渣油之外，还要将真空渣进行脱沥青以形成脱沥青油和脱沥青残渣或岩石。 然后可以在固定床反应区中加氢处理岩石，任选地在将岩石与芳族共进料和/或加氢处理溶剂组合之后。 这可以改善脱沥青岩石的转化率和/或改善脱沥青岩石和脱沥青油的组合转化率。

公开(公告)号：US20160369189A1

公开(公告)日：2016-12-22

申请号：US14901736

申请日：2014-06-30

申请人： SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V.

发明人： Andrew Mark Ward ,  Arno Johannes Maria Oprins ,  Thomas Hubertus Maria Housmans

IPC分类号： C10G69/06 ,  C10G69/00

CPC分类号： C10G69/06 ,  C10G69/00 ,  C10G69/04 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/1085 ,  C10G2400/20 ,  C10G2400/30 ,  Y02P30/40

摘要： The present invention relates to a process for the production of light olefins and aromatics from a hydrocarbon feedstock, comprising the following steps of: (a) feeding a hydrocarbon feedstock into a FCC unit (b) separating reaction products, which are generated from the FCC reaction, into a bottom stream, and middle stream and a top stream; (c) feeding the middle stream from (b) to a gasoline hydrocracker (GHC) unit, (d) separating reaction products of said GHC of step (c) into an overhead gas stream comprising hydrogen, methane and C2-C4 paraffins, and a bottom stream comprising aromatic hydrocarbon compounds, (e) feeding the overhead stream from the gasoline hydrocracker (GHC) unit into a steam cracker unit.

摘要翻译： 本发明涉及从烃原料生产轻质烯烃和芳族化合物的方法，包括以下步骤：（a）将烃原料进料到FCC装置中（b）分离由FCC生成的反应产物 反应，进入底部流，中流和顶流; （c）将中间物流从（b）加入到汽油加氢裂化器（GHC）单元中，（d）将步骤（c）的所述GHC的反应产物分离成包含氢，甲烷和C 2 -C 4链烷烃的塔顶气流，以及 包含芳族烃化合物的底部物流，（e）将来自汽油加氢裂化器（GHC）装置的塔顶馏出物进料到蒸汽裂化装置中。

公开(公告)号：US20160369188A1

公开(公告)日：2016-12-22

申请号：US14901947

申请日：2014-06-30

申请人： Thomas Hubertus Maria HOUSMANS ,  Arno Johannes Maria OPRINS ,  SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V.

发明人： Thomas Hubertus Maria Housmans ,  Arno Johannes Maria Oprins

IPC分类号： C10G69/02

CPC分类号： C10G69/02 ,  C10G65/00 ,  C10G65/10 ,  C10G65/18 ,  C10G67/0445 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2400/20 ,  C10G2400/30

摘要： The present invention relates to a process for upgrading refinery heavy residues to petrochemicals, comprising the following steps of: (a) separating a hydrocarbon feedstock in a distillation unit into a to overhead stream and a bottom stream (b) feeding said bottom stream to a hydrocracking reaction area (c) separating reaction products, which are generated from said reaction area of step (b) into a stream rich in mono-aromatics and in a stream rich in poly-aromatics (d) feeding said stream rich in mono-aromatics to a gasoline hydrocracker (GHC) unit, (e) feeding said stream rich in poly-aromatics to a ring opening reaction area.

摘要翻译： 本发明涉及一种将炼厂重质残渣升级至石化产品的方法，包括以下步骤：（a）将蒸馏单元中的烃原料分离成塔顶物流和塔底物流（b），将塔底物料送入 （c）将从步骤（b）的所述反应区域产生的反应产物分离成富含单芳族化合物的流和富含多芳族化合物的流（d）将富含单芳族化合物的所述物流 到汽油加氢裂化器（GHC）单元，（e）将富含多芳族化合物的物流进料到开环反应区。

公开(公告)号：US20160369175A1

公开(公告)日：2016-12-22

申请号：US15254453

申请日：2016-09-01

申请人： ENVIROLLEA INC.

发明人： Lucie B. WHEELER

IPC分类号： C10G21/28 ,  C09K8/34 ,  C10L1/08 ,  C10L10/12 ,  C10G21/16 ,  C10G21/20

CPC分类号： C10G21/28 ,  B01D11/0434 ,  C09K8/34 ,  C10G21/06 ,  C10G21/12 ,  C10G21/16 ,  C10G21/20 ,  C10G21/22 ,  C10G21/27 ,  C10G55/04 ,  C10G55/06 ,  C10G2300/1007 ,  C10G2300/1055 ,  C10G2300/1077 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/30 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4081 ,  C10G2300/44 ,  C10G2300/80 ,  C10G2400/04 ,  C10G2400/10 ,  C10L1/08 ,  C10L10/12 ,  C10L2200/0446 ,  C10L2270/026 ,  C10L2290/544

摘要： A process allowing the removal of contaminants from an unstable oil such as those produced by thermal or catalytic cracking, wherein, in at least one step of the process, mixing of the unstable oil with a pure or impure solvent having a dipole moment greater than 2 is performed. The stabilized diesels thereby obtained exhibit interesting properties among which significant stability features and are useful in numerous applications, some of these stabilized wide range diesels are new as well as their uses.

公开(公告)号：US20160362610A1

公开(公告)日：2016-12-15

申请号：US14844055

申请日：2015-09-03

申请人： Expander Energy Inc.

发明人： Steve Kresnyak

IPC分类号： C10G2/00 ,  C10G45/00 ,  C10G47/00 ,  C10G9/00 ,  C07C273/04 ,  C01B3/50 ,  C01B3/52 ,  C01B3/56 ,  C01B31/20 ,  C07C29/151 ,  C10G7/00 ,  C01B3/34

CPC分类号： C10G2/30 ,  C01B3/34 ,  C01B3/382 ,  C01B3/384 ,  C01B3/501 ,  C01B3/52 ,  C01B3/56 ,  C01B21/087 ,  C01B32/50 ,  C01B2203/0205 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/062 ,  C01B2203/1047 ,  C01B2203/1082 ,  C01B2203/1211 ,  C01B2203/141 ,  C07C1/0485 ,  C07C29/1518 ,  C07C273/04 ,  C10G7/00 ,  C10G9/00 ,  C10G21/003 ,  C10G45/00 ,  C10G45/58 ,  C10G47/00 ,  C10G67/049 ,  C10G2300/1022 ,  C10G2300/1077 ,  C10G2300/206 ,  C10G2300/42 ,  C10J3/00 ,  C10J2300/0913 ,  C10J2300/0959 ,  C10J2300/1659 ,  C10K3/06 ,  Y02P30/10 ,  Y02P30/30 ,  Y02P30/44

摘要： The present invention is directed to modifications of bitumen and heavy oil upgrading and refining processes to synthesize synthetic crude oil and other valuable synthesized hydrocarbon products in an efficient manner along with the production of commercially valuable co-products from by-products formed by the upgrading process.

摘要翻译： 本发明涉及沥青和重油改质和精炼方法的改进，以便以有效的方式合成合成原油和其它有价值的合成烃产品，以及从由升级过程形成的副产物生产商业上有价值的副产物 。

公开(公告)号：US20160312130A1

公开(公告)日：2016-10-27

申请号：US15105314

申请日：2014-12-05

申请人： IFP ENERGIES NOUVELLES

发明人： Isabelle MERDRIGNAC ,  Wilfried WEISS ,  Jerome MAJCHER

IPC分类号： C10G67/04 ,  C10L1/04 ,  C10L1/08

CPC分类号： C10G67/049 ,  C10G21/003 ,  C10G21/06 ,  C10G45/02 ,  C10G45/08 ,  C10G65/12 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2400/04 ,  C10G2400/06 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/10 ,  C10L2290/543 ,  C10L2290/544

摘要： Treating a hydrocarbon feed having a sulphur content of at least 0.5% by weight, an asphaltenes content of at least 1% by weight, an initial boiling point of at least 340° C. and a final boiling point of at least 480° C., in order to obtain at least one deasphalted oil fraction with a sulphur content of 0.5% by weight or less and a sediment content of 0.1% by weight or less.

摘要翻译： 处理硫含量为至少0.5重量％，沥青质含量为至少1重量％，初始沸点为至少340℃，最终沸点为至少480℃的烃原料。 ，以获得硫含量为0.5重量％以下，沉降物含量为0.1重量％以下的至少一种脱沥青油馏分。

公开(公告)号：US20160304794A1

公开(公告)日：2016-10-20

申请号：US15100745

申请日：2014-11-27

申请人： IFP ENERGIES NOUVELLES

发明人： Jerome MAJCHER ,  Isabelle MERDRIGNAC ,  Frederic FEUGNET

IPC分类号： C10G67/04

CPC分类号： C10G67/0463 ,  C10G21/003 ,  C10G21/14 ,  C10G45/08 ,  C10G45/20 ,  C10G47/00 ,  C10G49/04 ,  C10G49/16 ,  C10G53/06 ,  C10G67/00 ,  C10G67/14 ,  C10G2300/1014 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  Y02P30/20

摘要： Process for converting a heavy hydrocarbon feedstock with initial boiling point of at least 300° C. comprising: a) hydroconverting at least part of said feedstock; b) separating the effluent from stage a) to obtain light and heavy liquid fractions; c) at least two stages of deasphalting in series at least part of the heavy liquid fraction originating from stage b), allowing to separate at least one fraction of asphalt, at least one fraction of heavy deasphalted oil (heavy DAO) and at least one fraction of light deasphalted oil (light DAO), at least one deasphalting stage being carried out using a mixture of at least one polar solvent and at least one apolar solvent, said deasphalting stages being under subcritical conditions of the mixture of solvents; d) recycling at least part of said heavy deasphalted oil cut from stage c) upstream of hydroconverting a) and/or of the inlet of separating b).

摘要翻译： 用于将初始沸点为至少300℃的重质烃原料转化的方法，包括：a）将至少部分所述原料进行加氢转化; b）将流出物从阶段a）分离得到轻质和重质液体馏分; c）至少两个阶段，至少部分来自阶段b）的重质液体馏分至少部分脱沥青，允许分离至少一部分沥青，至少一部分重质脱沥青油（重DAO）和至少一种 轻度脱沥青油（轻质DAO）的分数，使用至少一种极性溶剂和至少一种非极性溶剂的混合物进行至少一个脱沥青阶段，所述脱沥青阶段处于溶剂混合物的亚临界条件下; d）从加压转化器a）和/或分离器b）入口的上游阶段c）回收至少部分所述重质脱沥青油。