公开(公告)号：US10400108B2

公开(公告)日：2019-09-03

申请号：US15142198

申请日：2016-04-29

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C09C1/48

摘要： The invention described herein relates to a novel process to create carbon black feed stocks derived from coal by utilizing direct coal liquefaction resulting in an economic process for producing carbon black feedstock. Moreover, relative to the current state of the art (use of FCC slurry oil), the invention process will be significantly more profitable when oil prices increase.

公开(公告)号：US07938953B2

公开(公告)日：2011-05-10

申请号：US12154011

申请日：2008-05-20

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C10G65/00

CPC分类号： C10G47/00 ,  C10G11/16 ,  C10G65/10 ,  C10G65/12 ,  C10G65/14 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4081

摘要： An improved process for heavy oil conversion and upgrading and a combined method for heavy oil conversion and vacuum gas-oil treatment are described herein. The method utilizes the creation and recycle of a separate product from the vacuum still, which is thereafter recycled back to the heavy oil conversion reactor. The result is the production of a higher quality medium gas oil product relative to the overall vacuum gas oil product which is acceptable for use in a typical vacuum gas oil treatment process. Additionally, there is a higher diesel yield selectivity from the heavy oil conversion unit.

摘要翻译： 本文描述了用于重油转化和升级的改进方法以及重油转化和减压瓦斯油处理的组合方法。 该方法利用从真空静止物中产生和再循环单独的产物，然后再循环回重油转化反应器。 其结果是相对于在典型的真空瓦斯油处理过程中可以使用的整个减压瓦斯油产品生产更高质量的中瓦斯油产品。 此外，来自重油转化装置的柴油产率选择性更高。

公开(公告)号：US07938952B2

公开(公告)日：2011-05-10

申请号：US12154010

申请日：2008-05-20

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C10G65/02

CPC分类号： C10G7/06 ,  C10G45/16 ,  C10G47/26 ,  C10G65/02 ,  C10G65/10 ,  C10G65/12

摘要： This invention relates to a novel integrated hydroconversion process for converting heavy atmospheric or vacuum residue feeds and also converting and reducing impurities in the vacuum gas oil liquid product. This is accomplished by utilizing two residue hydroconversion reaction stages, two vapor-liquid separators, and at least two additional distillate ebullated-bed hydrocracking/hydrotreating reaction stages to provide a high conversion rate of the residue feedstocks.

摘要翻译： 本发明涉及一种用于转化重大气压或减压渣油进料以及还原和还原真空瓦斯油液体产物中杂质的新型集成加氢转化方法。 这通过利用两个残余物加氢转化反应阶段，两个气液分离器和至少两个另外的馏出物沸腾床加氢裂化/加氢处理反应阶段来实现，以提供残余物原料的高转化率。

公开(公告)号：US20090288984A1

公开(公告)日：2009-11-26

申请号：US12154011

申请日：2008-05-20

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C10G65/02

CPC分类号： C10G47/00 ,  C10G11/16 ,  C10G65/10 ,  C10G65/12 ,  C10G65/14 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4081

摘要： An improved process for heavy oil conversion and upgrading and a combined method for heavy oil conversion and vacuum gas-oil treatment are described herein. The method utilizes the creation and recycle of a separate product from the vacuum still, which is thereafter recycled back to the heavy oil conversion reactor. The result is the production of a higher quality medium gas oil product relative to the overall vacuum gas oil product which is acceptable for use in a typical vacuum gas oil treatment process. Additionally, there is a higher diesel yield selectivity from the heavy oil conversion unit.

摘要翻译： 本文描述了用于重油转化和升级的改进方法以及重油转化和减压瓦斯油处理的组合方法。 该方法利用从真空静止物中产生和再循环单独的产物，然后再循环回重油转化反应器。 其结果是相对于在典型的真空瓦斯油处理过程中可以使用的整个减压瓦斯油产品生产更高质量的中瓦斯油产品。 此外，来自重油转化装置的柴油产率选择性更高。

公开(公告)号：US10351712B2

公开(公告)日：2019-07-16

申请号：US15142198

申请日：2016-04-29

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C09C1/48

CPC分类号： C09C1/48

摘要： The invention described herein relates to a novel process to create carbon black feed stocks derived from coal by utilizing direct coal liquefaction resulting in an economic process for producing carbon black feedstock. Moreover, relative to the current state of the art (use of FCC slurry oil), the invention process will be significantly more profitable when oil prices increase.

公开(公告)号：US20170313886A1

公开(公告)日：2017-11-02

申请号：US15142198

申请日：2016-04-29

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C09C1/48

CPC分类号： C09C1/48

摘要： The invention described herein relates to a novel process to create carbon black feed stocks derived from coal by utilizing direct coal liquefaction resulting in an economic process for producing carbon black feedstock. Moreover, relative to the current state of the art (use of FCC slurry oil), the invention process will be significantly more profitable when oil prices increase.

公开(公告)号：US20090288986A1

公开(公告)日：2009-11-26

申请号：US12154010

申请日：2008-05-20

申请人： James J. Colyar ,  John Duddy

发明人： James J. Colyar ,  John Duddy

IPC分类号： C10G67/02

CPC分类号： C10G7/06 ,  C10G45/16 ,  C10G47/26 ,  C10G65/02 ,  C10G65/10 ,  C10G65/12

摘要： This invention relates to a novel integrated hydroconversion process for converting heavy atmospheric or vacuum residue feeds and also converting and reducing impurities in the vacuum gas oil liquid product. This is accomplished by utilizing two residue hydroconversion reaction stages, two vapor-liquid separators, and at least two additional distillate ebullated-bed hydrocracking/hydrotreating reaction stages to provide a high conversion rate of the residue feedstocks.

摘要翻译： 本发明涉及一种用于转化重大气压或减压渣油进料以及还原和还原真空瓦斯油液体产物中杂质的新型集成加氢转化方法。 这通过利用两个残余物加氢转化反应阶段，两个气液分离器和至少两个另外的馏出物沸腾床加氢裂化/加氢处理反应阶段来实现，以提供残余物原料的高转化率。

公开(公告)号：US20070209965A1

公开(公告)日：2007-09-13

申请号：US11370184

申请日：2006-03-08

申请人： John Duddy ,  Lawrence Wisdom ,  Andrea Gragnani

发明人： John Duddy ,  Lawrence Wisdom ,  Andrea Gragnani

IPC分类号： C10G45/00 ,  B01J8/00

CPC分类号： C10G47/26 ,  C10G45/02

摘要： This invention relates to a process and an installation for treatment of a heavy petroleum feedstock, of which at least 80% by weight has a boiling point of greater than 340° C., whereby the process comprises the following stages: (a) hydroconversion in a boiling-bed reactor operating with a rising flow of liquid and gas, conversion in % by weight of the fraction having a boiling point of greater than 540° C. being from 10 to 98% by weight; (b) separation of the effluent obtained from stage (a) into a gas containing hydrogen and H2S, a fraction comprising the gas oil and optionally a fraction that is heavier than gas oil and a naphtha fraction; c) hydrotreatment by contact with at least one catalyst of at least the fraction comprising the gas oil obtained in stage (b); d) separation of the effluent obtained at the end of stage (c) into a gas containing hydrogen and at least one gas oil fraction having a sulfur content of less than 50 ppm, preferably less than 20 ppm, and more preferably less than 10 ppm, the hydroconversion stage (a) being conducted at a pressure P1 and the hydrotreatment stage (c) being conducted at a pressure P2, the difference ΔP=P1−P2 being at least 3 MPa, hydrogen supply for the hydroconversion (a) and hydrotreatment (c) stages being ensured by a single compression system with n stages.

摘要翻译： 本发明涉及一种用于处理重质石油原料的方法和装置，其中至少80重量％的沸点大于340℃，由此该方法包括以下阶段：（a）加氢转化 以液体和气体的上升流动运行的沸腾反应器，沸点大于540℃的馏分的重量百分比为10至98重量％; （b）将从阶段（a）获得的流出物分离成含有氢气和H 2 S的气体，包含瓦斯油和任选的比粗柴油重的馏分和石脑油馏分 ; c）通过与至少一种包含阶段（b）中获得的瓦斯油的馏分的催化剂接触进行加氢处理; d）将阶段（c）结束时得到的流出物分离成含有氢的气体和硫含量小于50ppm，优选小于20ppm，更优选小于10ppm的至少一种瓦斯油馏分 加氢转化阶段（a）在压力P 1下进行，加氢处理阶段（c）以压力P 2进行，差值ΔP= P1-P2为至少3MPa，加氢转化（a） 和加氢处理（c）阶段由具有n个阶段的单个压缩系统确保。

公开(公告)号：US20050075527A1

公开(公告)日：2005-04-07

申请号：US10373197

申请日：2003-02-26

申请人： Mathieu Pinault ,  Frederic Hoffmann ,  Stephane Kressmann ,  Pierre Porot ,  John Duddy

发明人： Mathieu Pinault ,  Frederic Hoffmann ,  Stephane Kressmann ,  Pierre Porot ,  John Duddy

IPC分类号： B01D19/00 ,  C10G49/12 ,  C07C7/00 ,  B01J10/00

CPC分类号： B01D19/0042 ,  C10G49/12

摘要： Method for processing hydrocarbons comprising at least two processing chambers and means for separating the liquid and gaseous fractions contained in the polyphasic mixture produced in the first processing chamber, said mixture coming from a zone (700) where a batch of liquid hydrocarbons, a gaseous batch and solid particles come into contact, said method comprising separation of liquid and gaseous phases located in the chamber. Equipment comprising: a) At least a first chamber comprising means inside said chamber for separating gaseous and liquid fractions coming from said zone, b) means for conveying said liquid fraction toward a second chamber, c) a second chamber comprising a second contact zone and means of introducing, into said zone, a gaseous batch and a liquid batch comprising at least a portion of the liquid fraction coming from the first chamber.

摘要翻译： 用于处理包含至少两个处理室的烃的方法和用于分离包含在第一处理室中产生的多相混合物中的液相和气态馏分的装置，所述混合物来自区域（700），其中一批液体烃，气态批料 并且固体颗粒接触，所述方法包括分离位于室中的液相和气相。 一种设备，包括：a）至少一个第一室，包括在所述室内的装置，用于分离来自所述区域的气态和液态馏分; b）用于将所述液体馏分输送到第二室的装置，c）第二室，包括第二接触区和 在所述区域中引入气态批料和包含至少一部分来自第一室的液体馏分的液体批料的装置。