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61. 发明申请

US20160097002A1 THERMAL CRACKING OF CRUDES AND HEAVY FEEDS TO PRODUCE OLEFINS IN PYROLYSIS REACTOR 审中-公开
标题翻译：热裂解产物的热裂解和重油进料在热解反应器中生产烯烃
公开(公告)号：US20160097002A1
公开(公告)日：2016-04-07
申请号：US14874755
申请日：2015-10-05
申请人： Lummus Technology Inc.
发明人： Kandasamy Meenakshi Sundaram
IPC分类号： C10G9/14 , C10G9/20 , C10G69/06
CPC分类号： C10G9/36 , B01J6/008 , B01J19/2425 , B01J2219/00157 , B01J2219/00159
摘要： Systems and processes for efficiently cracking of hydrocarbon mixtures, such as mixtures including compounds having a normal boiling temperature of greater than 450° C., 500° C., or even greater than 550° C., such as whole crudes for example, are disclosed.
摘要翻译：烃混合物的有效裂解的系统和方法，例如包括正常沸腾温度大于450℃，500℃，甚至大于550℃的化合物（例如整个原油）的混合物是披露

62. 发明授权

US09296959B2 Integration of solvent deasphalting with resin hydroprocessing and with delayed coking 有权
标题翻译：溶剂脱沥青与树脂加氢处理和延迟焦化的结合
公开(公告)号：US09296959B2
公开(公告)日：2016-03-29
申请号：US13833884
申请日：2013-03-15
申请人： Foster Wheeler USA Corporation
发明人： Daniel B. Gillis
IPC分类号： C10G67/04 , C10G69/06 , C10G55/04 , C10G67/00 , C10G9/00 , C10G21/00 , C10G53/06
CPC分类号： C10G67/0454 , C10G9/005 , C10G21/003 , C10G55/04 , C10G67/00 , C10G67/049 , C10G69/06
摘要： The invention is directed to a process that combines the solvent deasphalting with resin hydrotreatment and coupled with delayed coking so as to reduce the costs associated with performing each of the steps separately. The integrated process of the invention permits higher product yields coupled with lower energy and transportation costs.
摘要翻译：本发明涉及将溶剂脱沥青与树脂加氢处理结合并与延迟焦化相结合的方法，以便降低分别执行每个步骤所需的成本。本发明的综合方法允许更高的产品产量以及更低的能量和运输成本。

63. 发明授权

US09290706B2 Integrated process for upgrading heavy oil 有权
标题翻译：重油升级整合流程
公开(公告)号：US09290706B2
公开(公告)日：2016-03-22
申请号：US13851802
申请日：2013-03-27
申请人： CHINA UNIVERSITY OF PETROLEUM-BEIJING
发明人： Suoqi Zhao , Xuewen Sun , Zhiming Xu , Chunming Xu , Keng H. Chung
IPC分类号： C10G55/04 , C10G69/06 , C10G21/00 , C10G21/14 , C10G53/02 , C10G53/04 , C10G67/04
CPC分类号： C10G55/04 , C10G21/003 , C10G21/14 , C10G69/06 , C10G2300/206 , C10G2300/4081 , C10G2300/44
摘要： The invention provides an integrated process for processing heavy oil, wherein the integrated process at least comprises: solvent deasphalting is carried out for heavy oil material, and de-oiled asphalt phase is mixed with dispersing agent and then entered a thermal cracking reactor to undergo thermal cracking reactions. Upgraded oil can be obtained through the mixture of the de-asphalted oil and thermal cracking oil separated from thermal cracking reaction products. The solvent and heavy gas oil, which are separated from the thermal cracking reaction products, are respectively recycled back to the solvent deasphalting process as solvent and as mixed feed to remove asphaltene. The integrated process of the present invention solves the problems that solvent is difficult to be separated from asphalt with high softening point in solvent deasphalting process and hard asphalt is difficult to be transported.
摘要翻译：本发明提供了一种加工重油的综合方法，其中一体化方法至少包括：对重油材料进行溶剂脱沥青，脱油沥青相与分散剂混合，然后进入热裂解反应器进行热处理开裂反应。通过从热裂解反应产物中分离的脱沥青油和热裂解油的混合物可以获得升级的油。与热裂解反应产物分离的溶剂和重质瓦斯油分别作为溶剂和混合进料循环回到溶剂脱沥青法中以除去沥青质。本发明的一体化方法解决了在溶剂脱沥青工艺中溶剂难以与高软化点的沥青分离的困难，难以运输硬沥青的问题。

64. 发明授权

US09260670B2 Process for the selective hydrogenation and hydrodesulferization of a pyrolysis gasoline feedstock 有权
标题翻译：热解汽油原料的选择性加氢和加氢脱硫的方法
公开(公告)号：US09260670B2
公开(公告)日：2016-02-16
申请号：US13376531
申请日：2010-06-09
申请人： Dane Clark Grenoble , Paul Benjerman Himelfarb , Michael Norris Treybig , Brian Scott Vanderwilp
发明人： Dane Clark Grenoble , Paul Benjerman Himelfarb , Michael Norris Treybig , Brian Scott Vanderwilp
IPC分类号： C07C7/163 , C10G45/32 , C10G45/02 , C10G69/06
CPC分类号： C10G45/32 , C10G45/02 , C10G69/06 , C10G2300/104 , C10G2300/1044 , C10G2300/202 , C10G2300/4018 , C10G2300/4081 , C10G2400/30
摘要： Disclosed is a process for the selective hydrogenation of diolefins and sulfur compounds that are contained in a pyrolysis gasoline feedstream. The process includes utilizing a single hydrotreating reaction stage by introducing the pyrolysis gasoline feedstock that includes a diolefin concentration and an organic sulfur concentration into a reactor that is loaded with a high activity hydrotreating catalyst and which is operated under selective hydrogenation conditions. A reactor effluent having a reduced diolefin concentration and a reduced organic sulfur concentration is yielded from the reactor and is separated into a portion that is recycled as a reactor feed. The remaining portion of the reactor effluent is passed downstream for further processing or handling.
摘要翻译：公开了一种用于选择氢化包含在热解汽油原料流中的二烯烃和硫化合物的方法。该方法包括通过将包含二烯烃浓度和有机硫浓度的裂解汽油原料引入装载有高活性加氢处理催化剂并在选择性氢化条件下操作的反应器中来利用单一加氢处理反应阶段。从反应器产生具有降低的二烯烃浓度和降低的有机硫浓度的反应器流出物，并将其分离成作为反应器进料循环的部分。反应器流出物的剩余部分通过下游进行进一步处理或处理。

65. 发明授权

US09228139B2 Integrated hydroprocessing and steam pyrolysis of crude oil to produce light olefins and coke 有权
标题翻译：综合加氢处理和蒸汽热解原油生产轻质烯烃和焦炭
公开(公告)号：US09228139B2
公开(公告)日：2016-01-05
申请号：US13847918
申请日：2013-03-20
申请人： Raheel Shafi , Abdennour Bourane , Abdul Rahman Zafer Akhras , Essam Sayed , Ibrahim A. Abba
发明人： Raheel Shafi , Abdennour Bourane , Abdul Rahman Zafer Akhras , Essam Sayed , Ibrahim A. Abba
IPC分类号： C10G69/06 , C10G9/00 , C10G51/06 , C10G9/16 , C10B57/04 , C10G49/00 , C10G69/00 , C10G9/14
CPC分类号： C10G69/06 , C10B57/045 , C10G9/005 , C10G9/16 , C10G49/007 , C10G51/06 , C10G69/00 , C10G2300/201 , C10G2300/308 , C10G2400/20 , C10G2400/22 , C10G2400/30 , Y02P20/132
摘要： An integrated hydrotreating, steam pyrolysis and coker process for the direct processing of a crude oil is provided to produce olefinic and aromatic petrochemicals, and petroleum coke. Crude oil and recycled coker liquid product are charged to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent which is thermally cracked in the presence of steam to produce a mixed product stream. The residual liquid fraction recovered upstream of the thermal cracking unit or within the thermal cracking unit is thermally cracked under conditions effective to produce coke and coker liquid product. The coker liquid product is recycled to the step of hydroprocessing while the petroleum coke is recovered. Hydrogen from the mixed product stream is purified and recycled to the hydroprocessing zone, and olefins, aromatics and pyrolysis fuel oil are recovered from the separated mixed product stream.
摘要翻译：提供了一种用于直接加工原油的综合加氢处理，蒸汽热解和焦化工艺，以生产烯烃和芳香族石油化学品和石油焦炭。将原油和再循环焦化液体产物装入加氢处理区，该加氢处理区在有效地产生加氢处理流出物的条件下运行，该加氢处理流出物在蒸汽存在下被热裂解以产生混合产物流。在热裂解单元上游或在热裂解装置中回收的剩余液体馏分在有效生产焦炭和焦化液体产物的条件下被热裂解。在回收石油焦时，将焦化液体产物再循环至加氢处理步骤。将来自混合产物流的氢气纯化并再循环至加氢处理区，并从分离的混合产物流中回收烯烃，芳烃和热解燃料油。

66. 发明授权

US09090836B2 Upgrading hydrocarbon pyrolysis products 有权
标题翻译：升级烃热解产物
公开(公告)号：US09090836B2
公开(公告)日：2015-07-28
申请号：US13601207
申请日：2012-08-31
申请人： Stephen H. Brown , S. Mark Davis , Teng Xu , Keith G. Reed , Ananthakrishnan Bhasker
发明人： Stephen H. Brown , S. Mark Davis , Teng Xu , Keith G. Reed , Ananthakrishnan Bhasker
IPC分类号： C10L1/00 , H01B3/22 , C10G69/06 , C10G49/18
CPC分类号： C10G69/06 , C10G49/18
摘要： The invention relates to upgraded pyrolysis products, processes for upgrading products obtained from hydrocarbon pyrolysis, equipment useful for such processes, and the use of upgraded pyrolysis products.
摘要翻译：本发明涉及升级的热解产物，用于升级由烃热解获得的产物的方法，用于这些方法的设备和使用升级的热解产物。

67. 发明申请

US20150203770A1 PROCESS FOR CONVERTING A HYDROCARBON FEED AND APPARATUS RELATING THERETO 审中-公开
标题翻译：转化油料进料的方法和与其相关的装置
公开(公告)号：US20150203770A1
公开(公告)日：2015-07-23
申请号：US14673116
申请日：2015-03-30
申请人： UOP LLC
发明人： Robert S. Haizmann
IPC分类号： C10G69/06 , B01J8/22
CPC分类号： C10G69/06 , B01J8/22 , B01J2208/00796
摘要： The embodiments disclosed herein can provide a process for converting a hydrocarbon feed. The process may include hydrocracking the hydrocarbon feed slurried with a particulate catalyst in a presence of hydrogen in a hydrocracking reaction zone to produce a hydrocracked stream, separating at least a portion of the hydrocracked stream, and passing the at least the portion of the hydrocracked stream through a thermal cracking heating zone at conditions effective for thermally cracking the at least the portion of the hydrocracked stream.
摘要翻译：本文公开的实施方案可以提供用于转化烃进料的方法。该方法可以包括在加氢裂化反应区中在氢气存在下用颗粒催化剂浆化的烃进料加氢裂化以产生加氢裂化的流，分离至少一部分加氢裂化的物流，并将至少一部分加氢裂化物流通过热裂解加热区，在有效地热裂解加氢裂化物流的至少一部分的条件下。

68. 发明授权

US09057027B2 Process for cracking synthetic crude oil-containing feedstock 有权
公开(公告)号：US09057027B2
公开(公告)日：2015-06-16
申请号：US12478998
申请日：2009-06-05
申请人： Paul F Keusenkothen , James N McCoy , James Earl Graham , Chad David Reimann
发明人： Paul F Keusenkothen , James N McCoy , James Earl Graham , Chad David Reimann
IPC分类号： C10L1/04 , C10G69/06
CPC分类号： C10G69/06 , Y10S585/921
摘要： A process for steam cracking liquid hydrocarbon feedstocks containing synthetic crude oil comprises i) hydroprocessing a wide boiling range aliquot containing a) normally liquid hydrocarbon portion substantially free of resids and b) thermally cracked hydrocarbon liquid, boiling in a range from about 600° to about 1050° F., to provide a synthetic crude oil substantially free of resids; ii) adding to the synthetic crude oil a normally liquid hydrocarbon component boiling in a range from about 100° to about 1050° F.; and iii) cracking the mixture resulting from ii) in a cracker furnace comprising a radiant coil outlet to provide a cracked effluent, wherein the cracking is carried out under conditions sufficient to effect a radiant coil outlet temperature which is greater than the optimum radiant coil outlet temperature for cracking the synthetic crude oil separately. A method for upgrading synthetic crude for use in cracking is also provided, as well as a feedstock for cracking.

69. 发明授权

US08992765B2 Process for converting a hydrocarbon feed and apparatus relating thereto 有权
标题翻译：用于转换烃进料的方法和与其相关的装置
公开(公告)号：US08992765B2
公开(公告)日：2015-03-31
申请号：US13244083
申请日：2011-09-23
申请人： Robert Haizmann
发明人： Robert Haizmann
IPC分类号： C10G69/06 , C10G9/00 , C10G49/22 , C10G47/00
CPC分类号： C10G69/06 , B01J8/22 , B01J2208/00796
摘要： The embodiments disclosed herein can provide a process for converting a hydrocarbon feed. The process may include hydrocracking the hydrocarbon feed slurried with a particulate catalyst in a presence of hydrogen in a hydrocracking reaction zone to produce a hydrocracked stream, separating at least a portion of the hydrocracked stream, and passing the at least the portion of the hydrocracked stream through a thermal cracking heating zone at conditions effective for thermally cracking the at least the portion of the hydrocracked stream.
摘要翻译：本文公开的实施方案可以提供用于转化烃进料的方法。该方法可以包括在加氢裂化反应区中在氢气存在下用颗粒催化剂浆化的烃进料加氢裂化以产生加氢裂化的流，分离至少一部分加氢裂化的物流，并将至少一部分加氢裂化物流通过热裂解加热区，在有效地热裂解加氢裂化物流的至少一部分的条件下。

70. 发明申请

US20150060333A1 Treatment of Heavy Oils to Reduce Olefin Content 有权
标题翻译：重油处理降低油烯含量
公开(公告)号：US20150060333A1
公开(公告)日：2015-03-05
申请号：US14454001
申请日：2014-08-07
申请人： Michel Chornet , Christos Chronopoulos , Soumaine Dehkissia
发明人： Michel Chornet , Christos Chronopoulos , Soumaine Dehkissia
IPC分类号： C10G55/04 , C10G69/06 , C10G67/02
CPC分类号： C10G55/04 , C10G7/00 , C10G9/007 , C10G15/00 , C10G15/08 , C10G15/10 , C10G55/02 , C10G67/02 , C10G2300/302 , C10G2300/308
摘要： A process for treating heavy oil to provide a treated heavy oil having a reduced density and viscosity, as well as an olefin content that does not exceed 1.0 wt. %. The process comprises separating the initial heavy oil into a first fraction, which in general contains lower-boiling components, and a second fraction. The second fraction comprises a heavy oil having a p-value of at least 5% greater than the p-value of the initial heavy oil prior to separating the initial heavy oil into the first fraction and the second fraction, and the second fraction has an aromaticity that is no more than 5% less than the aromaticity of the initial heavy oil prior to separating the initial heavy oil into the first fraction and the second fraction. The second fraction then is upgraded to reduce the density and viscosity of the heavy oil. After the second fraction is upgraded, it is recombined with at least a portion of the first fraction to provide a treated heavy oil having an olefin content that does not exceed 1.0 wt. %. The separation of the initial heavy oil into first and second fractions enables one to achieve improved reduction of the density and viscosity of the treated heavy oil while maintaining the olefin content at an acceptable level.
摘要翻译：一种处理重油以提供具有降低的密度和粘度的处理过的重油以及不超过1.0重量％的烯烃含量的方法。％。该方法包括将初始重油分离成通常含有较低沸点组分的第一馏分和第二馏分。在将初始重油分离成第一馏分和第二馏分之前，第二馏分包含p值比初始重油的p值大至少5％的重油，第二馏分具有在将初始重油分离成第一馏分和第二馏分之前，初始重油的芳香度不超过5％的芳香度。然后第二级升级，以降低重油的密度和粘度。在第二级分升级之后，将其与至少一部分第一馏分重新组合以提供烯烃含量不超过1.0重量％的经处理的重油。％。将初始重油分离成第一和第二馏分使得能够在将烯烃含量保持在可接受的水平的同时实现经处理的重油的密度和粘度的改善的降低。

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