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1. 发明公开

US20240287393A1 SYSTEMS AND PROCESSES FOR REFORMING A LIQUID HYDROCARBON FUEL 审中-公开
公开(公告)号：US20240287393A1
公开(公告)日：2024-08-29
申请号：US18655962
申请日：2024-05-06
申请人： Saudi Arabian Oil Company
发明人： Guanghui Zhu , Maryam M. Al-Taher , Qingyuan Hu
IPC分类号： C10G27/04 , B01J31/02 , B01J35/56 , B01J35/66 , C10G61/02 , C10L1/04 , F02M27/02 , F02M31/12 , F02M31/16
CPC分类号： C10G27/04 , B01J31/0271 , B01J35/56 , B01J35/66 , C10G61/02 , C10L1/04 , F02M27/02 , F02M31/12 , F02M31/16 , C10G2300/307 , C10G2300/4068 , C10G2300/80 , C10G2400/02 , C10L2200/0423 , C10L2270/02 , C10L2290/06 , C10L2290/24
摘要： According to one or more other aspects of the present disclosure, a system for reforming a liquid hydrocarbon fuel includes a mixing zone with a fuel intake fluidly coupled to a liquid hydrocarbon fuel source and an oxygen-containing gas intake fluidly coupled to an oxygen-containing gas source. The mixing zone further includes at least one atomizing nozzle and a fuel distribution zone downstream the at least on atomizing nozzle. The system also includes a catalyst reaction zone downstream the mixing zone, including a monolith block having a plurality of flow channels defined by monolith walls and a reforming catalyst coated onto the monolith walls. The atomizing nozzle generates a plurality of droplets comprising the liquid hydrocarbon fuel suspended in oxygen-containing gas. The fuel distribution zone distributes the plurality of droplets to each of the plurality of flow channels to contact the reforming catalyst including N-hydroxyphthalimide.

2. 发明申请

US20130020233A1 PROCESSES FOR CATALYTICALLY REFORMING NAPHTHA 有权
标题翻译：用于催化改性萘的方法
公开(公告)号：US20130020233A1
公开(公告)日：2013-01-24
申请号：US13480837
申请日：2012-05-25
申请人： Aizeng MA , Jieguang Wang , Jincheng Pan
发明人： Aizeng MA , Jieguang Wang , Jincheng Pan
IPC分类号： C10G35/04 , C10G61/04 , C10G61/06 , C10G63/04
CPC分类号： C10G61/02 , C07C4/04 , C10G9/36 , C10G21/16 , C10G21/20 , C10G21/22 , C10G35/04 , C10G61/04 , C10G61/06 , C10G63/04 , C10G2300/1044 , C10G2300/202 , C10G2400/02 , C10G2400/20 , C10G2400/30 , C07C11/04 , C07C15/04 , C07C15/06 , C07C15/08 , C07C11/06 , C07C11/167
摘要： Disclosed herein is a process for catalytically reforming naphtha, comprising, in the presence of hydrogen gas, contacting naphtha with at least one reforming catalyst under the conditions of a pressure ranging from 0.15 to 3.0 MPa, a temperature ranging from 300 to 540° C., a volume space velocity ranging from 2.1 to 50 h−1, to carry out a shallow catalytic reforming reaction so as to achieve a naphthene conversion ratio of greater than 85 mass %, and a conversion ratio of paraffins to arenes and C4− hydrocarbons of less than 30 mass %.
摘要翻译：本文公开了一种催化重整石脑油的方法，包括在氢气存在下，在压力范围为0.15-3.0MPa，温度范围为300-540℃的条件下，将石脑油与至少一种重整催化剂接触。，体积空间速度为2.1〜50h -1，进行浅催化重整反应，以获得大于85质量％的环烷烃转化率，和链烷烃与芳烃和C 4烃的转化率小于30质量％。

3. 发明申请

US20100155300A1 Process for producing gasoline of increased octane and hydrogen-containing co-produced stream 审中-公开
标题翻译：生产汽油增加辛烷值和含氢共同生产流的方法
公开(公告)号：US20100155300A1
公开(公告)日：2010-06-24
申请号：US12317513
申请日：2008-12-24
申请人： Craig Y. Sabottke , John Gerard Matragrano , Alberto Ravella , Katie Severson , Stuart S. Shih , Bal Krishan Kaul , Jeenok Theresa Kim , John Harland Thurtell
发明人： Craig Y. Sabottke , John Gerard Matragrano , Alberto Ravella , Katie Severson , Stuart S. Shih , Bal Krishan Kaul , Jeenok Theresa Kim , John Harland Thurtell
IPC分类号： C10G35/04 , C10G35/00
CPC分类号： C10G61/02 , C10G35/04 , C10G61/00 , C10G63/00 , C10G63/04
摘要： The present invention is directed to a process for producing an increased yield of gasoline of increased octane rating by the integration of a membrane separation processing step into the gasoline production process. The integrated process also increases hydrogen production from the reformer.
摘要翻译：本发明涉及通过将膜分离处理步骤整合到汽油生产过程中来提高辛烷值等级提高的汽油产率的方法。整合过程还增加了重整器的氢产量。

4. 发明申请

US20040251170A1 Method for desulfurization and reforming of hydrocarbon stock 审中-公开
标题翻译：碳氢化合物原料的脱硫和重整方法
公开(公告)号：US20040251170A1
公开(公告)日：2004-12-16
申请号：US10489280
申请日：2004-03-11
发明人： Osamu Chiyoda , Hikoichi Iwanami
IPC分类号： C10G029/04 , C10G031/08
CPC分类号： C01B3/38 , C01B2203/0233 , C01B2203/127 , C10G29/04 , C10G29/06 , C10G29/16 , C10G31/08 , C10G35/06 , C10G45/10 , C10G61/02 , C10G67/00
摘要： A method for desulfurization of hydrocarbon comprising reducing the sulfur content of hydrocarbons containing sulfur compounds, which comprises mixing the hydrocarbons containing sulfur compounds with water vapor, and contacting the resultant mixture with a catalyst comprising an inorganic oxide support and either platinum or palladium fixed to the support, and with a desulfurizing material at a temperature of 300null C. or higher.
摘要翻译：一种烃的脱硫方法，包括减少含硫化合物的烃的硫含量，其包括将含硫化合物的烃与水蒸气混合，并将所得混合物与包含无机氧化物载体和固定到在300℃以上的温度下使用脱硫材料。

5. 发明授权

US2717230A Catalytic reforming of hydrocarbon charge stocks high in nitrogen compounds 失效
标题翻译：碳氢化合物催化重整烃类化合物高
公开(公告)号：US2717230A
公开(公告)日：1955-09-06
申请号：US23239451
申请日：1951-06-19
申请人： UNIVERSAL OIL PROD CO
发明人： MURRAY MAURICE J , VLADIMIR HAENSEL , GROTE HENRY W
IPC分类号： C10G45/52 , C10G61/02 , C10G67/08
CPC分类号： C10G67/08 , C10G45/52 , C10G61/02

6. 发明授权

US11713424B2 Use of Aromax® catalyst in sulfur converter absorber and advantages related thereto 有权
公开(公告)号：US11713424B2
公开(公告)日：2023-08-01
申请号：US15896507
申请日：2018-02-14
申请人： Chevron Phillips Chemical Company LP
发明人： Ryan W. Snell , Scott G. Morrison , Vincent D. McGahee , Xianghong Hao , Gabriela Alvez-Manoli
IPC分类号： C10G61/00 , C10G61/06 , C10G35/04 , C10G45/02 , C10G69/08 , B01D53/14 , C10G59/02 , B01J29/62 , B01J37/02 , C10G61/02
CPC分类号： C10G61/06 , B01D53/1468 , B01J29/62 , B01J37/0201 , C10G35/04 , C10G45/02 , C10G59/02 , C10G61/02 , C10G69/08 , B01D2257/304 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4031 , C10G2300/70 , C10G2300/701 , C10G2400/30
摘要： A process for operating a reforming system by operating a reforming section containing a plurality of reactors, wherein each of the plurality of reactors containing a reforming catalyst capable of catalyzing the conversion of at least a portion of the hydrocarbons in a treated hydrocarbon stream into a reactor effluent comprising aromatic hydrocarbons, and operating a sulfur guard bed (SGB) to remove sulfur and sulfur-containing hydrocarbons from a hydrocarbon feed to provide the treated hydrocarbon stream, where the SGB contains at least a layer of a SGB catalyst comprising the same catalyst as the reforming catalyst, and where each reactor of the plurality of reactors within the reforming section may be operated at a higher operating temperature than an operating temperature of the SGB. A system for carrying out the process is also provided.

7. 发明授权

US11692206B2 Production of aromatics by reverse water gas shift, fermentation and recycling to pyrolysis 有权
公开(公告)号：US11692206B2
公开(公告)日：2023-07-04
申请号：US17484185
申请日：2021-09-24
申请人： IFP Energies Nouvelles
发明人： Jean-Francois Joly , Frederic Feugnet
IPC分类号： B01D3/14 , B01D11/04 , B01J19/24 , C10G61/02 , C10K3/02 , C12M1/00 , C12P7/06
CPC分类号： C12P7/06 , B01D3/143 , B01D11/0488 , B01D11/0492 , B01J19/245 , C10G61/02 , C10K3/026 , C12M21/12 , B01J2219/0004 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/30
摘要： Device and process for the conversion of a feedstock of aromatic compounds, in which the feedstock is treated notably by means of a fractionation train (4-7), a xylene separation unit (10) and an isomerization unit (11), and in which a pyrolysis unit (13) treats a second hydrocarbon feedstock, produces a pyrolysis effluent feeding the feedstock, and produces a pyrolysis gas comprising CO, CO2 and H2; a reverse water gas shift RWGS reaction section (50) treats the pyrolysis gas and produces an RWGS gas enriched in CO and in water; a fermentation reaction section (52) treats the RWGS gas enriched in CO and in water, to produce ethanol and recycle the ethanol to the inlet of the pyrolysis unit.

8. 发明公开

US20230183585A1 PROCESS FOR SEPARATING CYCLIC PARAFFINS 审中-公开
公开(公告)号：US20230183585A1
公开(公告)日：2023-06-15
申请号：US17954072
申请日：2022-09-27
申请人： UOP LLC
发明人： Ram Ganesh Rokkam , Amit Jain , Ashish Mathur , Nirlipt Mahapatra , PRASENJIT BASU SARKAR , SOURABH MAITHIL
IPC分类号： C10G61/02 , C10G63/04 , C10G69/08
CPC分类号： C10G61/02 , C10G63/04 , C10G69/08 , C10G2400/20 , C10G2300/4081
摘要： A feed stream of cyclic paraffins may be separated to obtain an overhead of methylcyclopentane or cyclohexane and a bottoms stream cyclohexane or methylcyclohexane. The overhead stream may be subjected to separation of normal paraffins from non-normal paraffins with the former being isomerized or the entire overhead stream may be isomerized. In a further embodiment, the bottoms stream may be subjected to steam cracking. In an additional embodiment, the feed stream of cyclic paraffins may be formerly subjected to aromatic saturation.

9. 发明申请

US20160145507A1 TWO-STAGE REFORMING PROCESS CONFIGURED FOR INCREASED FEED RATE TO MANUFACTURE REFORMATE AND BENZENE 审中-公开
标题翻译：两级改造工艺配置成增加进料速率，以制造改性剂和苯甲酸
公开(公告)号：US20160145507A1
公开(公告)日：2016-05-26
申请号：US14549271
申请日：2014-11-20
申请人： Stephen Joseph Miller
发明人： Stephen Joseph Miller
IPC分类号： C10G61/02 , C10L10/10 , C10L1/06
CPC分类号： C10G61/02 , C10G35/06 , C10G35/065 , C10G59/00 , C10L1/06 , C10L10/10 , C10L2200/0423 , C10L2270/023 , C10L2290/543
摘要： Described herein is a two-stage reforming process using a unique configuration which allows the reforming unit to operate at a higher naphtha feed rate as compared to conventional reforming configurations. In the unique reforming process described herein, a naphtha feedstock undergoes a distillation step prior to the first reforming stage. The distillation step separates the naphtha feedstock into a top light C6/C7 stream, which typically accounts for between 5 and 20 percent of the overall feedstock, and a C8+ stream. The C8+ stream undergoes reforming in a first stage consisting of at least one reactor containing conventional metallic reforming catalyst, under conditions sufficient to convert the C8+ stream into a first intermediate reformate. The C6/C7 stream, bypasses the first stage and is combined with the intermediate reformate, and reformed in the second stage, at lower pressure than in the first stage, over a reforming catalyst containing a medium pore zeolite.
摘要翻译：本文描述的是使用独特结构的两级重整方法，其允许重整单元与常规重整构型相比在更高的石脑油进料速率下操作。在本文所述的独特的重整方法中，石脑油原料在第一重整阶段之前进行蒸馏步骤。蒸馏步骤将石脑油原料分离成顶部轻质C6 / C7流，其通常占整个原料的5％至20％，和C8 +流。在足以将C8 +物流转化为第一中间重整产物的条件下，在包含常规金属重整催化剂的至少一个反应器组成的第一阶段中，C8 +物流进行重整。 C6 / C7流绕过第一阶段并与中间重整产物组合，并且在比第一阶段更低的压力下，在含有中孔沸石的重整催化剂上重新形成第二阶段。

10. 发明申请

US20140353209A1 PROCESS FOR TREATING A NAPHTHA STREAM 审中-公开
标题翻译：处理海蜇流程的过程
公开(公告)号：US20140353209A1
公开(公告)日：2014-12-04
申请号：US13904061
申请日：2013-05-29
申请人： UOP, LLC
发明人： Steven F. Zink
IPC分类号： C10G35/00
CPC分类号： C10G35/00 , C10G27/06 , C10G45/02 , C10G61/02 , C10G67/12 , C10G69/08 , C10G2400/30
摘要： One exemplary embodiment can be a process for treating a naphtha stream. The process may include providing the naphtha stream to a fractionation zone. The fractionation zone may include a fractionation column producing a first stream having one or more C5− hydrocarbons and a second stream withdrawn at a lower elevation on the fractionation column than the first stream and having one or more C5+ hydrocarbons, and sending at least a portion of the second stream to an aromatics complex for producing at least one of benzene, toluene, and para-xylene.
摘要翻译：一个示例性实施方案可以是用于处理石脑油流的方法。该方法可以包括将石脑油流提供到分馏区。分馏区可以包括分馏塔，其产生具有一个或多个C5-烃的第一流和在分馏塔上比第一流在较低高度处排出的具有一个或多个C5 +烃的第二流，并且发送至少一部分的第二物流转化成用于生产苯，甲苯和对二甲苯中的至少一种的芳族化合物。

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