公开(公告)号：US20240050922A1

公开(公告)日：2024-02-15

申请号：US18267965

申请日：2021-12-09

申请人： IFP ENERGIES NOUVELLES

发明人： Nicolas LEGAGNEUX ,  Marie-Claire MARION ,  Karin BARTHELET ,  Patrick EUZEN ,  Joseph LOPEZ

IPC分类号： B01J20/08 ,  B01J20/32 ,  B01J20/28 ,  C10G25/05

CPC分类号： B01J20/08 ,  B01J20/3204 ,  B01J20/3236 ,  B01J20/28011 ,  B01J20/28061 ,  B01J20/28083 ,  B01J20/2809 ,  C10G25/05 ,  C10G2300/104 ,  C10G2400/02 ,  C10G2300/202

摘要： The present invention relates to a mass for trapping silicon compounds, comprising a porous alumina-based support and at least one metal chosen from the metals from groups VIB and VIIIB, and exhibiting a grain density of at least 1.20 g/ml, a specific surface of at least 300 m2/g and pores with a mean size of less than 6.5 nm, as determined by mercury porosimetry. The present invention also relates to a process for the preparation of said trapping mass and to a trapping process using said trapping mass.

公开(公告)号：US11891347B2

公开(公告)日：2024-02-06

申请号：US17584610

申请日：2022-01-26

申请人： Exelus Inc.

发明人： Mitrajit Mukherjee ,  Eric Daniel Gauthier ,  Kelly Ann Coley

IPC分类号： B01J29/06 ,  C07C2/58 ,  B01J29/08 ,  B01J29/70 ,  B01J37/30 ,  B01J37/02 ,  C01B39/20 ,  C01B39/02 ,  C01B39/46 ,  C10G29/20 ,  B01J29/90 ,  B01J29/12 ,  B01J38/10 ,  B01J29/74 ,  C07C2/56 ,  C07C2/54 ,  C07C9/14 ,  C07C9/16 ,  B01J29/14 ,  B01J37/08 ,  C10G99/00

CPC分类号： C07C2/58 ,  B01J29/08 ,  B01J29/082 ,  B01J29/084 ,  B01J29/087 ,  B01J29/088 ,  B01J29/123 ,  B01J29/126 ,  B01J29/143 ,  B01J29/7007 ,  B01J29/7057 ,  B01J29/7407 ,  B01J29/90 ,  B01J37/0201 ,  B01J37/024 ,  B01J37/08 ,  B01J37/30 ,  B01J38/10 ,  C01B39/026 ,  C01B39/20 ,  C01B39/46 ,  C07C2/54 ,  C07C2/56 ,  C07C9/14 ,  C07C9/16 ,  C10G29/205 ,  B01J2229/10 ,  B01J2229/18 ,  B01J2229/186 ,  B01J2229/20 ,  B01J2229/40 ,  C07C2529/08 ,  C07C2529/12 ,  C07C2529/14 ,  C07C2529/70 ,  C10G99/00 ,  C10G2300/104 ,  C10G2300/1081 ,  C10G2300/1092 ,  C10G2300/305 ,  C10G2300/70 ,  C10G2400/02 ,  Y02P20/584 ,  C07C2/58 ,  C07C9/16

摘要： Improved alkylation catalysts, alkylation methods, and methods of making alkylation catalysts are described. The alkylation method comprises reaction over a solid acid, zeolite-based catalyst and can be conducted for relatively long periods at steady state conditions. The alkylation catalyst comprises a crystalline zeolite structure, a Si/Al molar ratio of 20 or less, less than 0.5 weight percent alkali metals, and further having a characteristic catalyst life property. Some catalysts may contain rare earth elements in the range of 10 to 35 wt %. One method of making a catalyst includes a calcination step following exchange of the rare earth element(s) conducted at a temperature of at least 575° C. to stabilize the resulting structure followed by an deammoniation treatment. An improved method of deammoniation uses low temperature oxidation.

公开(公告)号：US11866663B1

公开(公告)日：2024-01-09

申请号：US18163556

申请日：2023-02-02

申请人： Saudi Arabian Oil Company

发明人： Mansour Ali Al-Herz ,  Ali Al Jawad ,  Qi Xu ,  Aaron Akah ,  Musaed Salem Al-Ghrami

IPC分类号： C10G69/04 ,  C07C4/06

CPC分类号： C10G69/04 ,  C07C4/06 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/301 ,  C10G2300/302 ,  C10G2300/308 ,  C10G2400/20 ,  C10G2400/22

摘要： Embodiments of the present disclosure are directed to a method of processing a hydrocarbon feed includes fractionating the hydrocarbon feed into a light stream and a heavy stream, hydrotreating the heavy stream to form a hydrotreated heavy stream, combining the light stream and the hydrotreated heavy stream to form a upgraded feed stream, and feeding the upgraded feed stream to a single Fluid Catalytic Cracking (FCC) reaction zone, thereby producing a product stream comprising light olefins. The light stream may comprise hydrocarbons boiling at less than 540° C. and the heavy stream may comprise hydrocarbons boiling at greater than 540° C. The FCC reaction zone may be operated in a down-flow configuration and the FCC may be operated under high severity conditions.

公开(公告)号：US20230193141A1

公开(公告)日：2023-06-22

申请号：US18060308

申请日：2022-11-30

申请人： PHILLIPS 66 COMPANY

发明人： Yangdong Pan

IPC分类号： C10G7/12 ,  G05B13/04

CPC分类号： C10G7/12 ,  G05B13/048 ,  C10G2300/301 ,  C10G2300/104 ,  C10G2300/1044

摘要： Processes and systems for controlling operation of a commercial refinery distillation column and/or splitter operable to separate hydrocarbons. An automated process controller (APC) receives signal from at least one analyzer that provides information about the concentration of at least a first chemical in a first fraction and a second chemical in a second fraction obtained from the distillation column. The APC comprises programming in the form of an algorithm that calculates real-time monetary values for the first chemical and the second chemical and alters the operation of the distillation column to change either the percentage of the first chemical in the second fraction or the percentage of the second chemical in the first fraction, thereby maximizing overall operational profit for the distillation column.

公开(公告)号：US20180273859A1

公开(公告)日：2018-09-27

申请号：US15996400

申请日：2018-06-01

申请人： UOP LLC

发明人： Stanley J. Frey ,  Hayim Abrevaya ,  Gregory R. Werba

IPC分类号： C10G63/04 ,  C10G35/06 ,  C10G35/22

CPC分类号： C10G63/04 ,  C07C4/18 ,  C07C2529/40 ,  C10G35/065 ,  C10G35/22 ,  C10G47/16 ,  C10G61/10 ,  C10G2300/1037 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/807 ,  C10G2400/20 ,  C10G2400/30 ,  C07C11/04 ,  C07C11/06 ,  C07C11/08 ,  C07C15/00

摘要： A process and apparatus for making aromatics are described. The process includes reforming a naphtha stream in a reforming zone to form a reformer effluent comprising aromatic compounds and non-aromatic compounds, wherein at least a portion of the aromatic compounds contain alkyl groups. The reformer effluent is heated and passed directly to an acid cracking reaction zone. The non-aromatic compounds are selectively cracked and at least a portion of the alkyl groups on the aromatic compounds are selectively dealkylated in the presence of an acid cracking catalyst to form a cracked reformer effluent comprising the aromatic compounds and cracked olefins.

公开(公告)号：US10011785B2

公开(公告)日：2018-07-03

申请号：US15035873

申请日：2014-11-20

申请人： UPM-Kymmene Corporation

发明人： Isto Eilos

IPC分类号： C10G3/00 ,  C01B3/38 ,  C01B3/48 ,  C10G65/00

CPC分类号： C10G65/00 ,  C01B3/38 ,  C01B3/48 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/047 ,  C01B2203/062 ,  C01B2203/1058 ,  C01B2203/1082 ,  C01B2203/1205 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/127 ,  C01B2203/148 ,  C10G3/50 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/104 ,  Y02P20/125 ,  Y02P30/20

摘要： The present invention relates to an integrated process for producing hydrocarbons, wherein feedstock originating from renewable sources is subjected to catalytic hydroprocessing followed by separation of an aqueous component, a heavy component, and a light component, separating carbon dioxide and hydrogen sulfide from said light component to obtain a recycle stream, followed by dividing the recycle stream to a first recycle stream and a second recycle stream, directing the first recycle stream to the hydroprocessing system, and the second recycle stream to a hydrogen plant, where the light component is converted to hydrogen, and directing the hydrogen to the hydroprocessing system.

公开(公告)号：US20180105756A1

公开(公告)日：2018-04-19

申请号：US15788249

申请日：2017-10-19

申请人： IFP Energies nouvelles

发明人： Adrien GOMEZ ,  Philibert LEFLAIVE ,  Clementina LOPEZ GARCIA ,  Annick PUCCI ,  Marie GODARD-PITHON ,  Jean-Luc NOCCA ,  Guobing ZHANG

IPC分类号： C10G65/16 ,  C10G65/00 ,  C10L1/06

CPC分类号： C10G65/16 ,  C10G45/02 ,  C10G45/32 ,  C10G49/22 ,  C10G65/00 ,  C10G65/02 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1088 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2400/02 ,  C10L1/06 ,  C10L2270/023 ,  C10L2290/543 ,  C10L2290/544

摘要： A process for the treatment of a gasoline containing sulphur-containing compounds, olefins and diolefins: a) fractionating the gasoline into at least: a light gasoline cut LCN; a primary intermediate gasoline cut, MCN; and a primary heavy gasoline cut HHCN; b) desulphurizing the primary intermediate gasoline cut MCN alone producing an at least partially desulphurized primary intermediate gasoline cut MCN; c) desulphurizing the primary heavy gasoline cut HHCN alone producing an at least partially desulphurized primary heavy gasoline cut HHCN; d) sending, as a mixture, the partially desulphurized primary intermediate gasoline cut MCN and the partially desulphurized primary heavy gasoline cut HHCN to a separation column separating a gaseous stream containing hydrogen and H2S, a secondary intermediate gasoline cut MCN with low sulphur and mercaptans contents and a secondary heavy gasoline cut HHCN containing sulphur-containing compounds including recombinant mercaptans; e) desulphurizing the secondary heavy gasoline cut HHCN obtained from step d).

公开(公告)号：US20170335204A1

公开(公告)日：2017-11-23

申请号：US15599939

申请日：2017-05-19

申请人： Ecolab USA Inc.

发明人： Kekeli Ekoue-Kovi ,  Ian Michael Jones

IPC分类号： C10G21/20

CPC分类号： C10G21/20 ,  C10G29/20 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/202 ,  C10G2300/207

摘要： The present invention generally relates to compositions and methods for scavenging hydrogen sulfide and/or mercaptans from fluids. More particularly, the invention relates to the use of compositions comprising a surfactant and the reaction product between a polyamine and a formaldehyde as a hydrogen sulfide or a mercaptan scavenger for hydrocarbon-containing fluids, particularly for natural gas, crude oil, field oil, fuel oil, naphtha, gasoline, kerosene, diesel, slurry oil, gas oil, resid, refinery gas, coal gas, tar, asphalt, coke gas, ammonia synthesis gas, gas from an industrial gas stream, or a sulfurization plant.

公开(公告)号：US09669382B2

公开(公告)日：2017-06-06

申请号：US14135750

申请日：2013-12-20

申请人： UOP LLC

发明人： Mohamed S. Shakur

IPC分类号： C07C5/22 ,  C07C5/13 ,  B01J19/24 ,  C10G45/62 ,  C10G45/58 ,  C10G70/04 ,  B01D53/22 ,  B01D53/68

CPC分类号： B01J19/24 ,  B01D53/228 ,  B01D53/68 ,  B01D2257/108 ,  B01D2257/2045 ,  C10G45/58 ,  C10G45/62 ,  C10G70/045 ,  C10G2300/104 ,  C10G2300/305 ,  C10G2300/4081 ,  C10G2300/42 ,  C10G2400/02

摘要： Methods and apparatuses are provided for isomerizing a hydrocarbon stream. The method includes isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream. The intermediate isomerized stream is fractionated to produce an off gas stream and a heavy isomerized stream, where the off gas stream includes an off gas recycle stream. The off gas recycle stream is dried in an off gas dryer to produce a hydrogen recycle stream, where the off gas drier includes an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream. The off dryer membrane includes a perfluorosulfonated ionomer. The hydrogen recycle stream is then fed into the reactor.

公开(公告)号：US20170152447A1

公开(公告)日：2017-06-01

申请号：US15324535

申请日：2015-07-06

申请人： SABIC GLOBAL TECHNOLOGIES B.V.

发明人： Thomas Hubertus Maria Housmans ,  Steve Turner

IPC分类号： C10G47/18 ,  C10L3/12 ,  C10G70/06

CPC分类号： C10G47/18 ,  C10G47/00 ,  C10G70/06 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/4081 ,  C10G2400/28 ,  C10G2400/30 ,  C10L3/12

摘要： The invention is directed to a process for producing BTX and LPG, comprising: a) contacting a feed stream comprising C5-C12 hydrocarbons in the presence of hydrogen with a hydrocracking catalyst in a hydrocracking reactor to produce a hydrocracking product stream comprising hydrogen, methane, LPG and BTX, b) separating the hydrocracking product stream into a first gas stream and a first liquid stream, c) separating the first gas stream to obtain a second gas stream comprising hydrogen and methane and a second liquid stream comprising LPG and BTX, wherein the separation is performed such that the second liquid stream is substantially free of hydrogen and methane, d) separating the second liquid stream into a third gas stream comprising LPG and a third liquid stream comprising BTX, wherein step (c) involves adding a part of the third liquid stream to the first gas stream to absorb the LPG in the first gas stream to obtain the second liquid stream or adding a part of the third liquid stream to a gas stream sep crated from the first gas stream to absorb the LPG in said gas stream separated from the first gas stream to obtain the second liquid stream.