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公开(公告)号:US12128378B2
公开(公告)日:2024-10-29
申请号:US17310072
申请日:2020-01-14
发明人: Andrew Mark Ward , Scott Stevenson , Arno Oprins , Zhun Zhao , Tim Abbott , Kenneth Francis Lawson , Joseph William Schroer , Michael Edward Huckman
IPC分类号: B01J19/00 , B01D53/047 , B01D53/26 , B01J4/00 , B01J6/00 , B01J19/24 , C01B3/12 , C01B3/34 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/04 , C07C4/00 , C07C4/02 , C07C4/04 , C07C29/132 , C07C29/152 , F25J3/02 , H01M8/04082 , H01M8/0606 , H01M8/0612 , H02J15/00 , H01M8/1007
CPC分类号: B01J19/0053 , B01D53/047 , B01D53/265 , B01J4/008 , B01J6/008 , B01J19/0033 , B01J19/2465 , C01B3/12 , C01B3/342 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/0417 , C01C1/0488 , C07C4/02 , C07C4/04 , C07C29/132 , C07C29/152 , F25J3/0233 , H01M8/04201 , H01M8/0606 , H01M8/0618 , H02J15/006 , H02J15/008 , B01D2256/16 , B01D2256/245 , B01J2219/00051 , B01J2219/00132 , B01J2219/00761 , B01J2219/0871 , C01B2203/0216 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0294 , C01B2203/04 , C01B2203/061 , C01B2203/066 , C01B2203/068 , C01B2203/085 , C01B2203/148 , H01M8/1007
摘要: An olefin synthesis plant comprising: a feed pretreatment section configured to pretreat a feed stream; a pyrolysis section comprising one or more pyrolysis reactors configured to crack hydrocarbons in the feed stream in the presence of a diluent to produce a cracked gas stream; a primary fractionation and compression section configured to provide heat recovery from and quenching of the cracked gas stream; remove a component from the cracked gas stream; and compress the cracked gas stream, thus providing a compressed cracked gas stream; and/or a product separation section configured to separate a product olefin stream from the compressed cracked gas stream, wherein the olefin synthesis plant is configured such that, relative to a conventional olefin synthesis plant, more of the energy and/or the net energy required by the olefin synthesis plant and/or one or more sections thereof, is provided by a non-carbon based and/or renewable energy source and/or electricity.
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公开(公告)号:US20240351963A1
公开(公告)日:2024-10-24
申请号:US18638036
申请日:2024-04-17
发明人: Rosette Barias
CPC分类号: C07C2/06 , B01D3/009 , B01J19/245 , C07C1/22 , C07C7/09
摘要: Systems and processes for the production of a high purity isobutylene stream, a high purity isooctene stream or for the co-production of a high purity isobutylene and a high purity isooctene. The systems and processes advantageously process mixed C4 hydrocarbon streams via etherification, back cracking, isomerization, and/or dimerization, along with various separation systems, to produce the desired high purity streams.
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公开(公告)号:US20240351878A1
公开(公告)日:2024-10-24
申请号:US18137083
申请日:2023-04-20
发明人: Neeraj Saxena , Andrew Richardson , Blake Stapper , Guisu Liu
CPC分类号: C01B17/58 , B01J19/245 , B01J2219/0004
摘要: A RedOx furnace and process is provided for regenerating a spent sulfuric acid stream or other sulfur-containing stream by decomposing the spent sulfuric acid stream and/or other sulfur-containing stream to recover sulfur dioxide from the streams. The RedOx furnace includes a reduction chamber having an interior atmosphere, an oxidation chamber having an interior atmosphere positioned downstream from, and in fluid communication with, the reduction chamber, an inlet for supplying a spent sulfuric acid stream or other sulfur-containing stream into the interior atmosphere of the reduction chamber, and an inlet for supplying a pure oxygen stream into the interior atmosphere of the reduction chamber.
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公开(公告)号:US12122747B2
公开(公告)日:2024-10-22
申请号:US17603549
申请日:2020-07-02
申请人: LG CHEM, LTD.
发明人: Jae Hun Jeong , Sung Kyu Lee , Yeon Uk Choo , Seok Goo Lee
IPC分类号: C07C67/08 , B01D17/02 , B01D19/00 , B01J19/00 , B01J19/24 , C07C67/475 , C07C67/52 , C07C69/82
CPC分类号: C07C67/08 , B01D17/0214 , B01D19/0036 , B01J19/0013 , B01J19/245 , B01J19/2465 , C07C67/475 , C07C67/52 , C07C69/82 , B01J2219/00033 , B01J2219/00087 , B01J2219/00108 , C07C67/08 , C07C69/82
摘要: The present disclosure relates to a continuous production system and a diester-material production unit included therein, wherein the production unit includes a reaction device in which an esterification reaction of dicarboxylic acid and a primary alcohol is performed, a column in which gas-liquid separation of the primary alcohol and the water introduced is performed, a heat exchange device for recovering heat of a gas phase line of the column, a condenser installed at a rear end of the heat exchange device and liquefying a mixture of a gas-phase primary alcohol and water, and a layer separator in which the layer separation of a mixture of a liquefied primary alcohol and water is performed, wherein the heat exchange device includes one or more of a first heat exchanger for performing heat exchange with a raw material feed line of the reaction device, a second heat exchanger for performing heat exchange with a line through which a low temperature stream flows in a process, and a third heat exchanger for performing heat exchange with condensed water generated in the process. According to the present disclosure, the amount of a coolant used and the volume of steam of a reactor may be reduced, and the thermal efficiency of the entire process may be improved.
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公开(公告)号:US12116327B2
公开(公告)日:2024-10-15
申请号:US17415379
申请日:2019-12-18
申请人: Neste Oyj
发明人: Marina Lindblad , Kaisa Lamminpää , José Luis González Escobedo , Reetta Karinen , Eveliina Mäkelä , Riikka Puurunen
IPC分类号: C07C1/22 , B01J19/00 , B01J19/24 , B01J23/648 , B01J23/882 , B01J23/883 , B01J23/888
CPC分类号: C07C1/22 , B01J19/0013 , B01J19/245 , B01J23/6484 , B01J23/882 , B01J23/883 , B01J23/8885 , B01J2219/0004 , B01J2219/00051 , C07C2523/648 , C07C2523/882 , C07C2523/883 , C07C2523/888
摘要: A process for selective removal of hydroxyl groups from phenolic compounds is disclosed. The process uses a combination of catalytic hydrodeoxygenation and catalytic direct deoxygenation to convert alkylphenols into alkylbenzenes.
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公开(公告)号:US12115512B2
公开(公告)日:2024-10-15
申请号:US18257475
申请日:2022-04-28
申请人: STAMICARBON B.V.
IPC分类号: B01J19/24 , B01J19/00 , C07C273/04
CPC分类号: B01J19/24 , B01J19/0066 , B01J19/249 , C07C273/04 , B01J2219/2458
摘要: Embodiments of the disclosure pertain to a chemical reactor comprising a mixing zone comprising first static mixer and a second static mixer both arranged in shell of the reactor, wherein the second static mixer is positioned further from said first inlet than said first static mixer, wherein the second static mixer is adapted for more intimate mixing of fluids in the reaction mixture than the first static mixer.
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公开(公告)号:US20240326008A1
公开(公告)日:2024-10-03
申请号:US18743252
申请日:2024-06-14
申请人: NGK INSULATORS, LTD.
发明人: Kazuki IIDA , Kosuke NAKAGAWA , Hirofumi KAN , Atsushi TORII
CPC分类号: B01J19/2485 , B01J8/009 , B01J8/06 , B01J2208/021 , B01J2219/2402 , B01J2219/2404 , B01J2219/2408 , B01J2219/2423
摘要: A monolith-type reactor includes a porous support body, a plurality of first cells through which a raw material gas flows, a plurality of second cells through which the sweep gas flows, separation membranes, and a catalyst. The first cells pass through the porous support body in a first direction. The second cells extend in the porous support body in the first direction. The separate membranes are respectively formed on inner peripheral surfaces of the first cells and permeable to a product of the conversion reaction. The catalyst is arranged inside the separation membranes, and promotes the conversion reaction. In a cross section taken along a second direction perpendicular to the first direction, the average cross-sectional area of the first cells is larger than the average cross-sectional area of the second cells.
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公开(公告)号:US12104016B2
公开(公告)日:2024-10-01
申请号:US17391806
申请日:2021-08-02
申请人: THE BOEING COMPANY
IPC分类号: C08G73/02 , B01J19/00 , B01J19/24 , C09D179/02
CPC分类号: C08G73/0266 , B01J19/0093 , B01J19/2415 , B01J19/242 , B01J19/2425 , B01J19/243 , C09D179/02 , B01J2219/00087 , B01J2219/00164 , B01J2219/00795 , B01J2219/00822 , B01J2219/00831 , B01J2219/00833 , B01J2219/00837 , B01J2219/0086 , B01J2219/00867 , B01J2219/00869 , B01J2219/00873 , B01J2219/00889 , B01J2219/00963 , B01J2219/24
摘要: A flow reactor system and methods having tubing useful as polymerization chamber. The flow reactor has at least one inlet and at least one mixing chamber, and an outlet. The method includes providing two phases, an aqueous phase and a non-aqueous phase and forming an emulsion for introduction into the flow reactor.
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公开(公告)号:US12091619B2
公开(公告)日:2024-09-17
申请号:US18347923
申请日:2023-07-06
发明人: Miao Sun , Sohel K Shaikh , Wojciech Andrzej Supronowicz , Chandrasekar Subramani , Eman Z Albaher
CPC分类号: C10G47/04 , B01J19/24 , B01J23/002 , B01J23/83 , C10G69/06 , C10G2300/4006 , C10G2300/4012 , C10G2300/706 , C10G2400/30
摘要: A method for upgrading mixed pyrolysis oil may include contacting the mixed pyrolysis oil with hydrogen in the presence of a mixed metal oxide catalyst at reaction conditions to produce a reaction effluent including light aromatic compounds. The mixed pyrolysis oil includes multi-ring aromatic compounds and is formed from light pyrolysis oil and heavy pyrolysis oil at a ratio of 10:90 to 40:60 with light pyrolysis oil representing a bottom stream of a gas steam cracker and heavy pyrolysis oil representing a bottom stream of a naphtha steam cracker. The mixed metal oxide catalyst includes a plurality of catalyst particles with each catalyst particles including a plurality of metal oxides. An associated system for upgrading mixed pyrolysis oil may include a pyrolysis upgrading unit housing the mixed metal oxide catalyst and a separation unit operable to separate used mixed metal oxide catalyst from the reaction effluent.
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公开(公告)号:US12091617B2
公开(公告)日:2024-09-17
申请号:US17837651
申请日:2022-06-10
发明人: Xiaochun Xu , Dario Campani , Hyung Rae Kim
CPC分类号: C10G3/42 , B01D3/14 , B01J8/1818 , B01J8/24 , B01J19/245 , C10L1/04 , C11C3/003 , B01J2219/0004 , C10G2300/1003 , C10G2300/1014 , C10G2300/202 , C10G2400/02 , C10L2200/0484
摘要: A method may include: providing bio waste stream wherein the bio waste stream comprises at least one bio waste selected from the group consisting of palm oil mill effluent, soapstock, and combinations thereof; introducing the bio waste effluent stream into a fluidized catalytic cracking unit; contacting the bio waste with a catalyst in the fluidized catalytic cacking unit; and cracking at least a portion of the bio waste stream to form cracked products that comprise a cracked product stream.
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