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公开(公告)号:US12091620B2
公开(公告)日:2024-09-17
申请号:US18444846
申请日:2024-02-19
发明人: Bruce D. Murray , Scott G. Morrison , Kenneth Fountain , Steven R. Horlacher , Vincent D. Mcgahee , Reza Khankal , David Dockter
CPC分类号: C10G69/14 , C10G1/002 , C10G1/10 , C10G67/16 , C10G69/08 , C10G69/126 , C10G2300/1003 , C10G2400/20 , C10G2400/30
摘要: A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream.
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公开(公告)号:US11939542B1
公开(公告)日:2024-03-26
申请号:US18464570
申请日:2023-09-11
发明人: Bruce D. Murray , Scott G. Morrison , Kenneth Fountain , Steven R. Horlacher , Vincent D. Mcgahee , Reza Khankal , David Dockter
CPC分类号: C10G69/14 , C10G1/002 , C10G1/10 , C10G67/16 , C10G69/08 , C10G69/126 , C10G2300/1003 , C10G2400/20 , C10G2400/30
摘要: A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream.
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公开(公告)号:US11713424B2
公开(公告)日:2023-08-01
申请号:US15896507
申请日:2018-02-14
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.
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公开(公告)号:US12077713B2
公开(公告)日:2024-09-03
申请号:US18449865
申请日:2023-08-15
发明人: Ronald G. Abbott , Scott G. Morrison , Steven R. Horlacher , Jamie N. Sutherland , Bruce D. Murray , Jacob M. Hilbrich , Charles T. Polito
CPC分类号: C10B53/07 , C10G45/26 , C10G45/50 , C10G51/023 , C10G57/02 , C10G2300/1003 , C10G2400/04 , C10G2400/06 , C10G2400/20 , C10G2400/22 , C10G2400/28 , C10G2400/30
摘要: This disclosure relates to the production of chemicals and plastics using pyrolysis oil from the pyrolysis of plastic waste as a co-feedstock along with a petroleum-based, fossil fuel-based, or bio-based feedstock. In an aspect, the polymers and chemicals produced according to this disclosure can be certified under International Sustainability and Carbon Certification (ISCC) provisions as circular polymers and chemicals at any point along complex chemical reaction pathways. The use of a mass balance approach which attributes the pounds of pyrolyzed plastic products derived from pyrolysis oil to any output stream of a given unit has been developed, which permits ISCC certification agency approval.
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公开(公告)号:US20240191149A1
公开(公告)日:2024-06-13
申请号:US18444846
申请日:2024-02-19
发明人: Bruce D. Murray , Scott G. Morrison , Kenneth Fountain , Steven R. Horlacher , Vincent D. Mcgahee , Reza Khankal , David Dockter
CPC分类号: C10G69/14 , C10G1/002 , C10G1/10 , C10G67/16 , C10G69/08 , C10G69/126 , C10G2300/1003 , C10G2400/20 , C10G2400/30
摘要: A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream.
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公开(公告)号:US20240034699A1
公开(公告)日:2024-02-01
申请号:US18225967
申请日:2023-07-25
发明人: Steven M. Bischof , Gregory G. Hendrickson , Uriah J. Kilgore , Bruce E. Kreischer , Scott G. Morrison , Ryan W. Snell , Orson L. Sydora
摘要: The present disclosure relates to the integration of systems and methods associated with steam cracking, oligomerization reactions, hydrogenation reactions, and aromatization reactions for the production of benzene via the hydrogenation of oligomers produced from ethylene. In some aspects, the disclosed systems and methods utilize one or more of an oligomerization process, a hydrotreating process, and an aromatization process for producing a benzene comprising effluent. In further aspects, the systems and methods disclosed herein utilize one or more selective oligomerization catalyst systems.
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公开(公告)号:US11479726B2
公开(公告)日:2022-10-25
申请号:US17487714
申请日:2021-09-28
发明人: Ronald G. Abbott , Scott G. Morrison , Steven R. Horlacher , Jamie N. Sutherland , Bruce D. Murray
摘要: This disclosure relates to the production of chemicals and plastics using pyrolysis oil from the pyrolysis of plastic waste as a co-feedstock along with a petroleum-based, fossil fuel-based, or bio-based feedstock. In an aspect, the polymers and chemicals produced according to this disclosure can be certified under International Sustainability and Carbon Certification (ISCC) provisions as circular polymers and chemicals at any point along complex chemical reaction pathways. The use of a mass balance approach which attributes the pounds of pyrolyzed plastic products derived from pyrolysis oil to any output stream of a given unit has been developed, which permits ISCC certification agency approval.
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公开(公告)号:US10052602B2
公开(公告)日:2018-08-21
申请号:US15629967
申请日:2017-06-22
发明人: Cori A. Demmelmaier-Chang , Daniel M. Hasenberg , Scott H. Brown , Vincent D. McGahee , Scott G. Morrison
CPC分类号: B01J8/009 , B01J8/0214 , B01J8/0278 , B01J8/0285 , B01J8/0403 , B01J8/0419 , B01J8/0492 , B01J8/0496 , B01J2208/00212 , B01J2208/0053 , B01J2208/00893 , B01J2208/027 , C01B3/501 , C07C5/41
摘要: The present invention discloses aromatization reactor vessels with hydrogen membrane tubes, and associated aromatization reactor vessel systems. Also disclosed are processes for conducting aromatization reactions utilizing these reactor vessels and systems.
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公开(公告)号:US11802250B1
公开(公告)日:2023-10-31
申请号:US18054169
申请日:2022-11-10
发明人: Bruce D. Murray , Scott G. Morrison , Kenneth Fountain , Steven R. Horlacher , Vincent D. Mcgahee , Reza Khankal , David Dockter
CPC分类号: C10G69/14 , C10G1/002 , C10G1/10 , C10G67/16 , C10G69/08 , C10G69/126 , C10G2300/1003 , C10G2400/20 , C10G2400/30
摘要: A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream.
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公开(公告)号:US11781073B2
公开(公告)日:2023-10-10
申请号:US18053518
申请日:2022-11-08
发明人: Ronald G. Abbott , Scott G. Morrison , Steven R. Horlacher , Jamie N. Sutherland , Bruce D. Murray , Jacob M. Hilbrich , Charles T. Polito
CPC分类号: C10B53/07 , C10G45/26 , C10G45/50 , C10G51/023 , C10G57/02 , C10G2300/1003 , C10G2400/04 , C10G2400/06 , C10G2400/20 , C10G2400/22 , C10G2400/28 , C10G2400/30
摘要: This disclosure relates to the production of chemicals and plastics using pyrolysis oil from the pyrolysis of plastic waste as a co-feedstock along with a petroleum-based or fossil fuel co-feed, or as a feedstock in the absence of a petroleum-based or fossil fuel co-feed. A mass balance accounting approach is employed to attribute the pounds of pyrolyzed plastic products derived from pyrolysis oil to any output stream of a given unit, which permits assigning circular product credit to product streams. In an aspect, the polymers and chemicals produced according to this disclosure can be certified under International Sustainability and Carbon Certification (ISCC) provisions as circular polymers and chemicals at any point along complex chemical reaction pathways.
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