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公开(公告)号：US11976245B2
公开(公告)日：2024-05-07
申请号：US17453799
申请日：2021-11-05
Inventor： Essam Abdullah Al-Sayed , Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner , Raghu Narayan , Meredith Lansdown
IPC: C10G69/06 , B01J19/24 , C10G9/36 , C10G21/00 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号：US11840673B2
公开(公告)日：2023-12-12
申请号：US17843990
申请日：2022-06-18
Inventor： Ujjal Mukherjee , Essam Abdullah Al-Sayed , Pedro Santos , Kareemuddin Shaik , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald M. Venner , Abdul Rahman Zafer Akhras
IPC: C10G69/06 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G47/30 , C10G49/02 , C10G21/00 , C10G47/26 , C10G55/04 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号：US20230340342A1
公开(公告)日：2023-10-26
申请号：US18344149
申请日：2023-06-29
Inventor： Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Essam Abdullah Al-Sayed , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald M. Venner
IPC: C10G69/06 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G47/30 , C10G49/02 , C10G21/00 , C10G47/26 , C10G55/04
CPC classification number: C10G69/06 , B01J19/245 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G47/30 , C10G49/02 , C10G21/003 , C10G47/26 , C10G55/04 , B01D3/06
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker
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公开(公告)号：US11753595B2
公开(公告)日：2023-09-12
申请号：US17843875
申请日：2022-06-17
Inventor： Ujjal Mukherjee , Essam Abdullah Al-Sayed , Pedro Santos , Kareemuddin Shaik , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald M. Venner , Abdul Rahman Zafer Akhras
IPC: C10G69/06 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G47/30 , C10G49/02 , C10G21/00 , C10G47/26 , C10G55/04 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号：US20220348834A1
公开(公告)日：2022-11-03
申请号：US17812808
申请日：2022-07-15
Inventor： Kareemuddin Shaik , Ujjal Mukherjee , Essam Abdullah Al-Sayed , Pedro Santos , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald M. Venner
IPC: C10G69/06 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G47/30 , C10G49/02 , C10G21/00 , C10G47/26 , C10G55/04
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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Patent Agency Ranking
公开(公告)号：US11180706B2
公开(公告)日：2021-11-23
申请号：US16820038
申请日：2020-03-16
Inventor： Essam Abdullah Al-Sayed , Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner , Raghu Narayan , Meredith Lansdown
IPC: C10G69/06 , C10G47/30 , C10G49/02 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G9/36 , C10G21/00 , C10G47/26 , C10G55/04 , B01D3/06 , B01D19/00
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号：US20200291311A1
公开(公告)日：2020-09-17
申请号：US16820038
申请日：2020-03-16
Inventor： Essam Abdullah Al-Sayed , Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner , Raghu Narayan , Meredith Lansdown
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号：US20200291310A1
公开(公告)日：2020-09-17
申请号：US16820249
申请日：2020-03-16
Inventor： Kareemuddin Shaik , Ujjal Mukherjee , Essam Abdullah Al-Sayed , Pedro Santos , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号：US20250051249A1
公开(公告)日：2025-02-13
申请号：US18797042
申请日：2024-08-07
Inventor： Kandasamy Sundaram , Essam Abdullah Al-Sayed , Ronald Venner , Kareemuddin Shaik , Ujjal Mukherjee , Mazin Tamimi , Peter Kuzma , Saud Al-Dulaijan , Pedro Santos , Ibrahim Abba , Theodorus L.M. Maesen , Khaled Al-Johani , Bala Ramachandran
Abstract: A process for converting whole crudes and other heavy hydrocarbon streams to produce ethylene. The process includes feeding a hydroprocessed medium boiling fraction, a hydroprocessed residue fraction, or both, and a light boiling fraction to a steam cracker and recovering a light fraction. The light fraction is fed to a first separator and recovering a C1-C3 stream and a mixed C4 and C4+ stream, comprising isoolefins, olefins, and dienes and feeding the mixed C4 and C4+ stream to a second separator and recovering a mixed C4 stream comprising isoolefins, olefins, and a C4+ stream. A portion of the mixed C4 stream is dimerized in a dimerization unit to produce a dimerized product stream, hydrogenated in a total hydrogenation system, producing a hydrogenated dimer product stream, and cracking the hydrogenated dimer product stream in a thermal cracking reactor system, producing one or more of hydrogen, methane, ethylene, propylene, n-butenes, and isobutene.
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公开(公告)号：US12098335B2
公开(公告)日：2024-09-24
申请号：US18344149
申请日：2023-06-29
Inventor： Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Essam Abdullah Al-Sayed , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald M. Venner
IPC: C10G69/06 , B01J19/24 , C10G9/36 , C10G21/00 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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