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公开(公告)号:US20200347309A1
公开(公告)日:2020-11-05
申请号:US16533510
申请日:2019-08-06
Applicant: Chevron U.S.A. Inc.
Inventor: Theodorus Ludovicus Michael MAESEN , Derek BLACKWELL , Viorel DUMA , Varut KOMALARAJUN , Alexander E. KUPERMAN , Hyunuk RYU , Horacio TREVINO , Alex YOON , Ujjal MUKHERJEE
Abstract: A catalyst system has been designed that disrupts the sedimentation process. The catalyst system achieves this by saturating key feed components before the feed components are stripped into their incompatible aromatic cores. The efficacy of this disruptive catalyst system is particularly evident in a hydrocracker configuration that runs in two-stage-recycle operation. The catalyst is a self-supported multi-metallic catalyst prepared from a precursor in the hydroxide form, and the catalyst must be toward the top level of the second stage of the two-stage system.
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公开(公告)号:US20220033723A1
公开(公告)日:2022-02-03
申请号:US17385782
申请日:2021-07-26
Applicant: Chevron U.S.A. Inc.
Inventor: Varut KOMALARAJUN , Theodorus Ludovicus Michael MAESEN
IPC: C10G67/02 , B01J23/888 , B01D3/14
Abstract: A hydrocracking process for converting a petroleum feed to lower boiling products. The process comprises hydrotreating a petroleum feed in a pre-treating zone in the presence of hydrogen to produce a hydrotreated effluent stream comprising a liquid product. At least a portion of the hydrotreated effluent stream is then passed to an MMS catalyst zone, and then to a hydrocracking zone. In one embodiment, the MMS catalyst zone comprises a self-supported multi-metallic catalyst prepared from a precursor in the oxide or hydroxide form. The percentage work of the hydrotreating in the pre-treating zone is maintained at a level of at least 56%.
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公开(公告)号:US20200048566A1
公开(公告)日:2020-02-13
申请号:US16533545
申请日:2019-08-06
Applicant: Chevron U.S.A. Inc.
Inventor: Theodorus Ludovicus Michael MAESEN , Derek BLACKWELL , Viorel DUMA , Varut KOMALARAJUN , Alexander E. KUPERMAN , Hyunuk RYU , Horacio TREVINO , Alex YOON , Ujjal MUKHERJEE
Abstract: A catalyst system has been designed that disrupts the sedimentation process. The catalyst system achieves this by saturating key feed components before the feed components are stripped into their incompatible aromatic cores. The efficacy of this disruptive catalyst system is particularly evident in a hydrocracker configuration that runs in two-stage-recycle operation. The catalyst is a self-supported multi-metallic catalyst prepared from a precursor in the hydroxide form, and the catalyst must be toward the top level of the second stage of the two-stage system.
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