Invention Grant
- Patent Title: Process for C5+ hydrocarbon conversion
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Application No.: US17282418Application Date: 2019-11-04
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Publication No.: US11352576B2Publication Date: 2022-06-07
- Inventor: John R. DeLaney , John J. Monson , Teng Xu , Kendele S. Galvan
- Applicant: ExxonMobil Chemical Patents Inc.
- Applicant Address: US TX Baytown
- Assignee: ExxonMobil Chemical Patents Inc.
- Current Assignee: ExxonMobil Chemical Patents Inc.
- Current Assignee Address: US TX Baytown
- Priority: EP19152835 20190121
- International Application: PCT/US2019/059689 WO 20191104
- International Announcement: WO2020/096972 WO 20200514
- Main IPC: C10G69/06
- IPC: C10G69/06 ; B01D3/10 ; B01D3/14 ; B01D3/40 ; B01J19/24 ; C07C4/04 ; C07C4/06 ; C07C7/10

Abstract:
In some examples, a vapor phase product and a liquid phase product can be separated from a heated mixture that can include steam and a hydrocarbon. The liquid phase product can be catalytically cracked in the presence of a fluidized catalyst to produce a catalytically cracked effluent. A bottoms product can be separated from the catalytically cracked effluent. The bottoms product can be hydroprocessed to produce a hydroprocessed product. For example, the bottoms product can be hydroprocessed under pre-treater hydroprocessing conditions to produce a pre-treated bottoms product and the pre-treated bottoms product can be hydroprocessed under bottoms product hydroprocessing conditions to produce the hydroprocessed product. A hydroprocessor heavy product can be separated from the hydroprocessed product. The vapor phase product can be steam cracked to produce a steam cracker effluent. A tar product and an upgraded steam cracker effluent can be separated from the steam cracker effluent.
Public/Granted literature
- US20210380892A1 Process for C5+ Hydrocarbon Conversion Public/Granted day:2021-12-09
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