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公开(公告)号:US11920094B2
公开(公告)日:2024-03-05
申请号:US16467294
申请日:2017-12-07
Applicant: SHELL OIL COMPANY
Inventor: Willem Derks
CPC classification number: C10G55/04 , C10G1/002 , C10G1/10 , C10G21/14 , C10G21/16 , C10G21/20 , C10G21/27 , C10G75/00 , C10G2300/1003 , C10G2300/202 , C10G2300/308
Abstract: The invention provides a method for pretreating a hydrocarbon steam cracker feed, comprising contacting the feed with a solvent to produce a pretreated feed having a reduced content of fouling components that cause fouling in the preheat, convection and radiant sections of the steam cracker and a rich solvent having an increased content of fouling components. The invention further provides a method for steam cracking hydrocarbons comprising: a) feeding a hydrocarbon steam cracker feed to the process; b) pretreating the feed by contacting the feed with a solvent to produce a pretreated feed having a reduced content of fouling components that cause fouling in the steam cracker and a rich solvent having an increased content of fouling components; c) heating the pretreated feed; and d) passing the pretreated feed through a steam cracker under cracking conditions to produce cracked products.
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公开(公告)号:US11891574B2
公开(公告)日:2024-02-06
申请号:US17441380
申请日:2020-04-14
Applicant: SHELL OIL COMPANY
Inventor: Jean-Paul Andre Marie Joseph Ghislain Lange , Luis Alberto Grau Lisnier , Willem Derks , Kai Jürgen Fischer
CPC classification number: C10G1/002 , C10G21/006 , C10G21/02 , C10G55/04 , C10G1/10
Abstract: The invention relates to a process for the recovery of aliphatic hydrocarbons from a liquid hydrocarbon feedstock stream, which comprises aliphatic hydrocarbons and additionally comprises aromatic hydrocarbons and/or polar components, said process comprising the steps of: feeding the liquid hydrocarbon feedstock stream to a first column; feeding a first solvent stream which comprises an organic solvent to the first column at a position which is higher than the position at which the liquid hydrocarbon feedstock stream is fed; contacting at least a portion of the liquid hydrocarbon feedstock stream with at least a portion of the first solvent stream; and recovering at least a portion of the aliphatic hydrocarbons by liquid-liquid extraction of aromatic hydrocarbons and/or polar components with organic solvent, resulting in a stream comprising recovered aliphatic hydrocarbons and optionally organic solvent and a bottom stream from the first column comprising organic solvent and aromatic hydrocarbons and/or polar components.
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