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公开(公告)号:US11597883B2
公开(公告)日:2023-03-07
申请号:US17341161
申请日:2021-06-07
申请人: UOP LLC
发明人: Mark Lapinski , Ram Ganesh Rokkam , Gregory Funk
摘要: Favorable isomerization conditions for producing normal paraffins can produce olefins. The process for separating normal paraffins from non-normal paraffins by adsorption has a limit on olefin concentration, so the olefins must be removed. We propose to remove olefins from the isomerization effluent stream that is recycled to the adsorption separation process.
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公开(公告)号:US20220389335A1
公开(公告)日:2022-12-08
申请号:US17341161
申请日:2021-06-07
申请人: UOP LLC
发明人: Mark Lapinski , Ram Ganesh Rokkam , Gregory Funk
摘要: Favorable isomerization conditions for producing normal paraffins can produce olefins. The process for separating normal paraffins from non-normal paraffins by adsorption has a limit on olefin concentration, so the olefins must be removed. We propose to remove olefins from the isomerization effluent stream that is recycled to the adsorption separation process.
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公开(公告)号:US20230036734A1
公开(公告)日:2023-02-02
申请号:US17859917
申请日:2022-07-07
申请人: UOP LLC
IPC分类号: C10G35/06
摘要: A process increases the concentration of normal paraffins in a feed stream comprising separating a naphtha feed stream into a normal paraffin rich stream and a non-normal paraffin rich stream. A naphtha feed stream may be separated into a normal paraffin stream and a non-normal paraffin stream. An isomerization feed stream is taken from the non-normal paraffin stream and isomerized over an isomerization catalyst to convert non-normal paraffins to normal paraffins and produce an isomerization effluent stream. The isomerization effluent stream may be separated into a propane stream and a C4+ hydrocarbon stream optionally in a single column. The C4+ hydrocarbon stream may be recycled to the step of separating a naphtha feed stream.
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公开(公告)号:US12024681B2
公开(公告)日:2024-07-02
申请号:US17859917
申请日:2022-07-07
申请人: UOP LLC
IPC分类号: C10G35/06
CPC分类号: C10G35/06 , C10G2300/1037
摘要: A process increases the concentration of normal paraffins in a feed stream comprising separating a naphtha feed stream into a normal paraffin rich stream and a non-normal paraffin rich stream. A naphtha feed stream may be separated into a normal paraffin stream and a non-normal paraffin stream. An isomerization feed stream is taken from the non-normal paraffin stream and isomerized over an isomerization catalyst to convert non-normal paraffins to normal paraffins and produce an isomerization effluent stream. The isomerization effluent stream may be separated into a propane stream and a C4+ hydrocarbon stream optionally in a single column. The C4+ hydrocarbon stream may be recycled to the step of separating a naphtha feed stream.
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