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公开(公告)号:US11760706B2
公开(公告)日:2023-09-19
申请号:US17634956
申请日:2020-07-02
Inventor: Bhupender S. Minhas , Jeevan S. Abichandani , Marcus L. H. van Nuland , Wai Kit Cheng , Chong-Jhoo Wang , Robert G. Tinger
CPC classification number: C07C7/144 , B01D61/007 , C07C7/005 , B01D2317/025
Abstract: Selective removal of non-aromatic hydrocarbons from a xylene isomerization process for para-xylene production is accomplished using a membrane unit positioned within a xylene recovery loop. The membrane unit may include a one-stage or multi-stage (e.g., two-stage) membrane system and may be configured to separate a membrane unit product stream from a non-aromatics rich stream, which can be removed from the xylene recovery loop. The membrane unit may have a xylene permeance of about 60 gm/m2/hr/psi and a xylene to non-aromatic permeance ratio of about 15.
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公开(公告)号:US11999692B2
公开(公告)日:2024-06-04
申请号:US18363360
申请日:2023-08-01
Inventor: Bhupender S. Minhas , Jeevan S. Abichandani , Marcus L. H. Van Nuland , Wai Kit Cheng , Chong-Jhoo Wang , Robert G. Tinger
CPC classification number: C07C7/144 , B01D61/007 , C07C7/005 , B01D2317/025
Abstract: Selective removal of non-aromatic hydrocarbons from a xylene isomerization process for para-xylene production is accomplished using a membrane unit positioned within a xylene recovery loop. The membrane unit may include a one-stage or multi-stage (e.g., two-stage) membrane system and may be configured to separate a membrane unit product stream from a non-aromatics rich stream, which can be removed from the xylene recovery loop. The membrane unit may have a xylene permeance of about 60 gm/m2/hr/psi and a xylene to non-aromatic permeance ratio of about 15.
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公开(公告)号:US20230406789A1
公开(公告)日:2023-12-21
申请号:US18363382
申请日:2023-08-01
Inventor: Bhupender S. MINHAS , Jeevan S. Abichandani , Marcus L.H. Van Nuland , Wai Kit Cheng , Chong-Jhoo Wang , Robert G. Tinger
CPC classification number: C07C7/144 , B01D2317/025 , C07C7/005 , B01D61/007
Abstract: Selective removal of non-aromatic hydrocarbons from a xylene isomerization process for para-xylene production is accomplished using a membrane unit positioned within a xylene recovery loop. The membrane unit may include a one-stage or multi-stage (e.g., two-stage) membrane system and may be configured to separate a membrane unit product stream from a non-aromatics rich stream, which can be removed from the xylene recovery loop. The membrane unit may have a xylene permeance of about 60 gm/m2/hr/psi and a xylene to non-aromatic permeance ratio of about 15.
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