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公开(公告)号:US20230313053A1
公开(公告)日:2023-10-05
申请号:US18310091
申请日:2023-05-01
申请人: University of Dayton
发明人: Albert S. Vam , Giacomo Flora
IPC分类号: C10G53/14 , B01D3/14 , B01D11/04 , B01D17/02 , B01D61/16 , C10G21/16 , C10G21/28 , C10G27/04
CPC分类号: C10G53/14 , B01D3/14 , B01D11/0492 , B01D17/02 , B01D61/16 , C10G21/16 , C10G21/28 , C10G27/04 , B01D2311/2634 , B01D2311/2669 , B01D2311/2696 , B01D2325/38 , C10G2300/202 , C10G2300/4081 , C10G2400/04 , C10G2400/08
摘要: A desulfurization system has an oxidation process unit, and a multi-stage, liquid-liquid extraction unit in series with the oxidation process unit. The multi-stage, liquid-liquid extraction unit spits a fuel input from the oxidation process unit into a desulfurized fuel that is output for use, and a by-product. A solvent/sulfur/hydrocarbon separation process unit receives the by-product from the multi-stage, liquid-liquid extraction unit.
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公开(公告)号:US11661557B2
公开(公告)日:2023-05-30
申请号:US17201903
申请日:2021-03-15
申请人: University of Dayton
发明人: Albert S. Vam , Giacomo Flora
IPC分类号: C10G53/14 , B01D17/02 , B01D3/14 , B01D11/04 , B01D61/16 , C10G21/16 , C10G21/28 , C10G27/04
CPC分类号: C10G53/14 , B01D3/14 , B01D11/0492 , B01D17/02 , B01D61/16 , C10G21/16 , C10G21/28 , C10G27/04 , B01D2311/2634 , B01D2311/2669 , B01D2311/2696 , B01D2325/38 , C10G2300/202 , C10G2300/4081 , C10G2400/04 , C10G2400/08
摘要: A desulfurization system has an oxidation process unit, and a multi-stage, liquid-liquid extraction unit in series with the oxidation process unit. The multi-stage, liquid-liquid extraction unit spits a fuel input from the oxidation process unit into a desulfurized fuel that is output for use, and a by-product. A solvent/sulfur/hydrocarbon separation process unit receives the by-product from the multi-stage, liquid-liquid extraction unit.
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公开(公告)号:US20210309925A1
公开(公告)日:2021-10-07
申请号:US17201903
申请日:2021-03-15
申请人: University of Dayton
发明人: Albert S. Vam
IPC分类号: C10G53/14 , C10G27/04 , C10G21/28 , C10G21/16 , B01D3/14 , B01D11/04 , B01D17/02 , B01D61/16
摘要: A desulfurization system has an oxidation process unit, and a multi-stage, liquid-liquid extraction unit in series with the oxidation process unit. The multi-stage, liquid-liquid extraction unit spits a fuel input from the oxidation process unit into a desulfurized fuel that is output for use, and a by-product. A solvent/sulfur/hydrocarbon separation process unit receives the by-product from the multi-stage, liquid-liquid extraction unit.
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