发明名称 GASOLINE DESULFURIZATION PROCESS
摘要 A catalytic cracked naphtha is desulfurized with minimum loss of olefins and octane. The naphtha is fed to a first distillation column reactor which acts as a depentanizer or dehexanizer with the lighter material containing most of the olefins and mercaptans being boiled up into a first distillation reaction zone where the mercaptans are reacted with diolefins to form sulfides which are removed in the bottoms along with any higher boiling sulfur compounds. The bottoms are subjected to hydrodesulfurization in a second distillation column reactor where the sulfur compounds are converted to H2S and removed. The lighter fraction containing most of the olefins is thus not subjected to the more harsh hydrogenation conditions of the second reactor.
申请公布号 EP0854901(A1) 申请公布日期 1998.07.29
申请号 EP19960924474 申请日期 1996.07.12
申请人 CHEMICAL RESEARCH & LICENSING COMPANY 发明人 HEARN, DENNIS;HICKEY, THOMAS, P.
分类号 C10G65/04;C10G35/06;C10G45/06;C10G45/08;C10G45/10;C10G45/32;C10G65/06 主分类号 C10G65/04
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