发明名称 Process for reducing the benzene content of gasoline
摘要 A process is described for alkylating benzene contained in a refinery gasoline stream, in which the refinery gasoline stream is contacted with an alkylating agent comprising one or more C2 to C5 olefins in an alkylation reaction zone under alkylation conditions to produce an alkylated effluent. The alkylation reaction zone comprises at least a first alkylation reaction stage and a second alkylation reaction stage and a portion of said alkylating agent is fed to each of said first and second alkylation reaction stages so that, although the molar ratio of alkylatable aromatic to alkylating agent in the total feed to the alkylation reaction zone is less than 1, the molar ratio of alkylatable aromatic to alkylating agent at the inlet of each of the first and second alkylation reaction stages is at least 1.0.
申请公布号 US9598330(B2) 申请公布日期 2017.03.21
申请号 US201114238592 申请日期 2011.11.30
申请人 BADGER LICENSING 发明人 Hwang Shyh-Yuan H.;Birkhoff Ronald;Guarino Richard F.;Moy J. Erik;Pherwani Geeta
分类号 C07C2/66;C07C2/64;C10G29/20 主分类号 C07C2/66
代理机构 Roberts Mlotkowski Safran Cole & Calderon P.C. 代理人 Roberts Mlotkowski Safran Cole & Calderon P.C.
主权项 1. A process for alkylating benzene contained in a refinery gasoline stream, said process comprising contacting said refinery gasoline stream with an alkylating agent comprising one or more C2 to C5 olefins in an alkylation reaction zone under alkylation conditions to produce an alkylated effluent, wherein said alkylation reaction zone consists of a first alkylation reaction stage and a second alkylation reaction stage, wherein a portion of said alkylating agent is fed to each of said first and second alkylation reaction stages so that the molar ratio of alkylatable aromatic to alkylating agent in the total feed to the alkylation reaction zone is less than 1, and the molar ratio of alkylatable aromatic to alkylating agent at the inlet of each of said first and second alkylation reaction stages is at least 1.0, wherein the alkylation reaction in each of said first and second alkylation reaction stages takes place over a catalyst comprising an MWW zeolite.
地址 Boston MA US