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    • 46. 发明申请
    • PROCESS FOR PRODUCING CUMENE
    • 生产过程的方法
    • US20110201858A1
    • 2011-08-18
    • US13119789
    • 2009-09-23
    • Shyh-Yuan Henry HwangDana E. JohnsonJoseph C. PetersChung-Ming ChiKevin J. FallonFrancis A. Demers
    • Shyh-Yuan Henry HwangDana E. JohnsonJoseph C. PetersChung-Ming ChiKevin J. FallonFrancis A. Demers
    • C07C2/00
    • C07C409/10C07C2/66C07C2/864C07C29/145C07C37/08C07C45/53C07C407/00C07C2529/08C07C2529/18C07C2529/40C07C2529/65C07C2529/70C07C15/085C07C31/10C07C49/08C07C39/04
    • In a process for producing cumene from acetone and benzene, a feed stream comprising acetone is contacted with hydrogen in the presence of a hydrogenation catalyst in a first reaction zone under hydrogenation conditions sufficient to convert at least part of the acetone to isopropanol and produce a first liquid effluent stream rich in isopropanol and a first vapor stream rich in unreacted hydrogen. Benzene is then added to at least part of the first liquid effluent stream, without intermediate purification of the first liquid effluent stream, and optionally to at least part of the first vapor stream, to form a second feed stream. The second feed stream is then contacted with an alkylation catalyst in a second reaction zone separate from the first reaction zone under alkylation conditions sufficient to maintain at least part of the second feed stream in the liquid phase and to cause at least part of the isopropanol in the second feed stream to react with the benzene to form cumene and water and produce a second effluent stream comprising at least cumene, water and unreacted benzene. Hydrogen is separated from the first vapor stream and/or the second effluent stream. At least part of the hydrogen is recycled to the first reaction zone and/or purged from the system.
    • 在从丙酮和苯生产异丙基苯的方法中,在氢化条件下,在氢化催化剂存在下,将含丙酮的进料流与氢气接触,在氢化条件下,将至少部分丙酮转化成异丙醇,并产生第一 富含异丙醇的液体流出物流和富含未反应氢的第一蒸气流。 然后将苯添加到至少部分第一液体流出物流中,而不用第一液体流出物流的中间纯化,以及任选地至少部分第一蒸气流,形成第二进料流。 然后在足以将至少部分第二进料流保持在液相中并使至少部分异丙醇在烷基化条件下与第一反应区分离的第二反应区中的第二进料流与烷基化催化剂接触 所述第二进料流与苯反应以形成异丙基苯和水,并产生包含至少异丙基苯,水和未反应的苯的第二流出物流。 氢气与第一蒸气流和/或第二流出物流分离。 至少部分氢被再循环到第一反应区和/或从系统中清除。