Propylene oxide process
    1.
    发明授权
    Propylene oxide process 失效
    环氧丙烷工艺

    公开(公告)号:US08207360B2

    公开(公告)日:2012-06-26

    申请号:US12657896

    申请日:2010-01-29

    IPC分类号: C07D301/12 C07D301/06

    摘要: A process for producing propylene oxide from propylene is disclosed. The process comprises reacting propylene and an oxidant selected from the group consisting of hydrogen peroxide and oxygen in a slurry comprising a catalyst and a solvent having a boiling point of 110° C. or lower to produce a reaction mixture. The reaction mixture including the catalyst is distilled to produce a vapor stream comprising propylene, propylene oxide, and at least a portion of the solvent, and a slurry stream comprising the solvent and the catalyst. At least a portion of the slurry stream is recycled to the reaction step.

    摘要翻译: 公开了一种由丙烯生产环氧丙烷的方法。 该方法包括在包含催化剂和沸点为110℃或更低的溶剂的浆料中使丙烯和选自过氧化氢和氧气的氧化剂反应以产生反应混合物。 包括催化剂的反应混合物被蒸馏以产生包含丙烯,环氧丙烷和至少一部分溶剂的蒸气流,以及包含溶剂和催化剂的浆料流。 将至少一部分浆料流再循环至反应步骤。

    Propylene oxide process
    2.
    发明申请
    Propylene oxide process 失效
    环氧丙烷工艺

    公开(公告)号:US20110190518A1

    公开(公告)日:2011-08-04

    申请号:US12657896

    申请日:2010-01-29

    IPC分类号: C07D301/06 C07D301/12

    摘要: A process for producing propylene oxide from propylene is disclosed. The process comprises reacting propylene and an oxidant selected from the group consisting of hydrogen peroxide and oxygen in a slurry comprising a catalyst and a solvent having a boiling point of 110° C. or lower to produce a reaction mixture. The reaction mixture including the catalyst is distilled to produce a vapor stream comprising propylene, propylene oxide, and at least a portion of the solvent, and a slurry stream comprising the solvent and the catalyst. At least a portion of the slurry stream is recycled to the reaction step.

    摘要翻译: 公开了一种由丙烯生产环氧丙烷的方法。 该方法包括在包含催化剂和沸点为110℃或更低的溶剂的浆料中使丙烯和选自过氧化氢和氧气的氧化剂反应以产生反应混合物。 包括催化剂的反应混合物被蒸馏以产生包含丙烯,环氧丙烷和至少一部分溶剂的蒸气流,以及包含溶剂和催化剂的浆料流。 将至少一部分浆料流再循环至反应步骤。

    Recovery of propane purge stream from a propylene oxide production process
    3.
    发明申请
    Recovery of propane purge stream from a propylene oxide production process 审中-公开
    从环氧丙烷生产过程中回收丙烷清洗流

    公开(公告)号:US20110147196A1

    公开(公告)日:2011-06-23

    申请号:US12655099

    申请日:2009-12-23

    申请人: Kimberly A. Petry

    发明人: Kimberly A. Petry

    IPC分类号: B01D3/14

    CPC分类号: B01D3/143

    摘要: A process for recovering a purified propane purge comprising fractionating in a first distillation column a feed stream comprising 2 to 10 wt % methanol, 5 to 20 wt % propylene, and 70 to 90 wt % propane thereby producing a first light product stream and a first heavy product stream, the first heavy product stream comprising less than 1.5 wt % propylene, and an amount of methanol that is at least 70 wt % of the methanol present in the first distillation column feed stream; and fractionating the first heavy product stream in a second distillation column at a pressure from 220 to 258 psia, thereby producing a second light product stream and a second heavy product stream, the second light product stream comprising at least 96 wt % propane and less than 1 wt. % methanol, and wherein an amount of propane present in the second light product stream is 20 to 45 wt % of the propane present in the first distillation column feed stream.

    摘要翻译: 一种用于回收纯化的丙烷吹扫的方法,包括在第一蒸馏塔中分馏含有2至10重量%甲醇,5至20重量%丙烯和70至90重量%丙烷的进料流,从而产生第一轻质产物流和第一 重产物流,包含小于1.5重量%丙烯的第一重质产物流和存在于第一蒸馏塔进料流中的甲醇的至少70重量%的甲醇量; 并在第二蒸馏塔中以220至258psia的压力对第一重质产物流进行分馏,由此产生第二轻质产物流和第二重质产物流,第二轻质产物流包含至少96重量%的丙烷和小于 1重量% %甲醇,并且其中存在于第二轻质产物流中的丙烷的量为第一蒸馏塔进料流中存在的丙烷的20至45重量%。