Multiple vapor feeds for hydrogenation process to produce alcohol
    2.
    发明授权
    Multiple vapor feeds for hydrogenation process to produce alcohol 有权
    多个蒸气进料用于氢化过程产生醇

    公开(公告)号:US08927790B2

    公开(公告)日:2015-01-06

    申请号:US13547162

    申请日:2012-07-12

    CPC classification number: C07C29/149 Y02P20/582 C07C31/08

    Abstract: The present invention relates to processes for the recovery of ethanol from a crude ethanol product obtained from the hydrogenation of acetic acid. The crude ethanol product is separated in a column to produce a distillate stream comprising ethyl acetate, ethanol and acetaldehyde and a residue stream comprising ethanol, acetic acid and water. The ethanol product is recovered from the residue stream. A liquid recycle stream is sent to a second vaporizer to form a second vapor feed stream that is fed to the hydrogenation reactor.

    Abstract translation: 本发明涉及从乙酸氢化获得的粗乙醇产物中回收乙醇的方法。 将粗乙醇产物在柱中分离以产生包含乙酸乙酯,乙醇和乙醛的馏出物流和包含乙醇,乙酸和水的残余物流。 从残余物流中回收乙醇产物。 将液体再循环流送入第二蒸发器以形成进料到氢化反应器的第二蒸气进料流。

    Integrated process for the production of vinyl acetate from acetic acid via ethylene
    5.
    发明授权
    Integrated process for the production of vinyl acetate from acetic acid via ethylene 有权
    通过乙烯从乙酸生产乙酸乙烯酯的综合方法

    公开(公告)号:US08309757B2

    公开(公告)日:2012-11-13

    申请号:US13310290

    申请日:2011-12-02

    Abstract: This invention provides an integrated two stage economical process for the production of vinyl acetate monomer (VAM) from acetic acid in the vapor phase. First, acetic acid is selectively hydrogenated over a hydrogenating catalyst composition to form ethylene either in a single reactor zone or in a dual rector zone wherein the intermediate hydrogenated products are either dehydrated and/or cracked to form ethylene. In a subsequent second stage so formed ethylene is reacted with molecular oxygen and acetic acid over a suitable catalyst to form VAM. In an embodiment of this invention reaction of acetic acid and hydrogen over a hydrogenation catalyst and subsequent reaction over a dehydration catalyst selectively produces ethylene, which is further mixed with acetic acid and molecular oxygen and reacted over a supported palladium/gold/potassium catalyst.

    Abstract translation: 本发明提供了一种用于在蒸气相中从乙酸生产乙酸乙烯酯单体(VAM)的综合两阶段经济方法。 首先,在氢化催化剂组合物中选择氢化乙酸,以在单个反应器区域或双重反应器区域中形成乙烯,其中中间氢化产物被脱水和/或裂化形成乙烯。 在随后的第二阶段中,如此形成的乙烯通过合适的催化剂与分子氧和乙酸反应以形成VAM。 在本发明的一个实施方案中,乙酸和氢气在氢化催化剂上的反应和随后的脱水催化剂反应选择性地产生乙烯,其进一步与乙酸和分子氧混合并在负载的钯/金/钾催化剂上反应。

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