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    • 3. 发明授权
    • Process for the production of n-butanol
    • 正丁醇生产工艺
    • US5922921A
    • 1999-07-13
    • US957914
    • 1997-10-27
    • Jerry D. UnruhDebra A. RyanShannon L. Dugan
    • Jerry D. UnruhDebra A. RyanShannon L. Dugan
    • C07B61/00C07C29/141C07C31/12C07C29/14
    • C07C29/141C12C11/02
    • Disclosed is the use of a Raney cobalt catalyst in the hydrogenation process for the production of n-butanol.A process for the production of purified n-butanol comprising contacting in a hydrogenation zone n-butyraldehyde and hydrogen with an active porous cobalt catalyst under hydrogenation conditions of temperature and pressure for the production of alcohols from aldehydes, either in the substantial absence of water, or in the presence of water in an amount up to about 6 wt % based on the weight of the liquid hydrogenation reaction product to produce said reaction product comprising n-butanol, and purifying said reaction product by fractional distillation in the presence of about 0.01 to about 6 wt % of water, based on the total weight of feed to the fractionating column.
    • 公开了在氢化方法中使用阮内钴催化剂生产正丁醇。 包括生产纯正丁醇的方法,包括在氢化反应正丁醛和氢气与活性多孔钴催化剂的氢化条件下在温度和压力下进行接触,用于在基本上不含水的情况下从醛生产醇, 或在水存在下,基于液体氢化反应产物的重量,至多约6重量%的量存在,以产生包含正丁醇的所述反应产物,并通过在约0.01至约20℃的存在下通过分馏纯化所述反应产物 约6重量%的水,基于进料至分馏塔的总重量。