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    • 3. 发明授权
    • Hydroformylation process including catalyst recycle
    • 加氢甲酰化工艺,包括催化剂循环
    • US08541627B2
    • 2013-09-24
    • US13001922
    • 2009-08-19
    • Eddy T. A. Van DriesscheRonald D. GartonCorey W. Reed
    • Eddy T. A. Van DriesscheRonald D. GartonCorey W. Reed
    • C07C45/50C07C29/14
    • C07C45/50C07C45/80Y02P20/584C07C47/02
    • An improved hydroformylation catalyst cycle is disclosed wherein the cobalt catalyst is recycled to the hydroformylation reaction mainly as a water soluble carbonyl salt, obtained from extraction of the acidic form of the homogeneous cobalt carbonyl catalyst from the hydroformylation product with an aqueous solution of a salt of a weaker acid. The organic product after extraction is submitted to a further demetalling step in the presence of a dilute acid and an oxidant. The water from this further demetalling step is suitable for use in the upstream extraction step. A free water phase present in the hydroformylation reaction product may be separated upstream from the extraction step and is suitable for use in the further demetalling step, such that the catalyst cycle has no waste water stream.
    • 公开了一种改进的加氢甲酰化催化剂循环,其中主要以水溶性羰基盐将钴催化剂再循环至加氢甲酰化反应,该水溶性羰基盐是从加氢甲酰化产物中提取酸性形式的均匀钴羰基催化剂得到的, 酸弱。 提取后的有机产物在稀酸和氧化剂存在下进一步脱金属步骤。 来自该进一步脱金属步骤的水适用于上游萃取步骤。 存在于加氢甲酰化反应产物中的游离水相可以从萃取步骤的上游分离,并且适合用于进一步脱金属步骤,使得催化剂循环不含废水流。
    • 8. 发明授权
    • Alcohol hydrogenation with intermediate recycle
    • 酒精氢化与中间回收
    • US5877358A
    • 1999-03-02
    • US717980
    • 1996-09-23
    • Ronald D. GartonDonald Q. BrownMagdiel Agosto
    • Ronald D. GartonDonald Q. BrownMagdiel Agosto
    • C07C29/141C07C29/16C07C29/14
    • C07C29/141
    • In the process of hydrogenating a crude aldehyde product formed from the oxo process into a crude alcohol product, which process includes: feeding the crude aldehyde product into a first reactor which contains a hydrogenation catalyst, thereby forming a first hydrogenated product; feeding the first hydrogenated product from the first reactor through at least one intermediate reactor, each intermediate reactor being connected in series and containing a hydrogenation catalyst, thereby forming at least one intermediate hydrogenated product; and feeding the intermediate hydrogenated product from a last intermediate reactor to a final reactor which contains a hydrogenation catalyst, thereby forming the crude alcohol product; the improvement including a step wherein: at least a portion of the first hydrogenated product is recycled to the first hydrogenation reactor; or at least a portion of the intermediate hydrogenated product is recycled to the first hydrogenation reactor or an intermediate reactor upstream of the intermediate reactor from which the intermediate hydrogenated product is removed.
    • 在将由羰基过程形成的粗醛产物氢化成粗醇产物的过程中,该方法包括:将粗醛产物进料到含有氢化催化剂的第一反应器中,从而形成第一氢化产物; 将来自第一反应器的第一氢化产物通过至少一个中间反应器进料,每个中间反应器串联连接并含有氢化催化剂,从而形成至少一种中间氢化产物; 并将中间体氢化产物从最后一个中间反应器进料至含有氢化催化剂的最终反应器,由此形成粗醇产物; 改进包括以下步骤:将至少一部分第一氢化产物再循环至第一氢化反应器; 或至少部分中间体氢化产物再循环至中间体反应器上游的第一氢化反应器或中间体反应器的中间体反应器,中间体氢化产物从中间体反应器中脱除。