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Process for the hydroformylation of olefins having 20 to 400 carbon atoms.

机译:具有20至400个碳原子的烯烃的加氢甲酰化方法。

摘要

Process for the hydroformylation of olefins containing 20 to 400 carbon atoms by reaction of the olefin with the synthesis gas in the presence of a catalyst of cobalt carbonyl and recovery of the cobalt catalyst by extraction of the reaction product with an acidic aqueous solution in the presence of oxygen and separation of the organic and aqueous phases, characterized in that (a) the aqueous phase is separated by a combination of (i) sedimentation and / or centrifugation, and (ii) one or more mechanical stages of coalescence , the organic phase so that the ratio of the aqueous phase dispersed in the organic phase is 0.5% by weight or less, based on the organic phase; and (b) is subjected to the organic phase obtained in step (a), to an electric field to coalesce the residual aqueous phase, dispersed.
机译:在羰基钴催化剂存在下,通过烯烃与合成气反应,使含20至400个碳原子的烯烃加氢甲酰化的方法,以及在酸性条件下,用酸性水溶液萃取反应产物,回收钴催化剂氧和有机相和水相的分离,其特征在于(a)通过(i)沉淀和/或离心分离以及(ii)一个或多个机械合并阶段(有机相)的组合来分离水相相对于有机相,分散在有机相中的水相的比例为0.5重量%以下。使(b)步骤(a)中获得的有机相经受电场以聚结分散的残余水相。

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