加氢和烯醛化均相络合催化具有活性高、选择性好、反应条件温和等优点,已被工业上大量采用。但由于反应物、催化剂、生成物处于同一液相中,反应后剩余的反应物、产物及倦化剂混合物需要分离,这不仅需要复杂的工艺,消耗能量,而且使收率降低和贵金属催化剂流失。该方法实际上只适合于C_5以下烯烃的反应。 Homogeneous hydrogenation and enalization complex catalyst with high activity, good selectivity, mild reaction conditions, etc., has been widely used in industry. However, since the reactants, the catalyst and the products are in the same liquid phase, the remaining reactants, products and the mixture of the burn-in agent need to be separated after the reaction, which requires not only complicated processes, energy consumption but also reduced yield and loss of noble metal catalyst . This method is only suitable for the reaction of olefins below C_5 in fact.