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    • 88. 发明授权
    • Catalyst recovery in the production of 2,5-dihydrofuran by isomerization
of vinyl oxirane
    • 通过乙烯基环氧乙烷的异构化生产2,5-二氢呋喃的催化剂回收
    • US6096673A
    • 2000-08-01
    • US66478
    • 1998-04-21
    • Martin Fischer
    • Martin Fischer
    • B01J31/40B01J38/00C07D307/28B01J20/34B01J38/48B01J38/54B01J38/56B01J38/68
    • B01J31/0265B01J31/0247B01J31/26B01J31/30B01J31/4015B01J31/403B01J31/4053C07D307/28B01J2231/52B01J27/08B01J31/1875Y02P20/584
    • An improved process is provided for the recovery of catalyst components from oligomeric impurities which are formed during the industrial preparation of 2,5-dihydrofuran by the catalytic isomerization of vinyl oxirane followed by an essential separation of the oligomeric by-products which otherwise cause deactivation of the catalyst. The catalyst components consist essentially of (a) an onium iodide and (b) a Lewis acid selected from the group consisting of the chloride, bromide or iodide of the metals zinc, tin, cobalt and bismuth, preferably zinc, where the catalyst optionally includes a donor ligand. This separation is carried out by the steps of extracting the initial product mixture containing zinc, cobalt or bismuth halides as Lewis acids with hydrocarbons or chlorinated hydrocarbons containing from 5 to 14 carbon atoms in order to form two separate phases on standing, separating off the extraction solvent phase which contains the dissolved catalyst and then recovering the separated catalyst by distilling off the extraction solvent. The recovery of tin iodide requires the presence of a special onium halide component such as phosphazenium or phosphazanium halides, preferably the iodides, having a high molecular weight and especially those which contain from 16 to 72 carbon atoms while remaining soluble in the extracting agent.
    • PCT No.PCT / EP96 / 04504 Sec。 371日期:1998年4月21日 102(e)1998年4月21日PCT PCT 1996年10月17日PCT公布。 公开号WO97 / 15392 日期1997年5月1日提供了一种改进的方法,用于通过乙烯基环氧乙烷的催化异构化在二恶烷的工业制备期间形成的低聚杂质回收催化剂组分,然后分解低聚副产物, 否则会导致催化剂失活。 催化剂组分基本上由(a)碘化铱和(b)选自金属锌,锡,钴和铋,优选锌的氯化物,溴化物或碘化物的路易斯酸,其中催化剂任选地包括 供体配体。 该分离通过以下步骤进行:将含有锌,钴或卤化铋作为路易斯酸的初始产物混合物与含有5至14个碳原子的烃或氯化烃一起提取,以便在静置时形成两个分开的相,分离萃取物 溶剂相,其含有溶解的催化剂,然后通过蒸馏出萃取溶剂回收分离的催化剂。 碘化锡的回收需要存在特别的卤化鎓成分,例如具有高分子量的磷腈鎓或磷酰卤卤化物,优选碘化物,特别是含有16至72个碳原子的那些,同时保持溶于萃取剂中。