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    • 10. 发明授权
    • Method for the continuous production of unsaturated carboxylic acid anhydrides
    • 连续生产不饱和羧酸酐的方法
    • US08084640B2
    • 2011-12-27
    • US12299217
    • 2007-03-14
    • Dirk BroellHermann Siegert
    • Dirk BroellHermann Siegert
    • C07C65/00
    • C07C51/56C07C51/567Y02P20/582C07C57/04
    • Process for continuously preparing unsaturated carboxylic anhydrides of the general formula I R—C(O)—O—C(O)—R  (I) in which R is an unsaturated organic radical having 2 to 12 carbon atoms by transanhydridization of an aliphatic carboxylic anhydride with a carboxylic acid of the general formula II R—COOH  (II) in which R is as defined above in a rectification column having an upper, middle and lower region, characterized in that f) an inert boiling oil is initially charged in the bottom of the column, g) the reactants are fed into a reaction region in stoichiometric ratios, h) the carboxylic acid formed as the by-product is withdrawn at the top of the column, i) the unconverted reactants are recycled into the reaction region and j) the product of the formula I is obtained via a side draw, preferably between the middle and lower column region.
    • 用于连续制备通式IR-C(O)-O-C(O)-R(I)的不饱和羧酸酐的方法,其中R是具有2至12个碳原子的不饱和有机基团,通过脂族羧酸酐的反式氢化 与具有上,中,下区域的精馏塔中的R如上定义的通式II R-COOH(II)的羧酸反应,其特征在于f)惰性沸腾油最初装入底部 ,g)将反应物以化学计量比进料到反应区域中,h)作为副产物形成的羧酸在塔的顶部排出,i)将未转化的反应物再循环到反应区域中, j)式I的产物通过侧拉取得,优选在中间和下部区域之间。