申请人:Bayer Aktiengesellschaft
公开号:US04162946A1
公开(公告)日:1979-07-31
A process for concentrating at least one of (a) individual halogenoanthraquinones (b) binary mixtures of di-halogenoanthraquinones and (c) binary mixtures of trihalogenoanthraquinones, from a mixture containing at least two halogenoanthraquinones, comprising subjecting said mixture containing at least two halogenoanthraquinones to fractional vacuum distillation in a heated rectification column having an efficiency corresponding to about 20 to 50 theoretical stages with an absolute pressure at the top of about 0.5 to 50 mm Hg and a reflux to take-off ratio of about 5/1 to 50/1. Advantageously, distillation is carried out continuously in a cascade of columns, the products withdrawn from the top of the first column being 2-chloroanthraquinone in the first stage, 1-chloroanthraquinone in the second stage, 1,6- and 1,7-dichloroanthraquinone in the third stage and 1,5- and 1,8-dichloroanthraquinone in the fourth stage, 1,4,5- and 1,4,6-trichloroanthraquinone being obtained in the sump of the 4th stage and being separated therefrom by film evaporation. The mixture of halogenoanthraquinones is advantageously a mixture of chloroanthraquinones such as is obtained by the action of chlorine, chloric acid or a chlorate on various industrial mixtures of nitro- or sulfo-anthraquinones.
从含有至少两种卤代蒽醌的混合物中浓缩至少一种(a)单独的卤代蒽醌(b)二卤代蒽醌的二元混合物和(c)三卤代蒽醌的二元混合物的方法,包括将含有至少两种卤代蒽醌的混合物置于带有对应于约20至50个理论级的加热精馏柱中进行分级真空蒸馏,柱顶处的绝对压力约为0.5至50毫米汞柱,回流至提取比约为5/1至50/1。优选地,蒸馏在级联柱中连续进行,从第一柱的顶部提取的产品为第一级的2-氯蒽醌,在第二级为1-氯蒽醌,在第三级为1,6-和1,7-二氯蒽醌,在第四级为1,5-和1,8-二氯蒽醌,1,4,5-和1,4,6-三氯蒽醌在第4级的底部得到,并通过薄膜蒸发与之分离。卤代蒽醌的混合物优选地是氯代蒽醌的混合物,如通过氯、氯酸或氯酸盐对各种工业混合物的硝基或磺酸盐蒽醌的作用而获得的混合物。