首页> 外国专利> METHOD FOR THE CONTINUOUS SEPARATION OF MIXTURES COMPRISING MORPHONLINE (MO), MONOAMINODIGLYCOL (ADG), AMMONIA AND WATER BY MEANS OF DISTILLATION

METHOD FOR THE CONTINUOUS SEPARATION OF MIXTURES COMPRISING MORPHONLINE (MO), MONOAMINODIGLYCOL (ADG), AMMONIA AND WATER BY MEANS OF DISTILLATION

机译:蒸馏法连续分离含吗啉(MO),单胺二乙醇(ADG),氨和水的混合物的方法

摘要

Processes for the continuous fractional distillation of a mixture comprising morpholine (MO), monoaminodiglycol (ADG), ammonia and water from a reaction of diethylene glycol (DEG) with ammonia, the process comprising: (i) separating off ammonia from the mixture at a top of a first distillation column K10; (ii) feeding a bottom fraction from the first distillation column to a second distillation column K20, wherein water and an organic product are separated off at a top of the second distillation column at a top temperature of 45 to 198° C. and a pressure in the range from 0.1 to 15 bar; (iii) feeding a bottom fraction from the second distillation column to a third distillation column K30, wherein morpholine and an organic product having a boiling point of 140° C. (1.013 bar) are separated off at a point selected from a top and a side offtake of the third distillation column, and monoaminodiglycol and an organic product having a boiling point of 190° C. (1.013 bar) are separated off at a bottom of the third ditillation column, and (iv) feeding the morpholine-comprising stream from the third distillation column to a fourth column K40, wherein morpholine is separated off at a side offtake of the fourth column, an organic product having a boiling point of ≦128° C. (1.013 bar) is separated off at a top of the fourth distillation column and an organic product having a boiling point of ≧128° C. (1.013 bar) is separated off at a bottom of the fourth distillation column.
机译:从二甘醇(DEG)与氨的反应中连续分馏包含吗啉(MO),单氨基二甘醇(ADG),氨和水的混合物的方法,该方法包括:(i)在第一蒸馏塔K10的顶部; (ii)将塔底馏分从第一蒸馏塔进料至第二蒸馏塔K20,其中在第二蒸馏塔的顶部在45至198℃的最高温度和压力下将水和有机产物分离出来。在0.1至15巴的范围内; (iii)将塔底馏分从第二蒸馏塔进料至第三蒸馏塔K30,其中吗啉和沸点<140℃(1.013bar)的有机产物在选自塔顶馏出物和塔顶馏出物的点分离出。在第三蒸馏塔的底部分离出第三蒸馏塔的侧排放口,并将单氨基二甘醇和沸点大于190°C(1.013 bar)的有机产物分离出来,并且(iv)进料含吗啉从第三蒸馏塔到第四塔K40的物流,其中吗啉在第四塔的侧馏分处分离出,沸点≤128℃(1.013bar)的有机产物在塔顶分离出。在第四蒸馏塔的底部分离出第四蒸馏塔和沸点≥128℃(1.013巴)的有机产物。

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