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    • 8. 发明申请
    • METHOD FOR THE CONTINUOUS SEPARATION OF MIXTURES COMPRISING MORPHONLINE (MO), MONOAMINODIGLYCOL (ADG), AMMONIA AND WATER BY MEANS OF DISTILLATION
    • 通过蒸馏法连续分离含有摩尔(MO),单胺基(ADG),氨和水的混合物的方法
    • US20120024689A1
    • 2012-02-02
    • US12443581
    • 2007-09-12
    • Helmut SchmidtkeOliver BußmannRalph VerschUdo RheudeUwe LeykManfred JuliusMartin RudloffErhard Henkes
    • Helmut SchmidtkeOliver BußmannRalph VerschUdo RheudeUwe LeykManfred JuliusMartin RudloffErhard Henkes
    • B01D3/34B01D3/14
    • C07C213/10C07D295/023C07C217/08
    • 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 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.
    • 用于从二甘醇(DEG)与氨的反应连续分馏含有吗啉(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顶部; (ii)将底部馏分从第一蒸馏塔进料到第二蒸馏塔K20,其中在顶部温度为45至198℃的温度下,在第二蒸馏塔的顶部分离出水和有机产物,并将压力 在0.1至15巴的范围内; (iii)将第二蒸馏塔的塔底馏分进料到第三蒸馏塔K30,其中将吗啉和沸点<140℃(1.013巴)的有机产物在选自顶部和 在第三蒸馏塔的底部分离出第三蒸馏塔的侧馏分和单胺二醇和沸点> 190℃(1.013巴)的有机产物,(iv)将含吗啉 从第三蒸馏塔到第四塔K40的流,其中吗啉在第四塔的出口侧分离出,沸点为&amp; NlE的有机产物为128℃(1.013巴)在顶部分离 的第四蒸馏塔和沸点为≧128℃的有机产物(1.013巴)在第四蒸馏塔的底部分离。