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    • 4. 发明授权
    • Methods of treating triethanolamine with acid components and basic components, and triethanolamine compositions containing the same
    • 用酸组分和碱性组分处理三乙醇胺的方法和含有它们的三乙醇胺组合物
    • US07550632B2
    • 2009-06-23
    • US11661544
    • 2005-08-04
    • Frank HaeseJohann-Peter MelderRoman DostalekManfred Julius
    • Frank HaeseJohann-Peter MelderRoman DostalekManfred Julius
    • C07C209/84
    • C07C213/10C07C215/08
    • Methods for improving color properties of triethanolamine, and triethanolamine compositions treated thereby, are disclosed, wherein the methods comprise: (a) providing a composition comprising triethanolamine; and (b) contacting the composition with an acid component and a basic component; wherein the acid component comprises an acid selected from the group consisting of phosphorous acid, hypophosphorous acid and mixtures thereof; and wherein the basic component comprises a compound selected from the group consisting of alkali metal hydroxides, alkaline earth metal hydroxides, ammonium hydroxides according to general formula (I), and mixtures thereof: [R1R2R3(2-hydroxyethyl)ammonium] hydroxide  (I) wherein R1, R2 and R3 each independently represents a C1-30 alkyl or a C2-10 hydroxyalkyl; with the proviso that where the basic component comprises an alkali metal hydroxide, the molar ratio of acid component: basic component is 1:0.1 to 1:1, and where the basic component comprises an alkaline earth metal hydroxide, the molar ratio of acid component: basic component is 1:0.05 to 1:0.5.
    • 公开了用于改善三乙醇胺的颜色特性和由此处理的三乙醇胺组合物的方法,其中所述方法包括:(a)提供包含三乙醇胺的组合物; 和(b)使组合物与酸组分和碱性组分接触; 其中所述酸组分包含选自亚磷酸,次磷酸及其混合物的酸; 并且其中所述碱性组分包括选自碱金属氢氧化物,碱土金属氢氧化物,根据通式(I)的氢氧化铵的化合物及其混合物:<?在线公式描述=“在线 公式“end =”lead“→> [R1R2R3(2-羟乙基)铵]氢氧化物(I)<?in-line-formula description =”In-line Formulas“end =”tail“?>其中R1,R2和R3 各自独立地表示C1-30烷基或C2-10羟基烷基; 条件是碱性成分含有碱金属氢氧化物时,酸成分:碱成分的摩尔比为1:0.1〜1:1,碱性成分为碱土金属氢氧化物时,酸成分 基本成分为1:0.05〜1:0.5。
    • 10. 发明授权
    • Method for the continuous separation by distillation of mixtures that contain morphonline (MO), monoaminodiglycol (ADG), ammonia and water by means of distillation
    • 通过蒸馏连续分离含有吗啉(MO),单氨基二甘醇(ADG),氨和水的混合物的方法
    • US08293075B2
    • 2012-10-23
    • US12443581
    • 2007-09-12
    • Helmut SchmidtkeOliver BuβmannRalph VerschUdo RheudeUwe LeykManfred JuliusMartin RudloffErhard Henkes
    • Helmut SchmidtkeOliver BuβmannRalph VerschUdo RheudeUwe LeykManfred JuliusMartin RudloffErhard Henkes
    • B01D3/14C07D295/02
    • C07C213/10C07D295/023C07C217/08
    • Processes for the continuous fractional distillation of a mixture containing morpholine (MO), monoaminodiglycol (ADG), ammonia and water from a reaction of diethylene glycol (DEG) with ammonia, the process including: (i) separating off ammonia from the mixture at a top of a first distillation column K10; (ii) feeding a bottom fraction from K10 to a second distillation column K20, in which water and an organic product are separated off at the top at a temperature at the top in the range from 45 to 198° C. and a pressure in the range from 0.1 to 15 bar; (iii) feeding a bottom fraction from K20 to a third distillation column K30, wherein the column K30 is a dividing wall column (DWC)which preferably has a dividing wall (DW) in the longitudinal direction of the column to form an upper combined column region (1), a lower combined column region (6), an inflow part (2,4) having an enrichment section (2) and a stripping section (4), and also an offtake part (3,5) having an enrichment section (3) and a stripping section (5), with the bottoms from K20 being fed in in the upper or middle third of the inflow part (2,4), based on the number of theoretical plates of the inflow part, ADG and organic products having a boiling point of >190° C. (1.013 bar) being discharge at the bottom, organic products having a boiling point of ≦128° C. (1.013 bar) being discharge at a top and MO being discharge from the middle or lower third of the offtake part (3,5) (side offtake), based on the number of theoretical plates of the offtake part.
    • 从二甘醇(DEG)与氨的反应中连续分馏含有吗啉(MO),单胺二甘醇(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K10进料到第二蒸馏塔K20,在第二蒸馏塔K20中,水和有机产物在顶部分离出,顶部温度为45-98℃,压力为 范围为0.1至15巴; (iii)从K20向第三蒸馏塔K30供给底部馏分,其中塔K30是分隔壁塔(DWC),其在塔的纵向方向上优选具有分隔壁(DW),以形成上部混合塔 区域(1),下部组合柱区域(6),具有浓缩部分(2)和汽提部分(4)的流入部分(2,4),以及具有富集部分 (3)和汽提部分(5),其中来自K20的底部基于流入部分的理论塔板的数量,ADG和 沸点为> 190℃(1.013巴)的有机产物在底部排出,沸点为&amp; NlE的有机产物; 128℃(1.013巴)在顶部排出,MO从 基于出料部分的理论塔板的数量,出口部分(3,5)(侧面)的中下三分之一。