首页> 外国专利> METHOD FOR OBTAINING PURE BUTYL ACRYLATE FROM RAW BUTYL ACRYLATE BY DISTILLATION, WHEREIN BUTYL STANDS FOR N-BUTYL OR ISOBUTYL

METHOD FOR OBTAINING PURE BUTYL ACRYLATE FROM RAW BUTYL ACRYLATE BY DISTILLATION, WHEREIN BUTYL STANDS FOR N-BUTYL OR ISOBUTYL

机译:蒸馏法从粗丙烯酸丁酯中纯化纯丙烯酸丁酯的方法,其中丁基丁酯为正丁基或异丁基

摘要

The invention relates to a method for obtaining pure butyl acrylate from raw butyl acrylate by distillation, wherein butyl stands for n-butyl or isobutyl, characterized in that the method is carried out in a dividing wall column (1) having dividing built-in components and an evaporator (7), in which dividing wall column a dividing wall (8) is arranged in the column longitudinal direction in such a way that an upper common column region (9), a lower common column region (14), a feed part (10, 12) having a side feed point (2) and a removal part (11, 13) having a side removal point (3) are formed, the column has a number of theoretical separating stages in the range of 20 to 80, wherein the number of theoretical separating stages of the dividing wall column (1) refers to the sum of the theoretical separating stages in the common upper column region (9), the common lower column region (14) and the feed part (10, 12), the side feed point (2) for the raw butyl acrylate is arranged at a theoretical separating stage in the region beginning at least two theoretical separating stages above the bottommost theoretical separating stage and ending at least two theoretical separating stages below the topmost theoretical separating stage, the side removal point (3) for the pure butyl acrylate is arranged at a theoretical separating stage in the region beginning at least two theoretical separating stages above the bottommost theoretical separating stage and ending at least two theoretical separating stages below the topmost theoretical separating stage, and the dividing wall (8) is arranged in the column in the region beginning at least one theoretical separating stage above the bottommost theoretical separating stage and ending at least one theoretical separating stage below the topmost theoretical separating stage, wherein the liquid amount ratio at the upper end of the dividing wall (8) to the enriching section (10) and to the stripping section (11) of the column is set in a range of 1:0.2 to 1:5.
机译:本发明涉及一种通过蒸馏从丙烯酸原丁酯中蒸馏得到纯丙烯酸丁酯的方法,其中丁基代表正丁基或异丁基,其特征在于,该方法在具有分立的内置组分的分壁塔(1)中进行。蒸发器(7),其特征在于,在分隔壁塔的上下方向上配置有分隔壁(8),以使上部的共用塔区域(9),下部的共用塔区域(14),进料形成具有侧进料点(2)的部分(10、12)和具有侧进料点(3)的除去部分(11、13),该塔的理论分离级数为20至80 ,其中分隔壁塔(1)的理论分离级数是指公共上塔区域(9),公共下塔区域(14)和进料部分(10)中理论分离阶段的总和,在图12)中,丙烯酸丁酯原料的侧进料点(2)设置在理论上在该区域中的理论分离阶段开始于最底部理论分离阶段之上的至少两个理论分离阶段并且结束于最顶部理论分离阶段之下的至少两个理论分离阶段,纯丙烯酸丁酯的侧去除点(3)布置在该区域中的理论分离阶段开始于最底部理论分离阶段之上的至少两个理论分离阶段,并终止于最顶部理论分离阶段之下的至少两个理论分离阶段,并且分隔壁(8)布置在该区域开始处的列中在最底部的理论分离阶段之上的至少一个理论分离阶段并且在最顶部的理论分离阶段之下的至少一个理论分离阶段结束,其中,在分隔壁(8)的上端处的液体量与浓缩部分(10)的比率并在范围内将色谱柱的汽提段(11)设置为e为1:0.2至1:5。

著录项

  • 公开/公告号WO2018114422A1

    专利类型

  • 公开/公告日2018-06-28

    原文格式PDF

  • 申请/专利权人 BASF SE;

    申请/专利号WO2017EP82186

  • 发明设计人 LANG ORTMUND;METZEN BERND;HECHLER CLAUS;

    申请日2017-12-11

  • 分类号C07C67/54;C07C69/54;

  • 国家 WO

  • 入库时间 2022-08-21 12:43:38

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