首页> 外国专利> Method for isolating pure t-butyl (meth) acrylate by distillation from crude t-butyl (meth) acrylate

Method for isolating pure t-butyl (meth) acrylate by distillation from crude t-butyl (meth) acrylate

机译:通过蒸馏从粗制(甲基)丙烯酸叔丁酯中分离出纯(甲基)丙烯酸叔丁酯的方法

摘要

The present invention relates to a process for obtaining pure t-butyl (meth) acrylate from crude t-butyl (meth) acrylate, which method comprises a split wall column (1) having a separating component and an evaporator (7). In this case, the dividing wall 8 is arranged in the column length direction in the dividing wall column, so that the upper joint column region 9, the lower joint column region 14, the side feed point (2) and an intake section (11, 13) having a side outlet point (3) and an intake section (2), wherein the column has a theoretical plate number in the range of 20 to 80 ( number of theoretical plates, the theoretical plate number of the partition wall column 1 refers to the sum of the theoretical plates in the joint upper column region 9, the joint lower column region 14 and the inlet zones 10, 12. Crude t-butyl (meth) acrylate The side feed point 2 for the trough is arranged in a theoretical plate in a region starting at at least two theoretical plates above the lowest theoretical plate and ending at at least two theoretical plates below the top theoretical plate, the pure t − The side discharge point 3 for butyl (meth) acrylate is arranged in a theoretical plate in an area starting at at least two theoretical plates above the lowest theoretical plate and ending at at least two theoretical plates below the top theoretical plate, The dividing wall 8 is arranged in a column in a region starting above at least one theoretical plate above the lowest theoretical plate and ending below at least one theoretical plate above the top theoretical plate, the enrichment zone 10 and the stripping zone 11 of the column. Minute introduced into The ratio of the liquid amount in the upper end of the wall (8) (upper end) is from 1: 5 is set to the range: 0.2 to 1.
机译:本发明涉及一种由粗制(甲基)丙烯酸叔丁酯获得纯的(甲基)丙烯酸叔丁酯的方法,该方法包括具有分离组分的裂壁塔(1)和蒸发器(7)。在这种情况下,分隔壁8在分隔壁列中沿列长度方向布置,从而上接合柱区域9,下接合柱区域14,侧进料点(2)和进气部分(11) ,13)具有侧出口点(3)和入口部分(2),其中塔的理论塔板数在20至80(理论塔板数,分隔壁塔1的理论塔板数指的是在接头上部塔区域9,接头下部塔区域14和入口区域10、12中理论塔板的总和。(甲基)丙烯酸叔丁酯粗料料斗的侧进料口2布置在从最低理论塔板上方至少两个理论塔板开始,到顶部理论塔板下方至少至少两个理论塔板结束的区域中的理论塔板,纯t-(甲基)丙烯酸丁酯的侧面排放点3布置在起始于的区域中的理论板块最低理论板上方的至少两个理论板,并在顶部理论板下方的至少两个理论板处终止。分隔壁8排列成一列,位于从最低理论板上方的至少一个理论板上方开始并终止于以下位置的区域中在塔的顶部理论塔板,富集区10和汽提区11上方至少有一个理论塔板。引入的分钟将壁(8)的上端(上端)中的液体量的比从1:5设置为范围:0.2到1。

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