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Method for obtaining pure tert-butyl (meth) acrylate from crude tert-butyl (meth) acrylate by distillation

机译:通过蒸馏从粗(甲基)丙烯酸叔丁酯中获得纯(甲基)丙烯酸叔丁酯的方法

摘要

In a method for obtaining pure tert-butyl (meth) acrylate from crude tert-butyl (meth) acrylate by distillation, the method comprises the steps of: separating a partition wall column (1) having a separating internal structure and an evaporator (7); In the bulkhead tower (1), a bulkhead (8) is arranged along the longitudinal direction of the tower, and an upper tower common area (9), a lower tower common area (14), a side part Forming a feed section (10, 12) having a feed port (2) and a discharge section (11, 13) having a side discharge port (3), said tower having a theoretical plate number in the range of 20 to 80; Here, the number of theoretical plates of the partition tower (1) is based on the total number of theoretical plates in the upper column common region (9), the lower column common region (14), and the supply units (10, 12). , The crude tert-butyl (meth) acryl The side supply port (2) of the plate is a theoretical plate in a region starting from a theoretical plate at least two stages above the lowest theoretical plate and ending with at least two theoretical plates below the highest theoretical plate. And the side outlet (3) of the pure tert-butyl (meth) acrylate is at least two stages above the lowest theoretical plate and higher than the highest theoretical plate. Are also arranged in the theoretical plate in the region ending with at least two theoretical plates, and the partition (8) in the column is located at the top starting from the theoretical plate at least one stage above the lowest theoretical plate. In the region ending with at least one theoretical plate below the theoretical plate, where it goes to the enrichment section (10) and the recovery section (11) of the column at the upper end of the partition (8). The amount ratio of the liquid is in the range of 1: 0.2 to 1: 5. And setting the method.
机译:在通过蒸馏从粗(甲基)丙烯酸叔丁酯中获得纯(甲基)丙烯酸叔丁酯的方法中,该方法包括以下步骤:分离具有分离内部结构的分隔壁塔(1)和蒸发器(7) );在隔板塔(1)中,沿塔的长度方向设置隔板(8),上部塔公共区域(9),下部塔公共区域(14),侧部形成进料部( 10、12)具有一个进料口(2)和一个排料段(11、13),其具有一个侧排料口(3),所述塔的理论塔板数为20-80。在此,分隔塔(1)的理论塔板数是基于上部塔共用区域(9),下部塔共用区域(14)以及供给单元(10、12)的理论塔板的总数。 )。 ,叔丁基(甲基)丙烯酸酯板的侧进料口(2)是理论板,该区域从理论板开始,至少在最低理论板的上方两级,并在至少以下理论板的下方终止最高理论板块。而且,纯的(甲基)丙烯酸叔丁酯的侧出口(3)在最低的理论塔板上方至少两级,而在最高的理论塔板上方至少两级。在至少两个理论塔板结束的区域中,理论塔板也布置在该塔板中,塔中的隔板(8)从理论塔板开始位于最低理论塔板上方至少一级。在以理论板下面的至少一个理论板为结尾的区域中,它到达隔板(8)上端的色谱柱的富集区(10)和回收区(11)。液体的量比在1:0.2至1:5的范围内。

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