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Purification of propylene oxide with aqueous acetone as a means of extraction distillation.

机译:用丙酮水溶液纯化环氧丙烷,作为萃取蒸馏的一种手段。

摘要

An impure propylene oxide feedstock contaminated with from about 50 to about 1000 ppm of methanol and from about 0 to about 1 wt. % of acetone is charged to the lower half of an extractive distillation column containing at least about 25 theoretical plates and an extractive distillation agent consisting essentially of a blend of acetone and water (acetone/water blend) containing about 20 to about 30 wt. % of acetone and, correspondingly, about 80 to about 70 wt. % of water is charged to the tower at a point 4 to 7 theoretical stages above the impure propylene oxide feed point; the extractive distillation agent being introduced into the extractive distillation column in the ratio of said feedstock to said extractive distillation agent of from about 5:1 to about 20:1, whereby an overhead distillate fraction is obtained consisting essentially of propylene oxide contaminated with not more than about 60 ppm of methanol, not more than about 0.02 wt. % of acetone and not more than about 0.3 wt. % of water.
机译:不纯的环氧丙烷原料被约50至约1000 ppm的甲醇和约0至约1 wt。 %的丙酮被装入含有至少约25个理论塔板的萃取蒸馏塔的下半部分和基本上由丙酮和水的混合物(丙酮/水的混合物)组成的萃取蒸馏剂,该混合物含有约20至约30wt。%的丙酮。 %的丙酮和相应地约80-约70wt。%的丙酮。在不纯的环氧丙烷进料点以上理论值的4至7阶段,将%的水注入塔中。以所述原料与所述萃取蒸馏剂的比例为约5∶1至约20∶1的方式将萃取蒸馏剂引入萃取蒸馏塔,由此获得塔顶馏出物馏分,所述馏出物馏分基本上由不被更多污染物污染的环氧丙烷组成。小于约60ppm的甲醇,不大于约0.02wt。%。 %的丙酮和不超过约0.3wt%。 %的水。

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