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    • 1. 发明授权
    • Process for preparing diacetoxybutene
    • 制备二乙酰氧基丁烯的方法
    • US5429721A
    • 1995-07-04
    • US245663
    • 1994-05-18
    • Hiroaki KandoriNobuyuki Murai
    • Hiroaki KandoriNobuyuki Murai
    • B01J23/44C07B61/00C07C67/055C07C67/54C07C69/16B01D3/10C07C69/02
    • C07C67/54C07C67/055
    • A process for preparing diacetoxybutene, including:reacting butadiene, acetic acid and oxygen in the presence of a palladium-based catalyst;feeding continuously the resulting reaction product into a first distillation tower;feeding continuously a withdrawn bottoms withdrawn from the first distillation tower into a second distillation tower;withdrawing bottoms containing high boiling point materials from the bottom of the second distillation tower, so that the content of the high boiling point materials in the bottoms of the second distillation tower is not more than 20 wt %;feeding continuously the withdrawn bottoms into a thin-film evaporator whose internal pressure is kept lower than the bottom pressure of the second distillation tower to carry out evaporation treatment; andrecycling the evaporated materials mainly containing diacetoxybutene into the second distillation tower.
    • 一种制备二乙酰氧基丁烯的方法,包括:在钯基催化剂存在下使丁二烯,乙酸和氧反应; 将所得反应产物连续进料到第一蒸馏塔中; 将从第一蒸馏塔排出的回收塔底馏分连续进料到第二蒸馏塔中; 从第二蒸馏塔的底部排出含有高沸点物质的塔底物,使得第二蒸馏塔底部的高沸点物质的含量不大于20wt%; 将取出的底部物料连续进入薄膜蒸发器,其内部压力保持低于第二蒸馏塔的底部压力以进行蒸发处理; 并将主要含有二乙酰氧基丁烯的蒸发材料回收到第二蒸馏塔中。
    • 2. 发明授权
    • Method for recovering 1,4-butanediol
    • 1,4-丁二醇的回收方法
    • US5397439A
    • 1995-03-14
    • US163554
    • 1993-12-09
    • Hiroaki KandoriKen Siraga
    • Hiroaki KandoriKen Siraga
    • B01J23/44B01J23/46C07B61/00C07C29/80C07C29/90C07C31/20B01D3/34
    • C07C29/80C07C29/90Y02P20/582Y10S203/20
    • A method for recovering 1,4-butanediol from a hydrolysate obtained by hydrolyzing diacetoxybutane, by (1) supplying the hydrolysate to a first distillation column, distilling off substantially all the amounts of water and acetic acid as the top stream from the first distillation column, and supplying a bottom liquid to a second distillation column, (2) distilling off diacetoxybutane and hydroxyacetoxybutane as the top or upper side stream from of the second distillation column, and circulating the distillates to a hydrolysis zone, while withdrawing crude 1,4-butanediol as a lower side stream in vapor phase from the second distillation column, (3) supplying the crude 1,4-butanediol and hydrogen gas to a hydrogenation reaction zone packed with a hydrogenation catalyst, and (4) supplying the hydrogenation reaction product to a third distillation column, distilling off low boiling point components and withdrawing 1,4-butanediol as the bottom or side stream from the third distillation column.
    • 通过(1)将水解产物供应到第一蒸馏塔中,从第一蒸馏塔蒸馏基本上所有量的水和乙酸作为顶部流,从通过水解二乙酰氧基丁烷获得的水解产物中回收1,4-丁二醇的方法 ,并向第二蒸馏塔供应底部液体,(2)从第二蒸馏塔蒸馏出二乙酰氧基丁烷和羟基乙酰氧基丁烷作为顶部或上部侧流,并将馏出物循环到水解区,同时取出粗品1,4- (3)将粗1,4-丁二醇和氢气供给到装有氢化催化剂的氢化反应区,和(4)将氢化反应产物供给到 第三蒸馏塔,蒸馏掉低沸点组分并从第三蒸馏塔中回收1,4-丁二醇作为底部或侧流 n。