首页> 外国专利> PROCESS FOR THE PREPARATION OF HIGHLY PURE ISOBUTENE BY DEHYDRATION OF TERTIARY BUTANOL ?PROCESS FOR THE PREPARATION OF HIGHLY PURE ISOBUTENE BY DEHYDRATION OF TERTIARY BUTANOL

PROCESS FOR THE PREPARATION OF HIGHLY PURE ISOBUTENE BY DEHYDRATION OF TERTIARY BUTANOL ?PROCESS FOR THE PREPARATION OF HIGHLY PURE ISOBUTENE BY DEHYDRATION OF TERTIARY BUTANOL

机译:叔丁醇脱水制备高纯度异丁烯的方法叔丁醇脱水制备高纯度异丁烯的方法

摘要

Tertiary-butanol in an aqueous solution containing from 40 to 90 percent by weight of tertiary butanol in homogeneous and liquid phase is dehydrated at a fixed catalytic bed consisting of a strongly acidic ion exchange resin at a temperature from 80 DEG to 150 DEG C. and at a pressure from 5 to 25 bars for the purpose of producing isobutene by dehydrating tertiary butanol. Thereupon the homogeneous, liquid reaction mixture is fractionated in a distillation sector separate from the reaction chamber, the isobutene being separated from the water and from the unreacted tertiary butanol. The unreacted tertiary butanol is returned as an aqueous solution in a circulating flow rate to the reactor under the conditions that the mixture of fresh-fed tertiary butanol and the circulating tertiary-butanol/water mix contains from 40 to 90 percent by weight of tertiary butanol at the reactor inlet.
机译:在由强酸性离子交换树脂组成的固定催化床中,在80至150℃的温度下,将含有均相和液相的40-90重量%的叔丁醇的水溶液中的叔丁醇脱水。为了通过使叔丁醇脱水而生产异丁烯,在5至25巴的压力下进行。然后,将均匀的液体反应混合物在与反应室分开的蒸馏区中分馏,将异丁烯与水和未反应的叔丁醇分开。在新鲜进料的叔丁醇和循环的叔丁醇/水混合物的混合物包含40-90重量%的叔丁醇的条件下,未反应的叔丁醇以水溶液的水溶液以循环流速返回到反应器。在反应堆入口

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