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Energy conservation during plural stage distillation

机译:多级蒸馏过程中的节能

摘要

In the multistage distillation of a methyl tertiary butyl ether reaction product comprising methyl tertiary butyl ether, tertiary butyl alcohol, methanol, isobutylene and water, the methyl tertiary butyl ether reaction product is separated in a primary methyl tertiary butyl ether distillation column into a lower boiling methyl tertiary butyl ether fraction and a higher boiling aqueous tertiary butyl alcohol fraction; the lower boiling aqueous tertiary butyl alcohol fraction is separated in a tertiary butyl alcohol distillation column into a vaporized overhead tertiary butyl alcohol fraction and a higher boiling water fraction; cooling water is charged to the reflux condenser for the tertiary butyl alcohol distillation column to liquify the vaporized, overhead tertiary butyl alcohol fraction and to convert the cooling water to wet steam, and the wet steam is independently charged to the reboiler for the primary methyl tertiary butyl ether distillation zone to supply the heat necessary for the distillation to be effected therein.
机译:在包含甲基叔丁基醚,叔丁醇,甲醇,异丁烯和水的甲基叔丁基醚反应产物的多级蒸馏中,将甲基叔丁基醚反应产物在伯甲基叔丁基醚蒸馏塔中分离至较低沸点。甲基叔丁基醚馏分和较高沸点的叔丁醇水溶液;较低沸点的叔丁醇水溶液馏分在叔丁醇蒸馏塔中分离成汽化的塔顶叔丁醇馏分和较高沸点的水馏分。将冷却水加入叔丁醇蒸馏塔的回流冷凝器中,以将汽化的塔顶叔丁醇馏分液化并将冷却水转化为湿蒸汽,并将湿蒸汽独立地加入伯甲基叔叔醇的再沸器中。丁基醚蒸馏区,以提供在其中进行蒸馏所需的热量。

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