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Process for the recovery of pure methylal from methanol-methylal mixtures

机译:从甲醇-甲醇混合物中回收纯甲醇的方法

摘要

In a process for recovering pure methylal from methanol- methylal mixtures, which can optionally contain still further compounds, the separation conducted in a rectification device comprising two rectifying columns. In the first rectifying column, the mixture to be separated is rectified under a pressure lower than that in the second column, into a methylal-rich, methanol-poor distillate, and into a practically methylal- free, methanol-rich sump product. The methylal-rich distillate of the first rectification is then separated in a second rectifying column, operated under a higher pressure than the first rectification column, into a compound stream containing methanol and methylal, which is then recycled to the first rectifying column, and into pure methylal as the sump product. In a specific refinement, the first rectification is preferably operated under a pressure of 1-22 bar absolute and the second rectification preferably under a pressure of 9-30 bar absolute, with the second rectification being operated under a pressure which is at least 8 bar higher than that of the first rectification.
机译:在用于从甲醇-甲基缩醛混合物中回收纯的甲基缩醛的方法中,该混合物可以任选地包含其他化合物,该分离在包括两个精馏塔的精馏装置中进行。在第一精馏塔中,将要分离的混合物在低于第二精馏塔的压力下精馏为富含甲基醇,贫甲醇的馏出液,以及几乎不含甲醇,富甲醇的贮槽产物。然后,在第二精馏塔中将第一精馏的富含甲缩醛的馏出物分离,该第二精馏塔在比第一精馏塔更高的压力下操作,分离成含有甲醇和甲缩醛的化合物物流,然后将其再循环至第一精馏塔,并进入纯甲缩醛作为贮槽产品。在特定的改进方案中,第一精馏优选在1-22bar绝对压力下操作,第二精馏优选在9-30bar绝对压力下操作,第二精馏在至少8bar的压力下操作。比第一次整改要高。

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