首页> 外国专利> METHOD FOR SEPARATING TRIOXAN FROM A TRIOXAN / FORMALDEHYDE / WATER MIXTURE BY PRESSURE CHANGE RECTIFICATION

METHOD FOR SEPARATING TRIOXAN FROM A TRIOXAN / FORMALDEHYDE / WATER MIXTURE BY PRESSURE CHANGE RECTIFICATION

机译:压力变动校正法从三恶英/甲醛/水混合物中分离三恶英的方法。

摘要

A process for separating trioxane from a feed stream I comprising formaldehyde, trioxane and water, in which a) a feed stream I comprising formaldehyde as main component and trioxane and water as secondary components is provided, b) the feed stream I, a recycle stream V and a recycle stream VII comprising formaldehyde as main component and water and trioxane as secondary components are fed into a first distillation stage and distilled at a pressure of from 0.1 to 2.5 bar to give a stream II comprising formaldehyde as main component and water as secondary component and a stream III comprising trioxane as main component and water and formaldehyde as secondary components and a stream X comprising water, trioxane and formaldehyde, c) the stream III is, if appropriate after removal of low boilers from the stream III in a low boiler removal stage, distilled in a second distillation stage at a pressure of from 0.2 to 17.5 bar, with the pressure in the second distillation stage being from 0.1 to 15 bar higher than the pressure in the first distillation stage, to give a stream IV consisting essentially of trioxane and the recycle stream V comprising trioxane as main component and water and formaldehyde as secondary components, c1) the stream IV is purified in at least one further trioxane distillation stage at a pressure at the top of from 0.5 to 2 bar to give purified trioxane as side offtake stream XII in the enrichment section of the column, d) the stream X and, if appropriate, a stream IX comprising water as main component are fed into a third distillation stage and distilled at a pressure of from 1 to 10 bar to give a stream VI consisting essentially of water and a recycle stream VII comprising formaldehyde as main component and water and trioxane as secondary components, is described.
机译:从包含甲醛,三恶烷和水的进料流I中分离三恶烷的方法,其中a)提供了包含甲醛作为主要组分和三恶烷和水作为次要组分的进料流I,b)进料流I,一种循环流将V和以甲醛为主要成分并以水和三恶烷为次要成分的再循环料流VII进料至第一蒸馏阶段,并在0.1至2.5bar的压力下蒸馏,以得到以甲醛为主要成分并以水为次要成分的料流II组分和以三恶烷为主要成分,水和甲醛为次要组分的物流III以及包含水,三恶烷和甲醛的物流X,c)如果合适,在低沸点物流中从低沸点物流中除去低沸点化合物后,物流III是除去阶段,在第二蒸馏阶段中在0.2至17.5巴的压力下蒸馏,第二蒸馏阶段中的压力为0.1 -比第一蒸馏步骤中的压力高15巴,以得到基本上由三恶烷和包含三恶烷作为主要组分和水和甲醛作为次要组分的循环物流V组成的物流IV,c1)至少在在塔顶浓缩区的顶部压力为0.5至2 bar的条件下再进行三恶烷蒸馏,以得到纯化的三恶烷作为侧流XII,d)物流X,如果合适的话,还包括水的物流IX描述了将主要组分进料到第三蒸馏阶段并在1至10巴的压力下蒸馏以给出基本由水组成的料流VI和包含甲醛作为主要组分和水和三恶烷作为次要组分的循环料流VII。

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