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Plural stage distillation of trioxane in the presence of a water-immiscible solvent

机译:在与水不混溶的溶剂存在下三恶烷的多级蒸馏

摘要

1,137,054. Production of pure trioxane. FARBENFABRIKEN BAYER, A.G. 13 Jan., 1966 [13 Jan., 1965], No. 1688/66. Heading C2C. Pure trioxane is obtained by distilling a mixture having a pH of from 1 to 3 of formaldehyde or paraformaldehyde, water, an acid and a trioxane organic solvent which is immiscible with water, separating out a solution of trioxane in the organic solvent from the vapours distilling over and, after the removal of the formic acid contained therein by means of an ion exchanger, separating the organic trioxane solution by fractional distillation into substantially pure trioxane and the organic solvent containing the impurities. The process is advantageously effected by distilling the initial mixture and introducing the vapours which distil over into the middle portion of a first distillation column, drawing off a substantially trioxane free aqueous formaldehyde solution from the sump of this column (which solution can be returned to the process after having been passed through an ion exchanger and optionally after having been concentrated), completely condensing in a reflux condenser the product forming at the head of the first distillation column, separating the organic and aqueous phases which are thereby formed, returning the aqueous phase to the head of the first distillation column, and feeding the organic phase containing the trioxane, after passing the organic phase through an ion exchanger into the middle portion of a second distillation column, such that the water-immiscible solvent, water and formaldehyde distil over at the head of said second column, while pure trioxane is obtained in the sump, the trioxane preferably being discharged in an inert gas atmosphere. Suitable solvents which are immiscible with water are, for example, methylene chloride, chloroform, benzene and cyclohexane. A suitable form of apparatus for carrying out the above process is described.
机译:1,137,054。生产纯三恶烷。 FARBENFABRIKEN BAYER,A.G.,1966年1月13日[1965年1月13日],第1688/66号。标题C2C。通过蒸馏除去甲醛或多聚甲醛的pH为1-3的混合物,水,酸和与水不混溶的三恶烷有机溶剂,然后从蒸气蒸馏中分离出三恶烷在有机溶剂中的溶液,从而获得纯的三恶烷。然后,通过离子交换剂除去其中所包含的甲酸,然后通过分馏将有机三恶烷溶液分离成基本上纯的三恶烷和含有杂质的有机溶剂。该方法有利地通过蒸馏初始混合物并将引入到第一蒸馏塔的中间部分的蒸气引入,从该塔的贮槽中抽出基本上不含三恶烷的甲醛水溶液(该溶液可以返回到蒸馏塔中)进行。在经过离子交换剂之后,以及可选地在浓缩之后进行),在回流冷凝器中完全冷凝在第一蒸馏塔顶部形成的产物,分离由此形成的有机相和水相,使水相返回将有机相通过离子交换剂进入第二蒸馏塔的中间部分后,将有机相送入第一蒸馏塔的顶部,然后将含有三恶烷的有机相进料,使水不混溶的溶剂,水和甲醛在在所述第二塔的顶部,虽然在集液槽中获得了纯三恶烷,但三恶烷优选在惰性气体气氛中排放。与水不混溶的合适的溶剂是例如二氯甲烷,氯仿,苯和环己烷。描述了用于执行上述过程的设备的合适形式。

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