首页> 外国专利> METHOD OF SEPARATING METHANOL FROM LOW BOILING ALIPHATIC ESTERS AND WATER BY AZEOTROPIC DISTILLATION WITH A HYDROCARBON

METHOD OF SEPARATING METHANOL FROM LOW BOILING ALIPHATIC ESTERS AND WATER BY AZEOTROPIC DISTILLATION WITH A HYDROCARBON

机译:油气共沸蒸馏从低沸点脂肪酯和水中分离甲醇的方法

摘要

Methanol is separated from a mixture comprising methanol, a low-boiling ester, e.g. methyl acrylate, which forms an azeotrope with methanol, an organic substance having a boiling point above the ester, and water by feeding the mixture through pipe 4 into distillation column I which contains a saturated C 1- C 7 hydrocarbon, e.g. cyclohexane in the vapour state. Vapours comprising methanol and hydrocarbon leave the head of column 1 and pass to condenser 10. The condensate flows to cool decanter 8 where two liquid layers are formed. The hydrocarbon layer and part of the methanol layer are returned through pipe 7 to column 1 and the remainder of the methanol layer is passed to distillation column 23 where it is freed from residual hydrocarbon and, possibly, ester. Pure methanol is withdrawn through pipe 26. The liquid which reaches the base of column 1 is passed to a hot decanter 3, where the liquid separates into an aqueous layer and an organic layer. The organic layer is fractionated in column 2, and the overhead vapours (methanol + water) is returned to column i through pipe 13. The mixture of ester and higher-boiling organic substance, withdrawn from the base of column 2, is separated in column 17. The aqueous layer from decanter 3 is fractionated in column 18. Vapours of ester and water flows from the head of column 18 into column 1 and water is discharged from the base of column 18. A polymerization inhibitor, such as hydroquinone, may be introduced into the system through pipes 27, 28. An aqueous solution of a copper salt may be introduced into the lower part of column 1 and the upper part of column 2.
机译:从包含甲醇,低沸点酯,例如甲醇和甲醇的混合物中分离甲醇。丙烯酸甲酯与甲醇,沸点高于酯的有机物和水形成共沸物,方法是将混合物经管道4送入蒸馏塔Ⅰ,该蒸馏塔中含有饱和的C 1 -C 7烃,例如碳酸氢钠。蒸气状态的环己烷。包含甲醇和碳氢化合物的蒸气离开塔1的顶部,并流至冷凝器10。冷凝液流至冷却de析器8,在此处形成两个液体层。碳氢化合物层和部分甲醇层通过管道7返回塔1,其余的甲醇层进入蒸馏塔23,从中除去残留的碳氢化合物和可能的酯。纯甲醇通过管道26抽出。到达塔1底部的液体进入热倾析器3,在该反应器中,液体分离为水层和有机层。有机层在塔2中分馏,塔顶蒸气(甲醇+水)通过管道13返回塔i。从塔2底部抽出的酯和高沸点有机物质的混合物在塔中分离。 17.来自倾析器3的水层在塔18中进行分馏。酯和水的蒸气从塔18的塔顶流入塔1,水从塔18的塔底排出。通过管道27、28将其引入系统中。可以将铜盐的水溶液引入塔1的下部和塔2的上部。

著录项

  • 公开/公告号ES342170A1

    专利类型

  • 公开/公告日1968-10-01

    原文格式PDF

  • 申请/专利权人 SOCIETE ANONYME MELLE - BEZONS;

    申请/专利号ES19670342170

  • 发明设计人

    申请日1967-06-22

  • 分类号C10G;

  • 国家 ES

  • 入库时间 2022-08-23 13:33:58

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