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Process for removing 2-butanol from tert.-butanol/water mixtures

机译:从叔丁醇/水混合物中除去2-丁醇的方法

摘要

2-Butanol is separated from an industrial mixture by separating water from the industrial mixture by distillation to obtain a distillate having a proportion by mass of water is greater than the limit concentration of the distillation boundary line connecting an azeotrope of tert-butanol and water, and an azeotrope of 2-butanol and water. Separating 2-butanol (SBA) from an industrial mixture which comprises SBA, tert-butanol (TBA) and water where the proportion by mass of water is greater than the limit concentration of the distillation boundary line connecting an azeotrope of TBA and water and an azeotrope of SBA and water, involves: (a) separating water from the industrial mixture by distillation to obtain a distillate, where the distillate has, in terms of the SBA, TBA and water in the industrial mixture, a proportion by mass of water, which at a pressure, is greater than the limit concentration of the distillation boundary line connecting an azeotrope of TBA and water, and an azeotrope of SBA and water; (b) subsequently changing the pressure so that the mixture has, in terms of the SBA, TBA and water in the distillate, a proportion by mass of water which is less than the limit concentration of the distillation boundary line connecting the distillation boundary line connecting an azeotrope of TBA and water, and an azeotrope of SBA and water; and (c) subsequently distilling the mixture at the same pressure into a stream comprising SBA and a stream comprising TBA and water. An independent claim is also included for SBA prepared by the inventive process.
机译:通过蒸馏从工业混合物中分离水,从而从工业混合物中分离出2-丁醇,以获得水的质量比大于连接叔丁醇和水的共沸物的蒸馏边界线的极限浓度的馏出物,和2-丁醇和水的共沸物。从包含SBA,叔丁醇(TBA)和水的工业混合物中分离出2-丁醇(SBA),其中水的质量比大于连接TBA和水与共沸物的共沸物的蒸馏边界线的极限浓度SBA和水的共沸物包括:(a)通过蒸馏从工业混合物中分离水以获得馏出物,其中馏出物就工业混合物中的SBA,TBA和水而言,占水的质量比例,其在压力下大于连接TBA和水的共沸物与SBA和水的共沸物的蒸馏边界线的极限浓度; (b)随后改变压力,以使混合物在馏出物中的SBA,TBA和水方面具有小于质量分数的水比例,该质量分数小于连接蒸馏边界线的蒸馏边界线的极限浓度。 TBA和水的共沸物,SBA和水的共沸物; (c)随后在相同压力下将混合物蒸馏成包含SBA的物流和包含TBA和水的物流。对于通过本发明方法制备的SBA也包括独立权利要求。

著录项

  • 公开/公告号EP1462432B1

    专利类型

  • 公开/公告日2013-08-14

    原文格式PDF

  • 申请/专利权人 EVONIK OXENO GMBH;

    申请/专利号EP20040100258

  • 发明设计人 BECKMANN ANDREAS DR.;REUSCH DIETER DR.;

    申请日2004-01-26

  • 分类号C07C29/80;C07C31/12;

  • 国家 EP

  • 入库时间 2022-08-21 16:35:41

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