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A method for recovering methyl tert-butyl ether in pharmaceutical process waste liquid by extractive distillation-adsorption coupling process

A technology of extraction and distillation of methyl tert-butyl ether, which is applied in the fields of ether preparation, chemical industry, ether separation/purification, etc. It can solve the problems of unavoidable, affecting the quality of intermediate E2, difficult recovery, etc., and achieve energy saving , Save equipment investment and reduce energy consumption

Active Publication Date: 2021-06-22
FUQING BRANCH OF FUJIAN NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] For the above-mentioned waste liquid produced, the recovery of the solvent methyl tert-butyl ether is a very difficult problem, this is due to the presence of multiple groups of binary azeotropes in the system under normal pressure, the binary azeotrope of ethanol and methyl tert-butyl ether The ethanol content in the meta-azeotropic composition is 7.7wt%, and the azeotropic temperature is 57.9°C; the ethanol content in the binary azeotropic composition of ethanol and water is 95.6wt%, and the azeotropic temperature is 78.2°C; The content of tert-butanol in the meta-azeotropic composition is 87.5wt%, and the azeotropic temperature is 80.3℃; the content of methyl tert-butyl ether in the binary azeotropic composition of methyl tert-butyl ether and water is 94.1wt%, and the azeotropic The temperature is 55.9°C; the n-butane content in the binary azeotropic composition of n-butane and water is 98.7wt%, and the azeotropic temperature is -1.72°C, so it is difficult to remove water, ethanol and tert-butanol in the mixture by ordinary rectification , needs to pass special rectification, such as extractive rectification or azeotropic rectification, but through extractive rectification or azeotropic rectification, it is necessary to introduce a third component as an extractant or entrainer, resulting in the circulation of methyl tert-butyl ether It is inevitable to introduce other impurities during use, which will affect the quality of intermediate E2

Method used

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  • A method for recovering methyl tert-butyl ether in pharmaceutical process waste liquid by extractive distillation-adsorption coupling process

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Embodiment 1

[0033] use figure 1 In the process flow shown, the body material of the extractive distillation tower T1 is SUS304, the tower is filled with BX regular wire mesh packing, the tower diameter is 1200mm, the number of theoretical plates is 32, and the extraction agent is fed from the sixth theoretical plate, the pharmaceutical process Waste liquid is fed from the 21st theoretical plate. Extractant recovery tower T2 tower body material is SUS304, the tower is filled with BX regular wire mesh packing, the tower diameter is 500mm, the number of theoretical plates is 24, and the 14th theoretical plate is fed. The body material of the n-butane separation tower T3 is SUS304, the tower is filled with BX regular wire mesh packing, the tower diameter is 600mm, the number of theoretical plates is 30, and the 13th theoretical plate is fed. Adsorption and dehydration towers A1~A4 are made of SUS304, with a tower diameter of 1200mm and a height of 3000mm. There are 503 DN38 tubes installed i...

Embodiment 2

[0037] use figure 1 In the process flow shown, the body material of the extractive distillation tower T1 is SUS304, the tower is filled with BX regular wire mesh packing, the tower diameter is 1200mm, the number of theoretical plates is 32, and the extraction agent is fed from the sixth theoretical plate, the pharmaceutical process Waste liquid is fed from the 21st theoretical plate. Extractant recovery tower T2 tower body material is SUS304, the tower is filled with BX regular wire mesh packing, the tower diameter is 500mm, the number of theoretical plates is 24, and the 14th theoretical plate is fed. The body material of the n-butane separation tower T3 is SUS304, the tower is filled with BX regular wire mesh packing, the tower diameter is 600mm, the number of theoretical plates is 30, and the 13th theoretical plate is fed. Adsorption and dehydration towers A1~A4 are made of SUS304, with a tower diameter of 1200mm and a height of 3000mm. There are 503 DN38 tubes installed i...

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Abstract

The invention belongs to the field of solvent recovery, and in particular relates to a method for recovering methyl tertiary butyl ether from waste liquid in a pharmaceutical process by an extractive distillation-adsorption coupling process. Using water as the extractant and the waste liquid of the pharmaceutical process respectively enter the extractive rectification tower according to a certain solvent ratio, the crude product containing n-butane and methyl tert-butyl ether is separated at the top of the extractive rectification tower, and the material in the tower still enters the extractant. The recovery tower recovers the extractant, and the extractant recovered from the column is cooled and returned to the extractive rectification tower for recycling; after the material at the top of the extractive rectification tower is stratified by the phase separator, the lower water phase is returned to the extractive rectification tower, The upper oil phase enters the adsorption dehydration system to obtain the n-butane-containing methyl tert-butyl ether material, which enters the n-butane separation tower, and the tower still obtains the methyl tert-butyl ether, which can be recycled as a pharmaceutical solvent. The invention uses the existing component water in the waste liquid as the extractant, effectively avoids introducing other components to affect the recycling use of methyl tertiary butyl ether, and is an efficient and energy-saving separation process.

Description

technical field [0001] The invention belongs to the field of solvent recovery, and in particular relates to a method for recovering methyl tert-butyl ether in pharmaceutical process waste liquid through an extractive distillation-adsorption coupling process. Background technique [0002] 4-Chloro-2-(trifluoroacetyl)aniline hydrochloride hydrate, referred to as E2, molecular formula: C 8 h 5 CIF 3 NO·HCl·H 2 O, molecular weight: 278, CAS number: 173676-59-0, is a white or light yellow crystalline powder, main use: as a key intermediate for the synthesis of anti-AIDS drug efavirenz. Intermediate E2 is obtained by using p-chloroaniline as the starting material, first performing condensation reaction with pivaloyl chloride, then undergoing acylation reaction and hydrolysis reaction, and finally refined. During the condensation reaction and acylation reaction, it needs to be carried out in a large amount of methyl tert-butyl ether solvent. The reaction process is accompanied ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C43/04C07C41/42C07C41/36
CPCC07C41/36C07C41/42C07C43/046Y02P20/10
Inventor 杨金杯陈文韬余美琼陈玉成
Owner FUQING BRANCH OF FUJIAN NORMAL UNIV
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