Desalting purification method for water-washing extraction water phase in RT base production process

A production process and water extraction technology, applied in amino compound purification/separation, organic chemistry, etc., can solve the problems of difficult filtration, inability to continue, and increased side reactions in the system, so as to achieve no waste residue generation, significant desalination effect, and reduced The effect of processing difficulty

Active Publication Date: 2020-01-10
SHANDONG SUNSINE CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, it is necessary to strictly control the amount of condensation and dehydration when using NaOH to desalt, otherwise sodium salt will be introduced into the system, causing blockage of the condensation system pipeline, increasing the specific gravity of the water in the washing process, and increasing the side reactions of the system; in addition, it is difficult to filter the condensation liquid after desalting with NaOH , cannot be carried out continuously, and the environment for cleaning filter residues is harsh
with Ca(OH) 2 The amount of desalination is relatively large, because Ca(OH) 2 Slightly soluble in water, it is difficult to reduce the carbonate content to less than 1% during production, and a large amount of lime waste residue will be generated after treatment, which is low in efficiency, and calcium salts will also be introduced into the system

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The method of desalination and purification of the aqueous phase by washing and extracting in the production process of RT base:

[0034] Take the nitrobenzene method RT base production process and wash and extract the water phase, and the acid-base titration method detects that the mass fraction of tetramethylammonium hydroxide in the water phase is 17.5%, the mass fraction of carbonate is 2.6%, and the specific gravity is 1.032 .

[0035] Take 500g of the water-washed extraction water phase of the above nitrobenzene method RT base production process, add 50g of aniline and mix evenly, and separate the water phase after standing for 1 hour. When it does not come out (the outflow speed of the distillate is slower than 5s / d), stop heating, use primary water as the refrigerant to cool down and recrystallize, and then filter with nitrogen to obtain 142g of needle-like crystals, and finally press the mass ratio of needle-like crystals to distilled water to be 1:1 , add dis...

Embodiment 2

[0037] The method of desalination and purification of the aqueous phase by washing and extracting in the production process of RT base:

[0038] Take the tetramethylammonium hydroxide waste liquid (extracted water phase of the water washing process of the nitrobenzene method RT base production process) that cannot be used due to many impurities in the nitrobenzene method RT base production process, and acid-base titration method The mass fraction of tetramethylammonium hydroxide in the detection waste liquid is 8.2%, the mass fraction of carbonate is 3.4%, and its specific gravity is measured as 1.045.

[0039] Get 500g of tetramethylammonium hydroxide waste liquid that cannot be used because of many impurity components in the above nitrobenzene method RT base production process, add 100g aniline and mix evenly, separate the water phase after standing for 1 hour, and then control the temperature for 75 ℃, vacuum -0.098MPa, under reduced pressure distillation, when the distilla...

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Abstract

The invention discloses a desalting purification method for a water-washing extraction water phase in an RT base production process, and belongs to the technical field of fine chemical engineering. The desalting purification method for the water-washing extraction water phase in the RT base production process comprises the following steps: adding aniline into the washing-extraction water phase inthe nitrobenzene method RT base production process, performing uniform mixing, standing the obtained solution for layering, and separating out the water phase; and carrying out reduced pressure distillation on the water phase separated after aniline extraction at 80 DEG C or below, stopping heating when fractions are basically not discharged, performing cooling recrystallization, carrying out solid-liquid separation to obtain needle-like tetramethylammonium hydroxide crystals, and finally adding distilled water into the tetramethylammonium hydroxide crystals to prepare a solution with the massfraction of 20-25% for recycling. Compared with existing treatment methods, the extraction, concentration and recrystallization method for desalting purification of the water-washing extraction waterphase (impurity-containing tetramethylammonium hydroxide aqueous solution) in the RT base production process has the advantages of effective reduction of the treatment difficulty, obvious desalting effect, no generation of waste residues, economical property and environmental protection.

Description

technical field [0001] The invention relates to the technical field of fine chemicals, in particular to a method for desalting and purifying the aqueous phase by washing and extracting water in the RT base production process. Background technique [0002] The production of 4-aminodiphenylamine (RT base) by the nitrobenzene method is the most widely used process at home and abroad at present, and it is a green and clean production process due to the substantial reduction of the three wastes. [0003] However, this method also has some disadvantages: [0004] 1) Tetramethylammonium hydroxide, an organic base catalyst commonly used in the condensation process in production, is easy to decompose when the temperature is higher than 80°C, and it will react with CO in the air 2 The reaction will generate carbonates. Excessive carbonate content in the system will cause more adverse effects on production. It is necessary to regularly deal with the carbonates in the water extraction ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/84C07C211/55
CPCC07C209/84C07C211/55
Inventor 郭焕宇刘传红齐步金刘彬张玉柱
Owner SHANDONG SUNSINE CHEM
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