Separation method of hydrogenated mixed liquor in production process of p-aminodiphenylamine

A technology for the separation of p-aminodiphenylamine and its separation method, which is applied in the field of separation of hydrogenation mixed liquid in the production of p-aminodiphenylamine, which can solve the problem of large loss of phase transfer catalyst and product, increased consumption of condensation reaction catalyst, increased difficulty and cost of post-processing, etc. problems, to achieve the effect of easy recycling, improving separation effect and reducing the difficulty of post-processing

Active Publication Date: 2018-05-15
QINGDAO UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this process are as follows: (1) In the process of oil-water separation, the phase difference between oil and water is small, the delamination speed is slow and the delamination effect is poor, and the phenomenon of water-in-oil and oil-in-water is serious, resulting in a large loss of phase transfer catalyst and product; (2) Washing and extraction consumes a lot of water, and ...

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Embodiment 1: A kind of separation method of hydrogenation mixed liquor in the production of p-aminodiphenylamine

[0018] (1) Taking the hydrogenated mixed liquid filtered by hydrogenation catalyst after the production reaction of p-aminodiphenylamine as the processing object, the hydrogenated mixed liquid is sent to the desolventization tower to remove methanol, and the desolventization tower is operated under reduced pressure, and the operating temperature is 40-42°C, the distilled methanol is extracted from the top of the tower, and the water content of methanol is 1-40%; the remaining mixture of tetramethylammonium hydroxide aqueous solution, aniline, and p-aminodiphenylamine is extracted from the bottom of the tower next process;

[0019] (2) Send the mixed liquid at the bottom of the tower obtained in step (1) into the extraction and separation tower, and at the same time, add n-hexane in the tower as the extraction solvent to fully contact and mix with the mixed...

Embodiment 2

[0021] Embodiment 2: a kind of separation method of hydrogenation mixed liquor in the production of p-aminodiphenylamine

[0022] (1) Treat the hydrogenated mixed liquid filtered by the hydrogenation catalyst after the production reaction of p-aminodiphenylamine as the processing object, send the hydrogenated mixed liquid to the desolventization tower to remove isopropanol, and the desolventization tower is operated under reduced pressure. The temperature is 70-72°C, the distilled isopropanol is extracted from the top of the tower, and the water content of isopropanol is 40%; Bottom mining enters the next process;

[0023] (2) Send the mixed liquid at the bottom of the tower obtained in step (1) into the extraction and separation tower. At the same time, benzene is incorporated into the tower as an extraction solvent to fully contact and mix with the mixed liquid. Benzene and tetramethylammonium hydroxide aqueous solution, aniline, p-amino The volume ratio of the mixed soluti...

Embodiment 3

[0025] Embodiment 3: a kind of separation method of hydrogenation mixed liquor in the production of p-aminodiphenylamine

[0026] (1) Treat the hydrogenated mixed liquid filtered by the hydrogenation catalyst after the production reaction of p-aminodiphenylamine as the processing object, send the hydrogenated mixed liquid to the desolventization tower to remove n-butanol, and the desolventization tower is operated under reduced pressure, and the operation The temperature is 40-72°C, the distilled n-butanol is extracted from the top of the tower, and the water content of n-butanol is 20%; Bottom mining enters the next process;

[0027] (2) Send the mixed liquid at the bottom of the tower obtained in step (1) into the extraction and separation tower, and at the same time, add toluene in the tower as an extraction solvent to fully contact and mix with the mixed liquid. Toluene and tetramethylammonium hydroxide aqueous solution, aniline, p-amino The volume ratio of the mixed solu...

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Abstract

The invention relates to the technical field of production of rubber antioxidant midbody, and particularly discloses a separation method of a hydrogenated mixture in the production process of p-aminodiphenylamine. The separation method is characterized in that hydrogenated mixed liquid is sent to a desolventizer tower to remove hydrogenation reaction solvent alcohol, and the rest mixed liquid is recovered from the tower bottom; the tower bottom mixed liquid is sent to an extraction separating tower, meanwhile an extraction solvent is melted in the tower, aniline and p-aminodiphenylamine in themixed liquid are extracted out to serve as an oil phase to be extracted from the tower top of the extraction tower, and a tetramethyl ammonium hydroxide water solution is extracted from the tower bottom; and the oil phase is sent to a distillation separation procedure, an extraction agent and aniline are steamed from the tower top respectively, and p-aminodiphenylamine is extracted out from the tower bottom. Compared with a traditional separation method, the separation method effectively improves the layering speed and the separation effect of the oil phase and a water phase, water consumption amount is small, the postprocessing difficult for recycling a condensation catalyst-tetramethyl ammonium hydroxide is reduced, consumption of the condensation catalyst is decreased, meanwhile the extraction agent is easy to recycle for cycle use, and the method is convenient and rapid, and economical and effective.

Description

(1) Technical field [0001] The invention relates to the technical field of production of rubber antioxidant intermediates, in particular to a method for separating a hydrogenated mixed liquid in the production of p-aminodiphenylamine. (2) Background technology [0002] The preparation reaction of p-aminodiphenylamine (RT-base), an important intermediate of p-phenylenediamine rubber antioxidant, is divided into two steps: first, aniline and nitrobenzene are condensed in the presence of a catalyst to form The condensation liquid of nitrodiphenylamine and p-nitrosodiphenylamine, the catalyst used in this step reaction is mainly a quaternary ammonium base phase transfer catalyst, such as tetramethylammonium hydroxide; then the condensation liquid is subjected to catalytic hydrogenation reaction to form The hydrogenation mixed solution containing p-aminodiphenylamine, in addition to the product-p-aminodiphenylamine, the mixed solution also contains aniline, a condensation reactio...

Claims

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Application Information

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IPC IPC(8): C07C209/86C07C211/54
CPCC07C209/86C07C211/54Y02P20/584
Inventor 丁军委于文龙刘福胜李明
Owner QINGDAO UNIV OF SCI & TECH
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