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Process for preparing phenylhydrazine sulfate by continuous method

A sulfate, continuous process technology, applied in the preparation of hydrazine, organic chemistry, etc., can solve the problems of low yield, poor yield reproducibility, restricting equipment efficiency, etc.

Pending Publication Date: 2021-04-27
NANTONG ACETIC ACID CHEM +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] However, the reaction of the subsequent reduction step is slow, and it often takes several hours to complete the reaction, which seriously restricts the equipment efficiency, such as the methods reported in the literature such as Organic Syntheses, 1941, 1,442, CN101928246, European Journal of Medicinal Chemistry, 2016, 120, 37-50, etc. Subsequent reduction and hydrolysis take more than 3 hours, and a large amount of wastewater is generated
The advantages of the continuous preparation of diazonium salts in the early stage are greatly reduced, and the yield obtained is often not high
In addition, most of the reduction methods reported in the literature are traditional batch reactions, and the temperature difference between different reaction areas such as the wall and the center of the kettle is large, and slight changes in the process conditions during the preparation of phenylhydrazine often lead to large fluctuations in the yield. poor reproducibility

Method used

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  • Process for preparing phenylhydrazine sulfate by continuous method
  • Process for preparing phenylhydrazine sulfate by continuous method
  • Process for preparing phenylhydrazine sulfate by continuous method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Embodiment 1, continuous method prepares aniline diazonium salt

[0043] Dissolve aniline in 15% sulfuric acid solution (aniline to sulfuric acid=1:1.2, molar ratio), 25% sodium nitrite solution according to aniline:NaNO 2= The ratio of 1:1.05 is pumped into the pipeline reactor by the metering pump respectively (see figure 1 diazotization zone), the temperature of the heat exchange medium (water bath or oil bath) is 25°C, and the residence time is 80s. The purity of the diazonium salt detected by sampling HPLC is about 97%, and the yield of the diazotization reaction is 96%. The obtained diazonium salt The solution is pumped directly into the next reaction.

[0044] The yield of aniline diazonium salt prepared by the method can be more than 95%.

Embodiment 2

[0045] Embodiment 2, continuous method prepares phenylhydrazine sulfate

[0046] The diazonium salt (the yield of diazotization reaction is estimated according to 95%), 20% NaHSO 3 Solution according to diazonium salt: NaHSO 3 = The ratio of 1:3 is pumped into the bamboo-shaped pulse tube reactor for continuous reaction (see figure 1 reduction zone), the temperature in this zone is set to T 1 ; After the material flows out, another metering pump is used to pump 40% dilute sulfuric acid into the reaction pipeline (see figure 1 hydrolysis zone) for hydrolysis, NaHSO in dilute sulfuric acid and reduction reaction 3 The molar weights are equal, and the temperature in the hydrolysis zone is set to T 2 , The material flowing out from the pipeline is directly passed into the crystallization kettle for cooling and crystallization, and then centrifugally filtered to obtain the product phenylhydrazine sulfate. The residence time in the reduction zone is set to t 1 , and the reside...

Embodiment 3

[0049] Embodiment 3, different NaHSO 3 Dosage

[0050] With reference to the method of embodiment 2, select the residence time and temperature condition of serial number 4 in table 1, change NaHSO 3 Dosage (referring to NaHSO 3 Consumption is the multiple of the amount of material of diazonium salt), other conditions are constant, and the result obtained is as shown in table 2:

[0051] Table 2. NaHSO 3 Dosage result

[0052]

[0053]

[0054] The result of table 2 shows: Yield increases with NaHSO 3 The increase of dosage increases, but when it exceeds 3 times, the range of increase is extremely limited.

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Abstract

The invention discloses a process for preparing phenylhydrazine sulfate by a continuous method, which comprises the following steps: reducing a phenyl diazonium salt solution by using a NaHSO3 solution to generate phenylhydrazine sulfate, the molar ratio of diazonium salt to NaHSO3 being 1: (2.5-5.5); and respectively pumping a phenyl diazonium salt solution and a sodium hydrogen sulfite solution into a pipeline reactor by a metering pump under the condition that the mixing temperature is 5-30 DEG C, controlling the temperature of the pipeline reactor in a sectional manner, performingfront stagecontrolling at 50-80 DEG C for retention time of 5-10 minutes, adding a dilute sulphuric acid solution into a reaction pipeline, performing rear stage controlling at 80-100 DEG C forretention time of 15-25 minutes, then introducing into a crystallization kettle, cooling to 0-5 DEG C, crystallizing, and centrifuging. A continuous method is used for replacing traditional intermittent operation, the operation efficiency and safety are greatly improved, workshops are saved, equipment investment is reduced, energy consumption is reduced, and manpower is reduced.

Description

technical field [0001] The invention relates to the field of chemical synthesis, in particular to a preparation method of phenylhydrazine sulfate. Background technique [0002] Phenylhydrazine salts (including hydrochloride, sulfate, etc.) have an extremely important position in the fields of fine chemicals and organic synthesis, especially as important raw materials and intermediates for medicines and pesticides, and can synthesize a series of medicines, dyes, and azo compounds And other raw materials of fine chemicals, such as pyrazolone pesticides, celecoxib and its similar series of APIs, etc. [0003] The synthetic method of phenylhydrazine salt is mainly through three steps of diazotization, reduction and acidification hydrolysis. Since the diazonium salt synthesized during the diazotization reaction is unstable and highly active, it can be decomposed and exploded by heat, friction, or impact, and the diazonium salt can be decomposed at room temperature, so the diazot...

Claims

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Application Information

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IPC IPC(8): C07C243/22C07C241/02
CPCC07C241/02C07C243/22
Inventor 庆九俞新南朱小刚刘芳
Owner NANTONG ACETIC ACID CHEM
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