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Preparation method of 3-acetamido-N,N-diacetoxyethylaniline

A technology of diacetoxyethylaniline and acetamido, which is applied in the field of organic chemical intermediate product preparation, can solve the problems of long operation time, high energy consumption, and strong smell of acetic acid, and achieve low waste water production, low energy consumption and material consumption, The effect of simple operation control and simple process flow

Active Publication Date: 2020-04-28
YANTAI ANOKY FINE CHEM CO LTD +7
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] First, the neutralization reaction mixture contains a large amount of water, which will cause partial hydrolysis of ethylene oxide during the hydroxyethylation reaction and increase the consumption of raw materials;
[0007] Second, the negative pressure distillation dehydration process takes a long time and consumes a lot of energy;
[0008] Third, after desalination by filtration, some products and by-product acetic acid adhere to the surface of the salt, which affects the total yield of the product, increases the difficulty of solid waste treatment, and has a strong smell of acetic acid during the operation

Method used

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  • Preparation method of 3-acetamido-N,N-diacetoxyethylaniline

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Embodiment 1 is the comparison of the technical solution of the present invention and the technical solution of the prior art during the workbench.

[0037] Add 110g of water into a 500ml four-necked bottle, add 150g of hydrochloride under stirring, heat up to 50°C, evenly add 32% liquid caustic soda dropwise until the end point pH=8-9, continue stirring at 60-65°C for 10min, Retest and adjust pH=8-9 with liquid caustic soda. Transfer the material to a separatory funnel, settle for 10-15min, separate out 180ml of mother liquor, transfer the oil phase into an autoclave, replace the gas in the autoclave with nitrogen three times, raise the temperature to 50°C, and feed ethylene oxide evenly for 7-8h Alkane 77.5g, after the addition, react at 50-55°C for 3.5h. Sampling and analysis showed that the middle class was 1.25%, and the main class was 97.27%. Transfer the material to a 500ml four-necked bottle, raise the temperature to 80°C, add 180g of acetic anhydride slowly o...

Embodiment 2

[0039] Embodiment 2 is mainly aimed at the comparison of ethylene oxide consumption.

[0040] Add 200ml of the mother liquor that has been used continuously for 8 times in a 500ml four-necked bottle, add 150g of hydrochloride under stirring, raise the temperature to 50°C, and evenly add 32% liquid caustic soda until the end point pH=8-9, at 60-65°C Stirring was continued for 10 min, and the test was repeated and the pH was adjusted to 8-9 with liquid caustic soda. Transfer the material to a separatory funnel, settle for 10-15 minutes, separate the oil phase, and filter the mother liquor while it is hot to obtain 44.7g of salt, 256ml of the mother liquor, 200ml for the next batch of experiments, and 56ml of the mother liquor for wastewater treatment. The oil phase was transferred into an autoclave, and the gas in the autoclave was replaced with nitrogen three times, then the temperature was raised to 50°C, and 72g of ethylene oxide was evenly introduced in 7-8h, and reacted at ...

Embodiment 3

[0042] Embodiment 3 is mainly aimed at the comparison of the amount of waste water produced.

[0043] Add 200ml of the mother liquor that has been used continuously for 9 times in a 500ml four-necked bottle, add 150g of hydrochloride under stirring, raise the temperature to 50°C, and evenly add 32% liquid caustic soda until the end point pH=8-9, at 60-65°C Stirring was continued for 10 min, and the test was repeated and the pH was adjusted to 8-9 with liquid caustic soda. Transfer the material to a separatory funnel, settle for 10-15min, separate the oil phase, and filter the mother liquor while it is hot to obtain 43.9g of salt, 258ml of mother liquor, of which 200ml is used for the next batch of experiments, and the remaining 58ml of mother liquor is used for wastewater treatment. The oil phase was transferred into an autoclave, and the gas in the autoclave was replaced with nitrogen three times, then the temperature was raised to 50°C, and 77.5g of ethylene oxide was evenly...

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Abstract

The invention discloses a preparation method of a dye intermediate that is 3-acetamido-N,N-dimethylformamide. The method comprises the following steps: adding a mechanically applied mother solution and m-aminoacetanilide hydrochloride into a neutralization reaction kettle, heating, neutralizing with a sodium hydroxide solution to the reaction endpoint, and carrying out liquid-liquid sedimentationlayering within the temperature range after heating; separating lower-layer salt and mother liquor, performing filtration to remove the salt while the mother liquor is hot, and applying the obtained mother liquor in the next batch; carrying out nitrogen displacement on the upper-layer oil phase, heating the material, and dropwise adding ethylene oxide to carry out a hydroxyethylation reaction; andafter the hydroxyethylation reaction is finished, transferring the material to an esterification kettle, heating, then dropwise adding acetic anhydride to carry out an esterification reaction, and cooling to 35 DEG C after the reaction is finished, thereby obtaining an acetic acid solution of 3-acetamido-N,N-diacetoxyethylaniline. The method is simple in technological process, easy to operate andcontrol, low in wastewater generation, and low in energy consumption and material consumption. A dehydration process before esterification is omitted, so that the production machine-hour is greatly shortened.

Description

technical field [0001] The invention belongs to the field of preparation of organic chemical intermediate products, and in particular relates to a preparation method of a dye intermediate 3-acetylamino-N,N-diacetoxyethylaniline. Background technique [0002] 3-Acetamido-N,N-diacetoxyethylaniline, commonly known as ruby ​​esterification solution, is a very important coupling component intermediate in disperse dyes. It is mainly used in the intermediates of synthetic dyes Disperse Red 167 and Disperse Red 74, etc. [0003] The traditional 3-acetamido-N,N-diacetoxyethylaniline production method comprises the following steps: [0004] 1. Neutralization - use m-aminoacetanilide hydrochloride as raw material, water as medium, neutralize with sodium hydroxide solution; 2. Hydroxyethylation - add ethylene oxide to the obtained reaction product for hydroxyethylation Reaction; 3. Negative pressure distillation and dehydration—the hydroxyethylated product is subjected to negative pre...

Claims

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Application Information

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IPC IPC(8): C07C233/43C07C231/12
CPCC07C231/12C07C233/43
Inventor 李连伟刘祥庆赵德禄许玉存渠晗曲雪云宋晓晨
Owner YANTAI ANOKY FINE CHEM CO LTD
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