Continuous hydrogenation method and application of ethyl pyrazine-2-carboxylate

A technology of ethyl formate and pyrazine, which is applied in the field of continuous hydrogenation of ethyl pyrazine-2-carboxylate, can solve problems such as difficulty in controlling spontaneous combustion of catalysts, heavy labor in autoclave operation, and inability to control excessive reduction, etc. Risk of spontaneous combustion, reduced risk of impurity formation, low cost effect

Active Publication Date: 2020-08-21
ASYMCHEM LIFE SCI TIANJIN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The technology described in this patented describes an improved way to make certain chemicals called pimelic acid or 4-(pirfenoxymonazo)acetic acid (PPMNA). These compounds have various uses such as being useful intermediates in medicine chemistry researches. They were made through reacting formaldehydes and amines under specific conditions. This was done successfully because it allowed these molecules to mix together while forming tiny particles that could move around inside liquid crystals. It resulted in better results when making new products like pesticides.

Problems solved by technology

This patented technical problem addressed by this patents relates to improving the efficiency and quality of producing chemicals from alkynes due to their potential explosion hazards during production processes such as hydrocracking. Current methods involve multiple steps that require significant amounts of energy input, which can lead to unsafe conditions when workers are exposed while performing these operations. Therefore there is an urgent demand for improved ways to produce chemistry with fewer steps without compromising on its overall effectiveness.

Method used

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  • Continuous hydrogenation method and application of ethyl pyrazine-2-carboxylate

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Effect test

Embodiment 1

[0041] Dispersion process: disperse ethyl pyrazine-4-carboxylate and hydrogen in collision convection (jet method), the gas-liquid ratio is 1:100, and form a gas-liquid mixture containing small droplets with a particle size of 50nm to 50μm , as the reaction raw material.

[0042] Continuous reaction: Pack 5% Ru / C catalyst in the reaction column. Alumina microspheres (1mm) are used at both ends, the mass of the middle catalyst is 28.38g, the filling height is 300mm, the filling diameter is 19.2mm, and the particle size of the catalyst is 1mm. It is used as the catalytic hydrogenation device 40 (fixed bed reactor).

[0043] The above-mentioned reaction raw materials are continuously passed into the above-mentioned catalytic hydrogenation device 40 (fixed-bed reactor) for catalytic hydrogenation reaction to obtain ethyl piperazine-4-carboxylate, wherein the catalytic hydrogenation device 40 (fixed-bed reactor) is controlled in two stages. temperature, and along the material flow...

Embodiment 2

[0045] Dispersion process: disperse ethyl pyrazine-4-carboxylate and hydrogen in collision convection (jet method), the gas-liquid ratio is 1:100, and form a gas-liquid mixture containing small droplets with a particle size of 50nm to 50μm , as the reaction raw material.

[0046] Continuous reaction: Pack 5% Ru / C catalyst in the reaction column. Alumina microspheres (1mm) are used at both ends, the mass of the middle catalyst is 28.38g, the filling height is 300mm, the filling diameter is 19.2mm, and the particle size of the catalyst is 1mm. It is used as the catalytic hydrogenation device 40 (fixed bed reactor).

[0047] The above-mentioned reaction raw materials are continuously passed into the above-mentioned catalytic hydrogenation device 40 (fixed-bed reactor) for catalytic hydrogenation reaction to obtain ethyl piperazine-4-carboxylate, wherein the catalytic hydrogenation device 40 (fixed-bed reactor) is controlled in two stages. temperature, and along the material flow...

Embodiment 3

[0049] Dispersion process: Disperse ethyl pyrazine-4-carboxylate and hydrogen gas by means of collision convection (jet flow method), with a gas-liquid ratio of 1:100, to form a gas-liquid mixture containing small droplets with a particle size of 50nm to 50μm. as a reaction material.

[0050] Continuous reaction: Pack 5% Ru / C catalyst in the reaction column. Alumina microspheres (1mm) are used at both ends, the mass of the middle catalyst is 28.38g, the filling height is 300mm, the filling diameter is 19.2mm, and the particle size of the catalyst is 1mm. It is used as the catalytic hydrogenation device 40 (fixed bed reactor).

[0051] The above-mentioned reaction raw materials are continuously passed into the above-mentioned catalytic hydrogenation device 40 (fixed-bed reactor) for catalytic hydrogenation reaction to obtain ethyl piperazine-4-carboxylate, wherein the catalytic hydrogenation device 40 (fixed-bed reactor) is controlled in two stages. temperature, and along the ...

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Abstract

The invention provides a continuous hydrogenation method of ethyl pyrazine-2-carboxylate. The continuous hydrogenation method comprises the following steps: dispersing a mixture of ethyl pyrazine-2-carboxylate and hydrogen to form a gas-liquid mixture containing small liquid drops with sizes of 50 nm-5 mm, wherein the gas-liquid mixture is used as a reaction raw material; and continuously inputting the reaction raw material into a fixed bed reactor, carrying out a catalytic hydrogenation reaction, and continuously discharging ethyl pyrazine-2-carboxylate, wherein the fixed bed reactor is divided into at least two temperature control sections along the flowing direction of the material, and the temperature of the latter temperature control section is controlled to be lower than the temperature of the former temperature control section. According to the above forced dispersion process, the reaction raw material can be subjected to high-performance mass transfer in the catalytic hydrogenation reaction process, so the sufficient reaction degree of the reaction raw material is improved, and reaction time is shortened. The fixed bed reactor is subjected to sectional temperature controlalong the flowing direction of the material, so heat accumulation can be effectively removed, a reaction state in the reactor can be effectively controlled, and the yield, purity and product performance stability of a target product, namely ethyl pyrazine-2-carboxylate are improved.

Description

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Claims

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Application Information

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Owner ASYMCHEM LIFE SCI TIANJIN
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