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Method for preparing piperazine pyridine compound through continuous reaction

A technology of piperazine pyridine and compounds, applied in the field of pharmaceutical synthesis, can solve problems such as safety, stability and high-efficiency reaction, low heat transfer efficiency, and overflow.

Pending Publication Date: 2021-07-16
浙江瑞博制药有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Low heat transfer efficiency will lead to high local temperature, and uneven mass transfer will lead to high local concentration of the material, which will easily lead to rapid temperature rise and lead to out-of-control reaction, eventually causing dangers such as overflow and explosion.
And as the reaction proceeds, the concentration of the reaction substrate will gradually decrease, and the reaction will gradually slow down or even stop. Even if the reaction time is increased, it is difficult to ensure the complete conversion of the reactant
On the one hand, it causes a large amount of unreacted Grignard reagent to be wasted; on the other hand, due to the high activity of Grignard reagent, post-processing such as quenching has a high risk
Therefore, it is difficult to meet the requirements of safety, stability and high efficiency of the reaction at the same time based on the batch tank process developed by the existing technology.

Method used

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  • Method for preparing piperazine pyridine compound through continuous reaction
  • Method for preparing piperazine pyridine compound through continuous reaction
  • Method for preparing piperazine pyridine compound through continuous reaction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] The prepared piperazine triethylamine compound solution is pumped into the static mixer and the pipeline reactor through the pump A and the pyridine solution through the pump B in proportion to control the temperature at 20°C, and the reaction time in the pipeline reactor is 240 seconds to carry out the condensation reaction. After 240 seconds, the quenched washing liquid is pumped into the static mixer for on-line mixing and quenching washing through the pump C, and then the on-line separation is carried out through the liquid-liquid separator, and the waste liquid phase enters the storage tank E. The organic phase enters the catalyst fixed-bed reactor, and at the same time, the hydrogen enters the fixed-bed reactor through the gas mass flow meter at a rate of 1.05 eq, and the hydrogen is first adsorbed on the surface by the palladium carbon of the fixed bed to form a fixed bed. The hydrogenation function back pressure valve controls the pressure to 0.5MPa, the reaction...

Embodiment 2

[0023] The prepared piperazine triethylamine compound solution is pumped into the static mixer and the pipeline reactor through the pump A and the pyridine solution through the pump B in proportion to control the temperature at 40°C, and the reaction time in the pipeline reactor is 160 seconds to carry out the condensation reaction. After 160 seconds, the quenching washing liquid is pumped into the static mixer for online mixing and quenching washing through the pump C, and then separated online by the liquid-liquid separator, and the waste liquid phase enters the storage tank E. The organic phase enters the catalyst fixed-bed reactor, and at the same time, the hydrogen gas enters the fixed-bed reactor at a rate of 1.2 eq through the gas mass flow meter, and the hydrogen is first adsorbed on the surface by the palladium carbon of the fixed bed to form a fixed bed. The hydrogenation function back pressure valve controls the pressure to 0.8MPa, the reaction temperature is control...

Embodiment 3

[0025] The prepared piperazine triethylamine compound solution is pumped through pump A and pyridine compound solution through pump B in proportion to the static mixer and pipeline reactor at the same time to control the temperature at 60°C. The reaction time in the pipeline reactor is 80 seconds for condensation reaction. The quenched washing liquid is pumped into the static mixer after 80 seconds through the pump C for online mixing and quenching washing, and then separated online by the liquid-liquid separator, and the waste liquid phase enters the storage tank E. The organic phase enters the catalyst-supported bed reactor, and at the same time, the hydrogen gas first enters the fixed-bed reactor through the gas mass flow meter at a rate of 1.4 eq, and the hydrogen is first adsorbed on the surface by the palladium carbon of the fixed-supported bed to form a fixed-supported bed. The hydrogenation function back pressure valve controls the pressure to 1.2MPa, the reaction tempe...

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PUM

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Abstract

The invention relates to a method for preparing a piperazine pyridine compound through a continuous reaction. The method comprises the steps of continuous condensation and hydrogenation. The continuous condensation reaction comprises the following steps: mixing a piperazine alkali solution and a pyridine solution which are used as raw materials, and reacting in a pipeline reactor. The reaction temperature of the pipeline reactor can be set in a temperature range of 10-80 DEG C, preferably 20-60 DEG C. The reaction time can also be set, for example, the reaction time ranges from 30 S to 300 S, and preferably, the reaction time is about 80 S. Then, a continuous hydrogenation reaction step is carried out, the temperature of the continuous hydrogenation reaction is controlled to be 10-100 DEG C, preferably about 40-80 DEG C, and the reaction time is controlled to be 20-200 S, preferably about 100 S. The continuous hydrogenation reduction reaction can be carried out in a catalyst fixed bed, and can also be carried out in a continuous microreactor.

Description

technical field [0001] The invention relates to the field of pharmaceutical synthesis, in particular to a preparation method of a piperazine pyridine compound. Background technique [0002] Palbociclib combined with letrozole as endocrine-based first-line therapy for patients with advanced breast cancer. [0003] The main synthetic method of palbociclib is 4-(6-aminopyridin-3-yl)piperazine-tert-butyl carboxylate and 6-bromo-2-chloro-8-cyclopentyl-5-methyl-pyridine Condensation of [2,3-D]pyrimidin-7(8H)-one, followed by heck reaction, and then deprotection to form a salt. Among them, the synthesis of 4-(6-aminopyridin-3-yl)piperazine-tert-butyl carboxylate, according to literature reports, mainly contains the following two synthetic routes: According to the WO2010020675 process description, using 5-chloro-2-nitro Pyridine and piperazine are condensed in tert-butanol, and then in tetrahydrofuran, potassium carbonate is used as a base, free amino groups are protected with Boc...

Claims

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Application Information

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IPC IPC(8): C07D213/75
CPCC07D213/75Y02P20/55
Inventor 罗力军朱国良许伟泽何前陈仟
Owner 浙江瑞博制药有限公司
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