Micro reaction system and method for preparing 2-methyl-4-amino-5-cyanopyrimidine using same

Patent metadata

Field	Value
Publication number	US-11554355-B2
Application number	US-202117467060-A
Country	US
Kind code	B2
Filing date	Sep 3, 2021
Priority date	Nov 5, 2020
Publication date	Jan 17, 2023
Grant date	Jan 17, 2023

Abstract

Disclosed herein relates to pharmaceutical engineering, and more particularly to a micro reaction system and a method for preparing 2-methyl-4-amino-5-cyanopyrimidine using the same. An acetamidine hydrochloride solution and an (dimethylaminomethylene)malononitrile solution are separately pumped into the micro reaction system including a micromixer and an agitating microchannel reactor in communication at the same time for a continuous condensation-cyclization reaction to obtain 2-methyl-4-amino-5-cyanopyrimidine.

First claim

What is claimed is:

1. A method for preparing 2-methyl-4-amino-5-cyanopyrimidine using a micro reaction system, the micro reaction system comprising a micromixer and an agitating microchannel reactor communicated in sequence, and the method comprising:
(1) pumping an acetamidine hydrochloride solution and a (dimethylaminomethylene)malononitrile solution separately into the micromixer at the same time followed by mixing;
(2) allowing the reaction mixture flowing out of the micromixer to enter the agitating microchannel reactor; and subjecting the reaction mixture to condensation-cyclization reaction; and
(3) collecting the reaction mixture flowing out of the micro reaction system; and subjecting the reaction mixture to separation and purification to obtain a target product 2-methyl-4-amino-5-cyanopyrimidine;
wherein the 2-methyl-4-amino-5-cyanopyrimidine is shown in formula (I); the acetamidine hydrochloride is shown in formula (II); the (dimethylaminomethylene)malononitrile is shown in formula (III); the condensation-cyclization reaction is shown in the following reaction scheme;

2. The method of claim 1 , wherein in step (1), the acetamidine hydrochloride solution is prepared by dissolving acetamidine hydrochloride in a methanol solution containing sodium methoxide at −20-15° C.; a molar concentration of sodium methoxide in the methanol solution is 0.5-7 mol/L; and a molar ratio of acetamidine hydrochloride in the acetamidine hydrochloride solution to the sodium methoxide in the acetamidine hydrochloride solution is controlled at 1:0.7-1.3.

3. The method of claim 1 , wherein in step (1), the (dimethylaminomethylene)malononitrile solution is prepared by dissolving (dimethylaminomethylene)malononitrile in methanol; and a molar concentration of the (dimethylaminomethylene)malononitrile in the (dimethylaminomethylene)malononitrile solution is 0.8-1.8 mol/L.

4. The method of claim 1 , wherein in step (1), the micromixer is a static mixer, a T-shaped micromixer, a Y-shaped micromixer, a coaxial flow micromixer or a flow-focusing micromixer.

5. The method of claim 1 , wherein in step (1), flow rates of the acetamidine hydrochloride solution and the (dimethylaminomethylene)malononitrile solution pumped into the micromixer are controlled to adjust a molar ratio of the acetamidine hydrochloride to the (dimethylaminomethylene)malononitrile to 1:0.6-1.2; and a temperature in the micromixer is controlled at −10-100° C.

6. The method of claim 1 , wherein the micro reaction system further comprises:
a first pump for feeding the acetamidine hydrochloride solution;
a second pump for feeding the (dimethylaminomethylene)malononitrile solution;
a gas-liquid separator; and
a back pressure valve;
wherein a first inlet of the micromixer is connected to the first pump; a second inlet of the micromixer is connected to the second pump; an outlet of the micromixer is connected to an inlet of the agitating microchannel reactor; a top of the gas-liquid separator is provided with a first port, a second port and a third port; the first port is connected to an outlet of the agitating microchannel reactor; the second port is configured to introduce nitrogen to provide a pressure in the gas-liquid separator, where a pressure of the nitrogen is 0-2.5 MPa; the third port is connected to the back pressure valve, where a back pressure of the back pressure valve is 0-2 MPa; and the pressure of the nitrogen is 0-0.5 MPa larger than a back pressure set by the back pressure valve.

7. The method of claim 1 , wherein in step (2), the agitating microchannel reactor comprises:
at least one reaction plate; and
at least one heat exchange plate;
wherein the at least one heat exchange plate fastened to the at least one reaction plate; each of the at least one reaction plate is provided with at least one inlet channel, at least one outlet channel, N reaction fluid channel(s) and N+1 mixing chambers, wherein Nis an integer equal to or greater than 1; each of the N+1 mixing chambers is a three-dimensional cavity; each of the N+1 mixing chambers is provided with a stirrer therein; the N+1 mixing chambers are communicated with the N reaction fluid channel(s); one end of the at least one inlet channel is connected to an inlet of the agitating microchannel reactor, and the other end of the at least one inlet channel is communicated with a mixing chamber adjacent thereto; one end of the at least one outlet channel is connected to an outlet of the agitating microchannel reactor, the other end of the at least one outlet channel is communicated with a mixing chamber adjacent thereto; each of the at least one heat exchange plate is provided with a temperature-control medium channel; two ends of the temperature-control medium channel are provided with a temperature-control medium inlet and a temperature-control medium outlet; the agitating microchannel reactor is arranged at a base or a support that is vibratile horizontally or vertically with a constant amplitude; a hydraulic diameter of the at least one inlet channel is 0.1-20 mm; a hydraulic diameter of the at least one outlet channel is 0.1-20 mm; a hydraulic diameter of the N reaction fluid channel(s) is 0.1-20 mm; a depth of each of the N+1 mixing chambers is 40-90% of a thickness of the at least one reaction plate; a hydraulic diameter of a cross-section of each of the N+1 mixing chambers is 2-50 mm; a volume of each of the N+1 mixing chambers is 1-50 mL; the stirrer is 30-95% by volume of each of the N+1 mixing chambers; and a vibration frequency of the base or support is controlled at 0-15 Hz.

8. The method of claim 7 , wherein the N+1 mixing chambers are cylindrical or prismatic.

9. The method of claim 7 , wherein the agitating microchannel reactor is a Coflore agitated cell reactor.

10. The method of claim 1 , wherein in step (2), a temperature in the agitating microchannel reactor is controlled at 0-100° C., and a residence time of the reaction mixture in the agitating microchannel reactor is controlled to 1-60 min.

11. A micro reaction system for preparing 2-methyl-4-amino-5-cyanopyrimidine, comprising:
a first pump;
a second pump;
a micromixer;
an agitating microchannel reactor;
a gas-liquid separator; and
a back pressure valve;
wherein the first pump is configured to feed an acetamidine hydrochloride solution; the second pump is configured to feed a (dimethylaminomethylene)malononitrile solution; a first inlet of the micromixer is connected to the first pump; a second inlet of the micromixer is connected to the second pump; an outlet of the micromixer is connected to an inlet of the agitating microchannel reactor; a top of the gas-liquid separator is provided with a first port, a second port and a third port; the first port is connected to an outlet of the agitating microchannel reactor; the second port is configured to introduce nitrogen to provide a pressure in the gas-liquid separator, where a pressure of the nitrogen is 0-2.5 MPa; the third port is connected to the back pressure valve; a back pressure of the back pressure valve is 0-2 MPa; and the pressure of the nitrogen is 0-0.5 MPa larger than a backpressure set by the back pressure valve;
the acetamidine hydrochloride solution and the (dimethylaminomethylene)malononitrile solution are pumped into the micromixer at the same time through the first pump and the second pump, respectively; the reaction mixture flowing out of the micromixer enters the agitating microchannel reactor and undergoes a continuous condensation-cyclization reaction; the reaction mixture flowing out of the agitating microchannel reactor enters the gas-liq

Assignees

• Univ Fudan

Inventors

• Chen Fener
• Jiang Meifen
• Cheng Dang
• Liu Minjie
• Huang Huashan

Classifications

• B01J2219/00909

  using filters · CPC title

• C07D239/42 Primary

  One nitrogen atom (nitro radicals C07D239/30) · CPC title

• B01J2219/00963

  Pressure · CPC title

• B01J2219/00889

  Mixing · CPC title

• B01J19/0093 Primary

  Microreactors, e.g. miniaturised or microfabricated reactors (laboratory containers with capillary fluid transport in microfabricated channels or chambers B01L3/5027) · CPC title