CN114437083A - Synthetic method of thioketone - Google Patents

Synthetic method of thioketone Download PDF

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Publication number
CN114437083A
CN114437083A CN202210127039.4A CN202210127039A CN114437083A CN 114437083 A CN114437083 A CN 114437083A CN 202210127039 A CN202210127039 A CN 202210127039A CN 114437083 A CN114437083 A CN 114437083A
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fluoro
triazolo
pyrimidine
methoxy
methoxypyrimidine
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田俊杰
朱恒营
索存川
季云飞
张海
刘振兴
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Dezhou Luba Fine Chemical Co ltd
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Dezhou Luba Fine Chemical Co ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D487/00Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00
    • C07D487/02Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00 in which the condensed system contains two hetero rings
    • C07D487/04Ortho-condensed systems

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  • Organic Chemistry (AREA)
  • Nitrogen Condensed Heterocyclic Rings (AREA)

Abstract

The invention belongs to the technical field of chemical synthesis, and particularly relates to a synthesis method of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione, which comprises the following steps: (1) dissolving 5-fluoro-4-hydrazino-2-methoxypyrimidine in a solvent for later use; (2) putting hydrogen peroxide into a storage tank for later use; (3) placing the carbon disulfide in a storage tank for later use; (4) at a certain temperature, respectively pumping 5-fluoro-4-hydrazino-2-methoxypyrimidine solution and carbon disulfide into a microchannel reactor I by using a diaphragm metering pump to complete the reaction; (5) then pumping hydrogen peroxide into a micro-channel reactor II by using a diaphragm metering pump, and finishing the oxidation reaction; (6) the reaction liquid is centrifuged by a centrifuge to obtain 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone solution. The method has the advantages of simple operation steps, low danger, high equipment utilization rate, complete reaction, high product stability and high yield.

Description

Synthetic method of thioketone
Technical Field
The invention relates to the technical field of chemical synthesis, in particular to a method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone.
Background
Florasulam is a triazolopyrimidine sulfonamide herbicide developed by the Dow agricultural science company in the United states, and the action mechanism of the florasulam is to inhibit the synthesis of acetolactate synthase so as to prevent the synthesis of related amino acid, so that the plants cannot synthesize protein to cause death. The florasulam is a high-efficiency low-toxicity broad-spectrum herbicide for preventing and killing broadleaf weeds by post-emergence stem and leaf treatment, and can effectively prevent and kill most broadleaf weeds such as cleavers, mai-home cocktails and the like in wheat fields and lawns.
8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione is used as an important intermediate for synthesizing florasulam, the synthesis reaction is an oxidation reaction which is one of 18 critical processes which are monitored in an important mode, and the conventional synthesis of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione generally adopts a kettle type reaction, so that the method is high in risk, low in equipment utilization rate, incomplete in reaction, poor in product stability, low in yield and not suitable for industrial production.
Disclosure of Invention
Aiming at the problems in the related art, the invention provides a synthetic method of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione.
The reaction equation is as follows:
Figure BDA0003500859020000011
in order to achieve the purpose, the invention provides the following technical scheme:
the invention provides a method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone, which comprises the following steps:
(1) dissolving 5-fluoro-4-hydrazino-2-methoxypyrimidine in a solvent for later use;
(2) putting hydrogen peroxide into a storage tank for later use;
(3) placing the carbon disulfide in a storage tank for later use;
(4) at a certain temperature, respectively pumping 5-fluoro-4-hydrazino-2-methoxypyrimidine solution and carbon disulfide into a microchannel reactor I by using a diaphragm metering pump, and finishing the reaction;
(5) then pumping hydrogen peroxide into a micro-channel reactor II by using a diaphragm metering pump, and finishing the oxidation reaction;
(6) the reaction liquid is centrifuged by a centrifuge to obtain 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone solution.
Preferably, the solvent is methanol or chloroform.
Preferably, the concentration of the 5-fluoro-4-hydrazino-2-methoxypyrimidine is 30-40%, and the dissolving temperature of the 5-fluoro-4-hydrazino-2-methoxypyrimidine solution is 30-40 ℃.
Preferably, the concentration of the hydrogen peroxide is 30% and 35%.
Preferably, the error of the diaphragm metering pump is less than 0.05%.
Preferably, the molar ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the carbon disulfide is 1: 1.10-1.30.
Preferably, the molar ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the hydrogen peroxide is 1: 1.05-1.20.
Preferably, the reaction temperature in the microchannel reactor I is 50-70 ℃; the residence time in the microchannel reactor I is 5-8 min.
Preferably, the reaction temperature in the microchannel reactor II is 30-50 ℃; and the residence time in the microchannel reactor II is 3-5 min.
Preferably, the rotating speed of the centrifugal machine is 2000-2500 r/min; the solid centrifuged by the centrifuge is sulfur.
Compared with the prior art, the invention has the beneficial effects that:
the method has the advantages of simple operation steps, low danger, high equipment utilization rate, complete reaction, high product stability and high yield, thereby being suitable for industrial production.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
The synthesis of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to this example had the following steps:
(1) transferring 1400Kg of dry methanol into a 3000L reaction kettle through a flowmeter, opening a manhole, adding 600Kg of 5-fluoro-4-hydrazino-2-methoxypyrimidine, heating to 30 ℃, stirring for 1h, fully dissolving for later use, and detecting the content of the 5-fluoro-4-hydrazino-2-methoxypyrimidine;
(2) setting the reaction temperature of a microchannel reactor I to be 50 ℃, respectively conveying 5-fluoro-4-hydrazino-2-methoxypyrimidine and carbon disulfide to two channels of the microchannel reactor I by using a diaphragm metering pump, adjusting the flow rate of the diaphragm metering pump, ensuring that the mol ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the carbon disulfide is 1:1.1, keeping the retention time of materials in the microchannel reactor I for 5min, and after the reaction is finished, feeding feed liquid into an intermediate storage tank for later use;
(3) setting the reaction temperature of the microchannel reactor II to be 30 ℃, respectively conveying the feed liquid and 30% of hydrogen peroxide which are subjected to upper reaction to two channels of the microchannel reactor II by using a diaphragm metering pump, adjusting the flow rate of the diaphragm metering pump, ensuring that the mol ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the hydrogen peroxide is 1:1.08, ensuring that the residence time of the materials in the microchannel reactor II is 3min, and after the reaction is finished, feeding the feed liquid into a finished product storage tank;
(4) and (3) conveying the feed liquid in the finished product tank to a centrifugal machine by using a gear pump, adjusting the rotating speed of the centrifugal machine to 2000r/min, and obtaining a methanol solution of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone after the centrifugation is finished, wherein the liquid phase normalization is 97.3%, and the yield is 92.5%.
EXAMPLES example 2
The synthesis of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to this example had the following steps:
(1) transferring 1400Kg of dry chloroform into a 3000L reaction kettle through a flowmeter, opening a manhole, adding 600Kg of 5-fluoro-4-hydrazino-2-methoxypyrimidine, heating to 30 ℃, stirring for 1h, fully dissolving for later use, and detecting the content of the 5-fluoro-4-hydrazino-2-methoxypyrimidine;
(2) setting the reaction temperature of a microchannel reactor I to be 60 ℃, respectively conveying 5-fluoro-4-hydrazino-2-methoxypyrimidine and carbon disulfide to two channels of the microchannel reactor I by using a diaphragm metering pump, adjusting the flow rate of the diaphragm metering pump, ensuring that the mol ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the carbon disulfide is 1:1.2, keeping the retention time of materials in the microchannel reactor I for 6min, and after the reaction is finished, feeding a feed liquid into an intermediate storage tank for later use;
(3) setting the reaction temperature of the microchannel reactor II to 50 ℃, respectively conveying the feed liquid and 30% of hydrogen peroxide which are subjected to upper reaction to two channels of the microchannel reactor II by using a diaphragm metering pump, adjusting the flow rate of the diaphragm metering pump, ensuring that the mol ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the hydrogen peroxide is 1:1.05, the retention time of the materials in the microchannel reactor II is 3min, and after the reaction is finished, feeding the feed liquid into a finished product storage tank;
(4) and (3) conveying the feed liquid in the finished product tank to a centrifuge by using a gear pump, adjusting the rotating speed of the centrifuge to 2000r/min, and obtaining a chloroform solution of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone after the centrifugation is finished, wherein the liquid phase normalization is 97.8%, and the yield is 93.3%.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (10)

1. A method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione, comprising the steps of:
(1) dissolving 5-fluoro-4-hydrazino-2-methoxypyrimidine in a solvent for later use;
(2) putting hydrogen peroxide into a storage tank for later use;
(3) placing the carbon disulfide in a storage tank for later use;
(4) at a certain temperature, respectively pumping 5-fluoro-4-hydrazino-2-methoxypyrimidine solution and carbon disulfide into a microchannel reactor I by using a diaphragm metering pump, and finishing the reaction;
(5) then pumping hydrogen peroxide into a micro-channel reactor II by using a diaphragm metering pump, and finishing the oxidation reaction;
(6) the reaction liquid is centrifuged by a centrifuge to obtain 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thioketone solution.
2. The method of claim 1, wherein in step one, the solvent is selected from the group consisting of chlorobenzene, toluene, dichloromethane, dichloroethane, benzene, xylene, chloroform, methanol, ethanol, and isopropanol.
3. The method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the concentration of 5-fluoro-4-hydrazino-2-methoxypyrimidine in the 5-fluoro-4-hydrazino-2-methoxypyrimidine solution is 20-60%; the dissolving temperature of the 5-fluoro-4-hydrazino-2-methoxypyrimidine solution is 20-40 ℃.
4. The method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the concentration of hydrogen peroxide is 27.5-70%.
5. The method of synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione of claim 1, wherein the tolerance of said diaphragm metering pump is less than 0.05%.
6. The method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the molar ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to the carbon disulfide is 1: 1.05-1.60.
7. The synthesis method of 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the molar ratio of the 5-fluoro-4-hydrazino-2-methoxypyrimidine to hydrogen peroxide is 1: 1.02-1.30.
8. The method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the reaction temperature in the microchannel reactor I is 10-80 ℃; the residence time in the microchannel reactor I is 5-20 min.
9. The method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the reaction temperature in the microchannel reactor II is 5-60 ℃; and the residence time in the microchannel reactor II is 2-10 min.
10. The method for synthesizing 8-fluoro-5-methoxy-2H- [1,2,4] triazolo [4,3-c ] pyrimidine-3-thione according to claim 1, wherein the rotation speed of the centrifuge is 1200-2500 r/min; the solid centrifuged by the centrifuge is sulfur.
CN202210127039.4A 2022-02-11 2022-02-11 Synthetic method of thioketone Pending CN114437083A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995012597A1 (en) * 1993-11-05 1995-05-11 Dowelanco 2-alkoxy-4-hydrazinopyrimidine compounds and their use in the preparation of 5-alkoxy-1,2-4-triazolo[4,3-c]pyrimidine-3(2h)-thione compounds
US5480991A (en) * 1993-11-05 1996-01-02 Dowelanco 2-Alkoxy-4-hydroazinopyrimidine compounds and their use in the preparation of 5-alkoxy-1,2,4-triazolo[4,3-c]pyrimidine-3(2H)-thione compounds
CN1205336A (en) * 1993-11-05 1999-01-20 道农业科学公司 5-Alkoxy [1,2,4] triazolo [1,5,-C] pyrimidine -2[3H]-thione compounds and their use
CN103923086A (en) * 2014-03-31 2014-07-16 齐鲁工业大学 Preparation method of 5-alkoxy-1,2,4-triazole[4,5-c]pyrimidine-3(2H)-thioketone

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995012597A1 (en) * 1993-11-05 1995-05-11 Dowelanco 2-alkoxy-4-hydrazinopyrimidine compounds and their use in the preparation of 5-alkoxy-1,2-4-triazolo[4,3-c]pyrimidine-3(2h)-thione compounds
US5480991A (en) * 1993-11-05 1996-01-02 Dowelanco 2-Alkoxy-4-hydroazinopyrimidine compounds and their use in the preparation of 5-alkoxy-1,2,4-triazolo[4,3-c]pyrimidine-3(2H)-thione compounds
CN1205336A (en) * 1993-11-05 1999-01-20 道农业科学公司 5-Alkoxy [1,2,4] triazolo [1,5,-C] pyrimidine -2[3H]-thione compounds and their use
CN103923086A (en) * 2014-03-31 2014-07-16 齐鲁工业大学 Preparation method of 5-alkoxy-1,2,4-triazole[4,5-c]pyrimidine-3(2H)-thioketone

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
刘敬等: "8-氟-5-甲氧基-1,2,4-三唑并[4,3-c]嘧啶-3(2H)-硫酮的合成", 《广东化工》 *
张梅凤等: "除草剂双氟磺草胺的合成", 《农药》 *
王胜得等: "除草剂双氟磺草胺的合成研究", 《农药科学与管理》 *

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Application publication date: 20220506