Disclosure of Invention
In order to solve the technical problems, the invention provides a preparation method of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine. The method has the advantages of simple synthetic route, less raw and auxiliary material feeding, low cost, less three wastes, environmental protection and high product purity, and is more suitable for industrial mass production.
The invention is realized by the following technical scheme:
a preparation method of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine comprises the following steps:
s1, stirring and mixing triethyl orthoformate and glacial acetic acid in a reaction kettle, and then introducing ammonia gas for pressure maintaining reaction;
s2; after the triethyl orthoformate and ammonia react, cooling, adding 1-aminopyrrole-2-formonitrile hydrochloride to continue to introduce ammonia for heating reaction, concentrating the solvent after the reaction is finished, adding deionized water, stirring, cooling, crystallizing, centrifuging to obtain a crude product of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, and refining to obtain a refined product of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine.
The reaction equation of the preparation method is as follows:
in the above method for preparing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the mass ratio of triethyl orthoformate to glacial acetic acid is 2.0-5.0:1, preferably 2.5-3.0: 1.
In the above method for producing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the temperature in step S1 is 45 to 90 ℃, preferably 60 to 90 ℃.
In the above method for producing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the mass ratio of triethyl orthoformate to ammonia gas is 1.5-5.0:1, preferably 2.0-4.0: 1.
In the above method for preparing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the mass ratio of the 1-aminopyrrole-2-carbonitrile hydrochloride to triethyl orthoformate is 1:2.0-8.0, preferably 1: 2.6-5.0.
In the above method for preparing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the reaction temperature in the step S2 is 30 to 80 ℃, preferably 60 to 70 ℃.
In the above-mentioned process for producing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the reaction is carried out under a pressure of 0.01 to 0.3MPa, preferably 0.02 to 0.1MPa, while maintaining the pressure.
In the above-mentioned process for producing 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the solvent for purification is one or more selected from methanol, ethanol and isopropanol, and the weight of the solvent is 5 to 20 times, preferably 7 to 15 times the weight of 1-aminopyrrole-2-carbonitrile hydrochloride.
Preferably, the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine comprises the following steps: stirring and mixing triethyl orthoformate and glacial acetic acid in a reaction kettle, inserting a vent pipe below the liquid level, heating to 30 ℃, introducing ammonia gas under a protective pressure, heating to 60-90 ℃ for reaction, adding 1-aminopyrrole-2-formonitrile hydrochloride after the reaction is finished and cooling, heating to 60-65 ℃, introducing ammonia gas for heat preservation reaction, concentrating under reduced pressure after the reaction is finished until no solvent is evaporated out, adding deionized water for pulping to obtain a crude wet product, dissolving the wet product with methanol, cooling and crystallizing after concentration, and centrifuging to obtain the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine refined product.
More preferably, the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine comprises the following detailed steps:
adding 720kg of triethyl orthoformate and 266kg of glacial acetic acid into a reaction kettle, stirring and heating to 30-35 ℃, vacuumizing the reaction kettle, introducing ammonia below the liquid level, keeping the temperature for 2h at 80-90 ℃ until the raw materials disappear, introducing 208kg of ammonia, cooling to below 50 ℃, adding 265kg of 1-aminopyrrole-2-formonitrile hydrochloride, sealing the reaction kettle, heating to 60-65 ℃ for ammonia-introducing heat-preserving reaction, after the reaction is finished, concentrating under reduced pressure until no solvent is evaporated, adding 1590kg of deionized water, pulping for 30min, centrifuging to obtain a crude product of 4-aminopyrrole [2,1-f ] [1,2,4] triazine, putting the crude product into 1877kg of methanol, heating to 50-55 ℃, stirring until the solid is completely dissolved, concentrating under reduced pressure to obtain a viscous feed liquid, cooling, crystallizing and centrifuging, the wet product was dried to obtain 212.9kg of a 4-aminopyrrolo [2,1-f ] [1,2,4] triazine competitive product.
The preparation method of the 7-iodopyrrolo [2,1-F ] [1,2,4] triazine-4-amine comprises the following steps:
(1) preparation of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine
Stirring and mixing triethyl orthoformate and glacial acetic acid in a reaction kettle, inserting a vent pipe below the liquid level, heating to 30 ℃, introducing ammonia gas under a protective pressure, heating to 60-90 ℃ for reaction, adding 1-aminopyrrole-2-formonitrile hydrochloride after the reaction is finished and cooling, heating to 60-65 ℃, introducing ammonia gas for heat preservation reaction, concentrating under reduced pressure after the reaction is finished until no solvent is evaporated out, adding deionized water for pulping to obtain a crude wet product, dissolving the wet product with methanol, cooling and crystallizing after concentration, and centrifuging to obtain the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine refined product.
(2) Preparation of 7-iodopyrrolo [2,1-F ] [1,2,4] triazin-4-amine
Reacting 4-aminopyrrolo [2,1-f ] [1,2,4] triazine and iodine in DMF at the temperature of below-5 ℃ for 1h, controlling the temperature to be between 10 ℃ below zero and 0 ℃, and adding a solution of N-iodosuccinimide and DMF; after the addition, the reaction is continued for 1.5 h; then adding aqueous solution of sodium sulfite and sodium hydroxide, stirring, crystallizing completely, centrifuging, and drying wet product to obtain 7-iodopyrrolo [2,1-F ] [1,2,4] triazine-4-amine.
In the preparation method of the 7-iodopyrrolo [2,1-F ] [1,2,4] triazine-4-amine, the mass ratio of the 4-aminopyrrolo [2,1-F ] [1,2,4] triazine to iodine is 20: 5.6. In the solution of N-iodosuccinimide and DMF, the mass ratio of the N-iodosuccinimide to the DMF is 32: 150. in the aqueous solution of sodium sulfite and sodium hydroxide, the mass ratio of water of the sodium sulfite to the water of the sodium hydroxide is 3: 2:100.
The invention has the beneficial effects that:
1. according to the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the excessive ammonia gas in the step of preparing the formamidine acetate can provide alkaline conditions for the next reaction, and the ammonia gas is used for replacing solid alkali for reaction, so that the cost of raw materials is lower. Meanwhile, the phenomenon of solution viscosity caused by a large amount of solid materials is avoided.
2. According to the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the ethanol generated in the first step of reaction provides a solvent for the next step of cyclization reaction, so that the solvent is not required to be added in the reaction, the raw material cost is greatly reduced, the discharge of waste liquid is reduced, and the preparation method is green and environment-friendly; the problem of complicated operation is also solved.
3. The reported synthetic method needs to add formamidine acetate with the mass ratio of 3-5 times of 1-aminopyrrole-2-formonitrile hydrochloride into the system and add solid base with the mass ratio of 5-8 times of formamidine acetate into the system, so that the reaction system is very viscous and the stirring paddle of the reaction kettle is easy to be stopped. According to the preparation method of the 4-aminopyrrole [2,1-f ] [1,2,4] triazine, only one solid of 1-aminopyrrole-2-formonitrile hydrochloride reacts in the formamidine acetate ethanol solution, the reaction system is uniform, the equipment is more friendly, and the production cost of the product is reduced.
4. According to the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the formamidine acetate ethanol solution obtained in the first step is directly subjected to the next step of reaction after 1-aminopyrrole-2-carbonitrile hydrochloride is added without crystallization and purification, so that the production period is shortened; more importantly, the operation steps are reduced, and the production cost is reduced.
5. According to the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the methanol recovered in the refining step can be applied to the production of the next batch, and the industrial popularization is very facilitated.
6. According to the preparation method of the 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, the liquid phase purity is far higher than 98% reported in the current literature by 99.75%; and a foundation is laid for producing high-quality iodides or bromides in the next step, and the purity of the liquid phase of the 7-iodopyrrolo [2,1-F ] [1,2,4] triazine-4-amine produced in the next step in the embodiment reaches over 99.2% without purification, so that the quality requirement that the purity of the liquid phase of the subsequent reaction step of the Reidcisvir is more than 99% is met.
Detailed Description
The present invention will be further described with reference to specific examples so that those skilled in the art may better understand the present invention, but the present invention is not limited thereto.
Example 1:
adding 200kg of triethyl orthoformate and 74kg of glacial acetic acid into a reaction kettle, stirring and heating to 30-35 ℃, vacuumizing the reaction kettle, introducing ammonia below the liquid level, keeping the pressure under airtight condition and 0.08-0.1MPa for reaction until the system does not heat up any more, keeping the temperature at 60-70 ℃ for 2h until the raw materials disappear, introducing 55kg of ammonia gas, cooling to below 50 ℃, adding 74kg of 1-aminopyrrole-2-formonitrile hydrochloride, sealing the reaction kettle, heating to 40-50 ℃, introducing ammonia gas for temperature-keeping reaction, after the reaction is finished, concentrating under reduced pressure until no solvent is evaporated, adding 444kg of deionized water, pulping for 30min, centrifuging to obtain a crude product of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, putting the crude product into 521kg of methanol, heating to 50-55 ℃, stirring until the solid is completely dissolved, concentrating under reduced pressure until the feed liquid is viscous, cooling, crystallizing, centrifuging, and drying the wet product to obtain 52.6kg of refined 4-aminopyrrolo [2,1-f ] [1,2,4] triazine product with liquid phase purity of 99.83% and molar yield of 76.1%.
Example 2:
adding 720kg of triethyl orthoformate and 266kg of glacial acetic acid into a reaction kettle, stirring and heating to 30-35 ℃, vacuumizing the reaction kettle, introducing ammonia below the liquid level, keeping the pressure under 0.01-0.05MPa for reaction until the system is not heated any more, keeping the temperature at 80-90 ℃ for 2h until the raw materials disappear, introducing 208kg of ammonia, cooling to below 50 ℃, adding 265kg of 1-aminopyrrole-2-formonitrile hydrochloride, sealing the reaction kettle, heating to 60-65 ℃, introducing ammonia for heat preservation reaction, after the reaction is finished, concentrating under reduced pressure until no solvent is evaporated, adding 1590kg of deionized water, pulping for 30min, centrifuging to obtain a crude product of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, putting the crude product into 1877kg of methanol, heating to 50-55 ℃, stirring until the solid is completely dissolved, concentrating under reduced pressure until the feed liquid is viscous, cooling, crystallizing, centrifuging, and drying the wet product to obtain 212.9kg of refined 4-aminopyrrolo [2,1-f ] [1,2,4] triazine product with liquid phase purity of 99.75% and molar yield of 85.5%.
1539kg of recovered refined methanol is used in the next batch production.
Example 3:
adding 480kg of triethyl orthoformate and 178kg of glacial acetic acid into a reaction kettle, stirring and heating to 30-35 ℃, vacuumizing the reaction kettle, introducing ammonia below the liquid level, keeping the pressure for 0.05-0.08MPa for reaction in a gas-tight manner until the temperature of the system does not rise any more, keeping the temperature at 70-80 ℃ for 2h until the raw materials disappear, introducing 140kg of ammonia gas at the moment, cooling to below 50 ℃, adding 177kg of 1-aminopyrrole-2-formonitrile hydrochloride, sealing the reaction kettle, heating to 50-60 ℃, introducing ammonia gas for temperature-keeping reaction, after the reaction is finished, concentrating under reduced pressure until no solvent is evaporated, adding 1062kg of deionized water for pulping for 30min, centrifuging to obtain crude 4-aminopyrrolo [2,1-f ] [1,2,4] triazine, putting the crude product into 1251kg of methanol recovered in example 2, heating to 50-55 ℃, stirring until the solid is completely dissolved, concentrating under reduced pressure until the material liquid is viscous, cooling, crystallizing, centrifuging, and drying wet product to obtain 132.5kg of refined 4-aminopyrrolo [2,1-f ] [1,2,4] triazine product with liquid phase purity of 99.89% and molar yield of 79.8%.
Example 47 preparation of iodopyrrolo [2,1-F ] [1,2,4] triazin-4-amine:
1. the reaction equation is as follows:
2. reaction operation:
adding 100kg of DMF into a clean and dry reaction kettle, adding 20kg of 4-aminopyrrolo [2,1-f ] [1,2,4] triazine prepared in the embodiment under stirring, and cooling to below-10 ℃; 5.6kg of iodine was added and reacted at-5 ℃ for 1 hour. Controlling the temperature to be-10-0 ℃, and adding a solution of 32 kgN-iodosuccinimide and 150 kgDMF; after the addition, the reaction was continued for 1.5 h. Adding 400kg of aqueous solution of 12kg of sodium sulfite and 10kg of sodium hydroxide, stirring for crystallization, centrifuging after complete crystallization, and drying a wet product to obtain 33.7kg of off-white 7-iodopyrrolo [2,1-F ] [1,2,4] triazin-4-amine with the yield of 86.9%; the purity of the liquid phase is 99.23%.