KR20220106414A - Method of preparing 3,5-diamino-1,2,4-triazole compound - Google Patents

Abstract

The present application relates to a method for obtaining 3,5-diamino-1,2,4-triazole by solid reaction of solid hydrazine and dicyandiamide under solvent-free conditions. Since the present invention can precisely control the amount of solid hydrazine, so that it is possible to secure price competitiveness and eco-friendliness.

Description

Method for preparing 3,5-diamino-1,2,4-triazole {METHOD OF PREPARING 3,5-DIAMINO-1,2,4-TRIAZOLE COMPOUND}

The present application relates to a method for obtaining 3,5-diamino-1,2,4-triazole by solid reacting solid hydrazine and dicyandiamide under solvent-free conditions.

3,5-diamino-1,2,4-triazole rich in nitrogen with a nitrogen content of about 70% (3,5-diamino-1,2,4-triazole, C ₂ H ₅ N ₅ ; hereinafter “ DAT") is widely used as a kinase inhibitor, a cathode catalyst, and a pharmaceutical intermediate. It is also widely used as a precursor for the synthesis of chemical intermediates of many organic materials and high energy density materials.

Conventional DAT synthesis was made through the reaction of dicyandiamide (dicyandiamide, C ₂ H ₄ N ₄ ) and hydrazine aqueous solution or hydrazine salt. US Patent No. US2648671A discloses a method for preparing DAT by reacting with dicyandiamide using a hydrazine salt as a precursor of hydrazine. On the other hand, Russian Patent RU2152389C1 discloses a method for preparing by adjusting the molar ratio of hydrazine:nitric acid:dicyandiamide to 1:2:1 and using water as a solvent. The above two manufacturing methods have disadvantages in that the purity of the product, DAT, is low because DAT salt may be produced as a by-product, and the manufacturing cost is high due to the cost of wastewater treatment because a solvent is used. In addition, an additional recrystallization process is required to remove the salt from the DAT salt.

On the other hand, anhydrous hydrazine (anhydrous hydrazine, H ₂ NNH ₂ ) is very toxic and cannot be used directly in a laboratory or production site, and an aqueous solution of hydrazine or a hydrazine salt diluted in water must be used instead. The aqueous hydrazine solution is relatively convenient to handle like the aqueous ammonia solution, but has a problem in that it contains a lot of water. As described above, the current DAT manufacturing process has high environmental pollution factors such as wastewater generation due to the introduction of an acid or base additive in addition to hydrazine and dicyandiamide, and there is a cost burden for separation and recovery due to the use of a solvent.

Solid hydrazine is safer and more convenient to use than liquid hydrazine aqueous solution, and it is a solid from which moisture is completely removed. It is a stable solid, but solid hydrazine shows high reactivity and selectivity comparable to anhydrous hydrazine. It has been reported (Org. Lett., 13, 6386 (2011); Adv. Syn. Catal., 2013, 355, 389.; Korean Patent No. 10-1305053;).

An object of the present application is to provide a method for obtaining 3,5-diamino-1,2,4-triazole by solid-reacting solid hydrazine and dicyandiamide under solvent-free conditions.

However, the problem to be solved by the present application is not limited to the problems mentioned above, and other problems not mentioned will be clearly understood by those skilled in the art from the following description.

The present application provides a solid reaction of solid hydrazine and dicyandiamide to obtain 3,5-diamino-1,2,4-triazole, 3,5-diamino-1,2,4-tri A method for preparing an azole is provided.

The method for obtaining 3,5-diamino-1,2,4-triazole according to the embodiments of the present application is a solid reaction of solid hydrazine and dicyandiamide under solvent-free conditions to 3,5-diamino- To obtain 1,2,4-triazole, 1) high yield can be achieved without additional additives, and 2) it is carried out under solvent-free conditions, so that wastewater and waste are not generated and the size of the reaction vessel can be reduced. , 3) It can save time and energy because it does not require a separation process, 4) It is easy to store and use and is not dangerous because solid hydrazine, which is stable at room temperature, is used, 5) It can be used in an anhydrous environment without water, 6) Since the amount of solid hydrazine can be precisely controlled, price competitiveness and eco-friendliness can be secured, and 7) because solid hydrazine produced using carbon dioxide is used, 3,5-diamino-1 according to the present invention, If the production of 2,4-triazole is commercialized, the reduction effect of carbon dioxide, a greenhouse gas, can be expected.

1A is a photograph of DAT synthesized according to Example 1 of the present application, and FIG. 1B is a photograph of DAT synthesized according to Comparative Example 1 of the present application.
2 is a ¹ H-NMR spectrum of DAT synthesized according to Example 1 of the present application.
3 is a ¹³ C-NMR spectrum of DAT synthesized according to Example 1 of the present application.
4 is GC-MS data of DAT synthesized according to Example 1 of the present application.
5 is a powder X-ray diffraction (XRD) data of DAT synthesized according to Example 1 of the present application.

Hereinafter, embodiments and examples of the present invention will be described in detail with reference to the accompanying drawings so that those skilled in the art to which the present invention pertains can easily carry out. However, the present application may be embodied in several different forms and is not limited to the embodiments and examples described herein. And in order to clearly explain the present invention in the drawings, parts irrelevant to the description are omitted, and similar reference numerals are attached to similar parts throughout the specification.

Throughout this specification, when a part is said to be "connected" with another part, it includes not only the case where it is "directly connected" but also the case where it is "electrically connected" with another element interposed therebetween. do.

Throughout this specification, when a member is said to be located “on” another member, this includes not only a case in which a member is in contact with another member but also a case in which another member is present between the two members.

Throughout this specification, when a part "includes" a certain component, it means that other components may be further included, rather than excluding other components, unless otherwise stated.

As used herein, the terms “about,” “substantially,” and the like, to the extent used herein, are used in or close to the numerical value when the manufacturing and material tolerances inherent in the stated meaning are presented, and to aid in the understanding of the present application. It is used to prevent an unconscionable infringer from using the mentioned disclosure unfairly.

As used throughout this specification, the term “step to” or “step for” does not mean “step for”.

Throughout this specification, the term "combination(s) of these" included in the expression of the Markush form means one or more mixtures or combinations selected from the group consisting of the components described in the expression of the Markush form, It means to include one or more selected from the group consisting of the above components.

Throughout this specification, reference to “A and/or B” means “A or B, or A and B”.

Hereinafter, embodiments of the present application have been described in detail, but the present application may not be limited thereto.

Herein, solid reaction of solid hydrazine and dicyandiamide to obtain 3,5-diamino-1,2,4-triazole (3,5-diamino-1,2,4-triazole; DAT) It provides a method for preparing 3,5-diamino-1,2,4-triazole comprising.

In one embodiment of the present application, the solid hydrazine may be represented by the following Chemical Formula 1:

[Formula 1]

.

.

In one embodiment of the present application, the 3,5-diamino-1,2,4-triazole may be represented by the following Chemical Formula 2 or Chemical Formula 3, and possible resonance structures thereof:

[Formula 2]

;

;

[Formula 3]

.

.

In one embodiment of the present application, the solid reaction may be performed under solvent-free conditions.

In one embodiment of the present application, the purity of the solid hydrazine and the dicyandiamide may be 99% by mass or more. If the purity is less than 99% by mass, there may be a problem in that the yield of the product is lowered or impurities are generated.

In one embodiment of the present application, the solid reaction may be carried out in a temperature range of about 80 °C to about 120 °C, but may not be limited thereto. For example, the solid reaction may be from about 80°C to about 120°C, from about 80°C to about 115°C, from about 80°C to about 110°C, from about 80°C to about 105°C, from about 80°C to about 100°C, about 80 °C to about 95 °C, about 80 °C to about 90 °C, about 80 °C to about 85 °C, about 85 °C to about 120 °C, about 85 °C to about 115 °C, about 85 °C to about 110 °C, about 85 °C to about 105 °C, about 85 °C to about 100 °C, about 85 °C to about 95 °C, about 85 °C to about 90 °C, about 90 °C to about 120 °C, about 90 °C to about 115 °C, about 90 °C to about 110 °C °C, from about 90 °C to about 105 °C, from about 90 °C to about 100 °C, from about 90 °C to about 95 °C, from about 95 °C to about 120 °C, from about 95 °C to about 115 °C, from about 95 °C to about 110 °C, about 95°C to about 105°C, about 95°C to about 100°C, about 100°C to about 120°C, about 100°C to about 115°C, about 100°C to about 110°C, about 100°C to about 105°C, about 105 C to about 120°C, from about 105°C to about 115°C, from about 105°C to about 110°C, from about 110°C to about 120°C, from about 110°C to about 115°C, or from about 115°C to about 120°C may be performed, but may not be limited thereto. When the solid reaction is carried out in a temperature range of less than about 80 ° C., a problem that the reaction proceeds slowly may occur, and when the solid reaction is carried out in a temperature range greater than about 120 ° C., 3, which is a product of the solid reaction; There may be a problem in that impurities are generated other than 5-diamino-1,2,4-triazole. In addition, when the solid reaction is not carried out in a temperature range of about 80° C. to about 120° C., there may be a problem in that 3,5-diamino-1,2,4-triazole with low purity is produced. The reaction rate may vary depending on the temperature at which the solid reaction is performed, and if the mixed powder is put in a closed container and the temperature is raised, the reaction may proceed rapidly.

In one embodiment of the present application, the solid reaction may be carried out by continuously mixing for the reaction time, but may not be limited thereto.

In one embodiment of the present application, the mixing may be performed by at least one selected from a mortar, a ball mill, a bead mill, and a kneader, but may not be limited thereto. have. In one embodiment of the present application, the mixing may be performed by mixing the reactants in a mortar and continuously grinding, or using a dispersion mixer device such as a ball mill, bead mill, and/or kneader, If the temperature is increased in the ball mill and bead mill apparatus, the reaction may proceed very quickly.

In one embodiment of the present application, the size of the balls and beads used in the ball mill and the bead mill, each independently, may be about 0.05 mm to about 3 mm, but may not be limited thereto. For example, the sizes of the balls and beads are, each independently, about 0.05 mm to about 3 mm, about 0.05 mm to about 2.5 mm, about 0.05 mm to about 2 mm, about 0.05 mm to about 1.5 mm, about 0.05 mm to about 1 mm, about 0.1 mm to about 3 mm, about 0.1 mm to about 2.5 mm, about 0.1 mm to about 2 mm, about 0.1 mm to about 1.5 mm, or about 0.1 mm to about 1 mm, However, the present invention is not limited thereto. In one embodiment of the present application, the size of the ball and the bead, each independently, may be about 0.1 mm to about 1 mm. The smaller the size of the balls and beads, the faster the reaction rate may be.

The balls and beads are, each independently, a metal material such as SUS and carbon steel; and/or a metal oxide material such as alumina, zirconia, and zirconia-yttria, but may not be limited thereto.

In one embodiment of the present application, the molar ratio of the reactants of the solid reaction may be from about 0.5 mol to about 5 mol of the solid hydrazine with respect to 1 mol of the dicyandiamide, but may not be limited thereto. When the molar ratio of the reactants of the solid reaction is less than about 0.5 mol of the solid hydrazine with respect to 1 mol of the dicyandiamide, the reaction does not proceed well and the unreacted dicyandiamide and the solid hydrazine may remain. , when the solid hydrazine exceeds about 5 mol, unreacted solid hydrazine may remain.

In one embodiment of the present application, the solid reaction may be carried out in a pressure range of about 0.1 MPa to about 5 MPa, but may not be limited thereto. For example, the solid reaction is about 0.1 MPa to about 5 MPa, about 0.1 MPa to about 4.5 MPa, about 0.1 MPa to about 4 MPa, about 0.1 MPa to about 3.5 MPa, about 0.1 MPa to about 3 MPa, about 0.1 MPa to about 2.5 MPa, about 0.1 MPa to about 2 MPa, or about 0.1 MPa to about 1.5 MPa may be carried out in a pressure range, but may not be limited thereto. In one embodiment of the present application, the solid reaction may be performed in a pressure range of about 0.1 MPa to about 1.5 MPa. Here, when the solid reaction is carried out in a pressure range of less than about 0.1 MPa, there may be a problem that the reaction proceeds slowly, and when the solid reaction is carried out in a pressure range of more than about 5 MPa, a hydrazine derivative is generated This can happen.

In one embodiment of the present application, the yield of 3,5-diamino-1,2,4-triazole obtained by the solid reaction is about 80% or more, about 85% based on the reactant dicyandiamide % or greater, about 90% or greater, or about 95% or greater. In one embodiment of the present application, the yield of 3,5-diamino-1,2,4-triazole obtained by the solid reaction is about 95% or more or about 98 based on the reactant dicyandiamide % or more.

In one embodiment of the present application, the solid reaction is, (a) mixing the solid hydrazine and the dicyandiamide in a solid state to obtain a mixed powder; and (b) putting the mixed powder in a reaction vessel and reacting the solid to obtain the 3,5-diamino 1,2,4-triazole; may include, but may not be limited to.

In one embodiment of the present application, an additive may be further included during the solid reaction, but may not be limited thereto.

In one embodiment of the present application, the additive may be one or more selected from water, hydrochloric acid, and nitric acid, but may not be limited thereto. When an additive is added during the solid reaction, the reaction is promoted, so there may be an advantage in that the efficiency of the 3,5-diamino-1,2,4-triazole manufacturing process is increased. However, there may be a problem in that DAT salts or other impurities are generated in addition to the product DAT.

In one embodiment of the present application, when the additive is further included, about 0.1 mol to about 1 mol of the additive may be additionally included with respect to 1 mol of the dicyandiamide, but may not be limited thereto. .

In one embodiment of the present application, the solid reaction may further include a lubricating solvent, but may not be limited thereto. When a lubricating solvent is further included in the solid reaction, a process of separating the product and the lubricating solvent may be additionally required.

In one embodiment of the present application, the lubricating solvent may include an alcohol having 1 to 15 carbon atoms, but may not be limited thereto. Specifically, the alcohol may include one or more selected from methanol, ethanol, propanol, butanol, pentanol, hexanol, heptanol, octanol, nonanol, decanol, and possible isomers thereof. may not be limited.

In one embodiment of the present application, the lubricating solvent may include an ether having 2 to 16 carbon atoms, but may not be limited thereto. Specifically, the ether may include one or more selected from dimethyl ether, diethyl ether, THF and dioxin, but may not be limited thereto.

In one embodiment of the present application, the lubricating solvent may include an aliphatic hydrocarbon having 5 to 15 carbon atoms, but may not be limited thereto. Specifically, the aliphatic hydrocarbon may include one or more selected from pentane, hexane, heptane, and possible isomers thereof, but may not be limited thereto.

In one embodiment of the present application, the lubricating solvent may include an aromatic hydrocarbon having 6 to 15 carbon atoms, but may not be limited thereto. Specifically, the aromatic hydrocarbon is benzene; toluene; xylene; and one or more selected from aromatic carbon compounds in which hetero atoms such as oxygen and nitrogen are substituted, may not be limited thereto.

In one embodiment of the present application, the lubricating solvent may include a polyol, but may not be limited thereto. Specifically, the polyol may include one or more selected from ethylene glycol, glycerol, erythritol, xylitol, and mannitol, but may not be limited thereto.

Hereinafter, the present application will be described in more detail using examples, but the following examples are only illustrative to aid understanding of the present application, and the content of the present application is not limited to the following examples.

[Example]

<Example 1: Preparation of 3,5-diamino-1,2,4-triazole (3,5-diamino-1,2,4-triazole, DAT) through solid reaction>

0.076 g of solid hydrazine and 0.042 g of dicyandiamide were placed in a mortar, ground and mixed evenly, put in a reaction vessel, and reacted at 100° C. for 10 to 20 hours to obtain 0.048 g of DAT. The yield of the DAT was 98% based on the dicyandiamide as a reactant. Elemental quantitative analysis results for the DAT (measurement equipment: Thermo Flash 2000, Flash EA1112; unit %) are shown in the table below.

C H N Calculated value (%) 24.24 5.09 70.67 Experimental value (%) 23.98 4.90 71.05

1 is a photograph of DAT synthesized according to Example 1 of the present application, showing that it is a white powder.

2 is a ¹ H-NMR spectrum of DAT synthesized according to Example 1 of the present application. D6-DMSO solvent was used, and the measured values are as follows. δ(ppm) = 10.23(s, 1H, NH), 5.08(s, 2H, NH ₂ ), 4.49(s, 2H, NH ₂ )

3 is a ¹³ C-NMR spectrum of DAT synthesized according to Example 1 of the present application. D6-DMSO solvent was used, and only one peak was observed at 159.3 ppm.

4 is GC-MS data of DAT synthesized according to Example 1 of the present application. The observed m/z peaks are 43, 57, 99.

5 is a powder X-ray diffraction (XRD) data of DAT synthesized according to Example 1 of the present application. The X-ray diffraction peak of the synthesized DAT and the peak of the JCPDS data of DAT coincide, and peaks corresponding to solid hydrazine and dicyandiamide used as reactants; and peaks of substances other than DAT as a product; was not observed.

Through the analysis result, it was confirmed that the purity of the DAT powder synthesized according to Example 1 of the present application was high.

<Example 2: Preparation of DAT through reaction temperature control>

In Example 1, the reaction temperature was adjusted to less than 80 °C and greater than 120 °C, and the reaction was carried out under the same conditions other than that. When the reaction temperature was less than 80° C., the reactants remained and the yield of DAT product was less than 20%. On the other hand, when the reaction temperature was higher than 120 DEG C, the mass and yield of the obtained DAT product were almost the same as those of Example 1, but trace impurities were observed.

<Example 3: Preparation of DAT through reaction time control>

In Example 1, the reaction time was adjusted to 5 hours and 40 hours, and the other conditions were the same to perform the reaction. When the reaction time was 5 hours, the reactants remained and the yield of DAT product was less than 50%. On the other hand, when the reaction time was 40 hours, the mass and yield of the obtained DAT product were almost the same as in Example 1.

<Example 4: Preparation of DAT through control of the molar ratio of reactants>

In Example 1, the molar ratio of the dicyandiamide and the solid hydrazine reactant was adjusted differently, and the reaction was performed under the same conditions other than that. When the molar ratio of dicyandiamide and solid hydrazine was about 1:0.5 or less, the DAT yield was less than 10%, so the reaction did not proceed well, and unreacted dicyandiamide and solid hydrazine remained. When the molar ratio of dicyandiamide to solid hydrazine was about 1:5 or more, a large amount of unreacted hydrazine remained and other hydrazine derivatives were produced.

<Example 5: Preparation of DAT through reaction pressure control>

In Example 1, the pressure of the solid reaction was adjusted differently, and the other conditions were the same to perform the reaction. When the reaction pressure was less than about 0.1 MPa, the production rate of DAT was slowed and the yield was less than 10%, and when the reaction pressure was 1 MPa, the obtained product and yield were almost the same as in Example 1.

<Example 6: Preparation of DAT containing water as an additive>

Under the same conditions as in Example 1, water was added in a ratio of 1 mol to 1 mol of dicyandiamide. The obtained product and yield were almost the same as in Example 1, but an additional process of drying water in the product was required.

<Example 7: Preparation of DAT containing hydrochloric acid as an additive>

Under the same conditions as in Example 1, hydrochloric acid was added to carry out the reaction. When hydrochloric acid was added in a ratio of 0.2 mol to 1 mol of dicyandiamide, the yield of the DAT product was about 95%. When hydrochloric acid was added in a ratio of more than 1 mol to 1 mol of dicyandiamide, the yield of the DAT product was less than about 10%, and the content of chlorine compounds including hydrazine chloride was 90% or more.

<Comparative Example 1: Preparation of DAT using a liquid hydrazine aqueous solution>

In Example 1, 50 μL of hydrazine monohydrate (64-65%) of the same molar number was added instead of solid hydrazine, and the other conditions were the same to perform the reaction. After the reaction, the solid compound was separated and dried, and the yield of the obtained product was about 30%. The generated DAT had a color such as yellow or pink, and the color changed according to the reaction conditions (FIG. 1b).

<Comparative Example 2: hydrazine hydrochloride (NH ₂ NH ₂ Preparation of DAT using HCl)>

In Example 1, 0.07 g of hydrazine hydrochloride having the same number of moles was added instead of solid hydrazine, and the other conditions were the same to perform the reaction. After the reaction, the solid compound was separated and dried, and the yield of the obtained product was about 30%, and the resulting solid contained impurities such as ammonium chloride (NH ₄ Cl).

The above description of the present application is for illustration, and those of ordinary skill in the art to which the present application pertains will understand that it can be easily modified into other specific forms without changing the technical spirit or essential features of the present application. Therefore, it should be understood that the embodiments described above are illustrative in all respects and not restrictive. For example, each component described as a single type may be implemented in a distributed manner, and likewise components described as distributed may also be implemented in a combined form.

The scope of the present application is indicated by the following claims rather than the above detailed description, and all changes or modifications derived from the meaning and scope of the claims, and their equivalent concepts should be construed as being included in the scope of the present application. .

Claims (14)

Solid reaction of solid hydrazine and dicyandiamide to obtain 3,5-diamino-1,2,4-triazole
A method for producing a 3,5-diamino-1,2,4-triazole comprising a.
The method of claim 1,
The solid reaction is a method for producing 3,5-diamino-1,2,4-triazole that is carried out under solvent-free conditions.
The method of claim 1,
The solid reaction is a method for producing 3,5-diamino-1,2,4-triazole that is carried out in a temperature range of 80 ℃ to 120 ℃.
The method of claim 1,
The solid reaction is a method for producing 3,5-diamino-1,2,4-triazole that is carried out while continuously mixing for the reaction time.
5. The method of claim 4,
The mixing is carried out by at least one selected from a mortar, ball mill, bead mill, and kneader, the method for producing 3,5-diamino-1,2,4-triazole.
The method of claim 1,
The molar ratio of the reactants of the solid reaction will be 0.5 mol to 5 mol of the solid hydrazine with respect to 1 mol of the dicyandiamide, 3,5-diamino-1,2,4-triazole.
The method of claim 1,
The solid reaction is carried out in a pressure range of 0.1 MPa to 5 MPa, the method for producing 3,5-diamino-1,2,4-triazole.
The method of claim 1,
The yield of 3,5-diamino-1,2,4-triazole obtained by the solid reaction is 80% or more, the method for producing 3,5-diamino-1,2,4-triazole.
The method of claim 1,
The solid reaction is
(a) mixing the solid hydrazine and the dicyandiamide in a solid state to obtain a mixed powder; and
(b) putting the mixed powder in a reaction vessel and reacting the solid to obtain the 3,5-diamino-1,2,4-triazole;
A method for preparing a 3,5-diamino-1,2,4-triazole comprising a.
The method of claim 1,
The method for producing 3,5-diamino-1,2,4-triazole further comprising an additive during the solid reaction.
11. The method of claim 10,
The additive is at least one selected from water, hydrochloric acid, and nitric acid, the method for producing 3,5-diamino-1,2,4-triazole.
11. The method of claim 10,
The method for producing 3,5-diamino-1,2,4-triazole further comprising 0.1 mol to 1 mol of the additive with respect to 1 mol of the dicyandiamide.
The method of claim 1,
A method for producing 3,5-diamino-1,2,4-triazole, which further comprises a lubricating solvent during the solid reaction.
14. The method of claim 13,
The lubricating solvent is one or more selected from alcohols having 1 to 15 carbon atoms, ethers having 2 to 16 carbon atoms, aliphatic hydrocarbons having 5 to 15 carbon atoms, aromatic hydrocarbons having 6 to 15 carbon atoms, and polyols, 3,5 - Method for preparing diamino-1,2,4-triazole.

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