CN106632357B - The method of one pot process TTBN - Google Patents

The method of one pot process TTBN Download PDF

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Publication number
CN106632357B
CN106632357B CN201610888311.5A CN201610888311A CN106632357B CN 106632357 B CN106632357 B CN 106632357B CN 201610888311 A CN201610888311 A CN 201610888311A CN 106632357 B CN106632357 B CN 106632357B
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China
Prior art keywords
ttbn
tngu
added
methenamine
pot
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CN201610888311.5A
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CN106632357A (en
Inventor
郑志花
马文兵
王建龙
陈丽珍
李永祥
曹端林
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North University of China
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North University of China
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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
    • C07D487/08Bridged systems

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention belongs to technical field of chemistry, specifically, are related to a kind of method of one pot process TTBN, are directly reacted with methenamine by TNGU acidic hydrolysis, one-pot synthesis TTBN is specifically included:At room temperature, TNGU is added in the acidic catalyst aqueous solution of a concentration of 2 8M, at 15 40 DEG C after 30 180min of stirring hydrolysis, is directly added into methenamine, 30 90min, one-pot synthesis TTBN are reacted at 30 60 DEG C.This invention simplifies the preparation processes of TTBN, and TNGU is hydrolyzed in acid condition, without separation, need not also prepare the barium salt of TNAE, but directly react one-pot synthesis TTBN with methenamine.

Description

The method of one pot process TTBN
Technical field
The invention belongs to technical field of chemistry, specifically, are related to a kind of method of one pot process TTBN.
Background technology
Existing pass N- (four azabicyclo [3.2.2] nonane -4- bases of 3,6,9- trinitro-s -1,3,6,9-) nitramine (N- (3,6, 9-trinitro-1,3,6,9-tetraazabicyclo [3,2,2] nonan-4-yl) nitramide, abbreviation TTBN) synthesis Method is seldom, and unique method is:By tetranitro glycoluril (TNGU) in NaHCO3After being hydrolyzed in aqueous solution, it is added into aqueous solution Ba(OH)2Acetum makes the pH value of reaction solution control in 4-5, and white barium salt precipitation is precipitated, barium salt solid is obtained by filtration.It will Methenamine is dissolved in 10% hydrochloric acid, and barium salt is added at 10 DEG C or less and stirs 5min, is warming up to 50 DEG C, is first precipitated after solid again Dissolving, it is cooling that solid is precipitated, product TTBN is obtained by filtration.The shortcomings that preparation method:(1) complex process, agents useful for same are more; (2) during preparing the barium salt of four nitramino ethane (TNAE), pH value needs to adjust to faintly acid from alkalescent, and TNAE pairs PH value is very sensitive, is extremely unstable between 3-8 in pH value, so causing raw material TNAE losses larger;(3) product yield It is low, purity is low.
Invention content
It is an object of the invention to be directed to after TNGU basic hydrolysises in the prior art, TNAE is prepared by adjusting pH value Barium salt, then react the technological deficiency for preparing TTBN with the methenamine being dissolved in advance in acid solution, a kind of operation letter be provided The high TTBN synthetic methods of list, high income, purity.
The embodiment provides a kind of method of one pot process TTBN, by TNGU acidic hydrolysis directly with black Lip river Tropine reacts, and one-pot synthesis TTBN is specifically included:At room temperature, TNGU is added to the acidic catalyst water of a concentration of 2-8M In solution, at 15-40 DEG C after stirring hydrolysis 30-180min, it is directly added into methenamine, reacts 30-90min at 30-60 DEG C, One-pot synthesis TTBN.
Further, which is hydrochloric acid, hydrobromic acid or sulfuric acid.
Further, the molar ratio of the methenamine and TNGU of addition is 0.8:1-1.5:1, TNGU and acidic catalyst rub You are than being 1:5-1:20.
Compared with prior art the beneficial effects of the invention are as follows:
(1) present invention is when TNGU is hydrolyzed, with HCl, HBr or H2SO4Acidic aqueous solution replaces NaHCO3Or the alkalinity of NaOH Hydrolysis, reduces the step of basic hydrolysis is acidified again so that hydrolysate TNAE divides during removing from from alkalescent to faintly acid From process, improve the stability of TNAE, make TNAE yields improve, to make TTBN yields improve;
(2) by one pot of progress of synthetic reaction of the hydrolysis of TNGU and TTBN, separation TNAE is both eliminated, middle is reduced The loss of product is managed, and makes to reduce using plurality of raw materials such as barium hydroxide, acetic acid, sodium bicarbonates.
(3) synthesis step is short, at low cost, high income, and purity is high.
Specific implementation mode
The present invention is described in detail below, but it should explanation, these embodiments are not the limit to the present invention System, those of ordinary skill in the art according in function, method or structure made by these embodiments equivalent transformation or replace Generation, all belong to the scope of protection of the present invention within.
A kind of method of one pot process TTBN is present embodiments provided, it is directly anti-with methenamine by TNGU acidic hydrolysis It answers, one-pot synthesis TTBN, i.e.,
At room temperature, TNGU is added to HCl, HBr or the H for filling 2-8M2SO4In the three-necked flask of aqueous solution, in 15- At 40 DEG C, it is sufficiently stirred hydrolysis 30-180min, the methenamine of 0.8-1.5 times of TNGU (molal quantity), stirring and dissolving is added Afterwards, it is warming up to 30-60 DEG C, 30-90min is reacted, filters after reaction, filter cake is washed with water to neutrality, dichloromethane washing two It is secondary, it is dried to obtain white solid, 73% or more yield.This process simplify the preparation processes of TTBN, by TNGU in acid condition Lower hydrolysis need not also prepare the barium salt of TNAE, but directly react one-pot synthesis TTBN with methenamine without separation.
In the present embodiment, the molar ratio of the methenamine and TNGU of addition is 0.8:1-1.5:1, TNGU and acidic catalyst The molar ratio of agent is 1:5-1:20.
Specific embodiment:
Embodiment 1
At room temperature, 3.2g TNGU are added in the three-necked flask of HCl/water solution for the 2M for filling 30mL, are stirred After 60min, 2.1g methenamines are added, after stirring and dissolving, is warming up to 40 DEG C, reacts 90min, filter after reaction, filter cake It is washed with water to neutrality, dichloromethane washes twice, and is dried to obtain white solid, yield 73%, purity 98%.
Embodiment 2
At room temperature, 3.2g TNGU are added in the three-necked flask of HCl/water solution for the 3M for filling 30mL, are stirred After 120min, 1.1g methenamines are added, after stirring and dissolving, is warming up to 60 DEG C, reacts 30min, filter after reaction, filter cake It is washed with water to neutrality, dichloromethane washes twice, and is dried to obtain white solid, yield 76%, purity 98%.
Embodiment 3
At room temperature, 3.2g TNGU are added in the three-necked flask of HBr aqueous solutions for the 4M for filling 30mL, are heated to 30 DEG C, after stirring 40min, 1.5g methenamines are added, after stirring and dissolving, is warming up to 35 DEG C, reacts 90min, after reaction Filtering, filter cake are washed with water to neutrality, and dichloromethane washes twice, and is dried to obtain white solid, yield 82%, purity 98%.
Embodiment 4
At room temperature, 3.2g TNGU are added to the H2SO for the 5M for filling 30mL4In the three-necked flask of aqueous solution, stirring 1.4g methenamines are added in 120min, after stirring and dissolving, are warming up to 40 DEG C, react 50min, filter after reaction, filter cake is used It is washed to neutrality, dichloromethane washes twice, and is dried to obtain white solid, yield 77%, purity 98%.
Embodiment 5
At room temperature, 3.2g TNGU are added in the three-necked flask of HCl/water solution for the 6M for filling 30mL, are stirred 1.2g methenamines are added in 180min, after stirring and dissolving, are warming up to 50 DEG C, react 60min, filter after reaction, filter cake is used It is washed to neutrality, dichloromethane washes twice, and is dried to obtain white solid, yield 73%, purity 98%.
Embodiment 6
At room temperature, 3.2g TNGU are added to the H2SO for the 3M for filling 20mL4In the three-necked flask of aqueous solution, 40 After DEG C stirring 30min, 1.5g methenamines are added, stirring and dissolving is warming up to 60 DEG C, reacts 30min, filters after reaction, Filter cake is washed with water to neutrality, and dichloromethane washes twice, and is dried to obtain white solid, yield 79%, purity 98.5%.
Embodiment 7
At room temperature, 3.2g TNGU are added in the three-necked flask of HCl/water solution for the 3.5M for filling 30mL, 30 After DEG C stirring 60min, 1.5g methenamines are added, stirring and dissolving is warming up to 40 DEG C, reacts 50min, filters after reaction, Filter cake is washed with water to neutrality, and dichloromethane washes twice, and is dried to obtain white solid, yield 86%, purity 99%.
Embodiment 8
At room temperature, 3.2g TNGU are added in the three-necked flask of HCl/water solution for the 8M for filling 30mL, are stirred After 120min, 1.5g methenamines are added, after stirring and dissolving, is warming up to 60 DEG C, reacts 40min, filter after reaction, filter cake It is washed with water to neutrality, dichloromethane washes twice, and is dried to obtain white solid, yield 76%, purity 98%.
The present invention has the advantages that:
(1) by one pot of progress of synthetic reaction of the hydrolysis of TNGU and TTBN, synthesis technology is simple.(2) when TNGU is hydrolyzed, It replaces alkaline aqueous solution to hydrolyze with acidic aqueous solution, reduces the step of basic hydrolysis is acidified again so that hydrolysate TNAE exempts from Decomposition during going from alkalescent to faintly acid improves the stability of TNAE, so that TNAE yields is improved, to make TTBN yields It improves;(3) intermediate link for preparing TNAE barium salts is eliminated, is reduced a variety of using barium hydroxide, acetic acid and sodium bicarbonate etc. Raw material has saved the cost of raw material.
It should be added that the present invention in implementation phase, also attempts to use other alternative solution synthesis TTBN, and It tests respectively, including:Scheme 1) it is directly reacted in acid condition with TNAE and can also synthesize TTBN;Scheme 2) by TNGU alkali Property hydrolysis after be acidified, being directly added into methenamine without separation also can one pot process TTBN.By verification, above two is closed At the method for TTBN, there are wretched insufficiencies:Intermediate regulations pH value can make TNAE decomposeds, so cause product TTBN yields low, Complex process, it is of high cost.In addition, scheme 2) in due to will produce a large amount of salt in acidization, influence reaction and be effectively performed.
The series of detailed descriptions listed above only for the present invention feasible embodiment specifically Bright, they are all without departing from equivalent implementations made by technical spirit of the present invention not to limit the scope of the invention Or change should all be included in the protection scope of the present invention.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie In the case of without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power Profit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent requirements of the claims Variation is included within the present invention.

Claims (3)

1. a kind of method of one pot process TTBN, which is characterized in that directly reacted with methenamine by TNGU acidic hydrolysis, one Pot synthesis TTBN, specifically includes:At room temperature, TNGU is added in the acidic catalyst aqueous solution of a concentration of 2-8M, in 15- After 40 DEG C of stirring hydrolysis 30-180min, it is directly added into methenamine, 30-90min, one-pot synthesis are reacted at 30-60 DEG C TTBN。
2. the method for one pot process TTBN according to claim 1, which is characterized in that the acidic catalyst is salt Acid, hydrobromic acid or sulfuric acid.
3. the method for one pot process TTBN according to claim 2, which is characterized in that the methenamine of addition with The molar ratio of the TNGU is 0.8:1-1.5:The molar ratio of 1, the TNGU and the acidic catalyst is 1:5-1:20.
CN201610888311.5A 2016-10-11 2016-10-11 The method of one pot process TTBN Expired - Fee Related CN106632357B (en)

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Citations (1)

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Publication number Priority date Publication date Assignee Title
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US9695177B2 (en) * 2014-09-29 2017-07-04 The United States Of America As Represented By The Secretary Of The Army Preparation of tetranitroglycoluril
US9512127B2 (en) * 2014-09-29 2016-12-06 The United States Of America As Represented By The Secretary Of The Army Process for the production of speherical tetranitroglycouril

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103087069A (en) * 2013-01-28 2013-05-08 南京理工大学 Synthesis method of 3,7-binitro-1,3,5,7-tetraazabicyclo[3.3.1]nonane

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2, 4, 6-三硝基-2, 4, 6-三氮杂环己酮合成及工艺优化;谭情情;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20140815(第8期);第B017-50页 *
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