CN102993114B - A kind of production method of 1H-TETRAZOLE-5-acetic acid - Google Patents

A kind of production method of 1H-TETRAZOLE-5-acetic acid Download PDF

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CN102993114B
CN102993114B CN201210383353.5A CN201210383353A CN102993114B CN 102993114 B CN102993114 B CN 102993114B CN 201210383353 A CN201210383353 A CN 201210383353A CN 102993114 B CN102993114 B CN 102993114B
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acetic acid
acid
reaction
tetrazole
production method
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CN102993114A (en
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张耀兵
王炳才
张燕程
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Jiang Shulin
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HUAFENG CHEMICAL CO Ltd NANTONG CITY
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Abstract

The invention discloses a kind of production method of 1H-TETRAZOLE-5-acetic acid, it is characterized in that: the method is reacted in two steps: 1) be initial substance with cyanoacetic acid, first react with chloro thing under solvent and catalyzer exist, temperature of reaction is 0-30 DEG C, and the time is that 1-3h obtains intermediate; 2) add sodiumazide by step 1 gained intermediate, under solvent and catalyzer exist, be warming up to 60-150 DEG C of reaction 6-8h, 30 DEG C are cooled to after reaction terminates, between sour souring soln pH to 1-2, be again cooled to 0-5 DEG C, filter and obtain target product 1H-TETRAZOLE-5-acetic acid.The invention has the advantages that: the present invention adopts low cost raw material, safety non-toxic, production technique is simple, easy to operate, and product yield is high, reaches 75-85%.

Description

A kind of production method of 1H-TETRAZOLE-5-acetic acid
Technical field
The present invention relates to a kind of production method of 1H-TETRAZOLE-5-acetic acid.
Background technology
1H-TETRAZOLE-5-acetic acid, molecular formula is C 3h 4n 4o 2, be a kind of white powder.At present, existing document (Inorganic Chemistry Communications, 2010,13:250-253) report the production method of 1H-TETRAZOLE-5-acetic acid, with 1H-TETRAZOLE-5-ethyl acetate for raw material, through zinc chloride or the obtained 1H-TETRAZOLE-5-acetic acid of Cadmium chloride fine powder hydrolysis, the method product yield is low, the highlyest can only reach 54%, and raw materials for production price, the zinc chloride of use or Cadmium chloride fine powder are dangerous poisonous, difficulty and product separation, cause the method to be unfavorable for applying.Therefore, in order to reduce raw materials cost and avoid using hazardous agents, find the operational path that is applicable to industrialization more, thus the yield of raising 1H-TETRAZOLE-5-acetic acid and quality extremely will there is Research Significance.
Summary of the invention
The object of this invention is to provide the production method of the 1H-TETRAZOLE-5-acetic acid that a kind of raw materials cost is low, technique is simple and safe, product yield is high.
In order to solve the problems of the technologies described above, the technical solution used in the present invention is: a kind of production method of 1H-TETRAZOLE-5-acetic acid, it is characterized in that: the method is reacted in two steps: 1) be initial substance with cyanoacetic acid, first react with chloro thing under solvent and catalyzer exist, temperature of reaction is 0-30 DEG C, and the time is that 1-3h obtains intermediate; 2) sodiumazide is added by step 1 gained intermediate, under solvent and catalyzer exist, be warming up to 60-150 DEG C of reaction 6-8h, 30 DEG C are cooled to after reaction terminates, between sour souring soln pH to 1-2, again be cooled to 0-5 DEG C, filter and obtain target product 1H-TETRAZOLE-5-acetic acid, its reactional equation is as follows:
Wherein, described R is pivaloyl group or trimethyl silicon based.
Further, catalyzer described in step 1) is tertiary amine compounds, described solvent benzol or toluene.
Further, described tertiary amine compounds is triethylamine, N, N-dipropyl-1-propylamine or DMA.
Further, step 2) described catalyzer is ammonium chloride or sub-amines catalyst, described solvent benzol or toluene.
Further, step 2) described acid is dilute hydrochloric acid or dilute sulphuric acid.
Further, described dilute hydrochloric acid or dilute sulphuric acid concentration are 15%.
The invention has the advantages that: the present invention adopts low cost raw material, safety non-toxic, production technique is simple, easy to operate, and product yield is high, reaches 75-85%.
Embodiment
Technical spirit of the present invention and beneficial effect can be fully understood in order to make the public; applicant will describe in detail the specific embodiment of the present invention below; but applicant is not the restriction to technical scheme to the description of embodiment, any changing in the form rather than substance according to the present invention's design all should be considered as protection scope of the present invention.
Embodiment 1
In the there-necked flask of 1000ml cleaning, add benzene 500ml, cyanoacetic acid 85g and triethylamine 138ml, stir and dirtyly add pivaloyl chloride 123ml, whole process temperature must not more than 30 DEG C, reinforced complete, in 20 ~ 30 DEG C of reaction 2h, and for subsequent use in this temperature.
Benzene 200ml is added, sodiumazide 71.5g and ammonium chloride 59g, dispersed with stirring in the flask of another 2000ml cleaning, cyanoacetic acid reaction solution is transferred in above-mentioned mixed solution, reinforced complete, be slowly warming up to 80 DEG C, and in this thermotonus 6h, be cooled within 30 DEG C and adjust pH to 1-2, slow stirred crystallization with the hydrochloric acid of 15%, temperature is down to 0-5 DEG C of filtration, time rinsing of filter cake frozen water 50ml × 3 is drained, drying, obtains White crystalline solid 103g, and yield is 80.4%.
Embodiment 2
Toluene 500ml, cyanoacetic acid 85g and triethylamine 138ml is added in the there-necked flask of 1000ml cleaning, stir and dirtyly add trimethylchlorosilane 86.4ml, whole process temperature must not more than 30 DEG C, reinforced complete, in 25 ~ 30 DEG C of reaction 2h, and for subsequent use in this temperature.
Toluene 200ml is added, sodiumazide 71.5g and succinimide 35g, dispersed with stirring in the flask of another 2000ml cleaning, cyanoacetic acid reaction solution is transferred in above-mentioned mixed solution, reinforced complete, be slowly warming up to 110 DEG C, and in this thermotonus 7h, be cooled within 30 DEG C and adjust pH to 1-2, slow stirred crystallization with the dilute sulphuric acid of 15%, temperature is down to 0-5 DEG C of filtration, time rinsing of filter cake frozen water 50ml × 3 is drained, drying, obtains White crystalline solid 98g, yield 76.5%.
Embodiment 3
Benzene 500ml, cyanoacetic acid 85g and xylidine 121ml is added in the there-necked flask of 1000ml cleaning, stir and dirtyly add trimethylchlorosilane 86.4ml, whole process temperature must not more than 30 DEG C, reinforced complete, in 25 ~ 30 DEG C of reaction 3h, and for subsequent use in this temperature.
Benzene 200ml is added, sodiumazide 71.5g and succinimide 35g, dispersed with stirring in the flask of another 2000ml cleaning, cyanoacetic acid reaction solution is transferred in above-mentioned mixed solution, reinforced complete, be slowly warming up to 80 DEG C, and in this thermotonus 7h, be cooled within 30 DEG C and adjust pH to 1-2, slow stirred crystallization with the hydrochloric acid of 15%, temperature is down to 0-5 DEG C of filtration, time rinsing of filter cake frozen water 50ml × 3 is drained, drying, obtains White crystalline solid 100g, yield 78%.

Claims (3)

1. a production method for 1H-TETRAZOLE-5-acetic acid, is characterized in that, the method is reacted in two steps:
1) take cyanoacetic acid as initial substance, first react with chloro thing under solvent and catalyzer exist, temperature of reaction is 0-30 DEG C, and the time is that 1-3h obtains intermediate; Described catalyzer is triethylamine, N, N-dipropyl-1-propylamine or N, N-xylidine, and solvent is benzene or toluene;
2) add sodiumazide by step 1 gained intermediate, under solvent and catalyzer exist, be warming up to 60-150 DEG C of reaction 6-8h, 30 DEG C are cooled to after reaction terminates, between sour souring soln pH to 1-2, be again cooled to 0-5 DEG C, filter and obtain target product 1H-tetrazolium-5-acetic acid; Described catalyzer is ammonium chloride or succinimide, and solvent is benzene or toluene;
Reactional equation is as follows:
Wherein, described R is pivaloyl group or trimethyl silicon based.
2. the production method of a kind of 1H-tetrazolium-5-acetic acid according to claim 1, is characterized in that, step 2) described in acid be dilute hydrochloric acid or dilute sulphuric acid.
3. the production method of a kind of 1H-tetrazolium-5-acetic acid according to claim 2, it is characterized in that, described dilute hydrochloric acid or dilute sulphuric acid concentration are 15%.
CN201210383353.5A 2012-10-11 2012-10-11 A kind of production method of 1H-TETRAZOLE-5-acetic acid Expired - Fee Related CN102993114B (en)

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CN103351352B (en) * 2013-07-15 2015-10-21 南通市华峰化工有限责任公司 A kind of 5-phenyl tetrazole novel synthesis
CN103508971A (en) * 2013-09-09 2014-01-15 南通市华峰化工有限责任公司 1H-tetrazole-5-acetic acid one-step synthesis production method
CN103508969A (en) * 2013-09-09 2014-01-15 南通市华峰化工有限责任公司 Synthesis production method of high-purity 1H-tetrazole-5-acetic acid
CN105037330A (en) * 2015-06-23 2015-11-11 西安近代化学研究所 Synthesis method of 4,5-di(1H-5-tetrazol)-1,2,3-triazole

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CN1314672C (en) * 2005-05-24 2007-05-09 南通市华峰化工有限责任公司 5-substituted aromatic laydrocarbon tetrazole production method
JP2011502141A (en) * 2007-10-29 2011-01-20 ナトコ ファーマ リミテッド 4- (Tetrazol-5-yl) -quinazoline derivatives as anticancer agents

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Inventor after: Zhang Yaobing

Inventor after: Wang Bingcai

Inventor after: Zhang Yancheng

Inventor before: Wang Defeng

Inventor before: Zhu Xiaofei

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Inventor before: Zhang Yaobin

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