CN102993089B - Method for synthesizing aminopyridine - Google Patents

Method for synthesizing aminopyridine Download PDF

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Publication number
CN102993089B
CN102993089B CN201210383381.7A CN201210383381A CN102993089B CN 102993089 B CN102993089 B CN 102993089B CN 201210383381 A CN201210383381 A CN 201210383381A CN 102993089 B CN102993089 B CN 102993089B
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China
Prior art keywords
aminopyridine
haloperidid
liquefied ammonia
synthetic method
synthesizing
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CN201210383381.7A
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Chinese (zh)
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CN102993089A (en
Inventor
王德峰
张燕程
张耀兵
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Huafeng Chemical Co., Ltd., Nantong
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HUAFENG CHEMICAL CO Ltd NANTONG CITY
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Abstract

The invention discloses a method for synthesizing aminopyridine, which is characterized by comprising the following steps of: adding a solvent and a catalyst in mixing liquid of halogenated pyridine and liquid ammonia; reacting at temperature of 200-1000 DEG C to obtain a crude product; and refining by methyl benzene to obtain the target product. The method for synthesizing aminopyridine has the advantages that the synthesizing method disclosed by the invention is simple, low in cost, easy in operation, good in product selectivity, and high in total yield to be 65-85%.

Description

A kind of synthetic method of aminopyridine
Technical field
The present invention relates to a kind of synthetic method of aminopyridine.
Background technology
Aminopyridine be contain ammonia the material with heterocycle structure, in vitochemical many fields, be widely used in, be the important intermediate of manufacturing the gas chromatography matter such as medicine, synthetic dyestuff, be mainly used in the high-end Field of Fine Chemicals such as medicine, agricultural chemicals and novel material.Along with scientific and technical development, the demand of high purity aminopyridine compounds also increases gradually, and the synthetic route of studying a kind of high-content, low cost and easy-operating aminopyridine becomes very meaningful.
Summary of the invention
The synthetic method that the object of this invention is to provide the aminopyridine that a kind of technique is simple, side reaction is little, 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 synthetic method of aminopyridine, it is characterized in that: in the mixed solution of haloperidid and liquefied ammonia, add solvent and catalyzer, at 200-1000 ℃ of temperature, reaction obtains crude product, by toluene is refining, obtain target product again, reaction equation is:
Wherein, described R 1for H, Cl, F, Br, R 2for H, Cl, F, Br, corresponding R 3and R 4be respectively H and NH 2.
Further, described solvent is quinoline or derivatives thereof.
Further, described catalyzer is palladium, ruthenium, rhodium or by three kinds of content of metal, is surpassed 10% carried catalyst.
Further, the mol ratio of described haloperidid and liquefied ammonia is 1:4-150, and catalyst levels is the 0.01-10% of haloperidid weight, and solvent load is the 1-50 of haloperidid weight.
Further, the mol ratio of described haloperidid and liquefied ammonia is 1:10-30, and catalyst levels is the 0.2-2% of haloperidid weight.
Further, described temperature of reaction is 250-450 ℃.
The invention has the advantages that: by halogenated pyrimidine and liquefied ammonia under catalysts and solvents effect, high-temperature high-voltage reaction obtains crude product, after refining, obtain target product, synthetic method of the present invention is simple, cost is low, easy to operate, product selectivity good, and total recovery reaches 65-85%.
Embodiment
In order to make the public can fully understand technical spirit of the present invention and beneficial effect; 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, anyly according to the present invention design, changes in the form rather than substance all and should be considered as protection scope of the present invention.
Embodiment 1
The 3-bromopyridine that adds 1mol in autoclave, the nanometer ruthenium C catalyst that the charge capacity of activated processing is 10% and the quinoline of 800 milliliters, close high-pressure reactor, pass into the liquefied ammonia of 20mol, after off-response device, be warmed up to 350 ℃, stirring reaction 12 hours, after reaction finishes, the liquefied ammonia that venting is unnecessary, adds 300 ml waters, stirs and is cooled to 0-5 ℃, filtration obtains 91 grams of solids, with refining 58.3 grams of 99.2% products, 65 ℃ of fusing points, yield 62% of obtaining of toluene.
Embodiment 2
The 2-chloropyridine that adds 1mol in autoclave, the nanometer ruthenium C catalyst that the charge capacity of activated processing is 10% and the quinoline of 800 milliliters, close high-pressure reactor, pass into the liquefied ammonia of 20mol, after off-response device, be warmed up to 350 ℃, stirring reaction 12 hours, after reaction finishes, the liquefied ammonia that venting is unnecessary, adds 300 ml waters, stirs and is cooled to 0-5 ℃, filtration obtains 102 grams of solids, with refining 68.6 grams of 99.1% products, fusing point 122.3-122.7 ℃, the yield 73% of obtaining of toluene.
Embodiment 3
In autoclave, add 2 of 1mol, 6-dichloropyridine, the charge capacity of activated processing is 10% nanometer ruthenium C catalyst and the quinoline of 800 milliliters, close high-pressure reactor, pass into the liquefied ammonia of 20mol, after off-response device, be warmed up to 350 ℃, stirring reaction 12 hours, after reaction finishes, the liquefied ammonia that venting is unnecessary, add 300 ml waters, stir and be cooled to 0-5 ℃, filter and obtain 89 grams of solids, with toluene refining obtain 99.1% 2,81.8 grams of 6-diamino-pyridine products, fusing point 121.1-122.3 ℃, yield 75%.
Embodiment 4
In autoclave, add 2 of 1mol, 6-bromine chloropyridine, the nanometer ruthenium C catalyst that the charge capacity of activated processing is 10% and the quinoline of 800 milliliters, close high-pressure reactor, pass into the liquefied ammonia of 20mol, after off-response device, be warmed up to 350 ℃, stirring reaction 12 hours, after reaction finishes, the liquefied ammonia that venting is unnecessary, add 300 ml waters, stirring is cooled to 0-5 ℃, filters and obtains 102 grams of solids, with refining 92.8 grams of 99.3% products that obtain of toluene, fusing point 122.3-122.7 ℃, yield 85.1%.

Claims (4)

1. a synthetic method for aminopyridine, is characterized in that: in the mixed solution of haloperidid and liquefied ammonia, add solvent and catalyzer, reaction obtains crude product at 200-1000 ℃ of temperature, then obtains target product by toluene is refining, and reaction equation is:
Wherein, described R 1for H, Cl, F, Br, R 2for H, Cl, F, Br, corresponding R 3and R 4be respectively H and NH 2; Described catalyzer is that charge capacity is 10% ruthenium C catalyst, and described solvent is quinoline.
2. the synthetic method of a kind of aminopyridine according to claim 1, is characterized in that: the mol ratio of described haloperidid and liquefied ammonia is 1:4-150, and catalyst levels is the 0.01-10% of haloperidid weight, and solvent load is the 1-50 of haloperidid weight.
3. the synthetic method of a kind of aminopyridine according to claim 2, is characterized in that: the mol ratio of described haloperidid and liquefied ammonia is 1:10-30, and catalyst levels is the 0.2-2% of haloperidid weight.
4. the synthetic method of a kind of aminopyridine according to claim 1, is characterized in that: described temperature of reaction is 250-450 ℃.
CN201210383381.7A 2012-10-11 2012-10-11 Method for synthesizing aminopyridine Expired - Fee Related CN102993089B (en)

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Publication number Priority date Publication date Assignee Title
CN103288720B (en) * 2013-06-09 2015-05-27 南通市华峰化工有限责任公司 High-pressure synthetic method of 2,6-diaminopyridine

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CN101723885A (en) * 2008-10-24 2010-06-09 朱比兰特奥甘诺斯有限公司 Improved method for preparing diaminopyridine
US20100160678A1 (en) * 2008-12-18 2010-06-24 E. I. Du Pont De Nemours And Company Process for the synthesis of 2,6-diamino-3,5-dinitrotoluene
WO2011084773A2 (en) * 2009-12-21 2011-07-14 E. I. Du Pont De Nemours And Company Process for the synthesis of 1-amino-3-halo-4,6-dinitrobenzene
CN102256946A (en) * 2008-12-18 2011-11-23 纳幕尔杜邦公司 Continuous liquid-phase process for the synthesis of diaminopyridines from glutaronitriles

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WO2006124283A1 (en) * 2005-05-12 2006-11-23 Boehringer Ingelheim International, Gmbh Bis-amination of aryl halides
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CN101723885A (en) * 2008-10-24 2010-06-09 朱比兰特奥甘诺斯有限公司 Improved method for preparing diaminopyridine
US20100160678A1 (en) * 2008-12-18 2010-06-24 E. I. Du Pont De Nemours And Company Process for the synthesis of 2,6-diamino-3,5-dinitrotoluene
CN102256946A (en) * 2008-12-18 2011-11-23 纳幕尔杜邦公司 Continuous liquid-phase process for the synthesis of diaminopyridines from glutaronitriles
WO2011084773A2 (en) * 2009-12-21 2011-07-14 E. I. Du Pont De Nemours And Company Process for the synthesis of 1-amino-3-halo-4,6-dinitrobenzene

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Efficient synthesis of aminopyridine derivatives by copper catalyzed amination reactions;Mohammed K. Elmkaddem等;《Chem. Commun.》;20091007;第46卷;第926页表格5中第3式化合物 *
Mohammed K. Elmkaddem等.Efficient synthesis of aminopyridine derivatives by copper catalyzed amination reactions.《Chem. Commun.》.2009,第46卷第926页表格5中第3式化合物.
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Inventor after: Wang Defeng

Inventor after: Zhang Yancheng

Inventor after: Zhang Yaobing

Inventor before: Wang Defeng

Inventor before: Zhu Xiaofei

Inventor before: Wang Bingcai

Inventor before: Zhang Yaobin

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Inventor before: Yu Jianjun

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Free format text: CORRECT: INVENTOR; FROM: WANG DEFENG ZHU XIAOFEI WANG BINGCAI ZHANG YAOBIN SHI FEI YU JIANJUN TO: WANG DEFENG ZHANG YANCHENG ZHANG YAOBING

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