Summary of the invention
In view of the deficiencies of the prior art, the purpose of the present invention is to provide a kind of chloro- nitrogenous hexa-member heterocycles of 5- cyano of 2-
The preparation method of object is closed, in order to industrial amplification production.
To achieve this purpose, the present invention adopts the following technical scheme:
The present invention provides a kind of preparation method of the chloro- nitrogenous 6-membered heterocyclic compound of 5- cyano of 2-, the method includes
Using the nitrogenous 6-membered heterocyclic compound of 2- hydroxyl -5- bromine as raw material, in the presence of a catalyst, under carbon monoxide atmosphere, methanol is made molten
Agent obtains 2- hydroxy nitrogen-containing hexa-member heterocycle -5- carboxylate methyl ester after coupling reaction occurs, and then successively passes through ammonolysis reaction, with trichlorine
Oxygen phosphorus carries out chlorination reaction, oxidation reaction, obtains the chloro- nitrogenous 6-membered heterocyclic compound of 5- cyano of the 2-;
Wherein, nitrogenous hexa-member heterocycle is pyridine or pyrimidine.
When nitrogenous hexa-member heterocycle is pyrimidine, specific reaction route is as follows:
When nitrogenous hexa-member heterocycle is pyridine, specific reaction route is as follows:
The preparation method of the chloro- nitrogenous 6-membered heterocyclic compound of 5- cyano of 2- provided by the invention, route is short, and raw material is easy to get,
Especially post-processing approach is simple, column Image processing is not necessarily to after every single step reaction, only by the washing of solvent, extraction
Reaction product is purified, compared to existing method for synthetic method there are routes long, more (such as mantoquitas of waste material of such compound
Equal waste materials), using high toxic materials such as phosgene, need the defect of column chromatographic purifying, the present invention may be implemented to amplify, and carry out industry
Metaplasia produces, and the waste material generated in production process is few, meets environmental requirement, has important value for actual production.
Preparation method provided by the invention is provided not only for the compound synthesis strategy such as cyanopyrimidine, and anti-
The intermediate that should be generated in the process, such as carboxylate methyl ester, amide pyrimidine, while providing the synthetic strategy of this kind of compounds.
Preferably, the catalyst is [1,1'- bis- (diphenylphosphine) ferrocene] palladium chloride dichloromethane complex.
Preferably, relative to the nitrogenous hexa-member heterocycle of 1g 2- hydroxyl -5- bromine, the dosage of the methanol is 8~12mL, such as
It can be 8mL, 8.5mL, 9mL, 9.5mL, 10mL, 10.5mL, 11mL, 11.5mL or 12mL etc..
Preferably, relative to the nitrogenous hexa-member heterocycle of 1g 2- hydroxyl -5- bromine, the dosage of the catalyst is 0.03~
0.08g, such as can be 0.03g, 0.04g, 0.05g, 0.06g, 0.07g or 0.08g etc..
Preferably, the coupling reaction further includes triethylamine.
Preferably, relative to the nitrogenous hexa-member heterocycle of 1g 2- hydroxyl -5- bromine, the dosage of the triethylamine is 1.1~1.3g,
Such as can be 1.1g, 1.15g, 1.16g, 1.18g, 1.19g, 1.2g, 1.25g, 1.26g, 1.28g, 1.29g or 1.3g etc..
In the present invention, after coupling reaction, it is only necessary to be washed, product 2- hydroxyl can be contained using diatomite filtering, methanol
Nitrogen hexa-member heterocycle -5- carboxylate methyl ester is purified, without complicated post-processing operation.
Preferably, the pressure of the coupling reaction be 0.5~0.8MPa, such as can be 0.5MPa, 0.55MPa,
0.6MPa, 0.65MPa, 0.7MPa, 0.75MPa or 0.8MPa etc..
Preferably, the temperature of the coupling reaction is 100~110 DEG C, such as can be 100 DEG C, 101 DEG C, 102 DEG C, 103
DEG C, 104 DEG C, 105 DEG C, 106 DEG C, 107 DEG C, 108 DEG C, 109 DEG C or 110 DEG C etc..
In the present invention, pressure and temperature controls within the above range simultaneously, it is ensured that reaction is gone on smoothly, yield
Reach highest.Pressure and temperature may generate security risk if excessively high;And pressure and temperature is if too low,
Reaction time is too long, and reaction yield reduces.
Preferably, the time of the coupling reaction be 90~100h, such as can be 90h, 91h, 92h, 93h, 94h,
95h, 96h, 97h, 98h, 99h or 100h etc..
Preferably, the ammonolysis reaction are as follows: 2- hydroxy nitrogen-containing hexa-member heterocycle -5- carboxylate methyl ester carries out in methyl alcohol with ammonium hydroxide
Reaction.
In the present invention, after ammonolysis reaction, amides compound is produced.
Preferably, relative to 1g 2- hydroxy nitrogen-containing hexa-member heterocycle -5- carboxylate methyl ester, the dosage of the ammonium hydroxide is 3.5~
5mL, such as can be 3.5mL, 3.7mL, 3.8mL, 3.9mL, 4mL, 4.2mL, 4.6mL, 4.8mL, 4.9mL or 5mL etc..
Preferably, the concentration of the ammonium hydroxide be 28wt.%~30wt.%, such as can be 28wt.%, 28.4wt.%,
28.6wt.%, 28.9wt.%, 29.4wt.%, 29.6wt.%, 29.8wt.% or 30wt.% etc..
Preferably, the temperature of the ammonolysis reaction is 30~35 DEG C, such as can be 30 DEG C, 31 DEG C, 32 DEG C, 33 DEG C, 34
DEG C or 35 DEG C etc..
Preferably, the time of the ammonolysis reaction be 90~100h, such as can be 90h, 91h, 92h, 93h, 94h,
95h, 96h, 97h, 98h, 99h or 100h etc..
Preferably, relative to 1g 2- hydroxy nitrogen-containing hexa-member heterocycle -5- carboxylate methyl ester, the dosage of the phosphorus oxychloride is 5~
7mL, such as can be 5mL, 5.5mL, 6mL, 6.5mL or 7mL etc..
In the present invention, use phosphorus oxychloride as raw material, chlorination reaction and oxidation reaction can be made anti-in same step
Middle progress is answered, process flow is simplified, it is only necessary to appropriate adjustment reaction temperature;And in existing method, such as
Route disclosed in US20111522952A1,2 chlorinations are until final synthesis cyano, intermediate reaction route up to 4-5
Step, considerably increases production cost, in the reaction time of consumption, is unfavorable for industrialized production.
Preferably, the temperature of the chlorination reaction is 50~55 DEG C, such as can be 50 DEG C, 51 DEG C, 52 DEG C, 53 DEG C, 54
DEG C or 55 DEG C etc..
Preferably, the time of the chlorination reaction be 2~3h, such as can be 2h, 2.1h, 2.2h, 2.3h, 2.4h,
2.5h, 2.6h, 2.7h, 2.8h, 2.9h or 3h etc..
Preferably, acid binding agent after 2~3h chlorination reaction, is directly being added into reaction solution, is carrying out oxidation reaction.
In reaction process of the invention, chlorination reaction while, also carries out the oxidation reaction of fraction, but oxygen at this time
It is slow to change reaction process, when chlorination reaction substantially completely after, the progress that acid binding agent promotes oxidation reaction, at this time oxidation reaction is added
It is dominant.
Preferably, the acid binding agent is n,N-diisopropylethylamine.
In the present invention, additive amount those skilled in the art of acid binding agent can suitably be adjusted according to the case where real reaction
It is whole.
Preferably, the temperature of the oxidation reaction is 75~85 DEG C, such as can be 75 DEG C, 76 DEG C, 77 DEG C, 78 DEG C, 79
DEG C, 80 DEG C, 81 DEG C, 82 DEG C, 83 DEG C, 84 DEG C or 85 DEG C etc..
Preferably, the time of the oxidation reaction is 20~25h, such as can be 20h, 21h, 22h, 23h, for 24 hours or 25h
Deng.
It preferably, further include that reaction solution is cooled to room temperature after the oxidation reaction, concentration, extraction, washing obtain
The chloro- nitrogenous 6-membered heterocyclic compound of 5- cyano of 2-.
In the present invention, it is cooled to room temperature after reaction, generally carries out the suitable volumes for being concentrated under reduced pressure into reaction solution, makes
It is extracted with extractant, reuses the alkali liquid washing as sodium bicarbonate aqueous solution, final product can be obtained.
Preferably, described to be extracted as extracting using extractant.
Preferably, the extractant includes in methyl tertiary butyl ether(MTBE), petroleum ether, tetrahydrofuran or 2- methyltetrahydrofuran
Any one or at least two combination;Preferably methyl tertiary butyl ether(MTBE).
In the present invention, when methyl tertiary butyl ether(MTBE) is as extractant, the effect of extraction is optimal, and other extractants extract effect
Fruit is poor, and such as petroleum ether, dissolubility of the product in petroleum ether is too low, will cause product loss;And such as tetrahydrofuran, each original
Material and impurity dissolubility in such solvent are preferable, so that the impurity that final products contain is more.
As optimal technical scheme, preparation method provided by the invention includes the following steps:
(1) using the nitrogenous 6-membered heterocyclic compound of 2- hydroxyl -5- bromine as raw material, at [1,1'- bis- (diphenylphosphine) ferrocene]
In the presence of palladium chloride dichloromethane complex, in CO gas atmosphere, methanol as solvent, triethylamine make alkali in pressure and are
0.5~0.8MPa, temperature are after 90~100h of coupling reaction occurs at 100~110 DEG C, to obtain 2- hydroxy nitrogen-containing hexa-member heterocycle-
5- carboxylate methyl ester;
(2) 2- hydroxy nitrogen-containing hexa-member heterocycle -5- carboxylate methyl ester is anti-by ammonolysis in 30~35 DEG C in methyl alcohol with ammonium hydroxide
90~100h is answered to obtain 2- hydroxy nitrogen-containing hexa-member heterocycle -5- formamide;Wherein ammonia concn is 28wt.%~30wt.%;
(3) by 2- hydroxy nitrogen-containing hexa-member heterocycle -5- formamide and phosphorus oxychloride in 50~55 DEG C of 2~3h of progress chlorination reaction
Afterwards, continue to add acid binding agent, adjustment temperature is 75~85 DEG C of progress 20~25h of oxidation reaction, and reaction solution is then cooled to room
Temperature, be concentrated under reduced pressure, extracted using extractant, wash to it is neutral be further concentrated after to obtain the chloro- 5- cyano of the 2- nitrogenous
6-membered heterocyclic compound.
The chloro- nitrogenous 6-membered heterocyclic compound of 5- cyano of the product 2- that preparation method provided by the invention is prepared, product
Purity is generally 99% or more, and the product purity that prior art method is prepared is generally only 97% or so.Compared to existing
There is method, method of the invention greatly promotes product purity.
Compared with the existing technology, the invention has the following advantages:
The preparation method of the chloro- nitrogenous 6-membered heterocyclic compound of 5- cyano of 2- provided by the invention, route is short, and raw material is easy to get,
Especially post-processing approach is simple, column Image processing is not necessarily to after every single step reaction, only by the washing of solvent, extraction
Reaction product is purified, it is long for there are routes in the synthetic method of such compound compared in existing method, waste material is more (such as
The waste materials such as mantoquita), using high toxic materials such as phosgene, need the defect of column chromatographic purifying, the present invention may be implemented to amplify, and carry out
Industrialized production, the waste material generated in production process is few, meets environmental requirement.Particularly with cyanopyrimidine or cyanopyridine class
The amplification production for closing object has important reference value, provides new strategy for practical amplification production.