Disclosure of Invention
The invention aims to provide a novel preparation method of a dabigatran etexilate intermediate through a great amount of experimental efforts aiming at the defects of the prior art, and the method is short in steps, simple to operate and suitable for industrial mass production.
The object of the invention can be achieved by the following measures:
A process for the preparation of a compound of formula I: reacting a compound shown in a formula V with a compound shown in a formula VI in the presence of alkali to obtain a compound III, reacting the compound III with p-aminobenzonitrile in the presence of alkali to synthesize a compound II, and finally performing hydrogenation cyclization reaction in the presence of a catalyst to obtain a compound I; the reaction route is as follows:
in the formula, X is selected from one or more halogens.
Reaction a relates to a process for the preparation of a compound of formula III,
X in each of the above formulae is preferably selected from one or two of chlorine and bromine.
The reaction solvent of reaction a may be a single solvent or a mixed solvent such as ethyl acetate, phenyl toluene, xylene, dichloromethane, dichloroethane, acetonitrile, DMF, etc., and among them, ethyl acetate and dichloromethane are preferred.
The base in reaction a may be an inorganic base such as sodium bicarbonate, sodium carbonate, potassium bicarbonate, potassium carbonate, etc., or an organic base such as triethylamine, pyridine, etc.
In the present invention, the compound of formula VI may be bromoacetyl bromide, bromoacetyl chloride, chloroacetyl chloride, or the like.
in the present invention, the temperature for dropping the compound of formula VI in the main reaction is not too high, and may be-5 deg.C to 40 deg.C, and generally room temperature or low temperature, preferably-5 deg.C to 15 deg.C.
the specific steps of the reaction a are as follows: mixing the compound of formula V, alkali and an anhydrous solvent, dropwise adding the compound of formula VI under stirring at a controlled temperature, continuously stirring for reaction after dropwise adding, adding water after reaction, stirring for layering, extracting a water layer with an organic solvent, combining organic layers, washing with saline solution, drying, filtering, and concentrating the filtrate under reduced pressure until the filtrate is dry to obtain the compound of formula III.
Reaction b relates to a process for the preparation of a compound of formula II,
In the reaction b, the base can be inorganic base, such as sodium bicarbonate, sodium carbonate, potassium bicarbonate, potassium carbonate, and the like, or organic base, such as triethylamine, pyridine, and the like. The temperature of the reaction can be 0-50 ℃, and is generally controlled to be between room temperature and the boiling point of the solvent, and the preferred temperature is 20-40 ℃.
One specific step of reaction b is: dissolving the compound shown in the formula III and p-aminobenzonitrile into solvents such as ethyl acetate, benzene, toluene, xylene, acetonitrile, dichloromethane, dichloroethane, chloroform and the like, adding alkali, stirring for reaction, adding water after the reaction is finished, stirring for demixing, extracting a water layer by using an organic solvent, combining organic layers, washing by using saturated sodium bicarbonate and saline solution respectively, drying the organic layers, and concentrating under reduced pressure until the organic layers are dried to obtain the compound shown in the formula II.
Reaction c relates to a process for the preparation of compounds of formula I,
In the reaction c, the catalyst is selected from a heavy metal catalyst or a composite catalyst of the heavy metal catalyst and an acid, wherein the heavy metal catalyst is selected from palladium carbon and palladium hydroxide, and the acid is sulfuric acid or acetic acid. In the invention, the acid is added during hydrogenation mainly for promoting intramolecular nitro transfer hydrogenation to directly form a ring, so that nitro reduction and ring formation are simultaneously completed to prepare the product compound shown in the formula (I), and the acid only needs a catalytic amount, or acetic acid can be directly used for replacing methanol, ethanol, ethyl acetate and the like and used as a solvent and a catalyst.
In the reaction c, hydrogen is introduced during hydrogenation; the reaction vessel may be either atmospheric or pressurized, the hydrogen pressure is generally controlled at 0-10 kg/cm2, and the hydrogenation reaction time is generally 8-10 hours.
the reaction solvent in reaction c may be selected from methanol, ethanol or ethyl acetate.
in the reaction c, the reaction temperature may be 0 to 60 ℃, and further may be from room temperature to the boiling point of the solvent, preferably within 20 to 50 ℃, and an excessively high temperature may cause side reactions.
The specific steps of the reaction c are as follows: dissolving the compound shown in the formula II in a solvent such as methanol, ethanol, ethyl acetate and the like, putting the mixture into a hydrogenation kettle, adding a noble metal catalyst such as palladium-carbon, palladium hydroxide and the like, adding a small amount of sulfuric acid or acetic acid, introducing N2 to replace oxygen in the kettle for three times, then using hydrogen to replace N2 in the kettle for three times, introducing hydrogen to stir for reaction after the replacement is finished, filtering the catalyst by pressure after the reaction is finished, and concentrating the catalyst by pressure reduction until the catalyst is dried to obtain the compound shown in the formula I.
The compound of formula V is used as a raw material to be prepared with a compound of formula VI to obtain a compound of formula III, then the compound of formula II is obtained with p-aminobenzonitrile under the action of alkali, and then the target product compound of formula I is obtained by transfer hydrogenation. The method has the advantages of short steps, mild conditions and high total reaction yield, and is suitable for industrial mass production.