CN113480438B - Preparation method of esmolol hydrochloride - Google Patents

Preparation method of esmolol hydrochloride Download PDF

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CN113480438B
CN113480438B CN202110815504.9A CN202110815504A CN113480438B CN 113480438 B CN113480438 B CN 113480438B CN 202110815504 A CN202110815504 A CN 202110815504A CN 113480438 B CN113480438 B CN 113480438B
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reaction
methanol
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CN113480438A (en
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冯宪东
周臣生
杨英英
张博
张继东
庞洪莉
崔学洋
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Shandong Anhong Pharmaceutical Co ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D301/00Preparation of oxiranes
    • C07D301/27Condensation of epihalohydrins or halohydrins with compounds containing active hydrogen atoms
    • C07D301/28Condensation of epihalohydrins or halohydrins with compounds containing active hydrogen atoms by reaction with hydroxyl radicals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/04Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reaction of ammonia or amines with olefin oxides or halohydrins
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/10Separation; Purification; Stabilisation; Use of additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D303/00Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02Compounds containing oxirane rings
    • C07D303/12Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
    • C07D303/18Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by etherified hydroxyl radicals
    • C07D303/20Ethers with hydroxy compounds containing no oxirane rings
    • C07D303/22Ethers with hydroxy compounds containing no oxirane rings with monohydroxy compounds
    • C07D303/23Oxiranylmethyl ethers of compounds having one hydroxy group bound to a six-membered aromatic ring, the oxiranylmethyl radical not being further substituted, i.e.

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Abstract

The invention provides a preparation method of esmolol hydrochloride. The method of the invention comprises the steps of: the thionyl chloride reacts with methanol to prepare methyl sulfite chloride; the p-hydroxy benzene propionic acid and methyl sulfite undergo substitution reaction to prepare methyl p-hydroxy benzene propionate; the method has the advantages of easily available raw materials, low cost, simple preparation method, high yield and high purity of target products, and market competitiveness.

Description

Preparation method of esmolol hydrochloride
Technical Field
The invention relates to a preparation method of esmolol hydrochloride, belonging to the field of pharmaceutical chemistry synthesis.
Background
Esmolol hydrochloride (Esmolol Hydrochloride) is a white or white-like crystalline powder, the chemical name of which is 4- [ 3- [ 1-methylethyl ] amino ] -2-hydroxy ] propoxy } phenylpropionic acid methyl ester hydrochloride, and the structural formula of the esmolol hydrochloride is shown as the following formula I. Esmolol hydrochloride is a beta 1 adrenergic receptor blocker with the characteristics of quick action, short action time and selectivity, and mainly acts on beta 1 adrenergic receptors of cardiac muscle; the beta 2 adrenergic receptor of the smooth muscle of the trachea and the blood vessel also has a blocking effect at a large dose; the device is mainly used for controlling ventricular rate during atrial fibrillation and atrial flutter and treating operation period hypertension and sinus tachycardia.
In the prior art, esmolol hydrochloride or intermediate preparation methods have been reported, for example: chinese patent document CN111620782A discloses a preparation method of esmolol hydrochloride intermediate; reacting p-bromophenol with methyl acrylate in the presence of a palladium catalyst and a phosphine ligand to generate 3- (4-hydroxyphenyl) methyl acrylate; the 3- (4-hydroxyphenyl) methyl acrylate is hydrogenated in the presence of a palladium carbon catalyst to obtain the target product methyl 4-hydroxyphenylpropionate, wherein the total yield is 70 percent and the purity is 99 percent. However, the invention uses palladium-carbon catalyst, and the cost is high; and the reaction selectivity is poor, the side reaction is more, and the yield and purity of the target product are lower.
For another example, chinese patent CN101891636a discloses a method for preparing esmolol hydrochloride optical isomer, dissolving methyl parahydroxybenzoate in anhydrous aprotic polar solvent, adding alkali to prepare phenoxide, then condensing with (S) -glycidyl derivative or (R) -glycidyl derivative to prepare intermediate, then hydrolyzing with isopropylamine to form salt with hydrogen chloride, obtaining optically active esmolol hydrochloride, and refining to obtain pure (S) -esmolol hydrochloride or (R) -esmolol hydrochloride. However, the invention has low yield of target products, and NaH is used in the preparation process, so that the risk is high, and the invention is not suitable for industrial production.
Disclosure of Invention
Aiming at the defects existing in the prior art, the invention provides a preparation method of esmolol hydrochloride. The method has the advantages of easily available raw materials, low cost and simple preparation method; the target product has high yield and purity and has market competitiveness.
Description of the terminology:
a compound of formula I: esmolol hydrochloride;
A compound of formula II: p-hydroxy benzene propionic acid;
A compound of formula III: methyl p-hydroxyphenylpropionate;
A compound of formula IV: methyl 3- [4- (2, 3-epoxypropoxy ] phenylpropionate;
a compound of formula V: esmolol.
The compound numbers and the structural formula numbers have the same reference relationship and are based on the structural formula.
The technical scheme of the invention is as follows:
a method for preparing esmolol hydrochloride, comprising the steps of:
(1) The thionyl chloride reacts with methanol to prepare methyl sulfite chloride; the compound of the formula II and methyl sulfite chloride undergo substitution reaction to prepare a compound of the formula III;
(2) In a solvent A, under the action of potassium carbonate and tetrabutylammonium bromide, carrying out etherification reaction on a compound of a formula III and epoxy chloropropane to obtain a compound of a formula IV;
(3) In a solvent B, subjecting a compound of the formula IV and isopropylamine to amination reaction to prepare a compound of the formula V;
(4) In a solvent C, the compound of the formula V and hydrogen chloride are salified to prepare esmolol hydrochloride.
According to the invention, in the step (1), the mass ratio of the methanol to the compound of the formula II is 3-4:1, and the molar ratio of the thionyl chloride to the compound of the formula II is 1.0-1.1:1.
According to a preferred embodiment of the present invention, in the step (1), the reaction temperature of the methanol and thionyl chloride is 0 to 10 ℃. The reaction time is 0.5-3.0h.
According to a preferred embodiment of the invention, in step (1), the substitution reaction temperature of the methyl sulfite chloride and the compound of formula II is 30-40 ℃. The reaction time is 0.5-1.0h.
According to a preferred embodiment of the present invention, in step (1), the thionyl chloride is added dropwise to the methanol.
According to the present invention, in the step (1), the reaction solution obtained by the reaction of thionyl chloride and methanol is directly subjected to the next reaction without being treated.
According to a preferred embodiment of the present invention, in the step (2), the solvent a is one of tetrahydrofuran, 2-methyltetrahydrofuran or acetonitrile; preferably, the solvent A is tetrahydrofuran; the mass ratio of the solvent A to the compound of the formula III is 3-4:1.
According to the invention, in the step (2), the molar ratio of potassium carbonate to the compound of the formula III is 1.5-3.0:1, the molar ratio of epichlorohydrin to the compound of the formula III is 1.5-4.0:1, and the mass ratio of tetrabutylammonium bromide to the compound of the formula III is 0.8-1.2:1.
According to a preferred embodiment of the present invention, in the step (2), the etherification reaction temperature is 60 to 65 ℃. The reaction time is 8.0-10.0h.
According to the present invention, in the step (2), the post-treatment step of the reaction liquid obtained by the etherification reaction is preferably as follows: the obtained reaction liquid is decompressed and concentrated, toluene is added into the concentrate and stirred evenly, and then the compound of the formula IV is obtained through water washing, anhydrous sodium sulfate drying and decompression distillation.
Preferably, in step (3), the solvent B is methanol; the mass ratio of the solvent B to the compound of the formula IV is 3-4:1.
According to a preferred embodiment of the invention, in step (3), the molar ratio of isopropylamine to the compound of formula IV is 2.0-2.5:1.
According to a preferred embodiment of the present invention, in the step (3), the amination reaction temperature is 45 to 55 ℃; the reaction time is 4.0-5.0h.
According to the invention, in the step (4), the solvent C is one or a mixture of two of methanol and ethyl acetate; preferably, the solvent C is a mixed solvent of methanol and ethyl acetate, and the mass ratio of the methanol to the ethyl acetate is 1:4-5; the mass ratio of the solvent C to the compound of the formula V is 3.5-4.5:1.
According to the invention, in the step (4), the salt forming reaction temperature is 0-10 ℃, and the pH value of a salt forming system is less than or equal to 2; the reaction time is 1.0-2.0h.
According to a preferred embodiment of the invention, in step (4), hydrogen chloride is introduced as a gas into the mixture of the compound of formula V and the solvent C.
According to a preferred embodiment of the present invention, in the step (4), the reaction mixture obtained by the salt-forming reaction of the compound of formula V with hydrogen chloride is worked up as follows: filtering the obtained reaction liquid, washing with ethyl acetate, and drying to obtain an esmolol hydrochloride crude product; the obtained esmolol hydrochloride crude product is dissolved in a mixed solvent of methanol and ethyl acetate, and then the esmolol hydrochloride is obtained through recrystallization, filtration, washing with ethyl acetate and drying.
Preferably, the mass ratio of the methanol to the esmolol hydrochloride crude product is 0.5-1.0:1, and the mass ratio of the ethyl acetate to the esmolol hydrochloride crude product is 3.0-4.0:1.
The reaction route of the invention is as follows:
The invention has the technical characteristics and beneficial effects that:
1. according to the invention, methyl sulfite is prepared by the reaction of thionyl chloride and methanol, and then the methyl sulfite is subjected to substitution reaction with parahydroxy phenylpropionic acid (II) to prepare methyl parahydroxy phenylpropionate (III), so that the use of a palladium catalyst is avoided, and the cost is low; and the reaction selectivity is high, the conversion rate is high, the side reaction is less, and the purity of the obtained methyl p-hydroxyphenylpropionate (III) is high.
2. The invention prepares 3- [4- (2, 3-epoxypropoxy ] methyl phenylpropionate (IV) by using tetrabutylammonium bromide as a phase transfer catalyst and alkali potassium carbonate, and has high etherification conversion rate.
3. In the salification process of esmolol, hydrogen chloride gas is preferably introduced, so that the salification conversion rate is high, and the product yield is high.
4. The invention preferably uses the mixed solvent of methanol and ethyl acetate to form salt and recrystallize, and has high product yield and high purity.
5. The method has the advantages of low-cost and easily-obtained raw materials, mild technological reaction conditions, simple preparation method and post-treatment, low cost, safe and safe use of dangerous reagents and contribution to industrial production; the reaction selectivity is high, the side reaction is less, the yield and purity of the target product are high, the yield of esmolol hydrochloride can reach 83.7%, and the purity can reach 99.7%.
Drawings
FIG. 1 is a high performance liquid chromatogram of esmolol hydrochloride obtained in example 1;
Fig. 2 is a high performance liquid chromatogram of esmolol hydrochloride obtained in example 2.
Detailed Description
The present invention is described in detail below with reference to examples, but the present invention is not limited thereto.
The methods described in the examples are conventional, unless otherwise specified; the reagents used are commercially available unless otherwise specified.
The yields in the examples are all molar yields.
Example 1
A method for preparing esmolol hydrochloride, comprising the steps of:
(1) 70.00g of methanol is added into a reaction bottle, the temperature is reduced to 5 ℃ by stirring, 15.00g (0.126 mol) of thionyl chloride is added dropwise at the temperature of 5 ℃ after 0.5h, and the reaction is carried out for 0.5h at the temperature of 5 ℃. Adding 20.00g (0.120 mol) of parahydroxyphenylpropionic acid (II), heating to 35 ℃, controlling the temperature to 35 ℃ for reacting for 0.5-1.0h, detecting that the reaction is complete by TLC, controlling the temperature to 30-40 ℃ and distilling under reduced pressure to obtain 21.62g of light yellow oily substance, wherein the purity is 99.9%, and the molar yield is 99.6% when the parahydroxyphenylpropionic acid methyl ester (III) is converted into 21.60 g;
(2) 70.00g of tetrahydrofuran, 35.00g (0.25 mol) of potassium carbonate, 20.00g of tetrabutylammonium bromide, 35.00g (0.38 mol) of epichlorohydrin and 20.00g (0.11 mol) of methyl p-hydroxyphenylpropionate (III) prepared in the step (1) are added into a reaction bottle, the mixture is stirred and heated to 60 ℃, the temperature is controlled to be 60 ℃ for reaction for 8.0 to 10.0h, TLC detection reaction is complete, the temperature is controlled to be 60 to 65 ℃ for reduced pressure concentration, 50.00g of toluene is added into the concentrate for uniform stirring, then 100ml of water is used for each time for three times of washing, anhydrous sodium sulfate is added for drying, suction filtration and reduced pressure distillation are carried out on the filtrate, so as to obtain light yellow oily matter 25.98g, the purity is 98.8%, and 3- [4- (2, 3-epoxypropoxy ] methyl phenylpropionate (IV) 25.67g is converted, and the molar yield is 97.9%;
(3) 70.00g of methanol, 11.26g (0.19 mol) of isopropylamine and 20g (0.085 mol) of methyl 3- [4- (2, 3-epoxypropoxy ] phenylpropionate (IV) prepared in the step (2) are added into a reaction bottle, the mixture is stirred and heated to 50 ℃, the reaction is carried out for 4.0 to 5.0 hours at the temperature of 50 ℃, the TLC detection reaction is complete, the reduced pressure distillation is carried out at the temperature of 45 to 55 ℃ to obtain 24.76g of light yellow oily matter with the purity of 93.5 percent, 23.15g of converted esmolol (V) and the molar yield of 92.6 percent;
(4) Adding 15.00g of methanol, 70.00g of ethyl acetate and 20g of esmolol (V) prepared in the step (3) into a reaction bottle, stirring and cooling to 5 ℃, introducing dry hydrogen chloride gas at the temperature of 5 ℃ until the pH value of the system is less than or equal to 2, stopping introducing the hydrogen chloride gas after the pH value reaches the requirement, stirring and reacting for 1.5h, carrying out suction filtration, leaching a filter cake by using 20.00g of ethyl acetate, and drying the filter cake to obtain 21.82g of esmolol hydrochloride crude product with the molar yield of 97.1% and the purity of 99.4%;
(5) Adding 15.00g of methanol, 70.00g of ethyl acetate and 20g of esmolol hydrochloride crude product into a reaction bottle, stirring and heating to 55-65 ℃ for dissolution, cooling to 0-10 ℃ for crystallization after solution clearing, stirring and crystallization at 0-10 ℃ for 1.0-2.0h, carrying out suction filtration, leaching a filter cake by using 20.00g of ethyl acetate, and drying the filter cake to obtain 19.12g of esmolol hydrochloride, wherein the molar yield is 95.6%, the purity is 99.7%, and a high-phase liquid chromatogram of a final product is shown in a figure 1; the total yield of esmolol hydrochloride is 83.7%.
Example 2
A method for preparing esmolol hydrochloride, comprising the steps of:
(1) Methyl parahydroxybenzoate (III) was prepared as in example 1;
(2) 70.00 g (0.25 mol) of acetonitrile, 35.00g (0.25 mol) of potassium carbonate, 20.00g (tetrabutylammonium bromide), 35.00g (0.38 mol) of epichlorohydrin and 20.00g (0.11 mol) of methyl p-hydroxyphenylpropionate (III) prepared in the step (1) are added into a reaction bottle, the mixture is stirred and heated to 60 ℃, the temperature is controlled to be 60 ℃ for reaction for 8.0 to 10.0h, TLC detection reaction is complete, the temperature is controlled to be 60 ℃ to 65 ℃ for reduced pressure concentration, 50.00g of toluene is added into the concentrate and stirred uniformly, then 100ml of water is used for each time for three times, the washed oil is dried by adding anhydrous sodium sulfate, suction filtration is carried out, and the filtrate is distilled under reduced pressure, thus obtaining light yellow oily matter 25.77g, the purity of 3- [4- (2, 3-epoxypropoxy) methyl phenylpropionate (IV) is converted into 25.43g, and the molar yield is 97.0 percent;
(3) 70.00g of methanol, 11.26g (0.19 mol) of isopropylamine and 20g (0.085 mol) of methyl 3- [4- (2, 3-epoxypropoxy ] phenylpropionate (IV) prepared in the step (2) are added into a reaction bottle, the mixture is stirred and heated to 50 ℃, the reaction is carried out for 4.0 to 5.0 hours at the temperature of 50 ℃, TLC detection reaction is complete, the temperature of 45 to 55 ℃ is controlled, and reduced pressure distillation is carried out, so as to obtain 24.61g of light yellow oily matter with the purity of 93.4 percent and the molar yield of 91.9 percent of converted esmolol (V) of 22.99 g;
(4) Adding 15.00g of methanol, 70.00g of ethyl acetate and 20g of esmolol (V) prepared in the step (3) into a reaction bottle, stirring and cooling to 5 ℃, introducing dry hydrogen chloride gas at the temperature of 5 ℃ until the pH value of the system is less than or equal to 2, stopping introducing the hydrogen chloride gas after the pH value reaches the requirement, stirring and reacting for 1.5h, carrying out suction filtration, leaching a filter cake by using 20.00g of ethyl acetate, and drying the filter cake to obtain 21.68g of esmolol hydrochloride crude product with the molar yield of 96.5% and the purity of 99.3%;
(5) Adding 15.00g of methanol, 70.00g of ethyl acetate and 20g of esmolol hydrochloride crude product into a reaction bottle, stirring and heating to 55-65 ℃ for dissolution, cooling to 0-10 ℃ for crystallization after solution clearing, stirring and crystallization at 0-10 ℃ for 1.0-2.0h, carrying out suction filtration, leaching a filter cake by using 20.00g of ethyl acetate, and drying the filter cake to obtain 19.02g of esmolol hydrochloride, wherein the molar yield is 95.1%, the purity is 99.7%, and a high-phase liquid chromatogram of a final product is shown in figure 2; the total yield of esmolol hydrochloride is 81.5%.
Comparative example 1
The preparation method of esmolol hydrochloride is as described in example 1, except that tetrabutylammonium bromide is not added in the etherification reaction process of the step (2), and the step (2) is specifically as follows:
step (2): 70.00g tetrahydrofuran, 35.00g (0.25 mol) potassium carbonate, 35.00g (0.38 mol) epichlorohydrin and 20.00g (0.11 mol) methyl p-hydroxyphenylpropionate (III) prepared in the step (1) are added into a reaction bottle, the temperature is raised to 60 ℃, the reaction is carried out for 8.0 to 10.0 hours under the condition of temperature control of 60 ℃, TLC detection is complete, the temperature is controlled to 60 ℃ and reduced pressure concentration is carried out, 50.00g toluene is added into the concentrate and stirred uniformly, then 100ml water is used for washing three times each time, after washing, anhydrous sodium sulfate is added for drying, suction filtration and reduced pressure distillation are carried out on the filtrate, thus obtaining 23.82g of light yellow oily matter, the purity of which is 95.2 percent, and the molar yield of 3- [4- (2, 3-epoxypropoxy) methyl phenylpropionate (IV) 22.68 percent is 86.5 percent.
Other steps and conditions were consistent with example 1.
As can be seen from the comparison of the comparative examples, the addition of tetrabutylammonium bromide as the phase transfer catalyst is beneficial to the improvement of the yield and purity of the target product.
Comparative example 2
A process for preparing esmolol hydrochloride as described in example 1, except that the process for preparing methyl (III) p-hydroxyphenylpropionate in step (1) is different, specifically as follows:
Step (1): 70.00g of methanol, 0.11g of concentrated sulfuric acid and 20.00g (0.120 mol) of p-hydroxy benzene propionic acid (II) are added into a reaction bottle, the temperature is raised to 55 ℃, the temperature is controlled to 55 ℃ for reaction for 5-6 hours, TLC detection reaction is complete, 0.20g of potassium carbonate is added, the temperature is controlled to 55 ℃ for reduced pressure distillation, 22.03g of light yellow oily matter is obtained, the purity is 93.3%, and the molar yield of p-hydroxy benzene propionic acid methyl ester (III) is converted into 20.55g, and the molar yield is 94.8%.
Other steps and conditions were consistent with example 1.
As can be seen from the comparison of the comparative examples, the preparation method of methyl parahydroxybenzoate (III) of the present invention is advantageous for obtaining the target product with high yield and high purity.

Claims (4)

1. A method for preparing esmolol hydrochloride, comprising the steps of:
(1) The thionyl chloride reacts with methanol to prepare methyl sulfite chloride; the compound of the formula II and methyl sulfite chloride undergo substitution reaction to prepare a compound of the formula III;
The mass ratio of the methanol to the compound of the formula II is 3-4:1, and the molar ratio of the thionyl chloride to the compound of the formula II is 1.0-1.1:1; the reaction temperature of the methanol and the thionyl chloride is 0-10 ℃; the sulfoxide chloride is added into the methanol in a dropwise manner; the substitution reaction temperature of the methyl sulfite chloride and the compound of the formula II is 30-40 ℃; the reaction liquid obtained by the reaction of the thionyl chloride and the methanol is directly subjected to the next reaction without treatment;
(2) In a solvent A, under the action of potassium carbonate and tetrabutylammonium bromide, carrying out etherification reaction on a compound of a formula III and epoxy chloropropane to obtain a compound of a formula IV;
The solvent A is tetrahydrofuran or acetonitrile; the mass ratio of the solvent A to the compound of the formula III is 3-4:1; the molar ratio of potassium carbonate to the compound of the formula III is 1.5-3.0:1, the molar ratio of epichlorohydrin to the compound of the formula III is 1.5-4.0:1, and the mass ratio of tetrabutylammonium bromide to the compound of the formula III is 0.8-1.2:1; the etherification reaction temperature is 60-65 ℃; the post-treatment steps of the reaction liquid obtained by the etherification reaction are as follows: concentrating the obtained reaction liquid under reduced pressure, adding toluene into the concentrate, stirring uniformly, washing with water, drying with anhydrous sodium sulfate, and distilling under reduced pressure to obtain a compound of formula IV;
(3) In a solvent B, subjecting a compound of the formula IV and isopropylamine to amination reaction to prepare a compound of the formula V;
The solvent B is methanol;
(4) In a solvent C, salifying a compound of the formula V with hydrogen chloride to prepare esmolol hydrochloride;
The solvent C is a mixed solvent of methanol and ethyl acetate, and the mass ratio of the methanol to the ethyl acetate is 1:4-5; the mass ratio of the solvent C to the compound of the formula V is 3.5-4.5:1; the salt forming reaction temperature is 0-10 ℃, and the pH value of a salt forming system is less than or equal to 2; hydrogen chloride is introduced into a mixed solution of a compound of formula V and a solvent C in the form of gas; the post-treatment steps of the reaction liquid obtained by the salification reaction of the compound of the formula V and hydrogen chloride are as follows: filtering the obtained reaction liquid, washing with ethyl acetate, and drying to obtain an esmolol hydrochloride crude product; the obtained esmolol hydrochloride crude product is dissolved in a mixed solvent of methanol and ethyl acetate, and then the esmolol hydrochloride is obtained through recrystallization, filtration, washing with ethyl acetate and drying.
2. The process for preparing esmolol hydrochloride according to claim 1, wherein in step (3) one or more of the following conditions are included:
i. The mass ratio of the solvent B to the compound of the formula IV is 3-4:1;
ii. The molar ratio of isopropylamine to the compound of formula IV is 2.0-2.5:1;
iii, the amination reaction temperature is 45-55 ℃; the reaction time is 4.0-5.0h.
3. The method for preparing esmolol hydrochloride according to claim 1, wherein in the step (4), the reaction time is 1.0-2.0h.
4. The preparation method of esmolol hydrochloride according to claim 1, wherein the mass ratio of methanol to esmolol hydrochloride crude product is 0.5-1.0:1, and the mass ratio of ethyl acetate to esmolol hydrochloride crude product is 3.0-4.0:1.
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