CN113698389A - Synthetic method of esomeprazole - Google Patents

Synthetic method of esomeprazole Download PDF

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CN113698389A
CN113698389A CN202110990882.0A CN202110990882A CN113698389A CN 113698389 A CN113698389 A CN 113698389A CN 202110990882 A CN202110990882 A CN 202110990882A CN 113698389 A CN113698389 A CN 113698389A
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esomeprazole
deionized water
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毛杰
张志伟
汪仁仲
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Anhui Dingwang Medicine Co ltd
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    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D401/00Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom
    • C07D401/02Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings
    • C07D401/12Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings linked by a chain containing hetero atoms as chain links

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Abstract

The invention discloses a synthetic method of esomeprazole, which comprises the following steps: firstly, preparing omeprazole thioether; secondly, preparing a crude product by taking omeprazole thioether and the like as raw materials; refining the obtained crude product for 3 times to obtain a refined intermediate; and thirdly, mixing the refined intermediate with deionized water, filtering, adding esomeprazole as a seed crystal, mixing magnesium chloride hexahydrate and deionized water, stirring, cooling, stirring for 30min, carrying out vacuum filtration, washing the obtained crystal with distilled water, and drying to obtain the esomeprazole. The preparation process is refined for three times, so that the yield and the purity in the subsequent processing process are improved under the condition of ensuring that the yield in the refining process is 90%, and the problems of low total yield, increased production cost and inconvenience for industrial production caused by unsatisfactory improvement of the purity in the existing method are solved.

Description

Synthetic method of esomeprazole
Technical Field
The invention belongs to the technical field of drug synthesis, and particularly relates to a synthetic method of esomeprazole.
Background
Proton pump inhibitors, the pure levorotatory isomer of omeprazole, are useful for the initial and long-term treatment of gastroesophageal reflux disease (GORD), including erosive reflux esophagitis, including erosive esophagitis, for long-term maintenance therapy of esophagitis and prevention of GORD recurrence, and for symptomatic treatment of GORD disease. The methods for preparing esomeprazole have been disclosed in the patent documents WO9617076, WO9617077, WO9208716, WO9602535 and the like in succession. CN1110477A discloses a method for producing esomeprazole magnesium salt by reacting magnesium chloride with esomeprazole sodium, but magnesium chloride is dissolved in water and alcohol solvent, which brings great difficulty to the subsequent separation and purification, and the method for purifying and refining esomeprazole magnesium is not disclosed in the patent. In addition, these processes often yield esomeprazole magnesium trihydrate or other unstable forms of esomeprazole magnesium, rather than the more stable dihydrate of esomeprazole magnesium.
Disclosure of Invention
The invention provides a synthetic method of esomeprazole.
The technical problems to be solved by the invention are as follows:
the products prepared in the prior art have obvious impurities, including various intermediates and reaction byproducts, which remain therein; the purity is not improved ideally, the total yield is low, the production cost is increased, and the industrial production is not facilitated. The purity of the raw material drug directly influences the safety of the drug, and the yield directly influences the cost of producing the drug, so that the development of a preparation process of esomeprazole with higher purity and yield is necessary.
The purpose of the invention can be realized by the following technical scheme:
a synthetic method of esomeprazole comprises the following steps:
firstly, mixing methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride solution and 2-mercapto-5-methoxy-1H-benzimidazole, then adding sodium hydroxide and deionized water, controlling the temperature of dripping to be 0-30 ℃, and reacting for 1H at the temperature of 20-30 ℃ after finishing dripping; after the reaction is finished, carrying out post-treatment; the post-treatment comprises the following specific steps: adding toluene with 2 times of the volume of the reaction solution into the obtained reaction solution, then regulating the pH value to 12-12.5 by using an acetic acid solution, stirring for 10min, standing for 10min, separating liquid, washing a toluene layer for 2-4 times by using a potassium carbonate solution, then adding seed crystal omeprazole thioether, stirring for 12h at 0-30 ℃, stirring for 30min at 0-5 ℃, filtering, and drying a filter cake for 2h at 40 ℃ to obtain the omeprazole thioether;
the reaction process is as follows:
Figure BDA0003232375840000021
secondly, mixing omeprazole thioether, toluene, D- (-) -diethyl tartrate and deionized water, heating to 48-54 ℃, adding tetraisopropyl titanate, stirring for 50min, cooling to 28-34 ℃, adding N, N-diisopropylethylamine, dropwise adding cumene hydroperoxide, reacting for 60-120min after the addition, adding ammonia water and sodium bisulfite, and reacting for 6h at 12-30 ℃; after the reaction is finished, post-treatment is carried out, and the specific process of the post-treatment is as follows: adjusting pH of the reaction solution to 12.5-12.9 with sodium hydroxide solution, stirring for 10min, standing for 10min for liquid separation, removing a toluene layer, then adding toluene and dichloromethane, adjusting pH to 9-9.2 with glacial acetic acid, heating to 38-43 ℃, stirring for 10min, standing for 10min for liquid separation, removing a water layer, and drying the toluene layer with anhydrous magnesium sulfate to obtain a crude product;
refining the obtained crude product for 3 times to obtain a refined intermediate;
the reaction process is as follows:
Figure BDA0003232375840000031
and thirdly, mixing the refined intermediate with deionized water, dissolving, filtering, adding esomeprazole as a seed crystal at the temperature of 30-40 ℃, mixing magnesium chloride hexahydrate with deionized water, dropwise adding the mixture within 1h, stirring for 12h, cooling to 0-5 ℃, stirring for 30min, carrying out vacuum filtration, washing obtained crystals with distilled water, and drying obtained wet products to constant weight at the temperature of 40 ℃ and 2-4kPa to obtain esomeprazole.
The reaction process is as follows:
Figure BDA0003232375840000032
further, in the first step, the ratio of the amount of methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride, 2-mercapto-5-methoxy-1H-benzimidazole, sodium hydroxide and deionized water was 42L: 12 kg: 9.8-9.9 kg: 5.4 kg: 24L.
Furthermore, the dosage ratio of omeprazole thioether, toluene, diethyl D- (-) -tartrate, deionized water, tetraisopropyl titanate, N-diisopropylethylamine, cumene hydroperoxide, ammonia water and sodium bisulfite is 15.6-15.7 kg: 65.8L: 1.96-1.97 kg: 31.32 mL: 1.35-1.36 kg: 0.9-1L: 9 kg; 51-52L: 2.47 kg; wherein the mass fraction of the ammonia water is 15-18%.
Further, the ratio of the amount of the purified intermediate to the deionized water in the third step was 11.8 kg: 47L; the dosage ratio of the magnesium chloride hexahydrate to the deionized water is 3.35-3.6 kg: 68.8-69L; the dosage ratio of the refined intermediate, the magnesium chloride hexahydrate and the esomeprazole seed crystal is 11.8 kg: 3.35 kg: 144.9 g.
Further, the refining operation comprises the steps of:
step S11, mixing the obtained crude product with acetonitrile, heating to 70 ℃, stirring for 15min, filtering while the mixture is hot, adding methanol and a refined intermediate into the filtrate after filtering, taking the refined intermediate as a seed crystal, curing for 1h at the temperature of 65-73 ℃, cooling, crystallizing, filtering to obtain a wet product, and drying for 3h at 40 ℃ and 2-4 kPa; wherein the dosage ratio of the crude product, the acetonitrile, the methanol and the refined intermediate in the step S11 is 17 kg: 96.77L: 10.26L: 7.33 g.
The invention has the beneficial effects that:
omeprazole thioether is added in the first step to serve as seed crystal, refining is carried out for three times in the preparation process in the second step, yield and purity in the subsequent processing process are improved under the condition that yield in the refining process is 90%, and esomeprazole is added in the third step to serve as seed crystal; the total yield is improved in the whole preparation process, the production cost is reduced, the industrial production is facilitated, the operation difficulty and the cost are reduced, and on the other hand, the impurity content in the product is also reduced.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
A synthetic method of esomeprazole comprises the following steps:
firstly, mixing methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride solution and 2-mercapto-5-methoxy-1H-benzimidazole, then adding sodium hydroxide and deionized water, controlling the temperature at the time of dripping to be 0 ℃, and reacting for 1H at the temperature of 20 ℃ after finishing dripping; after the reaction is finished, carrying out post-treatment; the post-treatment comprises the following specific steps: adding toluene with 2 times of the volume of the reaction solution into the obtained reaction solution, then regulating the pH value to 12 by using an acetic acid solution, stirring for 10min, standing for 10min, separating liquid, washing a toluene layer for 2 times by using a potassium carbonate solution, then adding seed crystal omeprazole thioether, stirring for 12h at 0 ℃, stirring for 30min at 0 ℃, filtering, and drying a filter cake for 2h at 40 ℃ to obtain the omeprazole thioether; the yield is 87.99 percent;
secondly, mixing omeprazole thioether, toluene, D- (-) -diethyl tartrate and deionized water, heating to 48 ℃, adding tetraisopropyl titanate, stirring for 50min, cooling to 28 ℃, adding N, N-diisopropylethylamine, dropwise adding cumene hydroperoxide, reacting for 60min after the addition, adding ammonia water and sodium bisulfite, and reacting for 6h at 12 ℃; after the reaction is finished, post-treatment is carried out, and the specific process of the post-treatment is as follows: adjusting pH of the reaction solution to 12.5 with sodium hydroxide solution, stirring for 10min, standing for 10min for liquid separation, removing toluene layer, adding toluene and dichloromethane, adjusting pH to 9 with glacial acetic acid, heating to 38 deg.C, stirring for 10min, standing for 10min, liquid separation, removing water layer, and drying the toluene layer with anhydrous magnesium sulfate to obtain crude product; the yield of the process is 80.4%;
refining the obtained crude product for 3 times to obtain a refined intermediate;
and thirdly, mixing the refined intermediate with deionized water, dissolving, filtering, adding esomeprazole as a seed crystal at the temperature of 30 ℃, mixing magnesium chloride hexahydrate with deionized water, dropwise adding the mixture within 1h, stirring for 12h, cooling to 0 ℃, stirring for 30min, carrying out vacuum filtration, washing obtained crystals with distilled water, and drying the obtained wet product at 40 ℃ and 2kPa to constant weight to obtain esomeprazole. The yield of this process was 92%.
Wherein, in the first step, the dosage ratio of methanol, 2-chloromethyl-4-methoxyl-3, 5-dimethylpyridine hydrochloride solution, 2-mercapto-5-methoxyl-1H-benzimidazole, sodium hydroxide and deionized water is 42L: 12 kg: 9.8 kg: 5.4 kg: 24L.
Wherein the dosage ratio of omeprazole thioether, toluene, D- (-) -diethyl tartrate, deionized water, tetraisopropyl titanate, N-diisopropylethylamine, cumene hydroperoxide, ammonia water and sodium bisulfite is 15.6 kg: 65.8L: 1.96 kg: 31.32 mL: 1.35 kg: 0.9L: 9 kg; 51L: 2.47 kg; wherein the mass fraction of the ammonia water is 15 percent.
Wherein, the dosage ratio of the refined intermediate to the deionized water in the third step is 11.8 kg: 47L; the dosage ratio of the magnesium chloride hexahydrate to the deionized water is 3.35 kg: 68.8L; the dosage ratio of the refined intermediate, the magnesium chloride hexahydrate and the esomeprazole seed crystal is 11.8 kg: 3.35 kg: 144.9 g.
Wherein the refining operation comprises the steps of:
step S11, mixing the obtained crude product with acetonitrile, heating to 70 ℃, stirring for 15min, filtering while the mixture is hot, adding methanol and a refined intermediate into the filtrate after filtering, taking the refined intermediate as a seed crystal, curing for 1h at the temperature of 65 ℃, cooling, crystallizing, filtering, and drying the wet product for 3h at 40 ℃ and 2 kPa; wherein the dosage ratio of the crude product, the acetonitrile, the methanol and the refined intermediate in the step S11 is 17 kg: 96.77L: 10.26L: 7.33 g. The yield of the refining process was 90%.
Example 2
A synthetic method of esomeprazole comprises the following steps:
firstly, mixing methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride solution and 2-mercapto-5-methoxy-1H-benzimidazole, then adding sodium hydroxide and deionized water, controlling the temperature at the time of dripping to be 20 ℃, and reacting for 1H at the temperature of 25 ℃ after finishing dripping; after the reaction is finished, carrying out post-treatment; the post-treatment comprises the following specific steps: adding toluene with the volume 2 times that of the obtained reaction solution into the obtained reaction solution, then regulating the pH value to 12 by using an acetic acid solution, stirring for 10min, standing for 10min, separating liquid, washing a toluene layer for 3 times by using a potassium carbonate solution, then adding seed crystal omeprazole thioether, stirring for 12h at the temperature of 20 ℃, stirring for 30min at the temperature of 0 ℃, filtering, and drying a filter cake for 2h at the temperature of 40 ℃ to obtain the omeprazole thioether; the yield is 88.12%;
secondly, mixing omeprazole thioether, toluene, D- (-) -diethyl tartrate and deionized water, heating to 50 ℃, adding tetraisopropyl titanate, stirring for 50min, cooling to 30 ℃, adding N, N-diisopropylethylamine, dropwise adding cumene hydroperoxide, reacting for 90min after the addition, adding ammonia water and sodium bisulfite, and reacting for 6h at 20 ℃; after the reaction is finished, post-treatment is carried out, and the specific process of the post-treatment is as follows: adjusting pH of the reaction solution to 12.5 with sodium hydroxide solution, stirring for 10min, standing for 10min for liquid separation, removing toluene layer, adding toluene and dichloromethane, adjusting pH to 9 with glacial acetic acid, heating to 40 deg.C, stirring for 10min, standing for 10min, liquid separation, removing water layer, and drying the toluene layer with anhydrous magnesium sulfate to obtain crude product; the yield of the process is 80.6 percent;
refining the obtained crude product for 3 times to obtain a refined intermediate;
and thirdly, mixing the refined intermediate with deionized water, dissolving, filtering, adding esomeprazole as a seed crystal at the temperature of 35 ℃, mixing magnesium chloride hexahydrate with deionized water, dropwise adding the mixture within 1h, stirring for 12h, cooling to 0 ℃, stirring for 30min, carrying out vacuum filtration, washing obtained crystals with distilled water, and drying the obtained wet product at 40 ℃ and 3kPa to constant weight to obtain esomeprazole. The yield of this process was 91%.
Wherein, in the first step, the dosage ratio of methanol, 2-chloromethyl-4-methoxyl-3, 5-dimethylpyridine hydrochloride solution, 2-mercapto-5-methoxyl-1H-benzimidazole, sodium hydroxide and deionized water is 42L: 12 kg: 9.8 kg: 5.4 kg: 24L.
Wherein the dosage ratio of omeprazole thioether, toluene, D- (-) -diethyl tartrate, deionized water, tetraisopropyl titanate, N-diisopropylethylamine, cumene hydroperoxide, ammonia water and sodium bisulfite is 15.6 kg: 65.8L: 1.96 kg: 31.32 mL: 1.35 kg: 0.9L: 9 kg; 51L: 2.47 kg; wherein the mass fraction of the ammonia water is 15 percent.
Wherein, the dosage ratio of the refined intermediate to the deionized water in the third step is 11.8 kg: 47L; the dosage ratio of the magnesium chloride hexahydrate to the deionized water is 3.35 kg: 68.8L; the dosage ratio of the refined intermediate, the magnesium chloride hexahydrate and the esomeprazole seed crystal is 11.8 kg: 3.35 kg: 144.9 g.
Wherein the refining operation comprises the steps of:
step S11, mixing the obtained crude product with acetonitrile, heating to 70 ℃, stirring for 15min, filtering while the mixture is hot, adding methanol and a refined intermediate into the filtrate after filtering, taking the refined intermediate as a seed crystal, curing for 1h at the temperature of 70 ℃, cooling, crystallizing, filtering, and drying the wet product for 3h at 40 ℃ and 2 kPa; wherein the dosage ratio of the crude product, the acetonitrile, the methanol and the refined intermediate in the step S11 is 17 kg: 96.77L: 10.26L: 7.33 g. The yield of the refining process was 90%.
Example 3
A synthetic method of esomeprazole comprises the following steps:
firstly, mixing methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride solution and 2-mercapto-5-methoxy-1H-benzimidazole, then adding sodium hydroxide and deionized water, controlling the temperature of dripping at 30 ℃, and reacting for 1H at the temperature of 30 ℃ after finishing dripping; after the reaction is finished, carrying out post-treatment; the post-treatment comprises the following specific steps: adding toluene with 2 times of the volume of the reaction solution into the obtained reaction solution, then regulating the pH value to 12.5 by using an acetic acid solution, stirring for 10min, standing for 10min, separating liquid, washing a toluene layer for 4 times by using a potassium carbonate solution, then adding seed crystal omeprazole thioether, stirring for 12h at 30 ℃, stirring for 30min at 5 ℃, filtering, and drying a filter cake for 2h at 40 ℃ to obtain the omeprazole thioether; the yield is 88.21%;
secondly, mixing omeprazole thioether, toluene, D- (-) -diethyl tartrate and deionized water, heating to 54 ℃, adding tetraisopropyl titanate, stirring for 50min, cooling to 34 ℃, adding N, N-diisopropylethylamine, dropwise adding cumene hydroperoxide, reacting for 120min after the addition, adding ammonia water and sodium bisulfite, and reacting for 6h at 30 ℃; after the reaction is finished, post-treatment is carried out, and the specific process of the post-treatment is as follows: adjusting pH of the reaction solution to 12.9 with sodium hydroxide solution, stirring for 10min, standing for 10min for liquid separation, removing toluene layer, adding toluene and dichloromethane, adjusting pH to 9.2 with glacial acetic acid, heating to 43 deg.C, stirring for 10min, standing for 10min, liquid separation, removing water layer, and drying the toluene layer with anhydrous magnesium sulfate to obtain crude product; the yield of the process is 80.4%;
refining the obtained crude product for 3 times to obtain a refined intermediate;
and thirdly, mixing the refined intermediate with deionized water, dissolving, filtering, adding esomeprazole as a seed crystal at the temperature of 40 ℃, mixing magnesium chloride hexahydrate with deionized water, dropwise adding the mixture within 1h, stirring for 12h, cooling to 5 ℃, stirring for 30min, carrying out vacuum filtration, washing obtained crystals with distilled water, and drying the obtained wet product at the temperature of 40 ℃ and 4kPa to constant weight to obtain esomeprazole. The yield of this process was 92%.
Wherein, in the first step, the dosage ratio of methanol, 2-chloromethyl-4-methoxyl-3, 5-dimethylpyridine hydrochloride solution, 2-mercapto-5-methoxyl-1H-benzimidazole, sodium hydroxide and deionized water is 42L: 12 kg: 9.9 kg: 5.4 kg: 24L.
Wherein the dosage ratio of omeprazole thioether, toluene, D- (-) -diethyl tartrate, deionized water, tetraisopropyl titanate, N-diisopropylethylamine, cumene hydroperoxide, ammonia water and sodium bisulfite is 15.7 kg: 65.8L: 1.97 kg: 31.32 mL: 1.36 kg: 1L: 9 kg; 52L: 2.47 kg; wherein the mass fraction of the ammonia water is 18 percent.
Wherein, the dosage ratio of the refined intermediate to the deionized water in the third step is 11.8 kg: 47L; the dosage ratio of the magnesium chloride hexahydrate to the deionized water is 3.6 kg: 69L; the dosage ratio of the refined intermediate, the magnesium chloride hexahydrate and the esomeprazole seed crystal is 11.8 kg: 3.35 kg: 144.9 g.
Wherein the refining operation comprises the steps of:
step S11, mixing the obtained crude product with acetonitrile, heating to 70 ℃, stirring for 15min, filtering while the mixture is hot, adding methanol and a refined intermediate into the filtrate after filtering, taking the refined intermediate as a seed crystal, curing for 1h at 73 ℃, cooling, crystallizing, filtering, and drying the wet product for 3h at 40 ℃ and 4 kPa; wherein the dosage ratio of the crude product, the acetonitrile, the methanol and the refined intermediate in the step S11 is 17 kg: 96.77L: 10.26L: 7.33 g. The yield in the purification process was 91%.
Comparative example 1
Compared with the example 1, the yield of the third step is 78 percent without three refining operations and the rest processes are kept unchanged.
In the description herein, references to the description of "one embodiment," "an example," "a specific example" or the like are intended to mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The foregoing is illustrative and explanatory only and is not intended to be exhaustive or to limit the invention to the precise embodiments described, and various modifications, additions, and substitutions may be made by those skilled in the art without departing from the scope of the invention or exceeding the scope of the claims.

Claims (5)

1. A synthetic method of esomeprazole is characterized by comprising the following steps:
firstly, mixing methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride solution and 2-mercapto-5-methoxy-1H-benzimidazole, then adding sodium hydroxide and deionized water, controlling the temperature of dripping to be 0-30 ℃, and reacting for 1H at the temperature of 20-30 ℃ after finishing dripping; after the reaction is finished, carrying out post-treatment; obtaining omeprazole thioether;
secondly, mixing omeprazole thioether, toluene, D- (-) -diethyl tartrate and deionized water, heating to 48-54 ℃, adding tetraisopropyl titanate, stirring for 50min, cooling to 28-34 ℃, adding N, N-diisopropylethylamine, dropwise adding cumene hydroperoxide, reacting for 60-120min after the addition, adding ammonia water and sodium bisulfite, and reacting for 6h at 12-30 ℃; after the reaction is finished, carrying out post-treatment to obtain a crude product; refining the obtained crude product for 3 times to obtain a refined intermediate;
and thirdly, mixing the refined intermediate with deionized water, dissolving, filtering, adding esomeprazole as a seed crystal at the temperature of 30-40 ℃, mixing magnesium chloride hexahydrate with deionized water, dropwise adding the mixture within 1h, stirring for 12h, cooling to 0-5 ℃, stirring for 30min, carrying out vacuum filtration, washing obtained crystals with distilled water, and drying obtained wet products to constant weight at the temperature of 40 ℃ and 2-4kPa to obtain esomeprazole.
2. The process for the synthesis of esomeprazole according to claim 1, wherein the refining operation comprises the steps of:
mixing the obtained crude product with acetonitrile, heating to 70 ℃, stirring for 15min, filtering while the mixture is hot, adding methanol and a refined intermediate into the filtrate after filtering, taking the refined intermediate as a seed crystal, curing for 1h at the temperature of 65-73 ℃, cooling, crystallizing, filtering to obtain a wet product, and drying for 3h at the temperature of 40 ℃ and 2-4 kPa; wherein, the dosage ratio of the crude product, the acetonitrile, the methanol and the refined intermediate is 17 kg: 96.77L: 10.26L: 7.33 g.
3. The method for synthesizing esomeprazole according to claim 1, wherein the using amount ratio of methanol, 2-chloromethyl-4-methoxy-3, 5-dimethylpyridine hydrochloride solution, 2-mercapto-5-methoxy-1H-benzimidazole, sodium hydroxide and deionized water in the first step is 42L: 12 kg: 9.8-9.9 kg: 5.4 kg: 24L.
4. The method for synthesizing esomeprazole according to claim 1, wherein the dosage ratio of omeprazole thioether, toluene, diethyl D- (-) -tartrate, deionized water, tetraisopropyl titanate, N-diisopropylethylamine, cumene hydroperoxide, ammonia water and sodium bisulfite in the second step is 15.6-15.7 kg: 65.8L: 1.96-1.97 kg: 31.32 mL: 1.35-1.36 kg: 0.9-1L: 9 kg; 51-52L: 2.47 kg; the mass fraction of the ammonia water is 15-18%.
5. The method for synthesizing esomeprazole according to claim 1, wherein the ratio of the amount of the refined intermediate to the deionized water in the third step is 11.8 kg: 47L; the dosage ratio of the magnesium chloride hexahydrate to the deionized water is 3.35-3.6 kg: 68.8-69L; the dosage ratio of the refined intermediate, the magnesium chloride hexahydrate and the esomeprazole seed crystal is 11.8 kg: 3.35 kg: 144.9 g.
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