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Synthetic method for preparing olmesartan medoxomil intermediate through continuous flow

A technology for olmesartan medoxomil and a synthesis method, applied in the field of drug synthesis, can solve the problems of long reaction time, limited production capacity, large amount of solvent used, etc., and achieve the effects of high purity, good quality and short reaction time

Active Publication Date: 2021-09-03
拓信达(启东)医药生物科技有限公司 +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0015] However, the control level of impurity A and impurity B in the examples is still 1.5%, and the synthesized olmesartan medoxomil cannot meet the requirements of raw materials, and there is no control of impurity C
And the amount of solvent used is large, the reaction time is long, generally 30 minutes to 48 hours, the production capacity is limited, and it is difficult to meet the demand for olmesartan medoxomil intermediates

Method used

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  • Synthetic method for preparing olmesartan medoxomil intermediate through continuous flow
  • Synthetic method for preparing olmesartan medoxomil intermediate through continuous flow
  • Synthetic method for preparing olmesartan medoxomil intermediate through continuous flow

Examples

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Effect test

Embodiment 1

[0037] Step 1, the preparation of formula II compound 4-(1-hydroxyl-1-methylethyl)-2-propylimidazole-5-carboxylic acid ethyl ester, 190g2-propyl-imidazole-4,5-dicarboxylate Acid diethyl ester (compound of formula I) was dissolved in a mixed solution of 338.2 g of tetrahydrofuran and 1316.3 g of toluene, stirred and dissolved into phase A, and the relative concentration was 0.1 g / mL. The commercially available methylmagnesium chloride tetrahydrofuran solution (3M) was used as phase B with a density of 1.04g / mL; the temperature of the reactor was set at 15°C, the flow rate of phase A was set at 10mL / min, and the flow rate of phase B was set at 1.13mL / min. Pump phase A and phase B into the mixer and then enter the reactor, retention time T Res =1.3min; set 10% hydrochloric acid aqueous solution as item C, and pump it into the quenching module at a feed rate of 5.52mL / min. The reaction liquid directly enters the continuous oil-water separator for continuous liquid separation, and...

Embodiment 2

[0042] Step 1, the preparation of formula II compound 4-(1-hydroxyl-1-methylethyl)-2-propylimidazole-5-carboxylic acid ethyl ester, 950g2-propyl-imidazole-4,5-dicarboxylate Acid diethyl ester (compound of formula I) was dissolved in 1.69kg of 2-methyltetrahydrofuran and 6.58kg of toluene mixed solution, stirred and dissolved into phase A, and the relative concentration was 0.1g / mL. The commercially available methylmagnesium chloride tetrahydrofuran solution (3M) was used as phase B with a density of 1.04g / mL; the temperature of the reactor was set at 15°C, the flow rate of phase A was set to 50mL / min, and the flow rate of phase B was set to 5.65mL / min. Pump phase A and phase B into the mixer and then enter the reactor, retention time T Res =1.3min; set 10% hydrochloric acid aqueous solution as item C, and pump it into the quenching module at a feed rate of 27.6mL / min. The reaction liquid directly entered the continuous oil-water separator for continuous liquid separation, and...

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Abstract

The invention discloses a synthetic method for preparing an olmesartan medoxomil intermediate through continuous flow, which belongs to the technical field of drug synthesis. The method comprises the following steps: step (1), dissolving a compound 2-propyl-4,5-imidazole dicarboxylic acid ethyl ester I in an organic solvent to form a reaction phase A; step (2), taking a commercially purchased methyl magnesium chloride solution as a reaction phase B; step (3), pumping the reaction phase A and the reaction phase B into a mixer by using a plunger pump at a certain flow rate, then feeding the mixture into a reactor, retaining for a certain time, quenching by using an acid water phase C, feeding the mixture into an oil-water continuous liquid separator, separating liquid to obtain an organic solution of a compound as shown in a formula II, desolventizing, and recrystallizing to obtain the compound as shown in the formula II. The technical problems of low purity and high cost in the existing preparation process are solved, the product is high in purity and few in impurities, the content of the key impurity A, the key impurity B and the key impurity C can be controlled to be 0.1% or below, the raw materials are cheap and easy to obtain, the reaction condition is mild, operation is easy and convenient, the synthesis efficiency is high, and the method is suitable for industrial production. A novel continuous flow path is provided for preparing the olmesartan medoxomil and the intermediate.

Description

technical field [0001] The invention belongs to the technical field of pharmaceutical synthesis, in particular to the synthesis of olmesartan medoxomil intermediate 4-(1-hydroxyl-1-methylethyl)-2-propylimidazole-5-carboxylic acid ethyl ester prepared by continuous flow method. Background technique [0002] Olmesartan medoxomil (formula III) is a novel angiotensin B receptor (AT1) inhibitor (ARB) jointly developed by Japan's Sankyo (Daiichi Sankyo) and U.S. Forest Laboratories. The English name is: Olmesartan Medoxomil , in May 2002, was approved by the US FDA for marketing, and the trade name was Benicar. In August 2002, it was approved to go on the market in Germany. It was approved for registration in China in 2013, and the product name is Aotan. In 2020, it will enter the second batch of national centralized procurement catalogues. [0003] [0004] Olmesartan medoxomil has unique pharmacokinetic and pharmacodynamic properties compared with other ARBs. Olmesartan m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D233/90
CPCC07D233/90
Inventor 皮红军姚彤吴江周威毛联岗吴晓发沈南星朱文涛
Owner 拓信达(启东)医药生物科技有限公司
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