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Industrial preparation method of sevoflurane

A technology of sevoflurane and potassium fluoride, which is applied in the field of preparation of the inhaled anesthetic sevoflurane, can solve the problems of time-consuming, difficult to remove, and non-recyclable, etc., so as to reduce the difficulty of rectification, ensure product quality, and improve The effect on product yield

Active Publication Date: 2015-04-22
HEBEI YIPIN PHARMA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Research has found that the direct distillation of solid-liquid mixed feed liquid is not conducive to industrial production: on the one hand, the temperature in the still gradually increases, and the boiling point of the received fraction gradually decreases, indicating that the residual solid and liquid in the still have side reactions, resulting in low-boiling It is a new impurity, and as the temperature rises, the impurity content increases. From the observation of the gas chromatogram, the retention time of this impurity is close to that of sevoflurane, and it is not easy to remove in the subsequent rectification process. Repeated rectification is required, which consumes man-hours and affects product yield. rate, which increases the production cost; on the other hand, most of the residue in the still is carbonized solid, which cannot be recycled, is difficult to handle, and causes great environmental pollution.

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0018] Example 1: Add 1,000 grams of potassium fluoride, 2,100 grams of chloromethyl ether, and 3,500 grams of polyethylene glycol 400 to the reactor in sequence, heat to 75-80°C for reflux reaction for 4 hours, and then cool down to 0-5°C Filtrate, then combine the collected filtrate with the last batch of residual liquid in the reactor, and then distill, collect fractions below 80°C to obtain 1891 grams of crude sevoflurane (GC99.4%, yield 90.0%), and the crude product is obtained by rectification 1724.5 grams of finished sevoflurane was obtained (99.999% content, 91.2% yield).

Embodiment 2

[0019] Example 2: Add 1,200 grams of potassium fluoride, 2,100 grams of chloromethyl ether, and 1,500 grams of diethylene glycol to the reactor in sequence, heat to reflux for 8 hours, cool down to 16-20°C, filter, collect the filtrate, and add the above batch Still residue distillation, collecting fractions below 80°C, to obtain 1854.3 grams of crude sevoflurane (GC99.5%, yield 88.3%), the crude product was rectified to obtain 1696.7 grams of qualified sevoflurane (content 99.999%, yield 91.5%) ).

Embodiment 3

[0020] Example 3: Add 900 grams of sodium fluoride, 2,100 grams of chloromethyl ether, and 1,450 grams of triethylene glycol to the reactor in sequence, heat to reflux for 6 hours, cool down to 10-15°C, filter, collect the filtrate, and add the above batch Still residual distillation, collecting fractions below 80°C, yielded 1915.2 grams of sevoflurane crude product (GC99.2%, yield 91.2%), the crude product was rectified to obtain 1769.6 grams of sevoflurane qualified product (content 99.998%, yield 92.4%) ).

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PUM

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Abstract

The invention discloses an industrial preparation method of sevoflurane. The method comprises the following steps: adding chloromethyl ether and alkali metal fluoride to a solvent, uniformly stirring and heating for a reflux reaction; after the reaction, cooling a reaction liquid to be less than 20 DEG C and filtering, combining a filtrate with reaction residual liquor and distilling under normal pressure; collecting fraction less than 80 DEG C so as to obtain crude sevoflurane, and rectifying so as to obtain a finished sevoflurane product. By optimizing the crude sevoflurane preparing step, namely adding a filtering and impurity removing step after fluoridation reaction, the industrial preparation method disclosed by the invention can be used for relieving a side reaction during distilling and avoiding the generation of some impurities, and especially impurities similar to the sevoflurane in retention time, so that rectifying difficulty is reduced, rectifying time is reduced and product quality is guaranteed; the content of the finished sevoflurane product can reach 99.999%, so that manpower and material resources can be saved and product yield can be improved to 92.4%; and meanwhile, generated cauldron bottom residue can be recycled, so that the industrial preparation method can be used for further improving yield and reducing cost, and the preparation method is more conducive to industrial production.

Description

technical field [0001] The invention relates to a preparation method of an inhalation anesthetic sevoflurane. Background technique [0002] Sevoflurane (1), the chemical name is 1,1,1,3,3,3-hexafluoro-2-fluoromethoxypropane, which is an ideal choice after halothane, enflurane and isoflurane. The inhalational anesthetic, which was approved by the US FDA in 1995, has short induction period, fast recovery, easy metabolism, low blood gas distribution coefficient, stable hemodynamics, small adverse reactions to the human body, easy adjustment of anesthesia depth, and non-flammable and explosive Etc. Therefore, it has been paid more and more attention and adopted in general anesthesia of operation, and has a broad market prospect. [0003] The most commonly used raw material in the synthetic method of sevoflurane is 1,1,1,3,3,3-hexafluoroisopropanol (hereinafter referred to as hexafluoroisopropanol), Bernad M Regan et al. in US Patents US3683092 and US3689571 It is reported th...

Claims

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Application Information

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IPC IPC(8): C07C43/12C07C41/01C07C41/34
CPCC07C41/01C07C41/34C07C41/42C07C43/123
Inventor 贾宗英赵翠然程瑶左凯亚张楠张晓彩
Owner HEBEI YIPIN PHARMA
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