Purification of isoflurane by extractive distillation

Abstract

A method for the separation of Isoflurane from its admixture with other compounds produced in the chlorination of 2-difluoromethoxy-1,1,1-trifluoroethane including subjecting the mixture to distillation, distilling off the Isoflurane and effecting said distillation as an extractive distillation employing an extractive solvent which retards the vapor pressure of Isoflurane.

Description

This invention relates to the purification of 2-chloro-2-difluoromethoxy-1,1,1-trifluoroethane of the formula CF.sub.3 CHClOCHF.sub.2. This material, commonly known as having the Isoflurane, is useful as an inhalation anesthetic and, as such, has to be produced essentially free of impurities.

The most important process for manufacturing Isoflurane involves the chlorination of 2-difluoromethoxy-1,1,1-trifluoroethane, CF.sub.3 CH.sub.2 OCHF.sub.2, b.p. 29.degree. C., under actinic light illumination.

This reaction generates a number of by-products in addition to Isoflurane. A typical product mixture may contain:

______________________________________Compound b.p. (.degree.C.) Yield (Wt. %)______________________________________1. Isoflurane CF.sub.3 CHClOCHF.sub.2 48 602. CF.sub.3 CH.sub.2 OCHF.sub.2 29 263. CF.sub.3 CHClOCClF.sub.2 53 24. CF.sub.3 CH.sub.2 OCClF.sub.2 37 45. CF.sub.3 CCl.sub.2 OCHF.sub.2 61 86. CF.sub.3 CCl.sub.2 OCClF.sub.2 75 0.2______________________________________

Compounds 2, 4, 5 and 6 can be separated from Isoflurane by precise fractional distillation in an efficient column. Compound 3, on the other hand, co-distills and may even form a minimum boiling azeotrope with Isoflurane. U.S. Pat. No. 3,720,587 recognizes this fact and discloses a method wherein acetone, methyl ethyl ketone or tetrahydrofuran is added to the crude mixture so as to form a maximum boiling azeotrope with Isoflurane. The CF.sub.2 CHClCClF.sub.2 and other by-products, being unaffected, are distilled from the azeotrope. The azeotrope is then broken by the addition of large quantities of water, allowing the distillation of Isoflurane as a water azeotrope which, after drying, yields essentially pure Isoflurane.

While this method is successful, it has several drawbacks. For example, the acetone-Isoflurane azeotrope contains about 30% acetone, requiring a larger vessel size to complete the distillation. Further, in order to break the azeotrope, at least an equal weight of water is required, thus necessitating an even larger vessel. The water left behind after the removal of Isoflurane contains residual organic materials together with azeotropic solvent and has to be treated before disposal. Finally, the Isoflurane obtained is wet and has to be dried, thus requiring another operational step.

There is a need, therefore, for an improved purification method to produce essentially pure Isoflurane, and that is the object of the present invention.

It has now been found that Isoflurane produced by the chlorination of CF.sub.3 CH.sub.2 OCHF.sub.2 may be obtained essentially pure by an extractive distillation process in a multi-stage column.

Extractive distillation is a method of separating close boiling compounds by carrying out a fractional distillation in a multi-stage column in the presence of an added solvent or solvent mixture. The solvent is added near the top of the column at the boiling temperature at that location which is close to the boiling temperature of the original mixture. The key to the process is to use a solvent that has a selective effect on the principal component of the original mixture, and will alter its relative volatility, i.e. retard its vapor pressure, thereby making possible an efficient separation which would not at all occur in the absence of such solvent.

The normal method of conducting an extractive distillation is in a continuous column with uniform continuous feeds near the top of the column. At the bottom, the contents of the reboiler are continuously removed. This should comprise mainly extraction solvent and the principal component of the original mixture. No original components difficult to separate by distillation should be present. Usually the selective solvent is isolated in a separate rectification column.

It is essential to practical extractive distillation that the selective solvent not form an azeotrope with any component of the mixture to be separated. For this reason, it is preferable for the solvent to boil a minimum of 25.degree. C. higher. This difference will also simplify recovery of the solvent for reuse.

There has been discovered the following series of solvents with which to separate Isoflurane from its synthesis by-products in an extractive distillation process:

______________________________________Solvent b.p. (.degree.C.)______________________________________dimethylformamide 145dimethylacetamide 165N-methylpyrrolidone 205acetone 57______________________________________

Each of these solvents alters the volatility of Isoflurane relative to the other organic components of the original mixture, thus making it possible to isolate Isoflurane dry and pure.

EXAMPLE 1

A batch extractive fractional distillation was carried out in an Oldershaw-type column containing twenty-four glass sieve trays with downcomers, and with a feed line located at Tray 15. Feed rate was maintained with a precision piston-type metering pump; feed temperature was controlled with an electric tube heater. A 500 g feed charge, having the following composition, was placed in a three liter still pot:

______________________________________ Charge Wt. % b.p. (.degree.C.)______________________________________Isoflurane CH.sub.3 CH.sub.2 OCHF.sub.2 0.1 29 CF.sub.3 CH.sub.2 OCClF.sub.2 0.3 37 CF.sub.3 CHClOCHF.sub.2 87.9 48 CF.sub.3 CHClOCClF.sub.2 1.3 53 CF.sub.3 CCl.sub.2 OCHF.sub.2 10.5 61 CF.sub.3 CCl.sub.2 OCClF.sub.2 0.1 75______________________________________

Hereafter, each compound is designated by its boiling point. All analytical data have been obtained by gas chromatography.

The charge was brought to total reflux and maintained there for forty-five minutes at which time the reflux, b.p. 46.degree. C., had the following composition:

______________________________________Reflux Composition Cpd Wt. %______________________________________ 29 1.4 37 3.1 48 92.8 53 1.9 61 0.8 75 0.1______________________________________

Feed of the extractive agent, dimethylformamide, DMF, was initiated at 20 ml/min, 56.degree. C., on Tray 15. When the overhead temperature rose to 55.degree. C. indicating loss of 48, distillate take-off was started and continued until the 48 content of the overhead reached 99%. The bulk of this forerun had the following composition:

______________________________________Forerun Cpd Wt. %______________________________________ 29 0.7 37 1.6 48 15.0 53 10.2 61 71.6 75 0.3 99.4______________________________________

Overhead take-off was then switched to final product for which the composition was:

______________________________________Extractive DistillationFinal Product Cpd Wt. %______________________________________ 29 0 37 0 48 99.1 53 Trace 61 0.9 75 0______________________________________

Isoflurane, Cpd. 48, could be separated from 6I by normal fractional distillation.

EXAMPLE 2

The equipment of Example 1 was modified by the addition of a second feed system at the top of the column, Tray 24, and a product removal system from the stillpot. This enabled operation of the entire assembly as a continuous distillation facility. An extractive distillation run was initiated by refluxing a small charge of 200-400 g of dimethylformamide, DMF, in the stillpot. Feed I on Tray 15 was crude Isoflurane, Feed II on Tray 24 was good quality DMF. Typically, crude Isoflurane had the following composition:

______________________________________Crude Isoflurane Cpd Wt. %______________________________________ 29 5.8 37 1.9 48 86.8 53 0.9 61 4.6 75 --______________________________________

Feeds I and II were initiated at the same time at 6 ml/min and 20 ml/min respectively, at the projected temperature within the column at steady state. In the usual run, two liters of crude Isoflurane was fed into the column. A typical distillate had the following composition:

______________________________________Extractive Distillation ADistillate Composition Cpd Wt. %______________________________________ 29 36.6 37 13.8 48 3.4 53 7.6 61 35.8 75 -- DMF 2.8 100.0______________________________________

The final product from Extractive distillation A was obtained by stripping the DMF solution obtained from the stillpot, through a fractionating column:

______________________________________Extractive Distillation AFinal Product Composition Cpd Wt. %______________________________________ 29 0.0065 37 0.0059 48 99.6 53 0.0013 61 0.0183 75 -- DMF 0.3______________________________________

By repeating the extractive distillation with this product and carefully fractionating, Isoflurane could be obtained in a purity greater than 99.9990.

It will be understood that the specification and examples are illustrative but not limitative of the present invention and that other embodiments within the spirit and scope of the invention will suggest themselves to those skilled in the art.

Claims

1. In a separation of Isoflurane from its admixture with other compounds produced in the chlorination of 2-difluoromethoxy-1,1,1-trifluoroethane by subjecting the mixture to distillation and distilling off the Isoflurane, the improvement which comprises effecting said distillation as an extractive distillation employing an extractive solvent which retards the vapor pressure of Isoflurane, said solvent selected from a group consisting of dimethylformamide, dimethylacetamide, N-methylpyrrolidone and acetone.

2. The process according to claim 1, wherein the extractive solvent is dimethylacetamide.

3. The process according to claim 1, wherein the extractive solvent is dimethylformamide.

4. The process according to claim 3, wherein the product of the extractive distillation is subjected to a further distillation to recover Isoflurane.

5. The process according to claim 1, wherein the extractive solvent is acetone.