Organic compounds -- part of the class 532-570 series – Organic compounds – Carboxylic acids and salts thereof
Reexamination Certificate
2002-01-08
2002-10-15
Killos, Paul J. (Department: 1625)
Organic compounds -- part of the class 532-570 series
Organic compounds
Carboxylic acids and salts thereof
Reexamination Certificate
active
06465688
ABSTRACT:
BACKGROUND OF THE INVENTION
The present invention relates to a process for the preparation of trifluoromethyl-substituted biphenylcarboxylic acids from the corresponding methyl-substituted biphenylcarbonitriles and to the novel trichloromethyl-substituted biphenylcarbonitriles and novel trifluoromethyl-substituted biphenylcarbonitriles occurring as intermediates thereof.
Trifluoromethyl-substituted biphenylcarboxylic acids are intermediates for the preparation of active pharmaceutical ingredients. 4′-(Trifluoromethyl)-2-biphenylcarboxylic acid itself is an active pharmaceutical ingredient known as xenalipin.
It is known that trifluoromethyl-substituted biphenylcarboxylic acids can be prepared by constructing the trifluoromethyl-substituted biphenyl system by means of an aryl coupling of suitable benzotrifluoride derivatives, using palladium, nickel, zinc, or Grignard reagents, wherein the carboxyl function of a precursor (for example, aldehyde or ester) is blocked with a suitable protective group in the appropriate coupling partner and, subsequent to the coupling, the carboxylic acid function is produced by transformation of the carboxyl precursor or elimination of the protective group (see, for example, Organ. Prep. Proced. Int., 27(3), 367 (1995), WO 00/32582 and EP-A 59983).
The suitability of these processes for the industrial scale is poor because organometallic compounds must be prepared and handled in all cases, which is possible only with great technological complexity. In addition, these methods, depending on the coupling method, use benzotrifluoride derivatives or substituted benzoic acid derivatives, which are costly and/or can be prepared only in a complex manner. Depending on the choice of the carboxyl precursor it is necessary for additional protective groups to be introduced and eliminated again.
Since there is still a need for a process which can be carried out reliably on the industrial scale without particular complexity and starting from easily available starting materials for the preparation of trifluoromethyl-substituted biphenylcarboxylic acids.
SUMMARY OF THE INVENTION
A process for the preparation of trifluoromethyl-substituted biphenylcarboxylic acids of the formula (I) has now been found
in which X
1
and X
2
are identical or different and in each case represent hydrogen, chlorine, or fluorine, comprising
(a) converting methyl-substituted biphenylcarbonitriles of the formula (IV)
in which X
1
and X
2
have the meanings stated for formula (I), into the corresponding trichloromethyl-substituted biphenylcarbonitriles of the formula (III)
in which X
1
and X
2
have the meanings stated for formula (I),
(b) converting the trichloromethyl group of the trichloromethyl-substituted biphenylcarbonitriles into a trifluoromethyl group, thereby obtaining trifluoromethyl-substituted biphenylcarbonitriles of the formula (II)
in which X
1
and X
2
have the meanings stated for formula (I), and
(c) converting the trifluoromethyl-substituted biphenylcarbonitriles to the corresponding trifluoromethyl-substituted biphenylcarboxylic acids by hydrolysis.
DETAILED DESCRIPTION OF THE INVENTION
X
1
and X
2
in the formulas (I) to (IV) preferably represent hydrogen. The trifluoromethyl group in the formulas (I) and (II), the trichloromethyl group in formula (III), and the methyl group in formula (IV) are preferably located in the position para to the biphenyl linkage. The carboxyl group in formula (I) and the nitrile group in formulas (II), (III), and (IV) are preferably in the position ortho to the biphenyl linkage. It is particularly preferred according to the invention to prepare 4′-(trifluoromethyl)-2-biphenyl-carboxylic acid from 4′-methyl-2-biphenylcarbonitrile.
The first stage of the process according to the invention, in preparation of the trichloromethyl-substituted biphenylcarbonitriles of the formula (III), can be carried out, for example, as a free-radical side-chain chlorination of corresponding methyl-substituted biphenylcarbonitriles of the formula (IV), in which elevated temperature, irradiation with a light source, and/or addition of a radical initiator are used. Particularly suitable light sources are halogen lamps and medium pressure and high pressure mercury lamps. Examples of suitable radical initiators are benzoyl peroxide, di-tert-butyl peroxide, 2,2′-azabis(isobutyronitrile), 2-phenylazo-2,4-dimethyl-4-methoxyvaleronitrile, tert-butylperoxy 2-ethylhexanoate, and others. It is preferred to employ a light source at elevated temperature.
The reaction temperature can be, for example, between 80° C. and 250° C. and is preferably 100° C. to 200° C., particularly 110° C. to 160° C.
The chlorinating agent preferably used for the first stage of the process according to the invention is elemental chlorine. Other chlorinating agents suitable for free-radical side-chain chlorinations can also be employed where appropriate.
It is possible to employ, for example, 2 to 10 equivalents (preferably 4 to 7 equivalents) of chlorinating agent per mole of methyl-substituted biphenylcarbonitrile of the formula (IV).
The free-radical side-chain chlorination is preferably carried out in the presence of solvents. Solvents are absolutely necessary if the methyl-substituted biphenylcarbonitriles of the formula (IV) are solid substances under the reaction conditions. Examples of suitable solvents are halogenated hydrocarbons such as chlorobenzene, dichlorobenzenes, and trichlorobenzenes, halogenated benzotrifluorides such as 4-chlorobenzotrifluoride, halogenated bis(trifluoromethyl)benzenes, and phosphorus oxychloride. It is possible to employ, for example, 0.5 g to 2.5 g of solvent per g of methyl-substituted biphenylcarbonitrile of the formula (IV). Preferred solvents are 2-chloro- and 4-chlorobenzotrifluoride.
The free-radical side-chain chlorination can be followed where appropriate by gas chromatography and preferably be carried out until the methyl-substituted biphenylcarbonitrile of the formula (IV) employed has been converted as far as possible into the desired product.
The reaction mixture after the first stage has been carried out can be worked up for example by initially removing chlorine that is still present, for example, by passing in an inert gas or applying a vacuum. The resulting crude product can be employed directly in the next reaction stage. If desired, the resulting trichloromethyl-substituted biphenylcarbonitrile of the formula (III) can also be purified further, for example, by crystallization or vacuum distillation. For the purpose of the process according to the invention the raw material present after removal of the excess chlorine is preferably processed further.
The second stage of the process according to the invention, the conversion of a trichloromethyl-substituted biphenylcarbonitrile of the formula (III) into the corresponding trifluoromethyl compound, can be carried out, for example, by reaction with a fluorinating agent such as anhydrous hydrofluoric acid, where appropriate in the presence of a fluorination catalyst such as antimony pentafluoride, antimony pentachloride, boron trifluoride, or titanium tetrachloride. Anhydrous hydrofluoric acid is preferably employed for this purpose.
It is possible to employ, for example, 200 to 500 ml of anhydrous hydrofluoric acid or a corresponding amount of another fluorinating agent per mole of trichloromethyl-substituted biphenylcarbonitrile of the formula (III). The amount of fluorination catalyst can be, for example, 0 to 0.2 mole per mole of trichloromethyl-substituted biphenylcarbonitrile.
The fluorination can be carried out, for example, by starting at a temperature below the boiling point (under atmospheric pressure) of hydrogen fluoride (for example, at −20° C. to +15° C.) and completing the fluorination at higher temperatures (for example, at 50° C. to 150° C.). Due to the vapor pressure of hydrogen fluoride at higher temperatures, this may result in pressures of up to, for example, 100 bar, which makes it necessary to use appropriately pr
Marhold Albrecht
Möller Peter
Peilstöcker Karen
Bayer Aktiengesellschaft
Gil Joseph C.
Henderson Richard E. L.
Oh Taylor Victor
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