USPatent applicationPatented

Process for preparing 2,4-dihydroxyphenyl 4-methoxybenzyl ketones

Granted 4 Dec 2012 · 2 office actions

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Abstract

The invention relates to a process for preparing 2,4-dihydroxyphenyl 4-methoxybenzyl ketones of the formula (I) by Friedel-Crafts acylation in hydrogen fluoride (HF). 2,4-Dihydroxyphenyl 4-methoxybenzyl ketones of the formula (I) in which R 1 and R 2 are each hydrogen, chlorine, fluorine, bromine, iodine, CF 3 , methyl, optionally substituted alkoxy, —OCF 3 , —C(CH 3 ) 3 , —CH 2 (CH 3 ) 2 , —CH(CH 3 ) 2 , R 3 is hydrogen, Cl, F, Br, optionally substituted alkyl, optionally substituted alkoxy, —C(CH 3 ) 3 , and X is hydroxyl, F, Cl, Br, optionally substituted alkoxy, are obtained in high yield and high purity by reacting phenylacetic acid derivatives of the formula (II) with phenols of the formula (III) in liquid hydrogen fluoride (HF). [structure]

Description

5 parts
›The invention relates to a process for preparing…

The invention relates to a process for preparing 2,4-dihydroxyphenyl 4-methoxybenzyl ketones of the formula (I) by Friedel-Crafts acylation in hydrogen fluoride (HF).

2,4-Dihydroxyphenyl 4-methoxybenzyl ketones of the general formula (I) are important synthesis units for preparing isoflavones, for example for formononetin or genistein, daidzein and coumestrol (general formula (IV)).

2,4-Dihydroxyphenyl 4-methoxybenzyl ketones have, for example, been obtained with very moderate yield by the time-consuming Hoeben-Hoesch reaction proceeding from phenylacetonitrile, resorcinol and hydrogen chloride (W. Baker et al., J. Chem. Soc 1929, 2902).

The reaction of resorcinol and phenylacetic anhydride or of the free acid in the presence of boron trifluoride etherate with a yield of 67% has also been described (S. Mohaty et al., Current Science, May 20, 1988, vol. 57, N. 10 and U.S. Pat. No. 5,981,775).

In addition, a synthesis of deoxybenzoin from resorcinol and 4-methoxyphenylacetic acid in the presence of 40 molar equivalents of a BF 3 /Et 2 O complex has been described (T. A. Hase in J. Chem Soc. Perkin Trans. 1, 1991, 3005).

Moreover, the synthesis of 2-phenylacetophenone derivatives from phenol and phenylacetic acid using dicyclohexylcarbodiimide (DCC) and 4-dimethylaminopyridine (DMAP) has been described (WO 2005/054169).

It is also known that benzoins can be obtained by means of Friedel-Crafts acylation in the presence of AlCl 3 (Indian J. Chem. vol. 6, 1968, p. 482).

Furthermore, it is known that polyhydroxybenzoins are obtainable by a microwave synthesis of ionic liquids in the presence of bis(trifluoromethyl)sulfonylamine or BF 3 /OEt 2 (Tetrahedron Letters, 47, 2006, 8375).

All of these methods have a series of disadvantages. These are a low yield, long reaction times or the use of expensive reagents such as DCC and DMAP. The use of catalysts such as BF 3 and AlCl 3 generates large amounts of wastewater which has to be disposed of in a complicated manner.

The BF 3 /Et 2 O complex is even unsuitable in practical terms for an industrial scale synthesis, since it possesses a very low flashpoint.

It has now been found that the synthesis of compounds (for example, 2,4-dihydroxyphenyl 4-methoxybenzyl ketones of the formula (I)

in which

R 1 and R 2 are each hydrogen, chlorine, fluorine, bromine, iodine, CF 3 , methyl, methoxy, optionally substituted alkoxy, —OCF 3 , —C(CH 3 ) 3 , —CH(CH 3 ) 2 , R 3 is hydrogen, Cl, F, Br, or optionally substituted alkyl, optionally substituted alkoxy, —C(CH 3 ) 3 , and X is hydroxyl, F, Cl, or optionally substituted alkoxy or Br, is possible with high yield and in high purity by reacting phenylacetic acid derivatives of the formula (II) with phenols of the formula (III) in liquid hydrogen fluoride (HF).

A further advantage of the process is that HF with a boiling point of 20° C. can be removed easily from the product by distillation and can therefore be recycled completely. HF is also a very inexpensive raw material and is prepared and used industrially on the thousand-tonne scale.

R 1 and R 2 are preferably hydrogen, methyl, methoxy, C 1 -C 6 -alkoxy, —OCF 3 , —C(CH 3 ) 3 ,

—CH(CH 3 ) 2 , or chlorine, fluorine, bromine, iodine, CF 3 .

R 1 and R 2 are more preferably hydrogen, methyl, methoxy, C 1 -C 4 -alkoxy, —C(CH 3 ) 3 ,

—CH(CH 3 ) 2 , or chlorine, fluorine, bromine, iodine, —CF 3 .

R 1 is most preferably methoxy. R 2 is most preferably hydrogen. R 3 is preferably hydrogen, C 1 -C 6 -alkyl, chlorine, fluorine, bromine, C 1 -C 6 -alkoxy, —C(CH 3 ) 3 . R 3 is more preferably hydrogen, C 1 -C 4 -alkyl, Cl, F, Br, C 1 -C 4 -alkoxy, —C(CH 3 ) 3 . R 3 is most preferably hydrogen. X is preferably hydroxyl, fluorine, chlorine, C 1 -C 6 -alkoxy, and more preferably hydroxyl, fluorine, chlorine, C 1 -C 4 -alkoxy. X is also preferably bromine.

Possible substituents for alkyl and alkoxy are: fluorine, chlorine, bromine, iodine, NO 2 , CN, SCN, NCO.

The reaction can optionally be accelerated by the addition of further catalysts. For example, catalysts, for example Lewis acids such as BF 3 , SbF 5 , PF 5 , BiF 3 , AsF 3 , AlCl 3 , SbCl 5 , TiCl 4 , NbCl 5 , SnCl 4 , SiCl 4 and InCl 3 , may be used. Preferred catalysts are: BF 3 , SbCl 5 , AlCl 3 , SiCl 4 , PF 5 . Particularly preferred catalysts are BF 3 , AlCl 3 , SbCl 5 .

When performing the process according to the invention, the reaction temperatures can be varied within a relatively wide range. In general, the temperatures are between −10° C. and 120° C. The temperatures are preferably between 0° C. and 50° C. Particular preference is given to reaction temperatures between 20° C. and 40° C.

The molar ratios of the hydrogen fluoride to the phenol of the formula (III) are variable within a wide range. In general, the process according to the invention is performed with molar ratios of hydrogen fluoride to the phenol of the formula (III) between 1:1 and 100:1. Preference is given to molar ratios of 50:1 to 10:1.

The process according to the invention can optionally be performed in the presence of further diluents. Suitable such diluents are, for example, ether, Freon, dichloromethane, dichloroethane, toluene and chlorobenzene.

Preference is given to performing the process without further diluents.

The reaction can be performed at ambient pressure under autogenous pressure, or under the pressure of a protective gas.

The compounds of the general formula (I) can be converted to compounds of the general formula (IV) according to the following scheme.

Suitable compounds for the reaction are, as well as CH(OEt) 3 , general compounds which, as well as a CH structural unit, possess nucleophilic leaving groups (Pivovarenko et al., Klim. Pirod. Soed. (Ukraine) 5 (1989), 639-643).

›PREPARATION EXAMPLES

Preparation of 1-(2,4-dihydroxyphenyl)-2-(4-methoxyphenyl)-ethanone

›Examples3
›Example 1

4-Methoxyphenylacetic acid (83.9 g), resorcinol (55 g) and hydrogen fluoride (450 g) are initially charged in an autoclave at −10° C., and the mixture is stirred at 20° C. for 12 h. Subsequently, the hydrogen fluoride is evaporated off at 40° C., and the precipitate is washed with water and dried.

This affords 123 g (91% of theory) of the product with a purity of 96% and a melting point (m.p.) of 160-162° C.

›Example 2

4-Methoxyphenylacetyl chloride (93 g), resorcinol (55 g) and hydrogen fluoride (450 g) are initially charged in an autoclave at −10° C., and the mixture is stirred at 20° C. for 12 h. Subsequently, the hydrogen fluoride is evaporated off at 40° C., and the precipitate is washed with water and dried.

This affords 125 g (92% of theory) of the product with a purity of 96%.

›Example 3

4-Methoxyphenylacetic acid (83.9 g), resorcinol (55 g) and hydrogen fluoride (300 g) are initially charged in an autoclave at −10° C., and the mixture is stirred at 20° C. for 12 h. Subsequently, the hydrogen fluoride is evaporated off at 40° C., and the precipitate is washed with water and dried.

This affords 120 g (89% of theory) of the product with a purity of 93%.

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Classifications

4 codes
IPC · International Patent Classification
Section C — Chemistry; metallurgy
  • C07D311/00
  • C07C49/00
USPC · US Patent Classification
568/331549/403

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Taylor Victor Oh
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