Organic compounds -- part of the class 532-570 series – Organic compounds – Amino nitrogen containing
Reexamination Certificate
1999-02-11
2003-01-07
Killos, Paul J. (Department: 1621)
Organic compounds -- part of the class 532-570 series
Organic compounds
Amino nitrogen containing
Reexamination Certificate
active
06504059
ABSTRACT:
The present invention relates to a process for the preparation of p-haloalkoxyanilines by catalytic hydroxylation of nitrobenzenes and subsequent etherification of the resulting OH group by reaction with halogenated olefins.
p-Haloalkoxyanilines are important intermediates in the preparation of insecticidal active ingredients (see for example EP-A 179 022, DE-A 36 27 161, EP-A 221 847, EP-A 235 089 and EP-A 343 110). These anilines are usually prepared by reacting halogenated olefins with p-nitrophenol derivatives and subsequently hydrogenating the nitro group (see for example EP-A 179 022 and EP-A 235 089), by reacting halogenated olefins with N-acylated p-aminophenols and subsequently cleaving off the N-acyl group (see for example EP-A 179 022 and EP-A 235 089), by reacting the salts of p-arninophenols with halogenated olefins (see for example EP-A 179 022 and U.S. Patent Specification No. 4,518,804) or by reacting p-fluoronitrobenzene derivatives with halogenoalcohols (see for example EP-A 235 089) and subsequently hydrogenating the nitro group catalytically.
A disadvantage of these processes is the number of process steps, particularly if the preparation of the corresponding starting materials is included. Thus, for example, p-nitrophenol derivatives have to be prepared in a preliminary step by nitration of a phenol, and, following reaction with halogenated olefins, a further step is required to reduce the nitro group. It is also a great disadvantage that during the nitration, positionally isomeric compounds are also formed which have to be removed. In the case of the reaction of N-acylated aminophenols, the insertion and cleaving off of the protective group mean a markedly increased process complexity. Preparation of the aminophenol salts by nitration of a phenol and subsequent hydrogenation and salt formation is also unfavorable in view of the number of process stages and the availability of the starting materials. This is also true of the reaction of p-fluoronitroaromatic compounds with halogenoalkanols.
The object is thus to find a process for preparing p-haloalkoxyanilines which avoids multistage and lengthy reaction sequences and uses readily available starting materials.
A process for preparing p-haloalkoxyanilines of the formula (I)
where
R
1
is hydrogen, halogen or C
1
-C
4
-halogenoalkyl and
R
2
to R
6
are, independently of one another, each hydrogen or halogen, at least one of the radicals R
1
to R
4
not being hydrogen,
has now been found, which comprises converting a nitrobenzene of the formula (II)
where
R
5
and R
6
are as defined for formula (I),
into a free aminophenol of the formula (III)
where
R
5
and R
6
are as defined for formula (I),
by catalytic reductive hydroxylation in the presence of an aqueous-acidic reaction medium, and reacting this aminophenol with a halogenated olefin of the formula (IV) or (V)
where
R
1
to R
4
are as defined for formula (I),
in the presence of water and a catalytic amount of base.
Halogen, also in halogenoalkyl, is, for example, fluorine, chlorine or bromine.
In preferred meanings, R
1
is C
1
-C
2
-halogenoalkyl, fluorine or chlorine, R
2
to R
4
are, independently of one another, hydrogen, fluorine or chlorine, and R
5
and R
6
are, independently of one another, hydrogen, fluorine, chlorine or bromine, at least one of the radicals R
5
and R
6
not being hydrogen.
In particularly preferred meanings, R
1
is perfluoro-C
1
-C
2
-alkyl such as trifluoromethyl or pentafluoroethyl, R
2
to R
4
are, independently of one another, fluorine or chlorine, and R
5
and R
6
are, independently of one another, hydrogen or chlorine, at least one of the radicals R
5
and R
6
being chlorine.
The catalytic reductive hydroxylation can, for example, be carried out with hydrogen under pressure at elevated temperature and in the presence of catalysts.
The aqueous acidic reaction medium can be a mixture of water and a strong acid. The strong acid may be inorganic or organic. Examples include sulfuric acid, hydrochloric acid, hydrobromic acid, phosphoric acid, methanesulfonic acid and toluenesulfonic acid. Preference is given to sulfuric acid and hydrochloric acid. The concentration of the acid in the aqueous acidic reaction mixture may, for example, be from 5 to 30% by weight, preferably from 10 to 20% by weight. The amount of acid can, for example, be from 0.5 to 10 equivalents of acid per equivalent of nitrobenzene of formula (II) used. This amount is preferably from 1 to 5 equivalents, in particular 1.2 to 3 equivalents.
For example, it is possible to use from 5 to 50% by weight, preferably from 10 to 25% by weight, of a nitrobenzene of the formula (II), based on the aqueous acidic reaction medium.
It is also possible, if desired, to work in the presence of a cosolvent. The cosolvents may be water-miscible organic solvents, for example water-miscible cyclic or open-chain ethers, such as tetrahydrofuran, 1,4-dioxane, glycol monoalkyl ethers or glycol dialkyl ethers, water-miscible esters or arnides, such as ethyl acetate, N,N-dimethylformamide, N,N-dimethylacetamide or N-methylpyrrolidone, lower aliphatic carboxylic acids, such as formic acid, acetic acid or propionic acid, water-miscible ketones, such as acetone or methyl ethyl ketone, or water-miscible alcohols, such as methanol, ethanol, propanol or ethylene glycol. Preference is given to methanol, ethanol, ethylene glycol, ethylene glycol monomethyl ether, ethylene glycol dimethyl ether and 1,4-dioxane. Cosolvents may optionally be used in from 0.05 to 3 times, preferably from 0.1 to 1 times, the quantity by weight, based on the nitrobenzene of the formula (II) used.
In addition to the cosolvent, it is also possible to use a water-insoluble organic solvent in which the nitrobenzene of the formula (II) used is at least partially soluble. Examples are optionally alkyl- and/or halogen-substituted aromatic hydrocarbons, such as benzene, toluene, xylenes, chlorobenzene, dichlorobenzenes, chlorotoluenes or dichlorotoluenes. Toluene and xylenes are preferred. Water-insoluble organic solvents may optionally be used in from 0.1 to 5 times, preferably from 0.25 to 3 times, the amount by weight, based on the nitrobenzene of the formula (II) used.
It is preferred to work in the presence of a cosolvent and a water-insoluble solvent. Suitable catalysts for the catalytic reductive hydroxylation are, for example, precious metals and precious metal compounds of the platinum group elements, in particular platinum and/or palladium and/or their compounds. The catalysts may be supported on a support material. Suitable support materials are, for example, silica gels, aluminum oxides, zeolites, molecular sieves or charcoals, whose coating with precious metals or precious metal compounds can, for example, be from 0.05 to 10% by weight, preferably from 0.1 to 5% by weight. It is possible to use, for example, from 0.001 to 0.3% by weight, preferably from 0.01 to 0.1% by weight, of the catalyst (calculated as metal), based on the nitrobenzene of the formula (II) used.
The catalytic reductive hydroxylation can be carried out, for example, at temperatures of from 50 to 160° C. and pressures of from 1 to 50 bar. Preferred conditions are 60 to 130° C. and 1.2 to 20 bar.
It is advantageous to thoroughly mix the reaction mixture during the hydrogen uptake, for example by using stirrers, lifter agitators or shaker autoclaves.
The reaction mixture which is present after the catalytic reductive hydroxylation is complete can, for example, be worked up by firstly removing the catalyst, for example by filtration, then separating off and removing the organic phase, adding a base to the aqueous phase and, for example, filtering the suspension which forms at a pH of approximately 5 to 8, washing the filtration residue with water and drying it. It is also possible to initially add sufficient base to the aqueous phase that the mixture becomes strongly alkaline, and then to remove undesired byproducts by extraction with an organic solvent and then to adjust the pH to a value in the range from approximately 5 to 8.
Mais Franz-Josef
Marhold Albrecht
Steffan Guido
Bayer Aktiengesellschaft
Killos Paul J.
Norris McLaughlin & Marcus P.A.
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