Claims
- 1. A process for preparing a 7-chloroquinoline-8-carboxylic acid of the formula (I) ##STR3## where R is methyl, by direct oxidation of the corresponding 8-methylquinoline compound in the presence of sulfuric acid, which comprises performing the oxidation with nitric acid or nitrogen dioxide in the presence of a vanadium(V) or vanadium (IV) compound, said vanadium compound being soluble in sulfuric acid or a mixture of sulfuric acid and nitric acid.
- 2. The process of claim 1, wherein the reaction is carried out in the presence of, or by passing in, air.
- 3. The process of claim 1, wherein the oxidation is carried out with recycling of the NO and NO.sub.2 containing off-gases.
- 4. The process of claim 3, wherein the off-gases are treated with oxygen or air.
- 5. The process of claim 1, wherein the vanadium compound is in the form of an oxide, a sulfate, a nitrate or an acetate.
- 6. The process of claim 1, wherein the vanadium compound is vanadium(V) oxide.
- 7. The process of claim 6, wherein said vanadium(V) oxide is in admixture with cobalt (II) acetate.
Priority Claims (1)
| Number |
Date |
Country |
Kind |
| 3706792 |
Mar 1987 |
DEX |
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Parent Case Info
This application is a continuation of application Ser. No. 158,910, filed on Feb. 22, 1988, now abandoned.
The known preparation of 7-chloro-3-methylquino-line-8-carboxylic acid proceeds via the corresponding bromomethyl compound as intermediate. This process, known from EP-A-104,389, has the disadvantage that an additional reaction step and thus more resources are required, and gives the desired target product only in a low yield.
The present invention provides a process for preparing a 7-chloroquinoline-8-carboxylic acid of the formula (I) ##STR2## where R is hydrogen, chlorine or methyl, by direct oxidation of the corresponding 8-methylquinoline compound in the presence of sulfuric acid.
A process of this type can be put into effect by directly oxidizing the corresponding 8-methylquinoline compound with nitric acid in the presence of sulfuric acid and a heavy metal compound, ie. in the presence of a catalyst. In place of nitric acid it is also possible to use the anhydride thereof, ie. nitrogen dioxide. In every case, the spent nitric acid or nitrogen oxides can be regenerated with molecular oxygen.
The process represents a substantial improvement in respect of resource requirements and yield and purity of the target product.
Suitable heavy metals for the purposes of the present invention are in particular those whose compounds occur in a plurality of valence states, such as cobalt and vanadium. Also suitable are elements such as: manganese, iron, cerium, molybdenum, copper, ruthenium and osmium. The heavy metal compounds can be used solo or mixed. Particular effectiveness is possessed by, and preference is therefore given to, vanadium or a mixture of vanadium and cobalt. The heavy metals are preferably used, ie. added, in the form of those compounds which are soluble in sulfuric acid or mixtures of sulfuric acid and nitric acid. Compounds within this meaning are in particular the oxides and naturally the sulfates, and also the nitrates and acetates. The heavy metal is required in a catalytic amount, ie. generally in an amount of less than 10, in particular less than 5% by weight, based on the reaction mixture in which it is to act. Even very small amounts, for example less than 1% by weight, are perfectly active.
Molecular oxygen is conveniently introduced into the system in the form of air, for example by a high-speed stream, and brings about an increase in selectivity and a higher rate of reaction.
The proposed preparation can be improved in respect of resource requirements and flexibility in a particular refinement of the invention: the direct oxidation with nitric acid or with nitrogen dioxide can be carried out by recycling the NO.sub.x -containing reaction off-gas. Advantageously, the off-gas is circulated and in the course of circulation is brought into contact, if desired, with molecular oxygen, ie. in practice with air, for regeneration.
The reaction is carried out at for example from 120.degree. to 180.degree. C., in particular at from 150.degree. to 170.degree. C. The 8-methylquinoline compound is present in solution in, for example, from 50 to 90% strength, preferably 70 to 85% strength, sulfuric acid, and moderately concentrated or concentrated nitric acid is used. In practice, for example, the methyl compound is introduced initially at from 150.degree. to 160.degree. C. in the catalyst-containing sulfuric acid, and about 3 to 6 equivalents of nitric acid, based on 1 mole of methyl compound, are then gradually added, or simply gaseous nitrogen dioxide is passed in. The saturation pressure can be atmospheric pressure or a slightly higher pressure. The reaction virtually goes to completion in the course of from 8 to 15 hours.
This is followed by dilution with water, adjustment to pH 0.5-3 (which precipitates all quinoline compounds including any byproducts), and extraction with methanol, isopropyl alcohol or the like to isolate the carboxylic acid as a residue which, if necessary, can be purified by recrystallization.
The reaction can be carried out batchwise, for example in a stirred kettle, or, in a conventional manner, continuously, using for example a stirred kettle with a downstream tubular reactor, a stirred kettle cascade or a tubular reactor; for the reaction with reactants which are supplied in gas form it is advantageous to use for example a bubble column or a gas jet reactor. Process arrangements usable here will be apparent to those trained in process engineering.
To obtain a particularly favorable result, the methyl compound is ideally as pure as possible; however, good results are also obtainable by using directly the reaction mixtures which, in sulfuric acid solution, contain a corresponding methylquinoline compound as obtained in a Skraup quinoline synthesis from an appropriately substituted toluidine and (meth)acrolein.
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| Number |
Name |
Date |
Kind |
| 3165548 |
Bartholome et al. |
Jan 1965 |
|
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Hagen et al. |
Dec 1986 |
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| 4715889 |
Hagen et al. |
Dec 1987 |
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Feb 1989 |
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| Number |
Date |
Country |
| 565899 |
Nov 1958 |
CAX |
| 0085182 |
Aug 1983 |
EPX |
| 126893 |
Dec 1984 |
EPX |
| 3202736 |
Aug 1983 |
DEX |
Non-Patent Literature Citations (2)
| Entry |
| "Advanced Organic Chemistry" (3rd Ed.) by Jerry March, p. 1072 (1985). |
| Advanced Inorganic Chemistry by Cotton and Wilkinson, p. 821 (3rd Ed.). |
Continuations (1)
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Number |
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| Parent |
158910 |
Feb 1988 |
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Patent Grant
5006659
