Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
  • C07C209/68—Preparation of compounds containing amino groups bound to a carbon skeleton from amines, by reactions not involving amino groups, e.g. reduction of unsaturated amines, aromatisation, or substitution of the carbon skeleton
  • C07C209/74—Preparation of compounds containing amino groups bound to a carbon skeleton from amines, by reactions not involving amino groups, e.g. reduction of unsaturated amines, aromatisation, or substitution of the carbon skeleton by halogenation, hydrohalogenation, dehalogenation, or dehydrohalogenation
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C211/00—Compounds containing amino groups bound to a carbon skeleton
  • C07C211/43—Compounds containing amino groups bound to a carbon skeleton having amino groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton
  • C07C211/44—Compounds containing amino groups bound to a carbon skeleton having amino groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton having amino groups bound to only one six-membered aromatic ring
  • C07C211/52—Compounds containing amino groups bound to a carbon skeleton having amino groups bound to carbon atoms of six-membered aromatic rings of the carbon skeleton having amino groups bound to only one six-membered aromatic ring the carbon skeleton being further substituted by halogen atoms or by nitro or nitroso groups
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C211/00—Compounds containing amino groups bound to a carbon skeleton
  • C07C211/62—Quaternary ammonium compounds
  • C07C211/64—Quaternary ammonium compounds having quaternised nitrogen atoms bound to carbon atoms of six-membered aromatic rings
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P20/00—Technologies relating to chemical industry
  • Y02P20/50—Improvements relating to the production of bulk chemicals
  • Y02P20/582—Recycling of unreacted starting or intermediate materials

Definitions

• the present invention is directed to a process for the preparation of chlorinated alkylanilines, in particular chlorinated 2,6-dialkylanilines.
• Meta-chlorinated 2,6-dialkylanilines are important starting materials for the preparation of chlorinated 4,4'-methylene-bis(2,6-dialkylanilines) which are used as chain extenders or cross linking agents in the polymer industry, for example in the preparation of polyurethanes and epoxy resins.
• US-A-3,962,336 discloses the preparation of 5-chloro-2-toluidine by reacting 2-toluidine hydrochloride with chlorine. Direct chlorination of other anilines, however, leads to the formation of product mixtures as described in GB-A-1 521 136.
• US-A-4,401 ,833 discloses the direct chlorination of the hydrochlorides of 2,6-dialkylanilines in an organic solvent system, wherein the hydrochlorides are sparingly soluble. Consequently, the bulk of the hydrochloride is present in crystalline form as a suspension. This process, however, results in 4-chloro-2,6-dialkylanilines only.
• the object of the present invention therefore, is to provide an effective and cost efficient process for the meta-selective chlorination of alkylanilines, in particular 2,6-dialkylanilines.
• R 1 , R 2 and R 3 independently are H or an alkyl group, with the proviso that at least one of R 1 and R 2 is an alkyl group, and X 1 and X 2 independently are H or CI, with the proviso that at least one of X 1 and X 2 is CI, or a sulfuric acid salt thereof, said process comprising:
• R 1 , R 2 and R 3 are as defined above, in the anilinium form in a mixture with sulfuric acid as solvent; and treating the mixture of step (a) with chlorine (CI 2 ) to obtain the alkylaniline of the formula (1) in the form of a sulfuric acid salt, optionally followed by treatment with a base to obtain the free alkylaniline.
• CI 2 chlorine
• the process of the invention allows meta-chlorination of alkylanilines of the general formula (2) with high selectivity and in excellent yields by using sulfuric acid as solvent.
• Sulfuric acid is essentially the sole solvent, while organic solvents are preferably absent.
• alkyl as used in the definition of R , R 2 and R 3 includes linear and branched alkyl groups.
• the alkyl group is a Ci_6 alkyl group, more preferably a Ci_4 alkyl group.
• Preferred alkyl groups include methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl and fe -butyl.
• More preferred alkyl groups are methyl, ethyl, n-propyl, isopropyl and sec-butyl. Most preferred alkyl groups represented by R 1 , R 2 and R 3 are methyl, ethyl and isopropyl.
• the residues R 1 and R 2 in the compounds of the formula (1) and (2) independently represent an alkyl group. More preferably, R 1 and R 2 are the same.
• R 3 in the compounds of the formulas (1) and (2) is H.
• the sulfuric acid (H 2 SO 4 ) used in the present process in admixture with the alkyl- aniline of the formula (2) preferably is a sulfuric acid having an acid concentration of at least 70% by weight, more preferably of at least 85% by weight, even more preferably of at least 90% by weight, and most preferably of at least 95% by weight. While meta- selectivity of the reaction is maintained even when sulfuric acid having an acid concentration of below 70% is used, yield is better at higher concentrations.
• the alkylaniline of the formula (2) in its anilinium form is provided by mixing the aniline with sulfuric acid.
• the alkylaniline will essentially be present in the form a sulfuric acid salt, i.e., the anilinium sulfate and/or the anilinium hydrogensulfate, which will react with the chlorine.
• the sulfuric acid is used in a molar excess with respect to the alkylaniline. This allows better mixing and probably dissolution of the anilinium salt in the sulfuric acid.
• the molar ratio of sulfuric acid to alkylaniline in the starting mixture preferably should be at least 1.8:1 , more preferably at least 2.5:1.
• the alkylaniline of the formula (2) can be provided in the form of an anilinium salt, preferably a sulfuric acid salt such as the anilinium hydrogensulfate or the anilinium sulfate, which is mixed with the sulfuric acid.
• Chlorination of the alkylanilines of the formula (2) is effected using chlorine gas which is introduced into or passed through the mixture with the sulfuric acid.
• the reaction is typically carried out at a temperature in a range of from 5 °C to 120 °C, preferably of from 10 °C to 100 °C. Lower or higher temperatures may work as well, but lower temperatures may result in a decrease in the reaction rate while higher temperatures will not increase yield.
• the product of the chlorination reaction essentially is the sulfuric acid salt of the chlorinated alkylaniline of the formula (1), i.e. the anilinium hydrogensulfate or the anilinium sulfate.
• the free chlorinated alkylaniline can be liberated from its salt by separating the sulfuric acid salts from the reaction mixture by crystallization followed by treatment with a base.
• the reaction mixture containing the sulfuric acid and the sulfuric acid salts will be treated directly with the base to neutralize the sulfuric acid and to liberate the chlorinated alkylaniline.
• Bases which may be used for treatment include organic bases such as triethylamine and inorganic bases such as alkali metal hydroxides and carbonates. Sodium or potassium hydroxide are preferred and are typically used in the form of aqueous solutions.
• the liberated chlorinated alkylaniline can be isolated according to known methods, for example by separating the organic layer or by extraction with a water immiscible solvent such as dichloromethane, ethyl acetate or toluene. The solvent may then be removed under reduced pressure.
• the chlorinated anilines may be purified by distillation.
• the process of the invention may be carried out in a closed or in an open system.
• the chlorination reaction is carried out in a closed system, which has the advantage that it does not exchange matter with its surroundings during the reaction.
• a closed system may be a sealed reaction vessel such as a sealed autoclave.
• Use of a closed system allows easy control of the stoichiometry of the reactants.
• the mixture of alkylaniline and sulfuric acid is charged into the reaction vessel, preferably an autoclave, and the reaction vessel is then sealed and the calculated amount of chlorine gas is added. Due to the use of a closed system, no reactants will leak so that a predetermined molar ratio of the reactants can be provided for controlling the process.
• the chlorination reaction of the invention can be carried out in an open system which allows the flow of matter out of the system boundaries.
• the open system used in the process of the invention may be an open reaction vessel such as a standard glass apparatus which is charged with the alkylaniline and the sulfuric acid to which chlorine gas is added.
• the chlorine gas is passed through the reaction mixture, for example using a dip pipe.
• the degree of chlorination may be controlled, for example, by adjusting the stoichiometry of the reactants, that is, the molar ratio of chlorine gas to alkylaniline of formula (2), the choice of the reaction system and the reaction temperature.
• a meta- substituted mono-chlorinated product is obtained in high yields if chlorine (C ) and alkylaniline are used in about stoichiometric amounts, i.e., if the molar ratio of chlorine molecules to alkylaniline is in the range of from 0.90:1 to 1.10:1 , more preferably in the range of from 0.95:1 to 1.05:1.
• the reaction is preferably carried out within the temperature range given above.
• the reaction time usually is in a range of from 5 min to 10 h.
• the molar ratio of chlorine to alkylaniline is increased, the 3,5-dichlorinated alkylaniline tends to become the main product of the chlorination reaction.
• this can be achieved by increasing the amount of added chlorine.
• the molar ratio of chlorine to alkylaniline is thus increased to at least 2:1 , more preferably to at least 3.5:1. Molar ratios exceeding 4.5:1 may not increase yield and/or may result in undesired side products such as higher chlorinated products.
• the reaction equilibrium may also be shifted to the dichlorinated reaction product by increasing the reaction temperature, for example within a range of from 60 °C to 90 °C. If the chlorination reaction is carried out in an open reaction vessel, the meta- substituted mono-chlorinated product is obtained in high yields if chlorine is passed through the reaction mixture. The dichlorinated compounds will be obtained only upon longer reaction times and by passing large amounts of chlorine through the reaction mixture.
• alkyl substituents of the anilines of the formula (2) are different, chlorination may result in different isomers.
• R 1 and R 2 are different alkyl groups and R 3 is H, two mono-chlorinated isomers will be obtained from which the predominant one is the isomer where the meta-position is sterically less hindered by the adjacent alkyl substituent.
• 2-isopropyl-6-methylaniline is chlorinated according to the process of the invention, a product mixture consisting of 3-chloro-6-isopropyl-2-methylaniline and 3-chloro-2-isopropyl-6-methylaniline is obtained in a ratio of about 4:1.
• the mixture to be treated with the chlorine essentially consists of the alkylaniline to be chlorinated and of sulfuric acid.
• the reaction mixture preferably is essentially free of organic solvents, as the presence of organic solvents may affect selectivity and/or yield of the chlorination reaction.
• the process of the present invention allows a selective meta-chlorination of alkylanilines of the formula (2) in high yields and with few side products. Unreacted starting material can be recycled.
• the present process thus, can be carried out in a simple manner and at low costs.
• Example 1 was repeated with a reaction time of 1 h.
• the obtained product contained (according to GC) 91.9% of 3-chloro-2,6-diethylaniline and 3.3% of starting material.
• Example 3
• Example 1 was repeated with a reaction time of 0.5 h.
• the obtained crude product contained (according to GC) 90.9% of 3-chloro-2,6-diethylaniline and 7.9% of starting material.
• Example 1 was repeated with a reaction time of 6 h and a molar ratio of C to 2,6-diethylaniline of 1.05:1.
• the obtained crude product contained (according to GC) 94.9% of 3-chloro-2,6-diethylaniline and 1.3% of 3,5-dichloro-2,6-diethylaniline. No starting material could be detected.
• Example 1 was repeated with a molar ratio of sulfuric acid to 2,6-diethylaniline of
• Example 9 was repeated with a molar ratio of Cl 2 to 2,6-diethylaniline of 2.1 :1 and a reaction temperature of 80 °C.
• the obtained crude product contained (according to GC) 12.7% of 3-chloro-2,6-diethylaniline and 55.4% of 3,5-dichloro-2,6-diethyl- aniline.
• a round bottom flask equipped with a reflux condenser and a stirring bar was charged with 5.0 g (33.5 mmol) of 2,6-diethylaniline and 50.8 g (497 mmol) of sulfuric acid (96 % by weight) and heated to 80 °C. Within 2 h 23.5 g (331 mmol) of chlorine gas were passed through the reaction solution using a dip pipe. The resulting mixture was stirred for another 3 h at 80 °C and then poured into 50 g of ice. The suspension was neutralized with 130 g of 30% aqueous sodium hydroxide and 90 g of ethyl acetate were added.
• Example 12 was repeated with a molar ratio of Cl 2 to 2,6-diethylaniline of 5:1.
• the obtained crude product contained (according to GC) 60.4% of 3-chloro-2,6-diethyl- aniline and 37.8 % of starting material.
• Example 12 was repeated with a molar ratio of sulfuric acid to 2,6-diethylaniline of 2:1 and a molar ratio of Cl 2 to 2,6-diethylaniline of 5:1.
• the obtained crude product contained (according to GC) 16.3% of 3-chloro-2,6-diethylaniline and 71.3% of starting material.
• Example 7 From Example 7 it will be seen that selective monochlorination rather than dichlorination takes place even if a mixture of dialkylaniline and 3-chloro-2,6-dialkylaniline is used as the starting material.
• Comparative Example 8 demonstrates that the use of a sulfuric acid derivative such as chlorosulfonic acid instead of sulfuric acid results in a mixture of mono- and di-chlorin- ated products in low yields.
• Examples 9 to 11 show that the di-meta-chlorinated product becomes the main product if chlorination is carried out with chlorine in excess or at higher temperatures. No para- chlorinated product could be detected demonstrating the high selectivity of the present process.
• a selectivity of more than 90% for chlorination in meta-position could also be achieved when an open reaction system was used (Examples 12 to 14). Conversion of the starting material increases with increasing amounts of chlorine gas passed through the starting mixture.
• Example 1 was repeated using 10.0 g (67.0 mmol) of 2-isopropyl-6-methylaniline instead of 2,6-diethylaniline as the substrate to evaluate the selectivity of the chlorination process with an asymmetrically substituted 2,6-dialkylaniline.
• the crude product obtained contained 3-chloro-6-isopropyl-2-methylaniline and 3-chloro-2-isopropyl-6- methylaniline as a 4:1 mixture (according to GC), thus demonstrating that also in case of asymmetrically substituted dialkylanilines only the meta-positions of the aromatic amine are chlorinated, with chlorination apparently being predominant at the position sterically less hindered by the adjacent alkyl substituent.
• Example 16 (Comparative Example)

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• 2011
  • 2011-08-16 EP EP11746178.0A patent/EP2606028A1/en not_active Withdrawn
  • 2011-08-16 BR BR112013003937A patent/BR112013003937A2/pt not_active IP Right Cessation
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