WO1997048665A1 - Procede d'acylation d'un compose aromatique - Google Patents
Procede d'acylation d'un compose aromatique Download PDFInfo
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- WO1997048665A1 WO1997048665A1 PCT/FR1997/001066 FR9701066W WO9748665A1 WO 1997048665 A1 WO1997048665 A1 WO 1997048665A1 FR 9701066 W FR9701066 W FR 9701066W WO 9748665 A1 WO9748665 A1 WO 9748665A1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/45—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by condensation
- C07C45/46—Friedel-Crafts reactions
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B41/00—Formation or introduction of functional groups containing oxygen
- C07B41/06—Formation or introduction of functional groups containing oxygen of carbonyl groups
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- 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 subject of the present invention is a process for the acylation of an aromatic compound, and in particular of an aromatic ether or thioether.
- the invention resides in a process for the acylation of an aromatic ether or thioether with anhydrides of carboxylic acids, preferably acetic anhydride.
- the invention applies more particularly to the preparation of alkoxy- or alkylthioaromatic alkyl ketones.
- acylation reagent a carboxylic acid, or one of its derivatives such as acid halide, ester or anhydride.
- the reaction is generally carried out in the presence of a catalyst of the Lewis acid type (for example AICI3) or of the Br ⁇ nsted acid type (H2SO4, HF, etc.).
- a catalyst of the Lewis acid type for example AICI3
- the Br ⁇ nsted acid type H2SO4, HF, etc.
- the object of the present invention is to provide a method enabling the abovementioned drawbacks to be overcome.
- aromatic compound means the classic concept of aromaticrté as defined in the literature, in particular by Jerry MARCH, Advanced Organic Chemistry, 4 ⁇ ,,, ⁇ edition, John Wiley and Sons, 1992, pp. 40 and following.
- aromatic ether or thioether denotes an aromatic compound in which a hydrogen atom directly linked to the aromatic nucleus is replaced respectively by an ether or thioether group.
- the subject of the present invention is a process for the acylation of an aromatic compound corresponding to the general formula (I):
- A symbolizes the remainder of a cycle forming all or part of a carbocyclic or heterocyclic, aromatic, monocyclic or polycyclic system, said cyclic residue being able to carry a radical R representing a hydrogen atom or one or more substituents, identical or different,
- A is the residue of a cyclic compound, preferably having at least 4 atoms in the ring, preferably 5 or 6, optionally substituted , and representing at least one of the following cycles:. an aromatic, monocyclic or polycyclic carbocycle,
- an aromatic, monocyclic or polycyclic heterocycle comprising at least one of the heteroatoms O, N and S,
- polycyclic carbocyclic compound is meant:. a compound consisting of at least 2 aromatic carbocycles and forming between them ortho- or ortho- and pericondensed systems,. a compound consisting of at least 2 carbocycles of which only one of them is aromatic and forming between them ortho- or ortho- and pericondensed systems. 2 ° - of an aromatic, monocyclic or polycyclic heterocyclic compound.
- polycyclic heterocyclic compound we define:. a compound consisting of at least 2 heterocycles containing at least one heteroatom in each cycle of which at least one of the two cycles is aromatic and forming between them ortho- or ortho- and pericondensed systems,
- a compound consisting of at least one hydrocarbon cycle and at least one heterocycle of which at least one of the cycles is aromatic and forming between them ortho- or ortho- and pericondensed systems.
- alkylene or alkylidene radical having from 1 to 4 carbon atoms, preferably a methylene or isopropylidene radical
- R Q represents a hydrogen atom or an alkyl radical having from 1 to 4 carbon atoms, a cyclohexyl or phenyl radical.
- a monocyclic, carbocyclic, aromatic compound such as, for example, benzene, toluene, isobutylbenzene, anisole, thioanisole, phenetole or veratrole, guaiacol, guetol,
- naphthalene 2-methoxynaphthalene
- a polycyclic, condensed, carbocyclic, partially aromatic compound such as, for example, tetrahydronaphthalene, 1,2-methylene dioxybenzene,
- a polycyclic, non-condensed, carbocyclic, partially aromatic compound such as, for example, cyclohexylbenzene
- a monocyclic, heterocyclic, aromatic compound such as, for example, pyridine, furan, thiophene,
- a polycyclic, condensed, aromatic, partially heterocyclic compound such as, for example, quinoline, indole or benzofuran,
- a polycyclic, non-condensed, aromatic, partially heterocyclic compound such as, for example, phenylpyridines, naphthylpyridines,
- a polycyclic, condensed, partially aromatic, partially heterocyclic compound such as, for example, tetrahydroquinoline
- a polycylic compound non-condensed, partially aromatic, partially heterocyclic, such as, for example, cyclohexylpyridine.
- A represents an aromatic ring, preferably a benzene or naphthalene ring.
- the aromatic compound of formula (I) can carry one or more substituents.
- the number of substituents present on the cycle depends on the carbon condensation of the cycle and on the presence or not of unsaturations on the cycle.
- the maximum number of substituents likely to be carried by a cycle is easily determined by a person skilled in the art.
- the radical or radicals R which are identical or different, preferably represent one of the following groups:. a hydrogen atom,. an alkyl radical, linear or branched, having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl,. a linear or branched alkenyl radical having from 2 to 6 carbon atoms, preferably from 2 to 4 carbon atoms, such as vinyl, allyl,.
- a linear or branched alkoxy radical having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms such as the methoxy, ethoxy, propoxy, isopropoxy, butoxy radicals, an alkenyloxy radical, preferably an allyloxy radical or a phenoxy radical,. a cyclohexyl, phenyl or benzyl radical,. an acyl group having from 2 to 6 carbon atoms,
- Rj represents a valential bond or a divalent, linear or branched, saturated or unsaturated hydrocarbon radical, having from 1 to
- R2 radicals represent a hydrogen atom or a linear or branched alkyl radical having from 1 to 6 carbon atoms
- X symbolizes a halogen atom, preferably a chlorine, bromine or fluorine atom.
- radicals R and the 2 successive atoms of the aromatic ring can be linked together by an alkylene, alkenylene or alkenylidene radical having from 2 to 4 carbon atoms to form a saturated, unsaturated or aromatic heterocycle having 5 to 7 carbon atoms.
- One or more carbon atoms can be replaced by another heteroatom, preferably oxygen or sulfur.
- the radicals R can represent a methylenedioxy or ethylenedioxy radical or a methylenedithio or ethylenedithio radical.
- the present invention applies very particularly to aromatic compounds corresponding to formula (I) in which the radical or radicals R represent an electron-donor group.
- the term “electro-donor group” is understood to mean a group as defined by H.C. BROWN in the work of Jerry MARCH - Advanced Organic Chemistry, chapter 9, pages 243 and 244 (1985).
- aromatic compounds preferably used correspond to formula (la):
- A symbolizes the remainder of a cycle forming all or part of a carbocyclic or heterocyclic, aromatic, monocyclic or polycyclic system: said cyclic residue being able to carry a radical R representing a hydrogen atom or one or more electron-donating substituents, identical or different,
- - n represents the number of substituents on the cycle.
- an alkyl radical linear or branched, having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl,
- a linear or branched alkenyl radical having from 2 to 6 carbon atoms, preferably from 2 to 4 carbon atoms, such as vinyl, allyl,
- a cyclohexyl, phenyl or benzyl radical a linear or branched alkoxy radical having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms such as methoxy radicals, ethoxy, propoxy, isopropoxy, butoxy, an alkenyloxy radical, preferably an allyloxy radical or a phenoxy radical,. a radical of formula:
- Rj represents a valence bond or a divalent hydrocarbon radical, linear or branched, saturated or unsaturated, having from 1 to 6 carbon atoms such as, for example , methylene, ethylene, propylene, isopropylene, isopropylidene; the radicals R2, which are identical or different, represent a hydrogen atom or a linear or branched alkyl radical having from 1 to 6 carbon atoms,
- two radicals R can be linked and form alkylenedioxy or alkylenedithio radicals, preferably a methylenedioxy, ethylenedioxy, methylenedithio or ethylenedithio radical.
- n is a number less than or equal to 4, preferably equal to 1 or 2.
- the process of the invention applies very particularly to effect the acylation of aromatic ethers and thioethers.
- A symbolizes the remainder of a cycle forming all or part of an aromatic, monocyclic or polycyclic carbocyclic system, system comprising at least one group YR ': said cyclic residue being able to carry one or more substituents,
- - R represents one or more substituents, identical or different
- R - R ' represents a hydrocarbon radical having from 1 to 24 carbon atoms, which can be a saturated or unsaturated, linear or branched acyclic aliphatic radical; a saturated, unsaturated or aromatic, monocyclic or polycyclic cycloaliphatic radical; a saturated or unsaturated, linear or branched aliphatic radical, carrying a cyclic substituent,
- R - R 'and R can form a ring optionally comprising another heteroatom, - n is a number less than or equal to 4.
- R ' herein, we denote, in a simplified manner, by "aikoxy or thioether groups", respectively groups of the R'-O- or R'-S- type in which R 'has the meaning given above.
- R 'therefore represents both an acyclic or cycloaliphatic, saturated, unsaturated or aromatic aliphatic radical as well as a saturated or unsaturated aliphatic radical carrying a cyclic substituent.
- R ' represents an acyclic aliphatic radical, saturated or unsaturated, linear or branched. More preferably, R' represents a linear alkyl radical or branched having from 1 to 12 carbon atoms, preferably from 1 to 6 carbon atoms: the hydrocarbon chain can possibly be interrupted by a heteroatom (for example, oxygen), by a functional group (for example -CO- ) and / or carrying substituents (for example, one or more halogen atoms).
- acyclic, saturated or unsaturated, linear or branched aliphatic radical may optionally carry a cyclic substituent.
- ring is preferably understood to mean a saturated, unsaturated or aromatic carbocyclic ring, preferably cycloaliphatic or aromatic, in particular cycloaliphatic ring comprising 6 carbon atoms in the ring or benzene.
- the acyclic aliphatic radical can be linked to the ring by a valential bond, a heteroatom or a functional group and examples are given above.
- the ring can be optionally substituted and, by way of examples of cyclic substituents, it is possible, among other things, to consider substituents such as R, the meaning of which is specified for the formula (! ').
- R 'can also represent a saturated carbocyclic radical or comprising 1 or 2 unsaturations in the ring, generally having from 3 to 8 carbon atoms, preferably 6 carbon atoms in the ring; said cycle possibly being substituted by substituents such as R.
- R 'can also represent an aromatic carbocyclic radical, preferably a monocyclic radical generally having at least 4 carbon atoms, preferably 6 carbon atoms in the ring; said ring possibly being substituted by substituents such as R.
- R aromatic carbocyclic radical
- D aromatic ethers or thioethers
- A may represent the remainder of an aromatic, monocyclic carbocyclic compound having at least 4 carbon atoms and preferably 6 carbon atoms or the remainder of a polycyclic carbocyclic compound which may be consisting of at least 2 aromatic carbocycles and forming between them ortho- or ortho- and pericondensed systems or by at least 2 carbocycles of which at least one is aromatic and forming between them ortho- or ortho- and pericondensed. Mention may more particularly be made of a naphthalene residue.
- the remainder A can carry one or more substituents on the aromatic ring.
- the remainder A can, inter alia, carry several aikoxy groups, it is possible according to the process of the invention to acylate polyalkoxylated compounds.
- R more preferably represents one of the following atoms or groups: an alkyl radical, linear or branched, having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl,
- a linear or branched aikoxy radical having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms such as the methoxy, ethoxy, propoxy, isopropoxy, butoxy, isobutoxy, sec-butoxy, tert-butoxy radicals,
- a halogen atom preferably a fluorine, chlorine or bromine atom, a trifluoromethyl radical.
- - n is a number less than or equal to 4, preferably equal to 0 or 1,
- - Y represents an oxygen or sulfur atom
- the radical R ' represents an alkyl radical, linear or branched, having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms, such as methyl, ethyl , propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl or a phenyl radical,
- radical or radicals R which are identical or different, represent one of the following atoms or groups:
- an alkyl radical linear or branched, having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl,.
- a linear or branched alkenyl radical having from 2 to 6 carbon atoms, preferably from 2 to 4 carbon atoms, such as vinyl, allyl,
- a linear or branched aikoxy radical having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms such as the methoxy, ethoxy, propoxy, isopropoxy, butoxy radicals, an alkenyloxy radical, preferably an allyloxy radical or a phenoxy radical,. a cyclohexyl, phenyl or benzyl radical,
- Rj represents a valential bond or a divalent hydrocarbon radical, linear or branched, saturated or unsaturated, having from 1 to 6 carbon atoms such as, for example, methylene, ethylene, propylene, isopropylene, isopropylidene ;
- X symbolizes a halogen atom, preferably a chlorine, bromine or fluorine atom.
- the radicals R 'and R placed on two vicinal carbon atoms can form together and with the carbon atoms which carry them, a ring having 5 to 7 atoms, possibly including another heteroatom.
- the radicals R 'and R and the 2 successive atoms of the benzene ring can be linked together and form an alkylene, alkenylene or alkenylidene radical having from 2 to 4 carbon atoms to form a saturated heterocycle , unsaturated or aromatic having 5 to 7 atoms.
- One or more carbon atoms can be replaced by another heteroatom, preferably oxygen or sulfur.
- the radicals OR 'and R may represent a methylenedioxy or ethylenedioxy radical and the radicals SR ′ and R may represent a methylenedithio or ethylenedithio radical.
- R ′ preferably represents an alkyl radical, linear or branched, having from 1 to 6 carbon atoms, preferably a methyl or ethyl radical or a phenyl radical.
- the benzene nucleus carries one or more identical or different substituents R.
- R preferably represents an alkyl radical, linear or branched, having from 1 to 6 carbon atoms, preferably a methyl or ethyl radical; an aikoxy radical, linear or branched, having from 1 to 4 carbon atoms, preferably a methoxy or ethoxy radical.
- - n is equal to 0 or 1
- R ′ represents an alkyl radical, linear or branched, having from 1 to 6 carbon atoms or a phenyl radical, preferably a methyl or ethyl radical,
- R represents an alkyl radical, linear or branched, having from 1 to 6 carbon atoms, preferably a methyl or ethyl radical; an aikoxy radical, linear or branched, having from 1 to 4 carbon atoms, preferably a methoxy or ethoxy radical.
- radicals YR 'and R form a methylenedioxy, ethylenedioxy, methylenedithio or ethylenedithio radical.
- phenolic compounds such as phenol, o-cresol, guaiacol, guetol, a -naphthol, ⁇ -naphthol,
- - monoethers such as anisole, ethoxybenzene (phenoxy), propoxybenzene, isopropoxybenzene, butoxybenzene, isobutoxybenzene, 1-methoxynaphthalene, 2-methoxynaphthalene, 2-ethoxynaphthalene; substituted monoethers such as 2-chloroanisole, 3-chloroanisole, 2-bromoanisole, 3-bromoanisole, 2-methylanisole, 3-methylanisole, 2-ethylanisole, 3-ethylanisole, 2-isopropylanisole, 3-isopropylanisole, 2-propylanisole, 3-propylanisole, 2-allylanisole, 2-butylanisole, 3-butylanisole, 2-benzylanisole, 2-cyclohexylanisole, 1-bromo-2- ethoxybenzene, 1-bromo-3-ethoxybenzene, 1-chloro-2-ethoxybenzene, 1 - chloro
- - thioethers such as thioanisole, t'o-thiocresol, m-thiocresol, p-thiocresol, 2-thioethylnaphthalene, S-phenylthioacetate, 3- (methylmercapto) aniline, phenylthiopropionate.
- the compounds to which the process according to the invention applies more particularly advantageously are benzene, toluene, isobutylbenzene, anisole, phenetole, veratrole, 1, 2-methylenedioxybenzene, 2-methoxynaphthalene and thioanisole.
- acylation reagent use is made of carboxylic acids and their derivatives, halides or anhydrides, preferably anhydrides.
- the acylation reagent more particularly corresponds to formula (II):
- - X ' represents:. a halogen atom, preferably a chlorine or bromine atom,
- R 3 represents a linear or branched alkyl radical having from 1 to 12 carbon atoms, preferably from 1 to 6 carbon atoms: the hydrocarbon chain can possibly be interrupted by a heteroatom (for example, oxygen), by a functional group (for example -CO-) and / or carrying a substituent (for example, a halogen or a group CF 3 ).
- R 3 preferably represents an alkyl radical having from 1 to 4 carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl.
- R 3 also represents an alkenyl radical having from 2 to 10 carbon atoms, such as in particular, methyl, propen-yl, buten-yl, penten-yl, hexen-yl, octen-yl, decen-yl.
- the radical R3 also preferably represents a phenyl radical which may be optionally substituted. Any substituent can be present on the cycle as long as it does not interfere with the desired product.
- an alkyl radical linear or branched, having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl,
- a linear or branched aikoxy radical having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms such as the methoxy, ethoxy, propoxy, isopropoxy, butoxy, isobutoxy, sec-butoxy, tert-butoxy, radicals.
- a hydroxyl group having from 1 to 6 carbon atoms, preferably from 1 to 4 carbon atoms such as the methoxy, ethoxy, propoxy, isopropoxy, butoxy, isobutoxy, sec-butoxy, tert-butoxy, radicals.
- a halogen atom preferably a fluorine, chlorine or bromine atom.
- the preferred acylating agents are acid anhydrides. They correspond more particularly to the formula (II) wherein R 3 and R 4 are identical and represent an alkyl radical having 1 to 4 carbon atoms or a phenyl radical.
- the acylating agent when it is an acid halide, it preferably corresponds to formula (II) in which X 'represents a chlorine atom and R3 represents a methyl or ethyl or phenyl radical.
- Acetic, propanoic, benzoic, monochloroacetyl, dichloroacetyl anhydride, benzoyl chloride, are the preferred acylating agents.
- the acylation reaction is carried out in the presence of a zeolitic catalyst.
- zeolite is meant a crystallized tectosilicate of natural or synthetic origin, the crystals of which result from the three-dimensional assembly of tetrahedral units of Si ⁇ 4 and TO4: T representing a trivalent element such as aluminum, gallium, boron, iron, preferably aluminum.
- aluminosilicate type zeolites are the most common. Zeolites present within the crystal lattice, a system of cavities linked together by channels of a well-defined diameter called pores.
- Zeolites can have a network of one-dimensional, two-dimensional or three-dimensional channels.
- use may be made of a natural or synthetic zeolite.
- natural zeolites which may be used, there may be mentioned, for example: chabazite, clinoptilolite, erionite, phillipsite, offerite.
- Synthetic zeolites are entirely suitable for implementing the invention.
- Examples of synthetic zeolites with a one-dimensional network include, among others, the zeolite ZSM-4, the zeolite L, your zeolite ZSM-12, the zeolite ZSM-22, the zeolite ZSM-23, the zeolite ZSM-48.
- zeolites with a two-dimensional network By way of examples of zeolites with a two-dimensional network preferably used, mention may be made of the ⁇ zeolite, mordenite, ferrierite.
- the zeolites with three-dimensional lattice one can name more particularly, the zeolite Y, the zeolite X, the zeolite ZSM-5, the zeolite ZSM-11, the offer.
- - ⁇ zeolites with an Si / Ai molar ratio greater than 8, preferably between 10 and 100, and even more preferably between 12 and 50,
- - Y zeolites in particular the zeolites obtained after desalumination treatment (for example hydrotreatment, washing with hydrochloric acid or treatment with SiCl 4) and mention may more particularly be made of US-Y zeolites with a Si / molar ratio Ai greater than 3, preferably between 6 and 60;
- the mesoporous zeolite of the MCM type more particularly MCM-22 and MCM-41 with an Si / Al molar ratio of between 10 and 100, preferably between 15 and 40.
- MCM-22 and MCM-41 with an Si / Al molar ratio of between 10 and 100, preferably between 15 and 40.
- Si / Al molar ratio of between 10 and 100, preferably between 15 and 40.
- use is preferably made in the process of the invention to ⁇ and Y zeolites.
- zeolites used in the process of the invention are known products described in the literature [cf. Atlas of zeolites structure types by WM Meier and DH Oison published by the Structure Commission of the International Zeolite Association (1978)].
- the zeolite constitutes the catalytic phase. It can be used alone or mixed with a mineral matrix.
- the term “catalyst” will denote the catalyst produced entirely from zeolite or from a mixture with a matrix prepared according to techniques known to those skilled in the art.
- the matrix can be chosen from metal oxides, such as aluminum, silicon and / or zirconium oxides, or also from clays and more particularly, kaolin, talc or montmorillonite.
- the active phase content represents from 5 to 100% of the weight of the catalyst.
- the catalysts can be in different forms in the process of the invention: powder, shaped products such as granules (for example example, extruded or balls), pellets, which are obtained by extrusion, molding, compacting or any other type of known process.
- powder shaped products such as granules (for example example, extruded or balls), pellets, which are obtained by extrusion, molding, compacting or any other type of known process.
- granules for example, extruded or balls
- pellets which are obtained by extrusion, molding, compacting or any other type of known process.
- it is the forms of granules or beads which have the most advantages both in terms of efficiency and in terms of ease of use.
- the acylation reaction is carried out according to a process for recirculating the reaction mixture on a fixed bed of catalyst.
- the first step is to mix in any way, the aromatic compound and the acylating agent.
- the aromatic compound and the acylating agent can be mixed in a mixing zone, then the mixture obtained is sent to the catalytic bed.
- one of the reagents can be introduced and sent to the catalytic bed, then the other reagent can be added all at once or gradually when the desired reaction temperature is reached .
- the aromatic compound is introduced and then the acylating agent is gradually added.
- the final ratio between the number of moles of aromatic compound and the number of moles of acylating agent can vary widely.
- the ratio can range from 0.1 to 20, and is preferably between 0.5 and 10.
- a preferred embodiment of the invention consists, in order to increase the yield by maintaining the activity of the catalyst, to use an excess of aromatic compound.
- an aromatic compound / acylating agent molar ratio is chosen equal to at least 1, preferably between 1 and 20 and even more preferably between 1 and 10.
- One of the reagents is generally used as reaction solvent but l
- the invention does not exclude the use of an organic solvent, the nature of which is determined by a person skilled in the art.
- the temperature of the mixture is brought to the temperature at which the reaction is carried out.
- the temperature at which the acylation reaction is carried out depends on the reactivity of the starting substrate and that of the acylating agent.
- the reactants are passed through a catalytic bed comprising at least one zeolite.
- the amount of catalyst that is used in the process of the invention can vary within wide limits.
- the catalyst can represent, by weight relative to the ether or the aromatic thioether committed, from 0.01 to 50%, preferably from 1.0 to 20%.
- reaction is carried out at atmospheric pressure but lower or higher pressures may also be suitable.
- pressures may also be suitable.
- the reaction mixture passes through the catalytic bed, preferably from bottom to top and at its outlet is returned to the reagent mixing zone in order to be recycled a number of times sufficient to obtain the conversion rate of the desired substrate, preferably, greater than 20%, and even more preferably between 50 and 100%.
- the substrate conversion rate is defined as the ratio between the number of moles of substrate transformed over the number of moles of substrate introduced.
- the linear speed of the liquid flow over the catalytic converter advantageously varies between 0.1 and 10 cm / s, preferably between 0.1 and 5 cm / s.
- the residence time of the material flow on the catalytic bed varies, for example, between 15 min and 15 h, and preferably between 30 mm and 10 h.
- a liquid phase comprising the aromatic acyl compound which can be recovered in a conventional manner, by distillation or by re-installation in an appropriate solvent, after preliminary elimination of the excess reactants.
- FIG. 1 For a better understanding of the invention, there is shown in the appended FIG. 1, one of the preferred embodiments of the invention.
- the aromatic compound preferably an aromatic ether or thioether
- the acylating agent is mixed. It is a stirred or non-stirred reactor, fitted with valves for the arrival of reagents and for emptying and equipped with a heating device or provided with a double jacket allowing the heating of the mixture by circulation of a liquid to adequate temperature. Agitation, which is not compulsory, can be carried out using an Impeller® agitator (2).
- the aromatic compound (3) and the acylating agent (4) are introduced into the reactor (1).
- the reaction mixture is sent via any suitable means, in particular a centrifugal pump (5), at (6) at the bottom of a tubular reactor (7) comprising the solid zeolitic catalyst placed in a fixed bed (8).
- the reaction mixture is returned via a conduit (10) to the reactor (1) and thus circulates in a closed loop.
- reaction mixture is recovered by draining the mixer (1) via a valve (11) not symbolized in the diagram.
- the process of the invention is particularly well suited to the preparation of 4-methoxyacetophenone commonly known as acetoanisole, by acetylation of the anisole.
- An advantage of the process of the invention is that the acylation reaction is carried out without O-dealkylation of the starting aromatic ether.
- the zeolitic catalyst is charged to form the catalytic bed which rests on a thickness (- 20 mm) of glass beads as well as the top of the bed which is covered with approximately 20 mm of glass beads 5 mm in diameter.
- the anisole is charged at room temperature in a 3-liter Sovirel® double jacket reactor (1); it is stirred (between 40 revolutions / min) and was circulated in a loop on the fixed bed for 15 min; the flow rate is maintained at 60 l / h throughout the duration of the reaction. There is a slight exotherm.
- the reaction medium is then heated using a thermostated bath, so as to have a constant temperature of 90 ° C., at the top of the catalytic bed.
- the acetic anhydride is poured in 4 h, maintaining the circulation of the medium. At the end of the casting, the reaction is maintained for 3 h at 90 ° C (ie 7 h in total).
- the temperature is allowed to drop to around 60 ° C., and the installation is drained. Nitrogen is blown through the fixed bed for 20 minutes
- a catalyst comprising 40% of binder (alumina) and 60% of a ⁇ zeolite sold by the company PQ.
- the zeolite used is a zeolite with a "S ⁇ / AI" ratio of 12.5.
- the number of moles of anisole is 20.9 mol and that of acetic anhydride is 10.45 mol • the molar ratio of anisole / acetic anhydride is 2/1.
- the reaction temperature is 90 ° C, as mentioned above.
- a yield (RR) of 4-methoxyacetophenone of 75% is determined by gas chromatography after 7 h.
- This operation is repeated on the same catalytic bed as before, 4 times.
- the yield (RR) is respectively 68,%, 65%, 62% and 59%
- the acetylation of the veratrole is carried out.
- a catalyst comprising 20% of binder (alumina) and 80% of a Y zeolite CBV780 sold by the company PQ. It is used at a rate of 21% compared to acetic anhydride, ie 225 g.
- the veratrole / anhydrous acetic molar ratio is 2/1.
- the reaction temperature is 90 ° C, as mentioned above.
- toluene acetylation is carried out, as in Example 1: the difference is that the reactor is larger, ie 20 I.
- a catalyst comprising 40% of binder (alumina) and 60% of a ⁇ zeolite sold by the company PQ.
- the zeolite used is a zeolite with an "Si / Ai" ratio of 12.5.
- the number of moles of toluene is 110 mol and that of acetic anhydride is 11.00 mol: the toluene / acetic anhydride molar ratio is 10.
- the reaction temperature is 150 ° C, as mentioned above.
- a yield (RR) of 4-methylacetophenone of 63% is determined by gas chromatography after 10 h.
- a catalyst comprising 40% of binder (alumina) and 60% of a ⁇ zeolite sold by the company PQ.
- the zeolite used is a zeolite with an "Si / Ai" ratio of 12.5.
- the number of moles of isobutylbenzene is 143 mol and that of acetic anhydride is 11 mol: the isobutylbenzene / acetic anhydride molar ratio is 13.
- the reaction temperature is 150 ° C., as mentioned previously.
- a yield (RR) of 4-isobutylacetophenone of 75% is determined by gas chromatography after 7 h.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/202,666 US6194616B1 (en) | 1996-06-20 | 1997-06-13 | Acylation method for an aromatic compound |
BR9709734A BR9709734A (pt) | 1996-06-20 | 1997-06-13 | Processos para acilação de um comosto aromático |
AU33479/97A AU3347997A (en) | 1996-06-20 | 1997-06-13 | Acylation method for an aromatic compound |
JP10502423A JP2000512308A (ja) | 1996-06-20 | 1997-06-13 | 芳香族化合物のアシル化方法 |
IL12754497A IL127544A0 (en) | 1996-06-20 | 1997-06-13 | Acylation method for an aromatic compound |
HU9903570A HU222542B1 (hu) | 1996-06-20 | 1997-06-13 | Eljárás aromás vegyületek acilezésére |
EP97929344A EP0906254A1 (fr) | 1996-06-20 | 1997-06-13 | Procede d'acylation d'un compose aromatique |
NO19985912A NO319392B1 (no) | 1996-06-20 | 1998-12-16 | Fremgangsmate for acylering av en aromatisk forbindelse |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR96/07691 | 1996-06-20 | ||
FR9607691A FR2750132B1 (fr) | 1996-06-20 | 1996-06-20 | Procede d'acylation d'un ether ou thioether aromatique |
Publications (1)
Publication Number | Publication Date |
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WO1997048665A1 true WO1997048665A1 (fr) | 1997-12-24 |
Family
ID=9493261
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR1997/001066 WO1997048665A1 (fr) | 1996-06-20 | 1997-06-13 | Procede d'acylation d'un compose aromatique |
Country Status (15)
Country | Link |
---|---|
US (1) | US6194616B1 (fr) |
EP (1) | EP0906254A1 (fr) |
JP (1) | JP2000512308A (fr) |
KR (1) | KR20000022034A (fr) |
CN (1) | CN1120825C (fr) |
AU (1) | AU3347997A (fr) |
BR (1) | BR9709734A (fr) |
FR (1) | FR2750132B1 (fr) |
HU (1) | HU222542B1 (fr) |
IL (1) | IL127544A0 (fr) |
NO (1) | NO319392B1 (fr) |
RU (1) | RU2223938C2 (fr) |
TW (1) | TW538031B (fr) |
WO (1) | WO1997048665A1 (fr) |
ZA (1) | ZA975413B (fr) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000040535A1 (fr) * | 1999-01-08 | 2000-07-13 | Rhodia Chimie | Procede de preparation d'un ether de type benzylique |
EP1138662A1 (fr) * | 2000-03-31 | 2001-10-04 | Council of Scientific and Industrial Research | Procédé pour la préparation de 4'-isobutylacétophénone |
JP2001278833A (ja) * | 2000-03-30 | 2001-10-10 | Council Scient Ind Res | 4’−イソブチルアセトフェノンの調製方法 |
EP1149819A1 (fr) * | 2000-03-31 | 2001-10-31 | Council of Scientific and Industrial Research | Procédé pour l'acylation de naphthyléthers |
EP1149818A1 (fr) * | 2000-03-31 | 2001-10-31 | Council of Scientific and Industrial Research | Procédé pour la préparation d' éthers acyl aromatiques |
US6316674B1 (en) | 2000-03-30 | 2001-11-13 | Council Scientific And Industrial Research | Process for the preparation of acyl aromatic ethers |
US6320082B1 (en) | 2000-03-30 | 2001-11-20 | Council Of Scientific And Industrial Research | Process for acylation of naphthyl ethers |
WO2009062742A2 (fr) * | 2007-11-16 | 2009-05-22 | Grace Gmbh & Co. Kg | Catalyseurs acides solides poreux, leurs procédés de fabrication, et procédés de fabrication de molécules organiques les utilisant |
US8710271B2 (en) | 2011-04-08 | 2014-04-29 | Basf Se | Process for the production of an acylation catalyst |
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ES2168963B1 (es) * | 2000-05-22 | 2003-08-01 | Univ Valencia Politecnica | Catalizador de acilacion itq-7 |
US7087791B2 (en) * | 2003-10-02 | 2006-08-08 | Council Of Scientific And Industrial Reasearch | Catalysed acylation of alkylated benzene derivatives |
CN101031543A (zh) * | 2004-09-29 | 2007-09-05 | 西巴特殊化学品控股有限公司 | 制备芳族苯硫基酮的方法 |
CN101157590B (zh) * | 2007-11-23 | 2010-06-02 | 武汉大学 | α-芳基羰基化合物的制备方法 |
KR20130006464A (ko) | 2010-03-09 | 2013-01-16 | 노버스 인터내쇼날 인코포레이티드 | 락톤 중간체를 통한 호모세린으로부터 메티오닌 또는 셀레노메티오닌의 제조 |
FR3030534B1 (fr) | 2014-12-22 | 2016-12-30 | Cdp Innovation | Nouveaux polymeres contenant des fonctions sulfonates metalliques, leurs procedes de preparation et leurs utilisations comme catalyseurs |
WO2018039845A1 (fr) * | 2016-08-29 | 2018-03-08 | 沈建美 | Procédé de préparation d'anhydride hydroxybenzoïque |
CN113943218B (zh) * | 2020-07-16 | 2023-08-18 | 帕潘纳(北京)科技有限公司 | 一种对苯基苯乙酮的制备方法及其应用 |
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EP0334096A2 (fr) * | 1988-03-19 | 1989-09-27 | Bayer Ag | Procédé pour la préparation de phénylcétones éthérifiées en position 4 |
EP0455332A2 (fr) * | 1990-04-04 | 1991-11-06 | Zeneca Limited | Acylation ou sulphonylation de composés aromatiques |
EP0459495A2 (fr) * | 1990-06-01 | 1991-12-04 | Hoechst Aktiengesellschaft | Procédé pour l'acylation de naphtyléthers à l'aide de catalyseurs zéolithiques |
FR2667063A1 (fr) * | 1990-09-26 | 1992-03-27 | Plasto Sa | Procede d'acylation d'hydrocarbures aromatiques. |
EP0701987A1 (fr) * | 1994-09-16 | 1996-03-20 | Cu Chemie Uetikon Ag | Procédé pour la préparation de cérones aromatiques |
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-
1996
- 1996-06-20 FR FR9607691A patent/FR2750132B1/fr not_active Expired - Fee Related
-
1997
- 1997-06-13 EP EP97929344A patent/EP0906254A1/fr active Pending
- 1997-06-13 JP JP10502423A patent/JP2000512308A/ja not_active Ceased
- 1997-06-13 IL IL12754497A patent/IL127544A0/xx unknown
- 1997-06-13 WO PCT/FR1997/001066 patent/WO1997048665A1/fr not_active Application Discontinuation
- 1997-06-13 CN CN97195644A patent/CN1120825C/zh not_active Expired - Fee Related
- 1997-06-13 BR BR9709734A patent/BR9709734A/pt not_active Application Discontinuation
- 1997-06-13 HU HU9903570A patent/HU222542B1/hu not_active IP Right Cessation
- 1997-06-13 KR KR1019980710432A patent/KR20000022034A/ko active IP Right Grant
- 1997-06-13 AU AU33479/97A patent/AU3347997A/en not_active Abandoned
- 1997-06-13 RU RU99101088/04A patent/RU2223938C2/ru not_active IP Right Cessation
- 1997-06-13 US US09/202,666 patent/US6194616B1/en not_active Expired - Fee Related
- 1997-06-19 ZA ZA975413A patent/ZA975413B/xx unknown
- 1997-09-11 TW TW086113192A patent/TW538031B/zh not_active IP Right Cessation
-
1998
- 1998-12-16 NO NO19985912A patent/NO319392B1/no unknown
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EP0316133A2 (fr) * | 1987-11-09 | 1989-05-17 | E.I. Du Pont De Nemours And Company | Procédé de préparation de 1,4-bis(4-phénoxybenzoyl)-benzène en présence d'une zéolithe comme catalyseur |
EP0334096A2 (fr) * | 1988-03-19 | 1989-09-27 | Bayer Ag | Procédé pour la préparation de phénylcétones éthérifiées en position 4 |
EP0455332A2 (fr) * | 1990-04-04 | 1991-11-06 | Zeneca Limited | Acylation ou sulphonylation de composés aromatiques |
EP0459495A2 (fr) * | 1990-06-01 | 1991-12-04 | Hoechst Aktiengesellschaft | Procédé pour l'acylation de naphtyléthers à l'aide de catalyseurs zéolithiques |
FR2667063A1 (fr) * | 1990-09-26 | 1992-03-27 | Plasto Sa | Procede d'acylation d'hydrocarbures aromatiques. |
EP0701987A1 (fr) * | 1994-09-16 | 1996-03-20 | Cu Chemie Uetikon Ag | Procédé pour la préparation de cérones aromatiques |
WO1996021637A1 (fr) * | 1995-01-13 | 1996-07-18 | Rhone-Poulenc Chimie | Procede facilitant la regeneration d'un catalyseur a base d'une zeolithe mis en oeuvre dans une reaction d'acylation, catalyseur et utilisation |
WO1996035656A1 (fr) * | 1995-05-12 | 1996-11-14 | Rhone-Poulenc Chimie | Procede d'acylation d'ethers aromatiques |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000040535A1 (fr) * | 1999-01-08 | 2000-07-13 | Rhodia Chimie | Procede de preparation d'un ether de type benzylique |
FR2788269A1 (fr) * | 1999-01-08 | 2000-07-13 | Rhodia Chimie Sa | Procede de preparation d'un ether de type benzylique |
US6608232B1 (en) | 1999-01-08 | 2003-08-19 | Rhodia Chimie | Method for preparing a benzylic-type ether |
US6316674B1 (en) | 2000-03-30 | 2001-11-13 | Council Scientific And Industrial Research | Process for the preparation of acyl aromatic ethers |
JP2001278833A (ja) * | 2000-03-30 | 2001-10-10 | Council Scient Ind Res | 4’−イソブチルアセトフェノンの調製方法 |
US6320082B1 (en) | 2000-03-30 | 2001-11-20 | Council Of Scientific And Industrial Research | Process for acylation of naphthyl ethers |
JP4491108B2 (ja) * | 2000-03-30 | 2010-06-30 | カウンシル・オブ・サイエンティフィック・アンド・インダストリアル・リサーチ | 4’−イソブチルアセトフェノンの調製方法 |
EP1149819A1 (fr) * | 2000-03-31 | 2001-10-31 | Council of Scientific and Industrial Research | Procédé pour l'acylation de naphthyléthers |
EP1149818A1 (fr) * | 2000-03-31 | 2001-10-31 | Council of Scientific and Industrial Research | Procédé pour la préparation d' éthers acyl aromatiques |
EP1138662A1 (fr) * | 2000-03-31 | 2001-10-04 | Council of Scientific and Industrial Research | Procédé pour la préparation de 4'-isobutylacétophénone |
WO2009062742A2 (fr) * | 2007-11-16 | 2009-05-22 | Grace Gmbh & Co. Kg | Catalyseurs acides solides poreux, leurs procédés de fabrication, et procédés de fabrication de molécules organiques les utilisant |
WO2009062742A3 (fr) * | 2007-11-16 | 2009-08-06 | Grace Gmbh & Co Kg | Catalyseurs acides solides poreux, leurs procédés de fabrication, et procédés de fabrication de molécules organiques les utilisant |
US8710271B2 (en) | 2011-04-08 | 2014-04-29 | Basf Se | Process for the production of an acylation catalyst |
Also Published As
Publication number | Publication date |
---|---|
HUP9903570A2 (hu) | 2001-06-28 |
CN1222131A (zh) | 1999-07-07 |
ZA975413B (en) | 1998-08-25 |
IL127544A0 (en) | 1999-10-28 |
NO985912L (no) | 1999-02-22 |
HU222542B1 (hu) | 2003-09-29 |
HUP9903570A3 (en) | 2001-07-30 |
BR9709734A (pt) | 1999-08-10 |
KR20000022034A (ko) | 2000-04-25 |
CN1120825C (zh) | 2003-09-10 |
EP0906254A1 (fr) | 1999-04-07 |
JP2000512308A (ja) | 2000-09-19 |
FR2750132B1 (fr) | 1998-08-14 |
AU3347997A (en) | 1998-01-07 |
NO319392B1 (no) | 2005-08-08 |
NO985912D0 (no) | 1998-12-16 |
FR2750132A1 (fr) | 1997-12-26 |
TW538031B (en) | 2003-06-21 |
RU2223938C2 (ru) | 2004-02-20 |
US6194616B1 (en) | 2001-02-27 |
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