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Europaisches Patentamt European Patent Office (J) Publication number 0 196 805 Office europeen des brevets A1

© EUROPEAN PATENT APPLICATION

© Application number. 86301727.3 © mt ci* C07C 45/46 , C07C 45/76 , C07C 49/83 C07C 49/84 © Date of filing: 11.03.86 , , C07C 49/813 , C07C 49/788 , C07C 149/32

© Priority: 13.03.85 US 711344 @ Applicant CELANESE CORPORATION 1211 Avenue of the Americas © Date of publication of application: New York New York 10036(US) 08.10.86 Bulletin 86/41 © Inventor: Davenport, Kenneth G. © Designated Contracting States: 3126 Crestwater AT BE CH DE FR GB IT LI LU NL SE Corpus Christi Texas(US) Inventor: Linstid, Clay H., Ill 3232 Halfpenny Corpus Christi Texas(US)

© Representative: De Minvielle-Devaux, Ian Benedict Peter et al CARPMAELS & RANSFORD 43, Bloomsbury Square London WC1A 2RA(GB)

© Acylation of naphthalenes.

Naphthalene substituted in the 2-or β-position with an electron-donating substituent can be acylated with high re- gioselectivity in the 6-position by using an acylating agent in substantially anhydrous which functions both as catalyst and solvent BACKGROUND OF THE INVENTION Additional literature which teaches the Friedel-Crafts acylation of naphthalene and its β-substituted derivatives Many general comments are made in the patent and include: technical literature that the Friedef-Crafts type acylation of Alverez in U.S. 3,758,544, and U.S. 3,873,594, teach- β-substituted naphthalenes can be carried out in the pres- es that in conventional inert solvents, i.e., chlorinated hy- ence of any Friedel-Crafts catalyst This statement is then drocarbons, Friedel-Crafts acylation of 2-methoxynaph- substantiated by particular reference to experiments using, thalene with is accomplished in only low e.g., aluminum chloride or zinc chloride catalyst in nitroben- yields. He found that chlorination in the 1-position was zene or chlorinated hydrocarbons, or boron trifluoride opti- necessary to improve the yield of the corresponding 6- mally in the presence of hydrogen fluoride. acetyl derivative. In the cited patent, anhydrous hydrogen Typically these references do not identify the position fluoride is identified as a typical but not preferred Friedel- of the acyl substitution on the naphthalene ring or do not Crafts catalyst provide such substitution in the 6-position with sufficient Muessdoerffer and Niederprum in German regioselectivity that a large scale manufacturing program Offenlegungschrift 2,616,986, published October 27, 1977, can be developed using the disclosed technology. claimed the acylation of phenols and substifuted phenols In our work on developing precursors for aromatic with an acyl chloride in the presence of hydrogen fluoride to monomers for polyesters, pharmaceuticals, and other value- yield the 4-acyl derivative in high yield with high selectivity. added chemicals, we were interested in obtaining nearly The inventors disclose that 2-naphthol and 7-chloro-2-naph- exclusively 6-acyl-2-naphthol and related 6-acyl-2-substi- thol can be acylated according to their invention. They do tuted naphthalenes in high conversions with high regioselec- not teach a method for the acylation of the naphthol deriva- tivity. tives nor do they indicate what isomer or isomers are A search of the literature provided the following per- manufactured by the claimed process. In view of the other tinent prior art cited prior art, one might be presumed to forecast that the Japanese Kokai Sho 54 [1979J-135756, Yasui et al., 1-acyl-2-hydroxynaphthalene would be formed. describes the preparation of 2-alkyl-6-acylnaphthalene from Lodewijk, U.S. 3,803,245, discloses the acylation of 2- the 2-alkylnaphthalene and acyl fluoride in hydrogen fluoride methoxynaphthalene using aluminum chloride catalyst in with boron trifluoride as a catalyst and in boron trifluoride as nitrobenzene with aluminum chloride, zinc chloride, or simi- a catalyst-solvent The reaction is claimed to be carried out lar Friedel-Crafts catalysts. at between -50°C. and + 100°C.; however, a reading of Organic Synthesis, Vol. 53, p. 5, teaches the acylation the textual portion of the disclosure teaches that yields and of 2-methoxynaphthalene in nitrobenzene with acetyl chlo- 6,-2-selectivity decrease markedly outside the range of ride in 45-48% yield. about-10° to +10°C. Further references teaching the acylation of naphtha- Eiglmeier, in U.S. 4,082,807, teaches the acylation of lene in Friedel-Crafts type reactions include: 2-methoxynaphthalene in anhydrous hydrogen fluoride with diketene to yield 1-acetoacetyl-2-methoxynaphthalene in 88% yield at -25°C. to -35°C. Given and Hammick, Journal Chemical Society [1947] Using the teaching of the above cited references, com- 1237 mercialization of the process has been difficult. Aluminum chloride, zinc chloride, and similar salts used as catalysts in Bui-Hoi et al., Journal Organic Chem.. 16, 988-94 (1951) their anhydrous state absorb water rapidly, hydrolyzing, and this becoming useless in the reaction. Nitrobenzene and the Gupta and Haksar Aara Univ. J. of Res., (Sci) XI, Pt 2, polyhalogenated hydrocarbons utilized as solvents are high 165-6 (1962) boiling, toxic materials. Nitrohydrocarbons, in the presence of the water invari- Arai, Tetrahedron Letters, 24, #14, pp. 1531-34(1983) ably required during the usual work-up, give rise to insepa- rable emulsions. Also, the usual Friedel-Crafts catalysts, Girdler et al., Journal Chemical Society [1966] C(Org.), when admixed with nitrohydrocarbons, generate a substan- 181 tial exothermic reaction which can be difficult to control. Conversions are low. When using metal halides in Harrison et al., Journal Med. Chem., 13, 203(1970) and the nitrohydrocarbons, isomeric mixtures are common, causing following Chemical Abstract references: additional separation steps to be necessary. For all of the above reasons and others, we developed CA 50,5625 c the herein claimed process. CA 50,7139 e SUMMARY OF THE INVENTION

CA 56,14136 d This invention relates to an improved process for the acylation of naphthalene substituted in the 2-position by an CA 57,15022 d electron-donating substituent By the process of this inven- tion the naphthalenic compound to be acylated is brought in CA 58,6663 e contact with substantially anhydrous hydrogen fluoride, con- tacted with an appropriate quantity of the acylating agent, CA 67,10907 y and heated to from about 40°C. to about 100°C for a time sufficient to cause substantially complete conversion of the CA 74,16093 w naphthalene compound to an acyl naphthalene. The hy- drogen fluoride is then removed by evaporation and the CA 80,2790 h acylnaphthalene is isolated. Although the process of this The process of this invention leads to intermediates in invention is useful in acylating any appropriately substituted the manufacture of valuable pharmaceuticals as disclosed in naphthalene, it is particularly useful in the acylation of the Alvarez patents, cited above. The process also provides compounds of the formula: intermediates for the manufacture of monomers as disclosed in the Yasui Japanese patent, loc cit. wherein R is hydroxy, lower alkyl, lower alkoxy, lower tain the desired product; and (5) thereby lower the cost of alkylthio, and halo. manufacture of the product Other advantages to be re- The acylating agent useful in the process of the alized by practicing the process of the present invention will present invention may conveniently be any commercially become obvious to those skilled in the art by studying the useful acylating agent The reaction is more particularly following description and the preferred embodiments of the useful when carried out with the lower alkyl carboxylic invention. acids, acid anhydrides, acid halides and ketene. The compounds useful in the process of this invention are the 2-substituted naphthalenes wherein the substituent DETAILED DESCRIPTION OF THE INVENTION is traditionally known as an ortho-para directing group, an electron-donating group, or by similar designation. Further, The purpose of the present invention is to (1) increase the substituent must not be reactive with hydrogen fluoride, the conversion of an appropriately β-substituted naphthalene as for example to irreversibly form a hydrofluoride salt, thus to an acylnaphthalene; (2) increase the amount of 6-acyl defeating the ortho-para directing influence of the group. substitution compound in the product (3) lower the amount Typically, the compounds most useful in the process of of by-products, particularly tarry by-products in the acylated this invention are characterized by the formula: material; (4) simplify the manipulative steps needed to ob-

wherein R is a member of the group consisting of hydroxy, 2-methylthionaphthalene lower alkyl, lower alkoxy, lower alkylthio, and halo. As used in the context of this invention: Lower alkyl 2-ethylthionaphthalene means C, to C4 alkyl and includes the methyl, ethyl, n- propyl, iso-propyl, n-butyl, sec-butyl, iso-butyl, and tert-butyl 2-isopropylthionaphthalene moieties. Lower alkoxy is meant to be a member of the group 2-fluoronaphthalene consisting of methoxy, ethoxy, n-propoxy, iso-propoxy, n- butoxy, sec-butoxy, iso-butoxy, and tert-butoxy. 2-chloronaphthalene Lower alkylthio is methylthio, ethylthio, n-proplythio, iso -propytthio, n-butylthio, sec-butylthio, iso-butylthio, or tert- 2-bromonaphthalene butylthio. Halo includes fluoro, chloro, bromo, and iodo. Com- 2-iodonaphthalene, and the like. pounds particularly useful in the process of the invention The acylating agent -most particularly useful for this include: present invention process includes a lower alkyl carboxylic acid or a derivative of the lower alkyl carboxylic acid, as for 2-naphthol example a carboxylic acid halide or anhydride, wherein by lower alkyl is meant the C2-C4 carboxylic acids and deriva- 2-methylnaphthalene tives thereof. Examples of acylating agents particularly useful in the 2-ethyinaphthalene present invention include , propionic acid, butyric acid, isobutyric acid, , propionic anhydride, 2-isopropylnaphthalene acetyl chloride, propionyi chloride, acetyl fluoride, propionyl fluoride, butyryl fluoride, acetyl iodide, propionyl bromide, 2'-(sec-butyl)naphthalene and the like. The process of the invention can be operated in a 2-methoxynaphthalene batch or semi-continuous manner. The acylation step of the process should be run in a closed system since hydrogen 2-ethoxynaphthalene fluoride is a toxic material which as a high vapor pressure, boiling at about ambient room temperature, and the ac- 2-n-propoxynaphthalene ylation step is carried out normally at above ambient room temperature, as for example at about 60°C. to about 80°C. 2-(tert-butoxy)naphthalene The process of the present invention is normally car- The residue is dissolved in an appropriate solvent, any ried out in the following manner. The appropriately substi- remaining hydrogen fluoride is neutralized and the resulting tuted naphthalene is brought into contact with substantially, product isolated and purified in a manner well-known to anhydrous hydrogen fluoride. Although an excess of hy- those skilled in the art drogen fluoride is acceptable and does not cause an appre- Typical of the process and the results therefrom are ciable loss of yield or regioselectivity, we have found it most the following specific examples which are provided as a advantageous to use about a 1:25 to about a 1:50 mole teaching of the process and are not to be construed as ratio of naphthalene derivative to hydrogen fluoride. limiting thereupon. The reaction can be carried out in the absence of an additional solvent However, it is not detrimental to the EXAMPLE 1 reaction to use an additional inert solvent Typically such additional solvents may include a chlorinated hydrocarbon A solution of 14.4 g. (0.1 moles) of β-naphthol and or the like. 24.0 g. (0.20 moles) of acetic acid is cooled to -30°C. in a The mixture is cooled to at least about -30°C. pref- stainless steel autoclave. The solution is purged with 50 erentially by contacting the vessel containing the mixture psig nitrogen for 15 minutes. Hydrogen fluoride, 100 g. (5.0 with a cryogenic mixture of liquified gases, solid carbon moles), is added and the autoclave sealed. dioxide or a similar material. The acylating agent is added The autoclave is rapidly heated to 80°C. and main- and the reaction vessel sealed in a manner to withstand the tained at that temperature for 60 minutes. The autoclave is vapor pressure of the hydrogen fluoride at the reaction then rapidly cooled to 40°C. The hydrogen fluoride is temperature. purged from the autoclave at about 40°C. and then a The cooling of the reaction vessel prior to addition of nitrogen sweep is maintained for an additional one hour to the acylafing agent is only for the purpose of minimizing any remove the last distillable traces of hydrogen fluoride. The reaction which might occur in admixing and to act to mini- product is dissolved in ethyl , poured onto ice, mize any heat of dissolution of the reactants in hydrogen neutralized with an aqueous solution containing 45% potas- fluoride. The cooling step is merely manipulative and does sium hydroxide until the aqueous solution was at about pH not limit or define the reaction conditions. 6.7. The aqueous layer is re-extracted with ethyl acetate. Typically, then, the reaction vessel is heated to the The organic layers are combined, washed with a saturated temperature of reaction. In the process herein described aqueous sodium chloride solution, dried and the solvent is and claimed, although some reaction does occur at tem- removed in vacuo. peratures below about 40°C., as for example at ambient Conversion, 93%; selectivity to 6-hydroxy-2-ac- room temperature, the greatest conversion to acylated etonaphthane and its acetate, 76%. naphthalene and the greatest regioselectivity to the 6-acyl In a similar manner, the following compounds are con- isomer occurs between about 40°C. and about 100°C. In a verted to the 6-acetyl derivative: preferred embodiment the reaction occurs at a temperature range of from about 60°C. to about 80°C. 2-methoxynaphthalene to 6-methoxy-2-acetonaphthone Reaction temperatures much above the above de- scribed range gives rise to products which are tarry, highly 2-methylnaphthalene to 6-methyl-2-acetonaphthone colored, and which are difficult to separate from the desired product by the usual isolation and purification techniques. EXAMPLE 2 The reaction is allowed to occur at the temperature range until the formation of the acyl naphthalene is substan- A solution of 14.4 g. (0.1 moles) of S-naphthol and tially complete, as for example, from about 30 to about 90 100 g. (5.0 moles) of hydrogen fluoride is prepared at - minutes. 30°C. Acetic anhydride, 10.2 g. (0.10 moles) is added and In a preferred embodiment a reaction time at the the reaction autoclave is sealed. The autoclave is heated preferred temperature range of about 60 minutes gives rise rapidly to 80°C. and held at that temperature for one hour. to a high conversion of starting material to a product of Isolation and purification of the resulting 6-hydroxy-2-aceto- which the acyl isomers contain a high proportion of the naphthone and its acetate is carried out as in Example 1. desired 6-acyl product without co-manufacture of substantial Conversion, 98%; selectivity to the 6,2 compound 63%. If quantities of undesired by-products. the reaction is carried out with 0.2 moles of acetic anhy- The order of addition of the individual reactants and dride the conversion is 99% and the selectivity is greater hydrogen fluoride as described above is only exemplitive. It than 85%. is also to be considered to be within the scope of the In a similar manner, the following compounds are con- invention to mix the 0-substftuted naphthalene and the ac- verted to their 6-acyl derivative: ylatng agent cool to below the boiling point of hydrogen fluoride, and to then add the hydrogen fluoride and any inert 2-methoxynaphthalene to 6-methoxy-2-acetonaphthone solvent; adding the p-substituted naphthalene to a cooled solution of the acylating agent in hydrogen fluoride is also to 2-ethoxynaphthalene to 6-ethoxy-2-acetonaphthone be considered to be an equivalent method to carry out the adding or mixing step of the process of this invention. 2-methylnaphthalene to 6-methyl-2-acetonaphthone The method or order of addition of the reactants does not change any of the other parameters or descriptions 2-chloronaphthalene to 6-chloro-2-acetonaphthone provided above. After completion of the reaction, the vessel containing the reaction product is typically cooled to about the boiling point of the hydrogen fluoride, the vessel is vented and the hydrogen fluoride is removed by evaporation and recovered. EXAMPLE 3 EXAMPLE 4

Acetyl fluoride, 9.3 g. (0.15 moles), is admixed with Ketene (8.4 g., 0.2 moles generated by thermolysis of 100 g. (5.0 moles) of hydrogen fluoride at -30°C.; the acetone) is added to 100 g. of HF and 14.4 g. 2-naphthol mixture is then added to 14.6 g. (0.1 moles) of 2- at -30°C. in an autoclave. The autoclave is sealed and the fluoronaphthalene in a stainless steel autoclave. The auto- temperature raised to 80°C. In the manner of the first three clave is sealed and the temperature quickly raised to 75°C. examples, 6-hydroxy-2-acetonaphthone is prepared. In the manner of the first two examples 6-acetyl-2- fluoronaphthalene is recovered.

1. A method for the acylation of a naphthalene compound of the formula:

(wherein R is an electron-donating group) with a acylating is from 30 to 90 minutes. agent which comprises contacting a reaction mixture of the naphthalene compound and the acylating agent with sub- 5. The method of any of Claims 1-4 wherein the naph- stantially anhydrous hydrogen fluoride at from 40° to 100° thalene compound to hydrogen fluoride mole ratio in the C for a time sufficient to cause substantially complete reaction mixture is from 1:25 to 1:50. acylation of the naphthalene compound to the 6-acylnaph- thalene compound, and isolating the product therefrom. 6. A method for the manufacture of 6-hydroxy-2-acetyl- naphthalene which comprises contacting a reaction mixture 2. The method of Claim 1 wherein the acylating agent is a of acetic anyhydride and 2-naphthol with hydrogen fluoride lower alkyl carboxylic acid, lower alkyl carboxylic acid anhy- in a mole ratio of 2-naphthol to hydrogen fluoride of 1:50 at dride, lower alkyl carboxylic acid halide or ketene. from 60° to 80° C for 30, minutes to 90 minutes and isolating the product therefrom. 3. The method of Claim 1 or 2 wherein R is hydroxy, lower alkyl, lower alkoxy, lower alkylthio, or halo. 7. The method of Claim 6 wherein the reaction is carried out at about 80° C for about 60 minutes. 4. The method of any of claims 1-3 wherein the tempera- ture acylation is from 60° to 80°C and the time of reaction