PROCESS FOR PRODUCING AROMATIC DIOLS

Abstract: An aromatic diol, e.g. hydroquinone, or a monoalkyl ether of an aromatic diol, e.g. the monomethyl ether of hydroquinone, is produced by transesterifiying a carboxylate ester of said aromatic diol or monoalkyl ether with an alcohol or phenol such as ethanol. A newly-formed ester such as ethyl acetate is co-produced by the reaction. The carboxylate ester is preferably produced by subjecting an aromatic ketone containing a hydroxy or alkoxy radical on the aromatic ring, e.g. 4-hydroxyacetophenone, to a Baeyer-­ Villiger oxidation.

Description: PROCESS FOR PRODUCING AROMATIC DIO;S AND THEIR ETHER DERIVATIVES This invention relates to an improved process for the production of aromatic diols and their monoalkyl ether derivatives. BACKGROUND OF T9E INVETION Aromatic diols such as hydroquinone are known commodities of commerce having use, for example as.photographic developers, polymerization inhibitors, dye intermediates and anti-oxidants. Bydroquinone (RQ) has been commercially produced by the manganese oxide-catalyzed oxidation of aniline to quinone followed by the iron-catalyzed reduction of the quinone to hydroquinone. A more recently developed method of producing hydroquinone comprises the diisopropylation of benzene to form para- diisopropylbenzene followed by peroxidation of the latter compound and acid-catalyzed decomposition of the diperoxide to produce hydroquinone and acetone. While there are advantages to each of these processes, a process of making aromatic diols such as hydroquinone with a lower cost of construction of a commercial unit and/or a lower cost of production would be highly desirable. The monoalkyl ethers of aromatic diols are also known compounds. In addition to some of the same uses mentioned for aromatic diols, these compcunds have use as bactericides and antiseptics, pharmaceuticals e.g. as expectorants and depigmentors, and fragrances. Aromatic diols and their dicarboxylate esters, e.g. the diacetate ester of hydroquinone (AHO), have also found application as monomers in the preparation of certain polymers, e.g. those capable of forming an anisotropic melt phase'and suitable for being formed into shaped'articles such as molded articles, fibers and films as shown, for example in U.S. Patents Nos. 4,330,457; 4,351,918; and 4,355,132. With regard to the process disclosed and claimed herein, the oxidation of ketones with peroxy comppunds to form esters, i.e. the "Baeyer-Villiger" reaction, is known in the art. Some references with disclosures of examples of this type of reaction and descriptions of their teachings are as follows: Hirao et al, Koen Yoshishu - Koryo, Terupen oyobi Sedyu Kagaku ni kansuru Toronkai, 23rd 1979, 131-3 (Japan). Chem. Soc. Japan: Tokyo, Japan, as abstracted in C.A. (1980,) 93, 7777n, show the Fries rearrangement of phenyl acetate and the Friedel-Crafts acetylation of phenol to form para-hydroxyacetophenone which is then oxidized with hydrogen peroxide using sulfuric acid as catalyst to para-hydroxyphenyl acetate; the latter is then hydrolyzed with sulfuric acid in acetic acid to yield hydroquinone. Von E. Doering et al, Journal of the American Chemical Society 72, 5515-5518 (1950) teach the Baeyer-Villiger oxidation of various aromatic ketones, including acetophenone and para-substituted benzophenones, to esters using peracetic acid as the oxidant and show that sulfuric acid has a "marked catalytic action" wit regard to the yield and reaction time (page 5517, col. 1). Ogata et al, Journal of Organic Chemistry 43, No. 12, 2417-2419 teach the Baeyer-Villiger oxidation of acetophenone and substituted acetophenones to the corresponding aryl acetates using permonophosphoric acid as oxidant and sulfuric acid as catalyst and show that the reaction rate is highly dependent on the acidity of the solution. Starcher et al, Journal of the American Chemical Society, 80, 4079-4082 (1958) teach the synthesis of lactones by means of the Baeyer-Villiger oxidation of cyclic ketones using peracetic acid as oxidant. in the paragraph bridging pages 4079 ad 4080, the authors state: "The absence of inorganic impurities, notably water, hydrogen peroxide, mineral acids and salts, reduced polymerization to a minimum during the reaction step and avoided many of the by-products which plagued previous investigators." Adam et al, Journal of Organic Chemistry, 44, No. 26, 4969 (1979) describe the use of bis(trimethylsilyl) monoperoxysulfate as a Baeyer-Villiger oxidant in the oxidation of ketones to their corresponding esters. The authors state that the shortcomings of a previously-used oxidant for this purpose, Caro's or monoperoxysulfuric acid, are "(i) the use of aqueous conditions, (ii) the presence of strong acid and (iii) undesirable side reactions." The alcoholysis or transesterification of an ester by reaction with an alcohol to form another ester of the acid moiety of the first ester with the alcolyzing alcohol, and the free alcohol of the first ester, is also kno,:n in the art. Thus, Bead, U.S. Patent No. 2,639,298 shows the "deesterification" of saligenin diacetate or substituted saligenin diacetates with methanol to produce saligenin or a substituted saligenin and methyl acetate. Fieser and Fieser "Advanced Organic Chemistry", Reinkold (1961), page 378, show the reaction of trilaurin with methanol to form methyl laurate and glycerol. Solomons, "Organic Chemistry, Second Edition" wiles (1980), page 771 shows the reaction of. methyl acrylate with n-butyl alcohol to form n-butyl acrylate and methyl alcohol. Copending application Serial No. 661,552 filed October 17, 1984 discloses and claims a method of producing aromatic diols or monomethyl ethers of aromatic diols by first subjecting an aromatic ketone containing a hydroxy, alkoxy or acyloxy radical on the aromatic ring, e.g. 4-hydroxyacetophenone, to a Bayer-Villiger oxidation using peracetic acid as oxidant under conditions such that the reaction mass contains no more than about 0.1 wt.% of sulfuric acid based on the weight of the initially added pure peracetic acid. The carboxylate esters may be hydrolyzed to the aromatic diols, e.g. hydroquinone, or to the monoalkyl ethers of the aromatic diols, e.g. the monomethyl ether of hydroquinone, by reacting the ester with water under acid conditions. While the recovery of the aromatic diol or the monoalkyl ether of the aromatic diol from the corresponding monocarboxylate ester as disclosed in previously cited application Serial No. 661,552 and the cited Hiroa et al article is satisfactory for many purposes, such method of recovery may have some disadvantages under certain circumstances. Thus, the hydrolysis of the monocarboxylate ester results in the formation of a free carboxylic acid as a by-product, e.g. acetic acid when a monoacetate is hydrolyzed. Although such carboxylic acid by-product may have value, it is obtained, due to the amount of water used for the hydrolysis reaction, as a relatively dilute aqueous solution from which it is uneconomical to recover the acid. Furthermore, the separation of carboxylic acid by-product from the aromatic diol or monoalkyl ether of' an aromatic diol product may be more difficult and consume a larger amount of energy than other by-products obtained from alternative recovery processes. SUMMARY OF THE INVENTION In accordance with this invention, a composition comprising a major proportion of a carboxylate ester of an aromatic diol, e.g. the monoacetate of hydroquinone (MAHO), or a carboxylate ester of a monalkyl ether of an aromatic diol, e.g. 4-acetoxyanisole, is reacted with an alcohol or phenol in a transesterification reaction to form an aromatic diol, e.g. hydroquinone (HQ) or a monoalkyl ether of an aromatic diol, e.g. the monomethyl ether of hydroquinpne (MEHQ) {hereinafter referred to as the "product phenolic compound") and a relatively easy to recover ester of the acid moiety of the aforesaid carboxylate ester and the reacting alcohol or phenol (hereinafter referred to as the "product ester"). The foregoing reaction may also be described as an "alcoholysis" if an alcohol is initially reacted with the ester of an aromatic diol or a wphenolysisz if a phenol is initially reacted. In most cases, the composition comprising the initial ester is produced by subjecting an aromatic ketone1 containing a hydroxy or alkoxy radical on the aromatic ring, e.g. 4-hydroxyacetophenone (4--dAP), to a "Baeyer-Villiger" oxidation using as oxidant a peroxy compound such as peracetic acid or hydrogen peroxide. Preferably, the oxidation is carried out using the process disclosed in previously cited copending application Serial No.661,552 including the use as oxidant of peracetic acid under conditions such that the reaction mass contains no more than about 0.1 weight percent of sulfuric acid based on the weight of the initally added pure peracetic acid. Desirably, the reaction mass also contains no more than about 5 weight percent of water based on the weight of pure peracetic acid initially added. This procedure would exclude the use in unmodified form of most commercial peracetic acid solutions which generally contain sulfuric acid and water in amcunts greater than the maximum amounts previously set out. The transesterification reaction of this invention proceeds as in equation (I)t EMI6.1 <tb> <SEP> 0 <SEP> 0 <tb> YO-Ar1 <SEP> 1 <SEP> R1OH <SEP> acid <SEP> + <SEP> ll <SEP> (I). <tb> oCR <SEP> OCR <SEP> + <SEP> R <SEP> or <SEP> } <SEP> -+YO-Ar1-OH <SEP> + <SEP> OCR <tb> where R is an alkyl radical, R1 is an alkyl, aryl or aralkyl radical, Arl is a divalent aromatic radical (all more specifically defined below) and Y is hydrogen, R,'o'r RC. If Y is RC=O, i.e. the initial aromatic diol ester is a diester, then the monoester as well as the diol will form if an insufficient amount of alcohol or phenol is supplied to the reaction. Thus, in this case, a sufficient amount of alcohol or phenol must be supplied to react with two carboxylate radicals per molecule of initial aromatic diol ester. If it is desired to transesterif, the monoacetate of hydroquinone (ttAHQ) to hydroquinone (HQ) and ethyl acetate using ethanol as the alcoholyzing alcohol, the reactior proceeds as in equation (it): EMI6.2 The carboxylate esters of aromatic diols or monoalkyl ethers of aromatic diols contemplated to be transesterified to aromatic diols or monoalkyl ethers of aromatic diols in accordance with this invention, may be produced by the Baeyer-Villiger oxidation of the corresponding aromatic ketone as shown in equation (III): : EMI6.3 <tb> <SEP> peroxy <SEP> 1 <SEP> OIl <tb> YO-Ar1-CR <SEP> + <SEP> [O1 <SEP> peroxy <SEP> || <SEP> (III) <tb> <SEP> compound <tb> If it is desired to produce MAHO from 4-hydroxyacetophenone (4-HAP) by a Baeyer-Villiger oxidation using peracetic acid as oxidant, the reaction proceeds as in equation (IV): EMI7.1 In equations (I) and tIT), Arl is a divalent aromatic radical. The specific nature of the radical is not critical but it is preferably a radical resulting from the removal of two ring hydrogen atoms from benzene, naphthalene, or biphenyl, either unsubstituted or with ring hydrogens substituted with. radicals such as methyl, tolyl; and appropriately masked amino, or sulfhydryl substituents. Ar1 is preferably 1,4-phenylene, 2,l-naphthylene, 2,6-naphthylene, 5-phenyl-1,2-phenylene, 3-phenyl-i, 4-phenylene or 3-methyl-1,4-phenylene with the ketocarbon and corresponding groups occupying the first stated numbered position of Ar when the positions are not equivalent. Most preferably Ar is 1,4-phenylene. The R groups in equations (I) and (III) are alkyl groups containing, for example 1 to 18 carbon atoms, preferably 1 to 4 carbon atoms, and may be the same or different when Y is R. More preferably, R is methyl, ethyl or propyl and most preferably methyl corresponding to the use of methyl ketones and ethers and acetate esters in the latter equations. The R1 radical in equation (I) may be alkyl containing 1 to 18 carbon atoms, preferably 1 to 4 carbon atoms; aryl such as phenyl or naphthyl which may be unsubstituted or substituted with radicals inert under the conditions of reaction such as alkyl, aryl, alkoxy or chloride; or aralkyl, e.g. having the fornula: EMI8.1 where R2 may be hydrogen or one or more inert substituents, e.g. alkyl, aryl, alkoxy or chloride, and n may be, for example, in the range of 1 to 4. The foregoing alkyl and alkoxy substituents may have a number or carbon atoms within 1 same ranges specified previously for 1 the same In ranges specified previously for Rand RÚ when RÚ is alkyl. in particularly preferred embodiments R1 is ethyl or n-butyl corresponding to the use of ethanol or n-butanol as the alcoholyzing alcohol. Most preferably the starting material for the transesterification is the monoacetate ester of hydroquinone (MAHQ) formed by the Baeyer-Villiger oxidation of 4-hydroxyacetophenone (4-HAP) and the products of the reaction are hydroquinone (HQ) and ethyl acetate formed by the alcoholysis of the MAHO with ethanol. If a monoalkyl ether of an aromatic diol is the desired products, the monoalkyl ether of the hydroxy aromatic ketone is first prepared using any of the techniques known in the art, e.g. reaction of the hydroxy aromatic ketone, e.g. 4-HAP, with an alkyl iodide such as methyl iodide under basic conditions. In producing esters of aromatic diols and esters of monoalkyl ethers of aromatic diols in accordance with equation (1), the aromatic ketone, e.g. the hydroxy aromatic ketone or a monoalkyl ether of ch hydroxy aromatic ketone, is subjected to a Baeyer-Villiger oxidation by reacting the ketone with a peroxy compound. The peroxy compound may be, for example, peracetic acid, hydrogen peroxide, perbenzoic acid, m-chloroperbenzoic acid, trifluoroperacetic acid, permonophosphoric acid and bis(trimethylsilyl) monoperoxysulfate. The amount of peroxy compound supplied to the reaction is in the range for example of about 0.5 to about 2 moles per mole of aromatic ketone. The reaction may be carried out at a temperature, for example, of'about 20 to 1400C and a pressure, for example, of about 25mm of mercury to about 2 atmospheres for a period, for example, of about 0.5 to about 3 hours. A solvent for the aromatic ketone may be used in the initial reaction solution e.g. an alkanoic acid such as glacial acetic acid or formic acid. Desirably, the Baeyer-Villiger oxidant is a purified peracetic acid which is contacted with the aromatic ketone under such conditions that the reaction solution contains no more than about 0.1 wt.9, preferably no more than about 0.05 wt.% of sulfuric acid based on the weight of pure peracetic acid initially added. Advantageously the reaction solution also contains no more than about 5 wt.%, preferably no more than about 2 wt.% of water based on the weight of pure peracetic acid. In general, the less the sulfuric acid and water present the better. Preferably, the peracetic acid is added in the form of a solution consisting essentially of about 5 to 4r wt.% peracetic acid and the remainder a solvent such as acetic acid, methyl acetate1 ethyl acetate, acetone or mixtures thereof. The hydroxy aromatic ketones which are starting materials for the production of monocarboylate esters of aromatic diols or monocarboxylate esters of monoalkyl ethers of aromatic diols, are compounds known in the art and may be produced by any known process. Preferably, however, they are produced by the Fries rearrangement of aryl carboxylates such as phenyl acetate, or the Friedel-Crafts acylation of phenols, e.g. the acetylation of phenol with acetic acid or anhydride, both reactions using hydrogen fluoride as catalyst, as disclosed, for example in previously cited copending application Serial No. 661,552. The transesterification of the monocarboxylate ester of the aromatic diol or the monocarboxylate ester of the monoalkyl ether of the aromatic diol, is carried out by contacting the ester with the alcoholyzing alcohol or phenolyzing phenol under acidic conditions and elevated temperature for a qeriod of time sufficient to permit the reaction to approach completion. Typically the amount-of alcohol used will be for example about 50 to 1000 preferably about 100 to 200 mol% based on the ester being alcoholyzed, the temperature will be about 20 to 2000C (broad range), preferably about 60 to 140 CC and the period of reaction will be for example, about 0.1 to 10, preferably about 0.5 to 4 hours. A solvent may be employed which may be, for example, the product ester or the acid moiety of the initial and product esters in free form, alone or in admixture, e.g. ethyl acetate and/or acetic acid in the case of the alccholysis of the monoacetate of hydroquinone (! Q) with ethanol. Other solvents which may be used are n-butyl acetate, propyl acetate, butyric acid, and propionic acid. However, use of these solvents in the alcoholysis of MAHQ with ethanol would complicate the solvent recovery system. If a solvent is employed, it is used in such quantity as to yield a solution of about 5 to 60 wt.%, preferably about 25.to 40 wt.% of monocarboxylate ester of either the aromatic diol or monoalkyl ether of an aromatic diol. Stirring or other mixing action is preferably employed during the reaction. The reaction is carried out in the presence of an acid catalyst. Acids which may be employed for this purpose are organic acids such as methanesulfonic acid,para-toluenesulfonic acid and benzenesulfonic acids, mineral acids such as sulfuric, hydrochloric and phosphoric acids and acidic ion-exchange resins e.g. sulfonic acid ion-exchange resins such as Amberlyst 15 sold by Rohm and Haas and Nafion 501 sold by duPont, The acid is usually employed in an amount, for example of about 0.1 to 5, preferably about 0.5 to 2 molF based on the monocarboxylate ester. In some instances, it may be desirable to employ a combination of alcohol or phenol and water to achieve a measure of both transesterification and hydrolysis of the monocarboxylate ester to obtain the aromatic diol or monoalkyl ether of aromatic diol and a mixture of newly synthesized ester and esterifying acid. For example, there may be some advantage to having a small amount of water remaining after the reaction since this may facilitate separation of an alcoholyzing alcohol, e.g. ethanol, and the product ester, e.g. ethyl acetate due to a favorable phase separation. If a mixture of alcohol or phenol and water is employed, the water will usually be present in an amount, for example, of about 25 to 100 molZ based on the alcohol. In this case, the combination of water and alcohol will generally be used in an amount within the ranges given above for the amount of alcohol employed when it is used without water. The product may be recovered by conventional purification methods usually involving a combination of crystallization, filtration, washing and distillation in any order deemed advantageous for the system at hand. The transesterification process of this invention provides for the recovery of product phenolic compound in relatively high yields. Thus the process generally results in a conversion of initial ester to all products of at least about 95%, preferably at least about 98% with efficiency to product phenolic compound of at least about 97t, preferably at about 99% and an efficiency to product ester of at least about 97%, preferably at least about 99t. DESCRIPTION OF SPECIFIC EMBODIMENTS The following examples further illustrate the in vention. Examples 1 to 7 illustrate the conversion of 4-hydroxy-acetophenonc (4-HAP)to the monoacetate ester of hydroguinone (MAHQ) by the Bayer-Villiger oxidation using a "purified" peracetic acid containing under 0.05 wt% of sulfuric acid and under 2 wt.% of water as the oxidizing agent. Example 1 To 650 grams of commercially available peracetic acid were slowly added 650 grams of acetic anhydride. This commer cial acid contained N40 wt. 8 peracetic acid, N13 wt.% water, N5 wt.% hydrogen peroxide and ¯ 1 wt.% sulfuric acid, and the purpose of the acetic anhydride treatment was to convert the water and hydrogen peroxide present to acetic acid and peracetic acid, respectively. The solution was cooled and stirred during the addition to maintain the termperature at (300C. The solution was then distilled under vacuum (20-30 mmHgA, N400C) through a one-inch Vigreux column. The initial 20cc. of distillate were discarded. Then, ¯ 1000cc. of material was distilled without reflux. This material referred to below as "purified peracetic acid solution" contained V27 wt.% peracetic acid and oJ73 wt.% acetic acid and was used for the oxidations of this and the following examples. In a solution of 60 grams of glacial acetic acid and 10 grams of acetic anhydride were dissolved 30 grams of 4-HAP. This solution was placed into a 250 cc. three-neck flask. While heating the solution to 600C, the flask was partially evacuated to a pressure of 60 mmEgA. This pressure was main tained throughout the experiment. To the solution were added 77.5 grams of the purified pre acetic acid solution containing 20.46 g of pure peracetic acid, fed dropwise over a period of 40 minutes, and the solution was heated for an additional 80 minutes. The initial mole ratio of peracetic acid to 4-HAP was 1.22. The solution was then cooled and analyzed by gas chromatography and other well-established procedures. The product solution weighed 171.3 grams and contained 18.0 wt% monoacetate ester of hydroquinone (MAHQ)! 0.47 wt% diacetate ester of hydroquinone (DAGO), 0.03 wtt hydroquinone (HQ), 0.05 wtF benzoquinone (by), 0.17 wt% 4-acetoxyacetophenone (4-AAP), and 0.41 wt% of 4-hydroxyacetophenone (4-HAP). Peracetic acid was not detected. This corresponds to 97% conversion of 4-HAP and 978 efficiency to hydroquinone and its esters. Example 2 The procedure of Example 1 was followed except that the tenperature employed was 800C, the solvent consisted of 70 g acetic acid and no acetic anhydride to which 4.4 mg of ethylene diamine tetraacetic acid (EDTA) were added and 51.7 grams of purified peracetic acid solution containing 13.65 of pure peracetic acid were fed over the 40 min. period. The initial mole ratio of peracetic acid to 4-HAP was 0.81. The product solution weighed 154.0 grams and contained 13.7 wt.% MABQ, 0.33 wt.% DAHQ, 0.78 wt.% HQ, 0.03 wt.% BQ, and 4.8 wt.% of 4-HAP, corresponding to 74.93% conversion of 4-HAP and 92.17% efficiency to HQ and its esters. Example 3 The procedure of Example 1 was followed except that the solvent consisted of 70 grams of acetic and no acetic anhydride to which 4.4 mg. of EDTA were added, and the purified peracetic acid solution was added over a 10 min. period and the reactior solution heated for an additional 40 min. period. The initial mole ratio of peracetic acid to 4-HAP was 1.22. The product solution weighed 177.3 grams and contained 16.8 wt. MAHQ, 0.26 wt.% of DAHQ, 0.13 wt.t HO, 0.13 wit;% BQ and 0.02 wt.% 4-HAP, corresponding to 99.88% conversion of 4-HAP and 90.978 efficiency to HQ and its esters. Example 4 The procedure of Example 2 was followed except that 51.7 grams of purified peracetic acid solution containing 14.37 grams of peracetic acid were fed over a 20 min. period, the solution was heated for an additional 40 min. and the solvent consisted of 60 grams of acetic acid and 10 grams of acetic anhydride. The initial mole ratio of peracetic acid to 4-HAP was 0.86. The product solution weighed 153.0 grams and contained 14.10 wt.% MAHQ, 1.10 wt.t DAHQ, 0.77 wt.% HO, 0.08 wt.% BQ and 4.60 wt. % 4-BAP corresponding to 75.41% conversion of 4-HAP and 97.97% efficiency to HQ and its esters. Example 5 The procedure of Example 1 was followed except that 62.1 grams of purified peracetic acid solution containing 17.26 grams of peracetic acid were fed over a 30 min. period, the solution was heated for an additional 30 min. and the solvent consisted of 70 grams of acetic acid to which was added 0.1 gram of sodium acetate. The initial mole ratio of peracetic acid to 4-HAP was 1.03. The product solution weighed 161.7 grams and contained 21.40 wt.% MARQ, 0.00 wt.% DO30, 0.02 wt.% HQ, 0.00 wt.% By and 0.55 wt.% 4-HAP corresponding to a conversion of 4-HAP of 97.04% and an efficiency to HQ and its esters of 100%. Example 6 The procedure of Example 1 was followed except that 107.4 grams of purified peracetic acid solution containing 29.11 grams of peracetic acid were fed over a 30 min. period, the solution was heated for an additional 30 min. and the 4-HAP solution consisted of 50.8 grams of acetic acid and 50.8 grams of 4-BAP. The initial mole ratio of peracetic acid to 4-HAP was 1.04. The product solution weighed 206.9 grams and con tained 21.9 wt.s MARY, 0.09 wt.% DARQ, 0.01 wt.t BQ, 0.01 wt.% HO and 1.70 wt.t 4-HAP corresponding to a normalized conversion of 4-HAP based on 88.858 accountability of products of 91.69% and a normalized efficiency to NO and its esters of 99.9%. Example 7 The procedure of Example 1 was followed except that 90.8 grams of purified peracetic acid solution containing 24.61 grams of peracetic acid were fed over a 30 min. period, the solution was heated for an additional 30 min. and the 4-HAP solution solution consisted of 69.1 grams of 90% formic acid and 40.3 grams of 4-HAP. The initial mole ratio of peracetic acid to 4-NAP was 1.09. The product solution weighed 198.5 grams and con tained 17.6 wt.% MAHQ, 0.17 wt.% DAHQ, 0.85 wt.% HQ; 0.04 wt.% HO and 1.10 wt.% 4-HAP corresponding to a normalized conversion of 4-HAP based on 88.99% accountability of products of 93.91% and a normal-ized efficiency to HQ and its esters of 99.70%. Example 8 This example illustrates the-use of hydrogen peroxide as the Baeyer-Villiger oxidant. The procedure of Example 7 was followed except that 26.1 grams of a 50 wt. % hydrogen peroxide solution in water were used as the oxidant in place of the peracetic acid solution and the 4-HAP solution consisted of 53.2 grams ot 90% formic acid and 30.0 grams of 4-HAP. The initial mole ratio of Hydrogen peroxide to 4-HAP was 1.09. The product solution weighed 105.2 grams and contained 6.00 wt.% MAHO, 0,0 wit.8 DAHQ, 8.10 wt.% HO, 0.0 wt.t BQ, and 5.00 wt.l 4-HAP corresponding to a normalized conversion of 4-HAP of 75.47% and a normalized efficiency to NO and its esters of 100.00% based on 71.488 accountability of products. Although this invention contemplates the transesterification of carbo wlate esters of aromatic diols or esters of monoalkyl ethers of aromatic diols produced by the Baeyer-Villiger oxidation of hydroxy- or alkoxy aromatic ketones regardless of which peroxy oxidant is used, comparison of the results of Example 8 with those of Example 7 nevertheless indicates that the use of peracetic acid in the absence of sulfuric acid as oxidant yields higher conversions of 4-HAP than hydrogen peroxide with equivalent efficiencies to HQ and its esters. This indicates that the use of such peracetic acid will result in somewhat higher transesterification yields of aromatic diol or monoalkyl ether of aromatic diol than if other peroxy compounds such as hydrogen peroxide is used as the Baeyer-Villiger peroxy oxidant. Example 9 This example illustrates the alcoholysis of fiLAHQ and DABQ with ethanol to form HQ and ethyl acetate. Product from several experiments as described in Example 1 were combined and most of the acetic acid removed by evaporation under vacuum at 1000C. Analysis of the nonvolatile portion showed that it contained 81.5wt.% MAHQ, 2.0 wt.% NO, 2.2 wt.% DABS, 1.5 wt.% 4-HAP, 0.01 wt.% BO, and 1.2 wt.% acetic acid. 28.0 Grams of this non-volatile material were added to a solution containing 25.9 grams of ethyl acetate, 11.0 grams of ethanol, 13.0 grams of acetic acid, and 0.29 gram of 70% methanesulfonic acid. This solution was stirred and refluxed at 87'C for two hours. Upon cooling to OOC a crystalline solid precipitated. The solid was filtered, washed with 10 ml of ethyl acetate, and dried in a vacuum dessicator. The dried solid weighed 2.59 grams and contained 93.9 wt.% HQ, 0.06 wt.% MAHO, 0.0 wt.% DAHQ, 0.0 wt.t BQ, and 1.2 wt.t acetic acid. The filtrate plus wash weighed 75.9 grams and contained 23.5 wt.% HQ, 0.30 wt.% Mao,. 0.0 wt.% DAHQ, 13.2 wt.% acetic acid, 63.3 wt.% ethyl acetate (an increase of 22.1 grams) and 2.1 wt.% ethanol (a decrease of 9.4 grams). These results show that the normalized conversion of MAHQ to HO was 99.18 and that normalized efficiency of HQ was 100% based on product accountability of EMI17.1 Example 10 This example illustrates the combined hydrolysis and alcoholysis of MAHQ and DABQ with water and ethanol to form HQ and ethyl acetate. Product from several experiments as described in Example 1 were combined and most of the acetic acid removed by evaporation under vacuum at 100 C. Analysis of the. nonvolatile portion showed that it contained 81.5 wt.E MAHO, 2.0 wt.% BQ, 2.2 wt.% DABS, 1.5 wt.% 4-HAP, 0.01 wt.% BQ, and 1.2 wt.% acetic acid. 30.0 Grams of this non-volatile material were added to a solution containing 25.5 grams of ethyl acetate, 7.9 grams of ethanol, 12.0 grams of acetic acid, 3.1 grams of water and 0.14 gram of 70% methanesulfonic acid. This solution was stirred and refluxed at 87.60C for one hour. The product was cooled to OOC, but no precipitate formed. The product weighed 77.5 grams and contained 23.3 wt.% HQ, 3.0 wt.% MAHQ, 0.0 wt.% DAHQ 21.7 wt.% acetic acid, 41.8 wt.% ethyl acetate (an increase of 6.9 grams) and 5.5 wt.% ethanol (a decrease of 3.6 grams). These results show that the normalized conversion of MAHQ to HQ was 91.5% and that the normalized efficiency to BQ was 1009 based on product accountability of 105.7t. Example 11 This example illustrates the methylation of 4-hydro xyacetophenone (4-HAP) to form p-methoxyacetophenone (PMAP). 50g (0.37mol) of 4-hydroxyacetophenone, 51.8 g (0.37 mol) of methyl iodide, and 51 g (0.37 mol) of potassium car bonate were dissolved in 55 ml of dry acetone and gently refluxed for 24 hours. After cooling the reaction mixture 200 ml of water were added to dissolve the precipitated potassium iodide. The resulting mixture was extracted three times with 200 ml of ether. The combined organic material was separated, washed with 10% sodium hydroxide, dried over anhydrous potas sium carbonate, filtered and evaporated. Distillation of the residue (110 C e 2 mmHgA) afforded 50 g (ca. 92% yield) of a white crystalline solid which was p-methoxyacetophenone (PMAP). Example 12 This example illustrates the Baeyer-Villiger oxidation of p-methoxyacetophenone (PMAP) to p-methoxyphenyl acetate (PMPA). The procedure of Example 1 was followed except that 24.2 grams of PMAP and 0.005 gram of EDTA were dissolved in 76.8 grams of acetic acid (no acetic anhydride), 45.7 grams of purified peracetic acid solution were added over a 20 min. period, and the reaction solution was heated for an additional 60 60 min. period. The initial mole ratio of peracetic acid to PMAP was 1.11. The product solution weighed 144.2 grams and con tained 13.70 wt% PMPA, 0.01 wt.% p-methoxyphenol, i.e. the monomethyl ether of hydroquinone (MEHQ), 4.30 wt.% PAP, and 0.90 wt.% peracetic acid, corresponding to 74.40% conversion of PMAP and 99.9% efficiency to PMPA. The PMPA may be alcoholized or alcoholyzed and hydrolyzed to MENO using the procedure of Examples 9 and 10. The procedures of Examples 1 to 10 can also be used to prepare, for example, 3-phenylcatechol from 2-hydroxy-5-phenyl acetophenone; phenylhydroquinone from 4-hydroxy-3 phenyl-acetophenone; methylhydroquinone from 4-hydroxy-3 methyl-acetophenone; catechol from 2-hydroxyacetophenone (2-HAP); guaiacol from 2-methoxyacetophenone; 2, 6-dihydroxynaphthalen (2,6-DBN) from 6-acetoxy 2-acetonaphthone; and 4,4'-biphenol from 4{4'-hydroxyphenyl) acetophenone. The alcoholysis procedure illustrated in Examples 9 and 10 may also be carried out using methanol, propanol or n-butanol to obtain methyl, propyl or n-butyl acetate respectively as a co-product with HQ.

Claims: Claims 1. A process comprising contacting a composition comprising a major proportion of a caXorlate ester of an aromatic diol or a carboxylate ester of a monoalkyl ether of an aromatic diol, with an alcohol or phenol at an elevated temperature and unaer acidic conditions for a period of time sufficient to transesterify said carborlate ester to the free aromatic diol or monoalkyl ether of an aromatic diol, and a newly-formed ester of said alcohol with the carboxylic acid moiety of said carboxylate ester. 2. The process of claim 1 wherein said alcohol or phenol is an alkanol containing 1 to 4 carbon atoms. 3. The process of claim 2 wherein said carboxylate ester is the monoacetate ester of hydroquinone, said alkanol is ethanol, said aromatic diol is hydroquinone and said newlyformed ester is ethyl acetate. 4. A process comprising subjecting an aromatic ketone containing a hydroxy or alkoxy radical on the aromatic ring, to a Baeyer-Villiger oxidation using a peroxy compound as oxidant to produce a reaction product comprising a carbo tlate ester of an aromatic diol or a carboxylate ester of a monoalkyl ether of an aromatic diol,and contacting a composition comprising a major proportion of a said carboxylate ester with an alcohol or phenol at an elevated temperature and under acidic conditions for a period of time to transesterify said carboxylate ester to the free aromatic diol or monalkyl ether of an aromatic diol, and a newly-formed ester of said alcohol or phenol with the carboxylic acid moiety of said carboxylate ester. 5. The process of claim 4 wherein said alcohol or phenol is an alkanol containing 1 to 4 carbon atoms. 6. The process of claim 4 wherein said aromatic ketone is 4-hydroxyacetophenonet said moncarboxylate ester is the monoacetate ester of hydroquinone, said alkanol is ethanol, said aromatic diol is hydroquinone and said newlyformed ester is ethyl acetate. 7. The process of claim 4 wherein said peroxy compound is peracetic acid employed such that the reaction mass of the Baeyer-Villiger oxidation contains no more than about 0.1 wt.96 of sulfuric acid based on the weight of peracetic acid initially added. 8. The process of claim 7 wherein the reaction mass of the Baeyer-Villiger oxidation also contains no more that about 5 wt.% of water based on the weight of peracetic acid initially added.

Inventors: HILTON, CHARLES BRUCE
Applicants: CELANESE CORPORATION
Application year: 1986
Main classification: C07C39
IPC codes: C07C69, C07C29, C07C39, C07C37, C07C45, C07C43, C07C50, C07C41, C07C49, C07C67, C07C27