Oxidative Coupling of Alkylphenols or 1-Naphthols Catalyzed by Metal Complexes of Keto Alcohol Compounds

The present invention relates generally to an improved process for preparing self-condensation products, such as diphenoquinones, biphenols, dinaphthenoquinones and binaphthols from alkylphenols, alkoxyphenols and naphthols and to a catalyst composition for use in said process. More particularly, the invention relates to a method of preparing carbon-carbon coupled condensation products of alkylphenols, alkoxyphenols or 1-naphthols by contacting an aqueous mixture of the phenol or naphthol with oxygen or an oxygen-containing gas optionally in the presence of a surfactant and sufficient alkaline material to sustain a pH in the range of 7.0-9.5 during the oxidative coupling reaction and a catalyst system comprising a cupric or manganous complex of a keto alcohol.

It is well known in the art that substituted phenols can be oxidized to yield self-condensation products, including diphenoquinones, biphenols and polyphenoxy ethers. The procedure employed in the preparation of these derivatives is generally referred to as the oxidative coupling of phenols.

The self-condensation products resulting from these oxidative coupling reactions can be catagorized as either the result of carbon-carbon coupling or carbon-oxygen coupling of said phenols. Diphenoquinones and biphenols are prepared by carbon-carbon coupling in accordance with the following general reactions depending upon the reactive sites available in the phenol employed. ##STR1## wherein R is hydrogen or R.sub.1 and wherein R.sub.1 is either alkyl, alkoxy, or another substituent all of which are well known in the art.

Similarly, polyphenoxy ethers are prepared by carbon-oxygen coupling in accordance with reactions such as the following general reaction: ##STR2## wherein R and R.sub.1 are as defined above and n is an integer.

A variety of materials, including metals and various salts and complexes thereof, have previously been disclosed as useful in promoting the oxidative coupling of alkylphenols. Thus, U.S. Pat. No. 2,785,188, discloses that copper powder may be utilized to prepare diphenoquinones from 2,6-dialkyl-4-halophenols. Similarly, various copper salts and combinations or complexes prepared from copper salts and a variety of nitrogen-containing compounds have been disclosed as useful in the preparation of both diphenoquinones and polyphenoxy ethers. These include, for example, cupric complexes of primary and secondary amines (U.S. Pat. No. 3,306,874); and cupric complexes of tertiary amines (U.S. Pat. Nos. 3,306,875 and 3,134,753); cupric complexes of pyridine (U.S. Pat. Nos. 3,219,625 and 3,219,626 both of which were issued to Blanchard et al.) and a mixture of a cupric halide or a cupric carboxylate and a tertiary amine (U.S. Pat. No. 3,384,619). Additional catalysts prepared from cuprous or cupric salts and amines have been disclosed as, for example, in U.S. Pat. Nos. 3,544,516; 3,639,656; 3,642,699 and 3,661,848, all of which were issued to Bennett and Cooper. Finally, U.S. Pat. No. 3,210,384 issued to Hay discloses the use of complexes of a basic cupric salt and a nitrile or tertiary amine and U.S. Pat. No. 3,549,670 issued to Spousta et al. describes the use of a copper or copper alloy catalyst and a nitrogen base. The use of cupric salts of carboxylic acids as the oxidizing agent in oxidative coupling reactions is also disclosed in the art. See, in the regard, U.S. Pat. No. 3,247,262.

The use of manganese and cobalt compounds has also been disclosed in U.S. Pat. Nos. 3,337,501 and 3,573,257.

The use of manganese amine chelates as oxidizing agents in oxidative coupling reactions is described in U.S. Pat. No. 3,825,521.

A variety of basic compounds have also been employed in oxidative coupling reactions. In many of these, such as those disclosed in U.S. Pat. No. 2,905,674 and in U.S. Pat. No. 2,785,188, the function of the alkaline materials was to react with an acidic component, such as HCl, liberated during the course of the reaction and, therefore, a stoichiometric amount of the base was used.

It should be noted that, previous methods of preparing coupled products from alkyl- or alkoxy-phenols have required the use of either organic solvents or stoichiometric amounts of organic oxidizing reagents. The present invention provides for a metal keto alcohol chelate catalyst system useful in the preparation of carbon-carbon coupled phenols or naphthols in an aqueous reaction medium. Also, with most of the prior art systems the resulting product or products were determined by the particular catalyst employed and could not easily be controlled. The present invention provides for a system which can be readily modified to produce either the biphenol or diphenoquinone directly from the reaction mixture.

In accordance with the present invention, it has been found that "alkyl- or alkoxy-phenols" and "1-naphthols" may be oxidatively coupled in a substantially basic aqueous medium if there is employed as a catalyst a system comprising a cupric or manganous chelate of keto alcohol.

It has also been found that the type of product which is produced can be controlled by the amount of alkaline material and by the amount of catalyst employed in the catalyst system. By comparison, the prior art catalysts and processes employing said catalysts have a number of disadvantages which have restricted the utility of said catalysts and processes. These include (a) the requirement that the reaction be conducted in an organic solvent, (b) the fact that the primary product produced is often the polyphenoxy ether, and (c) the inability to form the biphenol or binaphthol derivative directly and in substantial quantities without requiring that this material be produced by a subsequent hydrogenation of the diphenoquinone or dinaphthenoquinone prepared in the oxidative coupling reaction. These disadvantages have been overcome by the use of the catalyst and process of the present invention as is described in detail hereinafter.

In accordance with the present invention, condensation products such as diphenoquinones, biphenols, dinaphthenoquinones and binaphthols are selectively prepared by contacting a substantially basic aqueous mixture of an "alkylphenol", an "alkoxyphenol" or a "1-naphthol" with oxygen or an oxygen-containing gas in the presence of a catalyst composition comprising a cupric or manganous complex of a keto alcohol. In a preferred embodiment the aqueous mixtures additionally contain a surfactant. The phenols or naphthols, metal chelate complexes, and alkaline materials which may be utilized are critical to the present invention and are described in detail below.

The phenols which may be employed in carrying out the present invention include both alkylphenols and alkoxyphenols. Specific phenols which may be utilized are described in detail below.

The alkylphenols which may be utilized are defined as any alkylphenol having at least two alkyl substituents, with the proviso that the phenols which have only two alkyl substituents must have the substituents in the ortho, ortho(2,6 in the formula below), or ortho, para (2,4 in the formula below) positions. These phenols are frequently referred to by the position of the alkyl substituent or substituents on the benzene ring as set forth in the following formula: ##STR3##

The process of the invention is applicable to any alkyl phenol having at least two alkyl substituents and steric properties such as to permit a coupling reaction. Thus if the para position is substituted with an alkyl group at least one ortho position must be unsubstituted. If one ortho and the para position are substituted, at least one of those substituents must be a tertiary alkyl group. If both ortho positions are substituted, the para position must be unsubstituted and no more than one meta position may be substituted with a tertiary alkyl group.

Thus, the alkylphenols will have one of the following formulas: ##STR4## wherein R.sub.2 and R.sub.6 are alkyl and R.sub.3, and R.sub.5 are hydrogen or alkyl, and R.sub.4 is hydrogen with the proviso that R.sub.3 and R.sub.5 cannot both be tertiary alkyl. ##STR5## wherein R.sub.2 and R.sub.4 are alkyl, provided that at least one of said alkyl groups is a tertiary alkyl and R.sub.3 and R.sub.5 are hydrogen or alkyl.

As used herein, the term alkyl refers to any monovalent radical derived from a saturated aliphatic hydrocarbon by removal of one hydrogen atom therefrom. The term includes both straight chain and branched chain materials containing from 1 to about 12 carbon atoms. Preferred results are achieved with alkylphenols wherein the alkyl substituent contains from 1 to 5 carbon atoms.

The alkyl substituents are referred to herein as primary, secondary or tertiary alkyl depending upon the greatest number of carbon atoms attached to any single carbon atom in the chain.

Condensation products of any alkylphenol coming within the above-mentioned definition may be prepared in accordance with the present invention. As is apparent from that definition, the alkylphenols include dialkylphenols, trialkylphenols, and tetraalkylphenols. Specifically, the phenols which may be utilized include the following:

Ortho, para-substituted phenols including for example 2,4-ditertiary-butylphenol, 2-methyl-4-tertiary-butylphenol, 2-tertiary-butyl-4-methylphenol, 2,4-ditertiary-amylphenol, 2,4-ditertiary-mexylphenol, 2-isopropyl-4-tertiary-butylphenol, 2-secondary-butyl- 4-tertiary-butylphenol, 2-tertiary-butyl-3-ethyl-4-methylphenol, 2,5-dimethyl-4-tertiary-butylphenol, and 2-methyl-3-ethyl-4-tertiary-butylphenol.

Representative 2,6-dialkylphenols (ortho, ortho-substituted) include, for example 2,6-xylenol, 2-methyl-6-butylphenol, 2,6-diisobutylphenol, 2-octyl-6-methylphenol, 2-isobutyl-6-dodecylphenol, 2-ethyl-6-methylphenol, 2-methyl-6-tertiary-butylphenol, 2,6-diisopropylphenol, 2,6-disecondary-butylphenol, 2,6-ditertiary-butylphenol, and 2-cyclohexyl-6-methylphenol.

When an ortho, para substituted alkylphenol is employed the coupling reaction proceeds in accordance with the following reaction resulting in the o, o'-coupled product. ##STR6## In this reaction each R represents hydrogen or an alkyl group as defined above depending upon whether di, tri, or tetra substituted alkylphenol is utilized.

Similarly, with the ortho, ortho-substituted alkylphenols, the reaction results in he p,p'-coupled product in accordance with the following reaction where R is hydrogen or alkyl depending upon which of the above-mentioned alkylphenols is used as the starting material. ##STR7##

It has also been found that alkoxyphenols may be oxidatively coupled in accordance with the present invention. These include among others 2,6-disubstituted phenols wherein at least one of the substituents is an alkoxy group containing up to about six carbon atoms such as methoxy, ethoxy, propoxy, butoxy and pentoxy. In addition to the 2,6-dialkoxyphenols, 2-alkyl-6-alkoxyphenols, wherein the alkyl groups are as defined above for the alkylphenols, may be utilized. As used herein the term alkoxyphenols is intended to include both types of compounds. These compounds may be represented by the following general formulas: ##STR8## wherein each R is any alkyl group as defined above for the alkylphenols or OR and R.sub.1 is either hydrogen or methyl, provided that the substituents adjacent to R.sub.1 and OH cannot both be tertiary alkyl or tertiary alkoxy. Representative alkoxyphenols which may be utilized include, for example, 2,6-dimethoxyphenol, 2,6-diethoxyphenol, 2,6-dibutoxyphenol, 2-methoxy-6-pentoxyphenol, 2-methyl-6-methoxyphenol and 2-ethyl-6-propoxyphenol, 2-methoxy-3-ethoxy-6-methylphenol.

When these phenols are utilized the reaction proceeds in accordance with the following representative reaction resulting in the p,p'-coupled material. ##STR9##

Mixtures of 2 different phenols may also be utilized. When this is done, there generally results a mixture of three different materials. Two of these are the products of the oxidative coupling of one molecule of one of the phenols with a second molecule of the same phenol. The third product is that resulting from the oxidative coupling of one molecule of the first phenol with one molecule of the second phenol. The products may be separated prior to use, as is well understood in the art.

Moreover, 1-naphthol and substituted 1-naphthols having at least 1 unsubstituted position ortho or para to the hydroxyl group may also be employed. The naphthols which may be coupled in accordance with the present invention are represented by the following general formula: ##STR10## wherein R.sub.2, R.sub.3 and R.sub.4 are hydrogen, alkyl containing from 1 to 5 carbon atoms, or alkoxy containing from 1 to 6 carbon atoms, provided that either or both R.sub.2 or R.sub.4 are hydrogen and R.sub.5, R.sub.6, R.sub.7, and R.sub.8 are hydrogen, alkyl containing from 1 to 5 carbon atoms or alkoxy containing from 1 to 6 carbon atoms provided that tertiary alkyl or tertiary alkoxy groups may not be attached to adjacent carbon atoms of the naphthalene molecule.

Representative naphthols which may be utilized include, for example, 1-naphthol, 2-methyl-1-naphthol, 2,3-dimethyl-1-naphthol, 4-ethyl-1-naphthol, and 2-methoxy-1-naphthol.

When a naphthol is employed, the coupling reaction takes place in accordance with the following general reaction depending upon the reactive positions -- i.e., those either ortho or para to the hydroxy group -- available. Thus, if R.sub.2 is hydrogen and R.sub.4 is alkyl or alkoxy ##STR11## Similarly, if R.sub.4 is hydrogen and R.sub.2 is alkyl or alkoxy, the coupling products are the 4,4'-binaphthol and the 4,4'-dinaphthenoquinone. When both R.sub.2 and R.sub.4 are hydrogen the products may be a mixture of the 2,2'-; 2,4'- and 4,4'-binaphthols and dinaphthenoquinones.

It should be specifically noted that the term "alkyl phenol" is hereby defined as only those alkyl phenols of formulas I and II and their isomers, the term "alkoxy phenol" is hereby defined as only those alkoxy phenols of formula III and their isomers and that the term "1-naphthols" is defined as only those 1-naphthols of formula IV and their isomers.

One of the essential components of the catalyst system of the present invention is a metal chelate of a keto alcohol. By the term metal chelate or complex of a keto alcohol is meant those complexes in which the metal cation group forms a bridge between the oxygen atoms of the keto and alcohol group. It is therefore important to appreciate that not all keto alcohol compounds will form complexes useful in the process of the present invention. For example a amino substituted keto alcohol may well have the amino group disposed such that the complex will be formed by bridging a keto group through the metal cation to the amine group rather than to the alcohol group. A more detailed description of chelates or complexes may be found in Chemistry of the Coordination Compounds, by J. C. Bailar, Reinhold Publishers, N.Y. 1956. A preferred complex is the cupric 3-acetyl-1-propanol complex.

Other keto alcohols useful to form complexes within the scope of the invention include the following: ##STR12##

Preferred keto alcohol useful in forming metal chelates include:

1. Aliphatic keto alcohols where at least one hydroxyl group is separated by 1-4 carbon atoms from the keto group. A representative ketone is fructose.

2. Cycloaliphatic keto alcohols where the keto and the hydroxyl group are separated by no more than 4 and preferably 2 carbon atoms. Representative structure include: ##STR13## where R is any inert substituent.

3. Aralkyl keto alcohols wherein the aryl group is pyridyl or phenyl. Representative structures include: ##STR14## wherein AR and AR' are ##STR15## and n is zero to 3.

The metal source for this complex is a cupric or manganous ion which, may be conveniently added to the chelating agent such as for example as acetates, formates or chlorides.

The metal chelates are prepared by reacting the keto alcohols with a source of the appropriate metal ions. The metal ion source may include various metal salts including halides, halo hydroxides, carboxylates, acetates, nitrates, sulfates, alkyl sulfates, aryl sulfates, carbonates, hydroxides or chlorates.

Some of the chelates are commercially available but those that are not may be prepared in any manner and the preparation thereof has not been found to be critical to the present invention. Similarly the ratio of keto alcohols to metal source has been found to be not narrowly critical. It should be noted however that if the ratio of keto alcohol to metal source is less than one, less complex is formed. The following three methods have been employed but other methods, which will be readily apparent to those skilled in the art from the description of the invention given herein, may also be utilized.

First, suitable amounts of the keto alcohols and a source of cupric or manganous ions may be combined in a suitable medium such as water and reacted to form the chelate. The chelate is prepared by simply stirring the solution for a period of time. If desired, heat may be applied to accelerate formation of the chelate.

Alternatively, the keto alcohols and the source of the metal ion may simply be combined and added to the reaction mixture wherein the chelate of the keto alcohol is formed. When this is done any basic compounds required to neutralize acidic by-products of the chelates forming reaction is also added directly to the reaction mixture.

Finally, the keto alcohol the source of metal ion, and any required basic compound may be added separately to the reaction medium and the complex formed in situ. As mentioned above, the method by which the metal complex is prepared has not been found to be critical to the present invention. However, further improved conversion results have been achieved when the source of metal ion and the keto alcohol are combined prior to addition to the reaction medium.

The amount of metal chelate employed has not been found to be narrowly critical to the process of the present invention. However, it is preferred to employ at least .02 mmols of the chelate per 100 mmols of alkylphenol. If less than this amount is used the reaction is slower and the yields are low. Similarly, the maximum amount of chelate employed is not generally greater than 1 mmol of the complex per 100 mmol of alkylphenol. At amounts much in excess of this the cost of the catalyst results in a uneconomic system. Higher levels of catalysts within the range of 0.02 to 1 mmol per 100 mmols of alkylphenols tend to favor diphenoquinone formation.

Although any of the above-mentioned metal chelate may be used, improved conversion results have been achieved with the cupric complexes.

As mentioned above, an advantage of the catalyst system and of the process of the present invention is that the reaction can be carried out in an aqueous medium instead of an organic solvent as has been used in prior art systems. However, it has not been found to be critical to the present invention to employ a water soluble metal complex. Thus, materials which are insoluble in water as well as those which are soluble may be utilized.

The catalyst composition of the present invention may also include, as an optional component thereof, a surfactant. The presence of a surfactant aids in the dispersion of the solid products thereby moderately improving conversion results. Additionally the surfactant allows for easier cleaing of large reactors. A variety of surfactants, also known as dispersants, are well known in the art and, as used herein, the term surfactant is intended to refer to organic compounds that contain in the molecular both hydrophobic and hydrophilic groups.

Surfactants are often classified, based on the hydrophilic (water liking) group which they contain, as either anionic, cationic, nonionic, or amphoteric. Any such surfactants may be employed in the present invention.

Surfactants are discussed in detail in the Encyclopedia of Chemical Technology, Kirk-Othmer, Second Edition Vol. 19 at pages 508-509, and any of the surfactants described therein may be utilized in the present invention.

The amount of surfactant employed has not been found to be critical to the utility of the catalyst system in carrying out the improved process of the present invention. However, if the use of a surfactant is desirable such as for example to increase the amount of carbon-carbon coupled product, there should be included in the reaction mixture at least about 0.2 mmol of surfactant per 400 mmol of phenol or naphthol. Preferred conversion results are achieved when the amount of surfactant employed is equal to from about 0.2 to about 0.6 mmol of surfactant per 400 mmol of phenol or naphthol. Additional amounts of the surfactant may be employed; however, the use of greater amounts of surfactant has usually not been found to significantly increase the total yield of product and it is, therefore, not generally desirable to include additional material in the reaction mixture. When a cupric alkyl sulfate as defined above is employed, both as the metal ion source and as the surfactant, the amount of said material employed is preferably equal to at least 0.2 mmol per 400 mmols of phenol or naphthol -- i.e., the preferred amount of metal compound plus the preferred amount of surfactant.

In accordance with the present invention, an alkaline material is also included in the catalyst composition to ensure that the pH during the reaction is maintained in the range of 7-9.5. It has been found that the use of an alkaline material to raise the pH in the present system increases the conversion to carbon-carbon coupled products and decreases the conversion to carbon-oxygen coupled products. The use of such a material to maintain the required pH also increases the rate of the oxidative coupling reaction and decreases the amount of the metal compound which must be utilized.

The alkaline material useful in achieving the pH of the reaction and the improved results of the present invention is selected from the group consisting of alkali metal hydroxides, alkali metal carbonates, and alkali metal bicarbonates. The alkaline material may be added ether as a single compound or as a mixture of compounds. Representative materials which may be employed include, for example, sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, lithium carbonate, sodium bicarbonate, rubidium carbonate, ribidium hydroxide, cesium bicarbonate, and cesium hydroxide.

The amount of alkaline material employed has not been found to be narrowly critical to the present invention as long as the required pH range is maintained. However, preferred results are achieved when the amount of said material is equal to at least about 3 millimols per 100 mmols of phenol or naphthol. Smaller amounts of alkaline material will normally result in a reaction pH of less than 7 and will normally cause a low molar conversion of starting compound to final product. A preferred pH range is from about 8 to 9.5. Increased amount of alkaline material may also be utilized in carrying out the present invention. It has been found that, for a given set of reaction conditions, increasing the amount of alkaline material increases the total conversion to carbon-carbon coupled products and the relative amount of diphenoquinone, or dinaphthenoquinone as compared to the amount of biphenol, or binaphthol. Thus, by varying the amount of alkaline material to vary th pH within the required pH range of 7-9.5, the type of product can be controlled.

Besides the selective production of carbon-carbon coupled products, an additional advantage of the catalyst system of the present invention is the ability to control the type of carbon-carbon coupled product produced. Thus, it is possible to prepare selectively either diphenoquinone or biphenol or dinaphthenoquinone or binaphthol, in accordance with the present invention. This result is achieved by controlling the amount of alkaline material included in the system. Generally, as the amount of alkaline material is increased, the percentage of quionine derivative produced also increases. Therefore to obtain larger amount of biphenolic product as opposed to quinone derivatives it is desirable to use sufficient alkaline material to raise the pH of the reaction material to a range of about 7.0-9.5, preferably 8.0-9.0. Higher pH values resulted in significant levels of oligomer formation. (carbon-oxygen coupled products.)

As mentioned above, an advantage of the catalyst system and process of the present invention is that it makes it possible for the oxidative coupling reaction to be carried out in an aqueous medium. The amount of water employed has not been found to be critical to the present invention and any amount of water which will permit the reaction mixture to be stirred during the course of the reaction may be employed. It should also be noted again that it is not essential that the various components be soluble in water and the term aqueous mixture as used herein is intended to include solutions, slurries, suspensions and the like.

The components of the reaction mixture may be combined in any suitable manner. Thus, the phenol or naphthol, surfactant, metal complex, alkaline material and water may be combined in any order in a suitable reaction vessel. Alternatively, and in a preferred method, the phenol or naphthol and optionally the surfactant are combined in water in a suitable reaction vessel, the mixture is stirred rapidly, preferably by utilizing a stainless steel impeller turning at 3000-8,000 RPM and an aqueous mixture of the metal salt compound and keto alcohol is added, followed by an aqueous solution of the alkaline material to maintain desired pH. In modifications of this procedure the metal complex may be added prior to heating or the metal complex and some alkaline material may particuarly at low pH ranges be combined prior to addition to the reaction mixture.

The reaction mixture comprising phenol or naphthol, water metal complex and alkaline material is contacted with a suitable oxidizing agent to convert the phenol or naphthol to the desired product. Oxidizing agents which may be employed in carrying out the present invention include oxygen either alone or as an oxygen-containing gas, such as air. The oxygen may be introduced into the reaction mixture either directly as oxygen gas or as an oxygen-generating material such as ozone, hydrogen peroxide, or an organic peroxide. The amount of oxygen utilized should be sufficient to obtain the desired conversion of the phenol or naphthol to the coupled product. To assure that sufficient oxygen is present, oxygen should be introduced into the reaction mixture continuously during the course of the reaction.

The reaction conditions -- i.e., time and temperature -- employed have not been found to be narrowly critical to the process of the present invention. Preferred results have been achieved when the reaction mixture is maintained at from about 80.degree. C. to 90.degree. C. during the course of the reaction. However, temperatures above and below this preferred range may be utilized. At lower temperatures the reaction rate is reduced and at temperatures below about 40.degree. C. it is so slow as to result in an uneconomic system. When operating at atmospheric pressure, as is desirable in some commercial operations, the practical upper limit on the temperature is 100.degree. C., the boiling point of the water.

If the reaction is conducted at increased oxygen pressure, the reaction time is decreased, the total yield of coupled product is usually increased, and the relative amount of quinone derivative is also usually increased.

The amount of time required for completion of the reaction depends on the temperature employed and other variables such as the pressure, concentration of phenol or naphthol and the amount of metal complex, surfactant if present, and alkaline material employed. However, it has been found that, when conducted at atmospheric pressure, the reaction is usually completed in 6 hours or less.

Although, as mentioned above, the process of the present invention results primarily in the production of carbon-carbon coupled products, there are also sometimes included in the solids removed from the reaction mixture the following: (a) unreacted phenol or naphthol, and (b) low molecular weight polyphenoxy ether. The polyphenoxy ether and phenol or naphthol may be removed by washing the solids with a solvent in which these materials are soluble, such as an aromatic hydrocarbon -- e.g., toluene, benzene, or a halogenated solvent -- e.g., methylene chloride. If it is desired to separate the materials from each other and from the solvent, this may be done by distillation.

If the reaction results in the mixture of biphenol and diphenoquinone, bisphenol and stilbene quinone, or binaphthol and dinaphthenoquinone, these materials may be separated by any method known in the art. An especially convenient way of separating the materials is to stir the solid product with a dilute aqueous solution of sodium hydroxide, which converts the biphenol or binaphthol to the sodium salt which is usually soluble in water. The insoluble diphenoquinone or dinaphthenoquinone may then be filtered off and the biphenol or binaphthol recovered by adding the aqueous solution of the sodium salt thereof to a dilute solution of a strong acid such as hydrochloric acid from which the biphenol or binaphthol precipitates. Alternatively, the entire product may be hydrogenated or chemically reduced and converted to only the biphenol or binaphthol.

The diphenoquinones and/or biphenols as well as the binaphthols, and dinaphthenoquinones produced in accordance with the present invention are suitable for any of the uses of these materials which have heretofore been described in the art. Thus, the diphenoquinones and dinaphthenoquinones may be used as inhibitors of oxidation, peroxidation, polymerization and gum formation in gasolines, aldehydes, fatty oils, lubricating oils, ethers and similar compounds as mentioned in U.S. Pat. No. 2,905,674 issued to Filbey. The diphenoquinones may also be hydrogenated, employing conventinal techniques, to yield the corresponding biphenol. The biphenols may be employed as stabilizers in gasoline and other petroleum products as described in U.S. Pat. No. 2,479,948 issued to Luten et al. They may also be utilized as intermediates in the manufacture of such useful products as sulfones, carbonates, and epoxy resins. In order to describe the present invention so it may be more clearly understood the following examples are set forth. These examples are given primarily for the purpose of illustration and any enumeration of detail contained therein should not be interpreted as a limitation on the concept of the present invention.

In the examples the products are analyzed for weight percent of the corresponding diphenoquinone. The amount of corresponding biphenol was arrived at by substracting the diphenoquinone amount from the theoretical 100% carbon-carbon coupled composition of the product.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.43 grams (4 mmols) of 96% 3-acetyl-1 -propanol,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; .2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline curciform stainless impeller turning at about 6,000 rpm there was added the stirred copper 3-acetyl-1-propanol complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 0.92 grams of sodium hydroxide (as 23 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 99+ mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 38.0 grams of the product was obtained as a green solid which contained 46.8 weight percent of the diphenoquinone and 53 weight percent of the biphenol.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.41 grams (4 mmols) of 99% 4-hydroxy-3-methyl-2 butanone,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper butanone complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 1.80 grams of sodium hydroxide (as 45 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, waShed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 99.sup.+ mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 35.7 grams of the product was obtained as a green solid which contained 48 weight percent of the diphenoquinone and 52 weight percent of the biphenol.

Into a first Flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.72 grams (4 mmols) of D-(-)-fructose,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper fructose complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 1.32 grams of sodium hydroxide (as 33 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the container. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that all of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 41.6 grams of the product was obtained as a green solid which contained 52.4 weight percent of the diphenoquinone and 47.6 weight percent of the biphenol.

Into a first flask there was added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.56 grams (4 mmols) of 97% o-hydroxyacetophenone,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper hydroxyacetophenone complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 2.28 grams of sodium hydroxide (as 57 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 97 mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 35.5 grams of the product was obtained as a green solid which contained 46.9 weight percent diphenoquinone and 53 weight percent of the biphenol.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.85 grams (4 mmols) of dl-benzoin,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper benzoin complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 1.08 grams of sodium hydroxide (as 27 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 91.6 mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 34.9 grams of the product was obtained as a green solid which contained 16.1 weight percent of the diphenoquinone and 83 weight percent of the biphenol.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.86 grams (4 mmols) of .alpha.- pyridoin,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; .2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper pyridoin complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 1.88 grams of sodium hydroxide (as 47 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 99.sup.+ mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 36.3 grams of the product was obtained as a green solid which contained 35.7 weight percent of the diphenoquinone and 64 weight percent of the biphenol.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

1.29 grams (4 mmols) of hydrindantin,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; .2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rmp there was added the stirred copper hydrindantin complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 2.36 grams of sodium hydroxide (as 59 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 99.sup.+ mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 35.6 grams of the product was obtained as a green solid which contained 44.2 weight percent of the diphenoquinone and 55 weight percent of the biphenol.

Into a first flask there were added;

0.5 grams (2 mmols) of manganous acetate Mn(OAc).sub.2.4H.sub.2 O,

0.41 grams (4 mmols) of 3-acetyl-1-propanol,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 48.8 grams (400 mmols) of 2,6-xylenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred manganous propanol complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 0.56 grams of sodium hydroxide (as 14 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause low bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 85.2 mol percent of the 2,6-xylenol had reacted.

The solid product was then washed with xylene to remove xylenol oligomer and dried at 60.degree. C. overnight. 23.5 grams of the product was obtained as a yellow solid which contained almost none of the diphenoquinone and 99.sup.+ weight percent of the biphenol.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.41 grams (4 mmols) of 96% acetyl-1-propanol,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 84.1 grams (400 mmols) of 98% 2.6-di-t-butylphenol.

To the resulting slurry whih was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper propanol complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 0.24 grams of sodium hydroxide (as 6 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that 84.0 mol percent of the butylphenol had reacted.

The solid product was then washed with xylene to remove oligomer and dried at 60.degree. C. overnight. 59.5 grams of the product was obtained as a red solid which contained mostly the diphenoquinone.

Into a first flask there were added;

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.72 grams 4 mmols) of D-(-)-fructose,

25 grams of ion exchanged water.

Into a 500 ml. flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 28.8 grams (200 mmols) of 1-naphthol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper fructose complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 1.04 grams of sodium hydroxide (as 26 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 1/2]hour, oxygen flow was reduced and maintained at a level sufficient to cause low bubbling in a bubbler attached to the top of the condenser. The tmperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatography. The analysis indicated that all of the 1-naphthol was reacted.

The solid product was then washed with xylene to remove oligomer and dried at 60.degree. C. overnight. 28.5 grams of the product was obtained as a dark solid which contained mostly carbon-carbon coupled product.

Into a first flask there were added:

0.4 grams (2 mmols) of cupric acetate Cu(OAc).sub.2.H.sub.2 O,

0.72 grams (4 mmols) of D-(-)-fructose,

25 grams of ion exchanged water.

Into a 500 ml flask, fitted with a gas addition tube, a condenser, a thermometer, and a stirrer capable of operating at speeds in the range of from about 3,000 to about 8,000 rpm there were added; 0.2 grams of sodium lauryl sulfate, 200 grams of deionized water and 41.2 grams (200 mmols) of 2,4-di-t-butylphenol.

To the resulting slurry which was stirred using a Labline cruciform stainless steel impeller turning at about 6,000 rpm there was added the stirred copper fructose complex solution prepared above. The resulting mixture was stirred for 5 minutes and heated to 80.degree. C. 1.04 grams of sodium hydroxide (as 26 ml of 1.0 N) solution was added during the course of the reaction to maintain the pH of the mixture at 9. The mixture was stirred under oxygen. The oxygen flow was rapid at the beginning to flush the system. After about 178 hour, oxygen flow was reduced and maintained at a level sufficient to cause slow bubbling in a bubbler attached to the top of the condenser. The temperature was controlled by a Therm-O-Watch temperature controller. The reaction mixture was stirred vigorously and maintained under oxygen for the prescribed reaction time of 6 hours.

The reaction slurry was cooled to room temperature acidified to pH 3 with HCl, filtered to remove the water phase, washed twice with 175 ml water. A sample of the solid was removed, dissolved in acetone and analyzed by gas-liquid chromatogrphy. The analysis indicated that all of the 1-naphthol was reacted

The solid product was then washed with xylene to remove oligomer and dried at 60.degree. C. overnight. 39.9 grams of the product was obtained as a yellow solid which contained almost none of the diphenoquinone and mostly carbon-carbon coupled product.