JP2011105667A - Method for producing phenyl ester - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a phenyl ester in good yield by the esterification reaction of phenol with a carboxylic acid represented by general formula (I). <P>SOLUTION: The method for producing the phenyl ester including esterifying the phenol with the carboxylic acid represented by general formula (I): CH<SB>2</SB>=C(-R<SB>1</SB>)-CO<SB>2</SB>H (I) (wherein, R<SB>1</SB>is hydrogen or methyl) by an acid catalyst in a solvent forming an azeotrope with water includes adding each 2-50 mol% of boric acid and a 2,2-dialkylmalonic acid represented by general formula (II): R<SB>2</SB>-(R<SB>3</SB>-)C(-COOH)<SB>2</SB>(II) (wherein, R<SB>2</SB>and R<SB>3</SB>are each linear or branched 2-10C alkyl) based on the carboxylic acid represented by general formula (I) to the reaction system of the esterification reaction. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a method for producing a phenyl ester from phenol and a specific carboxylic acid by an esterification reaction with high yield.

  In general, the reaction for directly producing a phenyl ester from carboxylic acid such as acrylic acid or methacrylic acid and phenol has an equilibrium constant ≦ 0.01. Is difficult. For this reason, when synthesizing the phenyl ester, 1) a method using an active acylating agent such as an acid chloride disclosed in Patent Documents 1 to 4 and an acid anhydride disclosed in Patent Document 5 2) A method using a dehydrating agent such as DCC or polyphosphoric acid is considered desirable. However, these methods are expensive due to the use of expensive raw materials. For this reason, various studies have been made on esterification methods using an acid catalyst such as sulfuric acid or an ion exchange resin as a catalyst, and toluene or xylene as a dehydrating solvent.

  Patent Documents 6 and 7 disclose a method for producing a phenyl ester using a strongly acidic ion exchange resin as a reaction catalyst. However, in this method, the reaction conversion rate is as low as about 50%, and the selectivity is not satisfactory as about 80%. For this purpose, after completion of the reaction, toluene as a dehydrating solvent is recovered, and then raw methacrylic acid and phenol are recovered by distillation. Next, after the crude phenyl methacrylate is distilled off, it is dissolved in a hydrocarbon solvent such as hexane, and acrylic acid and phenol are neutralized and washed with a weak alkali. Thereafter, a complicated process of distilling off the hydrocarbon solvent and obtaining the purified phenyl ester by distillation must be performed.

  Non-Patent Documents 1 and 2 report a method of synthesizing a boric acid ester from boric acid and an aromatic alcohol and synthesizing a carboxylic acid ester of an aromatic alcohol by substituting the carboxylic acid. However, in this method, since boric acid is used stoichiometrically, the treatment of boron in the waste liquid becomes a problem.

  Patent Documents 8 and 9 and Non-Patent Document 3 report examples in which a sulfuric acid / boric acid complex is used when an aliphatic or aromatic carboxylic acid is reacted with phenol by dehydration esterification. In this method, some carboxylic acid phenyl esters are obtained in a yield of 90% or more. However, since the reaction temperature is high and the reaction time is long, it is difficult to say that it is a general phenyl ester synthesis method.

  As catalysts other than acids, Patent Document 10 discloses a tin compound, Patent Document 11 discloses a lead compound, and Patent Document 12 discloses a method of synthesizing a phenyl ester using a catalyst in which a tin compound and a lead compound are mixed. However, none of the yields has reached a satisfactory level.

  Recently, Patent Document 13 uses a hydrolyzable tetravalent zirconium compound and / or a tetravalent hafnium compound and any one or more acidic compounds of sulfonic acid, heteropolyacid and super strong acid as a catalyst. The manufacturing method of the aromatic ester compound characterized by this is disclosed. Patent Document 14 discloses a method for esterifying phenols, which is a heteropolyacid carrier or a heteropolyacid salt carrier. Further, Patent Document 15 discloses a method for esterifying phenols using a catalyst comprising a super strong acid and / or heteropoly acid and / or heteropoly acid salt and a boronic acid and / or boronic acid ester and / or boron oxide. Yes. However, none of these methods is an industrial esterification method with a low yield.

Japanese Patent Publication No. 50-23019 JP-A 62-63541 JP-A-5-345743 JP-A-2005-112864 JP 2000-191590 A Japanese Patent Laid-Open No. 62-132840 JP-A-63-57554 US Pat. No. 3,772,389 JP 60-258144 A Japanese Patent Laid-Open No. 2-115141 Japanese Patent Laid-Open No. 2-117645 Japanese Patent Laid-Open No. 2-124849 JP 2006-83068 A JP 2006-136842 A JP 2006-218358 A

Hirao et al., Journal of Chemical Society of Japan (Industrial Chemistry), 56, 371, 1953 Hirao et al., Japanese Pharmaceutical Journal, 74, 1073, 1954 W. Williams, Lawrence. Jr, Tetrahedron Letters, 3453, 1971

  An object of this invention is to provide the method of manufacturing a phenyl ester from a phenol and specific carboxylic acid with a sufficient yield by esterification reaction.

The method for producing a phenyl ester according to the present invention includes:
In a solvent azeotropic with water, phenol and the following general formula (I)

(In formula I, R ₁ represents hydrogen or a methyl group)
A process for producing a phenyl ester, which is esterified with an acid catalyst,
In the reaction system of the esterification reaction, boric acid and the following general formula (II)

(In Formula II, R ₂ or R ₃ represents a linear or branched alkyl group having 2 to 10 carbon atoms)
2 to 50 mol% of the 2,2-dialkylmalonic acid represented by the formula (I) is added to the carboxylic acid represented by the general formula (I).

  According to the present invention, the phenyl ester of the carboxylic acid represented by the general formula (I) can be produced with high yield.

  The present inventors diligently studied a method for efficiently producing a phenyl ester from a phenol and a carboxylic acid by using a method of inexpensive esterification, and in the process, the boric acid-sulfuric acid complex disclosed in Patent Document 8 was catalyzed. The method for synthesizing aromatic esters was discussed. As a result, the mechanism of the esterification reaction using boric acid is that boric acid and carboxylic acid are converted into anhydrides with a sulfuric acid catalyst, and the acid anhydride reacts with aromatic alcohols to synthesize esters, and the carboxylic acid used. It was assumed that free carboxylic acid would react with boric acid as follows:

  According to this assumption, when the energy state and activation energy of the reaction intermediate are calculated using the computational chemistry method, the activation energy is large in the method using boric acid as it is, and the energy state of the reaction system is higher than the raw material system. Therefore, it was proved difficult to increase the yield.

  Therefore, in order to obtain phenyl esters efficiently, we investigated the intermediate model of boric acid and carboxylic acid using detailed quantum chemical calculations. As a result, by using a boric acid derivative in which a part of boric acid is blocked in the form of a cyclic acid anhydride with a carboxylic acid that is not easily involved in the esterification reaction, the energy state of the reaction system is lower than that of the raw material system, and further It has been found that the activation energy to the body is lower than that of the system using boric acid alone, and the present invention has been achieved.

  That is, the method for producing a phenyl ester according to the present invention is a method for producing a phenyl ester in which a phenol and a carboxylic acid represented by the general formula (I) are esterified with an acid catalyst in a solvent azeotropic with water. In the esterification reaction system, boric acid and the 2,2-dialkylmalonic acid represented by the general formula (II) are each 2 to 50 mol% based on the carboxylic acid represented by the general formula (I). It is characterized by adding.

  The present invention will be described in detail below.

In the carboxylic acid represented by the general formula (I), R ₁ represents hydrogen or a methyl group.

In the 2,2-dialkylmalonic acid represented by the general formula (II), R ₂ or R ₃ represents a linear or branched alkyl group having 2 to 10 carbon atoms. Examples of the linear or branched alkyl group having 2 to 10 carbon atoms include ethyl group, propyl group, isopropyl group, butyl group, isobutyl group, pentyl group, isopentyl group, hexyl group, octyl group, nonyl group, decyl group, etc. Is mentioned. Considering practically, it is preferable that it is C3-C5. R ₂ or R ₃ is preferably a branched alkyl group. When R ₂ or R ₃ is a branched alkyl group, the boric acid derivative blocked with 2,2-dialkylmalonic acid is difficult to be hydrolyzed, and the stability of the intermediate as a catalyst tends to be good. . As the branched alkyl chain, an isopropyl group and an isobutyl group are more preferable.

R ₂ or R ₃ may be the same group or different groups. From the viewpoint of the synthesis of 2,2-dialkylmalonic acid, R ₂ or R ₃ are preferably the same group.

  As the solvent, any solvent can be used as long as it can be azeotroped with water. However, since it is preferable to set the reaction temperature to 100 ° C. or higher for producing the phenyl ester, generally a higher azeotropic point is preferable unless a pressurized reactor is used. For example, it is preferable to use an aromatic solvent such as toluene, xylene, ethylbenzene or cumene. From the viewpoint of cost, toluene and xylene are more preferable.

  As the acid catalyst, any acid may be used as long as it can be used for the esterification reaction. However, sulfuric acid and strong acid ion exchange resin are preferable for the esterification of phenol. The usage-amount of an acid catalyst can be arbitrarily set between 0.1-20 mol% with respect to the carboxylic acid shown by the said general formula (I). However, if the amount is too small, the reaction time becomes long, and if the amount is too large, side reactions increase, so 1 to 10 mol% is preferable, and 3 to 7 mol% is more preferable.

  In the present invention, 2,2-dialkylmalonic acid represented by the general formula (II) is added to the esterification reaction system in an amount of 2 to 50 mol% based on the carboxylic acid represented by the general formula (I). . If it is less than 2 mol%, the reaction rate becomes slow and side reactions occur. On the other hand, if the amount exceeds 50 mol%, 2,2-dialkylmalonic acid represented by the general formula (II) is generally expensive and expensive, so that anhydrous 2,2-dialkylmalonic acid and boric acid are anhydrous. It is necessary to devise measures to reduce costs, such as collecting things. However, adding such a process complicates the process and increases the cost. Preferably, it is 3-7 mol%.

  In the present invention, boric acid is also added in an amount of 2 to 50 mol% with respect to the carboxylic acid represented by the general formula (I) in the esterification reaction system. If it is less than 2 mol%, the reaction rate becomes slow and side reactions occur. On the other hand, if it exceeds 50 mol%, it is necessary to devise measures to reduce the cost, such as recovering 2,2-dialkylmalonic acid and boric anhydride. However, adding such a process complicates the process and increases the cost. Preferably, it is 3-7 mol%.

  As described above, if 2,2-dialkylmalonic acid and boric acid are used within the range of 2 to 50 mol%, the effects of the present invention can be obtained even if used in any proportion. It is preferable to use it.

  The amount of the phenol used may be more or less than the equivalent amount with respect to the carboxylic acid represented by the general formula (I). However, considering the efficiency of the reaction, the purification step after the reaction, etc., the amount of phenol is preferably between 80 and 99 mol% with respect to the charged amount of the carboxylic acid represented by the general formula (I), More preferably, it is 85 mol% to 95 mol%.

  Although the reaction temperature depends on the acid concentration, it is preferably carried out at 100 ° C. or higher in order to set the reaction time to about 10 to 24 hours. If the reaction temperature is less than 100 ° C., the reaction rate becomes extremely slow, which is not practical reaction conditions. However, since the carboxylic acid of the general formula (I) may be polymerized when reacted at a high temperature, it is preferable to perform the esterification reaction at 140 ° C. or lower.

  In order to prevent polymerization of the carboxylic acid represented by the general formula (I) or the synthesized phenyl ester, it is preferable to add a polymerization inhibitor in the reaction system. The kind of polymerization inhibitor is not specifically limited, The 1 type may be used or 2 or more types may be used. Examples of the polymerization inhibitor include hydroquinone, p-methoxyphenol, 2,4-dimethyl-6-tert-butylphenol, 2,6-di-tert-butyl-4-methylphenol, tert-butyl-catechol, 2, Such as 6-di-tert-butyl-4-methylphenol, pentaerythritol, tetrakis (3,5-di-tert-butyl-4-hydroxyhydrocinnamate), 2-sec-butyl-4,6-dinitrophenol Phenol compounds, N, N-diisopropylparaphenylenediamine, N, N-di-2-naphthylparaphenylenediamine, N-phenylene-N- (1,3-dimethylbutyl) paraphenylenediamine, N, N′-bis (1,4-Dimethylphenyl) -paraphenylenediamine, N- (1, Amine compounds such as -dimethylphenyl) -N'-phenyl-paraphenylenediamine, 4-hydroxy-2,2,6,6-tetramethylpiperidine-N-oxyl, 4-benzoyloxy-2,2,6, N-oxyl compounds such as 6-tetramethylpiperidine-N-oxyl and bis (1-oxyl-2,2,6,6-tetramethylpiperidin-4-yl) sebacate, copper, copper (II) chloride, chloride Examples thereof include metal compounds such as iron (III). Although the usage-amount of a polymerization inhibitor should just be determined suitably, 100 ppm or more is preferable with respect to the carboxylic acid shown by the said general formula (I) to be used, and 500 ppm or more is more preferable in order to acquire sufficient polymerization prevention effect. On the other hand, from the viewpoint of cost, the amount of the polymerization inhibitor used is preferably 10,000 ppm or less, and more preferably 5000 ppm or less in consideration of product coloring, convenience in use, and the like.

  It is also preferable to bubble an oxygen-containing gas such as air in the esterification reaction liquid in order to prevent polymerization. The amount of oxygen-containing gas such as air to be introduced can be set in a timely manner so as to obtain a desired polymerization preventing effect. For example, when air is used as the oxygen-containing gas, it is preferably bubbled at 0.5 to 3.0 ml / min with respect to 1 mol of the carboxylic acid represented by the general formula (I) used. It is particularly preferable to add a polymerization inhibitor to the esterification reaction liquid and perform the reaction while introducing an oxygen-containing gas such as air into the reaction liquid from the viewpoint of amplification of the polymerization prevention effect.

  After the esterification reaction, the reaction solution is distilled and purified as it is, or the reaction solution is treated by a usual post-treatment method, such as adding water to the two-phase system and then extracting and purifying the phenyl ester. By doing so, a purified phenyl ester can be obtained.

  Hereinafter, the present invention will be described in more detail with reference to examples.

Example 1
To a four-necked flask with Dean Stark, 0.24 mol of methacrylic acid and 0.20 mol of phenol were dissolved in 10 mol of xylene and added. Further, 4-hydroxy-2,2,6,6-tetramethylpiperidine-N-oxyl 0.3 mmol and hydroquinone 0.45 mmol were added as polymerization inhibitors. Furthermore, 0.01 mol of sulfuric acid was added as an esterification catalyst, 0.01 mol of boric acid and 0.01 mol of diisopropylmalonic acid were added as additives, and the bath temperature was raised to 140 ° C. while aeration. The reaction was carried out while controlling the degree of vacuum of the reaction system so as to keep the reaction temperature at 130 ° C. and refluxing dehydration.

  For analysis of the product, the peak areas of methacrylic acid, phenol, and phenyl methacrylate were measured by GLC (GC, gas chromatography). For convenience, conversion rate = 100 × (area of phenyl methacrylate) / (area of phenol + It was calculated by the area (%) of phenyl methacrylate.

The analysis conditions of GLC are as follows.
Column DB-1 × 30m
Carrier gas Helium detector FID
Column temperature 50 ° C. × 5 minutes, temperature increase 10 ° C./minute, 220 ° C. × 10 minutes inlet temperature 250 ° C.
Detector temperature 250 ° C.

  The conversion reached 85% after 17 hours of reaction.

(Comparative Example 1)
The same procedure as in Example 1 was conducted except that 0.015 mol of sulfuric acid was added as the esterification catalyst, 0.015 mol of boric acid was added as an additive, and diisopropylmalonic acid was not added. The conversion was 75% after 9 hours of reaction.

(Comparative Example 2)
The same procedure as in Example 1 was performed except that 0.004 mol of boric acid was added as the additive and diisopropylmalonic acid was not added. The conversion for 17 hours was 64%.

(Example 2)
The same procedure as in Example 1 was performed except that 0.01 mol of diethylmalonic acid was added instead of 0.01 mol of diisopropylmalonic acid. After 18 hours of reaction, the conversion reached 83%.

(Example 3)
The same procedure as in Example 1 was performed except that 0.01 mol of dihexylmalonic acid was added instead of 0.01 mol of diisopropylmalonic acid. The conversion reached 80% after 17 hours of reaction.

Example 4
Instead of 0.24 mol of methacrylic acid, 0.24 mol of acrylic acid was added, the bath temperature was raised to 130 ° C., and the pressure reduction of the reaction system was controlled to maintain the reaction temperature at 120 ° C. The reaction was performed in the same manner as in Example 1 except that the reaction was performed while dehydrating. The conversion reached 80% after 18 hours of reaction.

(Comparative Example 3)
The same procedure as in Example 1 was performed except that 0.002 mol of boric acid was added as the additive and 0.002 mol of diisopropylmalonic acid was added. The conversion for 19 hours was 65%.

  The results of the examples and comparative examples are shown in Table 1.

Claims (1)

In a solvent azeotropic with water, phenol and the following general formula (I)

(In formula I, R ₁ represents hydrogen or a methyl group)
A process for producing a phenyl ester, which is esterified with an acid catalyst,
In the reaction system of the esterification reaction, boric acid and the following general formula (II)

(In Formula II, R ₂ or R ₃ represents a linear or branched alkyl group having 2 to 10 carbon atoms)
A method for producing a phenyl ester, wherein 2 to 50 mol% of a 2,2-dialkylmalonic acid represented by the formula (I) is added to the carboxylic acid represented by the general formula (I).