JP2008285447A - Method for producing diepoxy compound - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a safe, easy and new method for producing a diepoxy compound by a rapid reaction of a diolefin with an aqueous solution of hydrogen peroxide under a mild condition entirely without using a halogen compound at the epoxidation reaction. <P>SOLUTION: The method for producing the diepoxy compound comprises using a diolefin diester compound having a specific structure and the aqueous solution of the hydrogen peroxide as an oxidizer, and further using a tungsten compound and a quaternary ammonium hydrogen sulfate as catalysts, to epoxidize both of the two olefin positions of the diolefin. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention is useful as a raw material for surfactants and paints, as well as a diepoxy monomer containing two epoxy groups in the molecule that are expected to be widely used as raw materials or intermediates for various organic chemical products. In addition, the present invention relates to a method for completely epoxidizing two olefin sites existing in a halogen-free manner. In particular, the present invention relates to a novel process for producing a diepoxy compound in which diolefins and a hydrogen peroxide aqueous solution are reacted in the presence of tungsten oxide as a catalyst to epoxidize both double bonds.

In recent years, the development of better polymer materials has been promoted along with the increase in demand for precision machinery products. Epoxy resins have a wide range of industrial uses as thermosetting resins and other reactive resins, and have been studied and developed from various fields. Further, the cured epoxy resin can be imparted with heat resistance, transparency and properties as a useful electronic material, and is currently widely used in the industry as a component or intermediate for coatings, adhesives, inks, and sealants. In particular, diepoxy compounds containing two epoxy groups in the molecule are attracting attention as a new raw material for epoxy resins because they can synthesize various oligomers.

Here, the diepoxy compound containing two epoxy groups in the molecule refers to those obtained by epoxidizing both chain and cyclic olefins among the corresponding diolefins. The technology to epoxidize (diepoxidize) two double bonds (olefins) with two different reactivities with high efficiency may be low reactivity or limited to a certain type of structure. Many.

  Conventionally, peracids such as peracetic acid and perbenzoic acid have been used as oxidants used for diepoxidation of olefins (see Patent Document 1-3, Patent Document 5, and Non-Patent Document 1). Since two equivalents of the agent-derived acid are generated, there is a problem such as corrosion of the apparatus. Furthermore, the oxidant-derived acid easily reacts with the epoxy group to open the epoxy group, so that the diepoxy compound cannot be obtained in high purity and high yield (see Patent Document 2). A diepoxidation method that strictly removes moisture and suppresses side reactions has also been reported (see Patent Document 3), but it uses organic solvents in large quantities, and is disadvantageous for industrialization from the viewpoint of reaction operation and cost. . On the other hand, hydrogen peroxide water is inexpensive and non-corrosive, has no by-product after the reaction or is water, has a low environmental load, and is an excellent oxidizing agent for industrial use.

As a method for producing a compound by epoxidation of diolefins using hydrogen peroxide solution as an epoxidizing agent, (1) Diolefin epoxidation reaction using quaternary ammonium phosphorus tungstate as a catalyst (see Non-Patent Document 2) (2) A method of epoxidizing a diolefin using an organic rhenium oxide as a catalyst (see Non-Patent Document 3) has been reported. However, in the above method (1), although the reaction conversion rate and diepoxidation selectivity of diolefin are good, a highly toxic reaction solvent is necessary (chloroform and benzene), so the environmental burden is large and there is a problem with safety. is there. In the method (2), the substrate dependency is high and the organic rhenium oxide is very expensive, so that it is industrially disadvantageous from the viewpoint of cost.

On the other hand, it has been pointed out that in the epoxidation reaction of olefins, the reaction is greatly hindered by the presence of halogen ions in the reaction system, resulting in a decrease in reaction yield and catalytic activity. In order to improve the rate and catalytic activity, ammonium hydrogen sulfate and alkyl sulfate are used without using ammonium halide (Non-patent Document 4).
Accordingly, there is a strong demand for the development of a method for producing a diepoxy compound selectively from diolefins in a high yield and at a low cost by a simple operation without using an organic solvent under mild conditions.

JP 2006-52177 A JP 2006-188476 A JP 2004-182648 A JP-A-5-59030 J. Am. Chem. Soc., 1959, 81, 3350. J. Org. Chem., 1996, 61, 5307. TetrahedronLett., 1999, 40, 2997. OrganicProcess Research & Development, 2004, 8, 524. Chem. Commun., 2003, 16, 1977.

  It is an object of the present invention to provide a new process for producing a safe and easy diepoxy compound by a rapid reaction of a diolefin and an aqueous hydrogen peroxide solution without using any halogen compound in an epoxidation reaction under mild conditions. It is what.

  In order to solve the above-mentioned problems, the present inventors have carried out a reaction between a specific diolefin and a hydrogen peroxide solution using a quaternary ammonium hydrogen sulfate and a tungsten compound as a catalyst. Both of these olefin moieties were epoxidized with high efficiency, and a diepoxy compound containing two types of epoxy groups in the molecule was found to be selectively produced in high yield, and the present invention was completed.

According to the present invention, the following inventions are provided.
(1) General formula (B)

(In the formula, R ¹ and R ² are each independently the same or different, and are a hydrogen atom, a hydroxy group, a halogen atom, a carboxyl group, an alkyl group having 1 to 4 carbon atoms, an alkoxy group having 1 to 4 carbon atoms, carbon A cycloalkyl group having 3 to 7 carbon atoms, an aryl group, an aralkyl group, an acyl group or an acyloxy group, wherein R ³ and R ⁴ are independently the same or different, and an alkyl group having 1 to 4 carbon atoms or 3 carbon atoms; -7 represents a cycloalkyl group, an aryl group or an aralkyl group.) By the oxidation reaction of a diolefin diester compound represented by the following general formula (A)

(In the formula, R ¹ and R ² are each independently the same or different, and are a hydrogen atom, a hydroxy group, a halogen atom, a carboxyl group, an alkyl group having 1 to 4 carbon atoms, an alkoxy group having 1 to 4 carbon atoms, carbon A cycloalkyl group having 3 to 7 carbon atoms, an aryl group, an aralkyl group, an acyl group or an acyloxy group, wherein R ³ and R ⁴ are independently the same or different, and an alkyl group having 1 to 4 carbon atoms or 3 carbon atoms; In the step of producing a diepoxy compound represented by -7, a hydrogen peroxide aqueous solution is used as an oxidizing agent and a tungsten compound and hydrogen sulfate quaternary are used as a catalyst. A method for producing diepoxy compounds in which ammonium is used to epoxidize two olefins.
(2) The process as described above, wherein the reaction is carried out without using any halogen.

The method for producing diepoxy compounds provided by the present invention is useful as a raw material for various polymers such as agrochemical / pharmaceutical intermediates, plasticizers, adhesives, paint resins, and sealants, and is useful in various industrial fields including chemical industries. The diepoxy compound, which is a simple substance, can be produced safely and efficiently by the reaction of the corresponding diolefins and aqueous hydrogen peroxide solution. In addition, since this production method is halogen-free, the burden on the environment can be greatly reduced, and the performance of various polymers can be expected to be improved because there is no possibility that halogen will be mixed into various polymers as final products. In addition, since this production method does not use an acid or a base except for a post-treatment operation, it can be produced at low cost, high efficiency, and high selectivity.

  The raw diolefin compound in the present invention is, for example, the following general formula (B)

(In the formula, R ¹ and R ² are each independently the same or different, and are a hydrogen atom, a hydroxy group, a halogen atom, a carboxyl group, an alkyl group having 1 to 4 carbon atoms, an alkoxy group having 1 to 4 carbon atoms, carbon A cycloalkyl group having 3 to 7 carbon atoms, an aryl group, an aralkyl group, an acyl group or an acyloxy group, wherein R ³ and R ⁴ are independently the same or different, and an alkyl group having 1 to 4 carbon atoms or 3 carbon atoms; A cycloalkyl group, an aryl group, or an aralkyl group of ˜7).

Specific examples of the diolefin compound include, for example, dimethyl 4- (4-methyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate, diethyl 4- (4-methyl-3-pentenyl) − 4-cyclohexene-1,2-dicarboxylate, dipropyl 4- (4-methyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate, dibutyl 4- (4-methyl-3-pentenyl) − 4-cyclohexene-1,2-dicarboxylate, diphenyl 4- (4-methyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate, dimethoxyl 4- (4-methyl-3-pentenyl) − 4-cyclohexene-1,2-dicarboxylate, dimethyl 4- (4-ethyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate, dimethyl 4- (4-ethyl-3-hexenyl)- 4-cyclo Hexene-1,2-dicarboxylate, ethylmethyl 4- (4-ethyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate, and the like.

  The starting diolefin compound in the present invention is preferably dimethyl 4- (4-methyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate, diethyl 4- (4-methyl-3-pentenyl). -4-cyclohexene-1,2-dicarboxylate, and the like.

The amount of aqueous hydrogen peroxide used in the production method of the present invention is not limited, and the reaction to diolefins occurs depending on the amount used, but is generally 1.5 to 5.0 equivalents, preferably Is selected from the range of 2.1 to 2.5 equivalents.

The concentration of the aqueous hydrogen peroxide solution used in the production method of the present invention is not limited, and the reaction to diolefins occurs depending on the concentration, but generally 1 to 80%, preferably 10 to 60%. Selected from a range.

Examples of the quaternary ammonium hydrogen sulfate include tetrahexyl ammonium hydrogen sulfate, tetraoctyl ammonium hydrogen sulfate, methyl trioctyl ammonium hydrogen sulfate, tetrabutyl ammonium hydrogen sulfate, ethyl trioctyl ammonium hydrogen sulfate, cetylpyridinium hydrogen sulfate, methyl Examples thereof include methyltrioctylammonium sulfate and bis (methyltrioctylammonium sulfate), and tetrahexylammonium hydrogensulfate, tetraoctylammonium hydrogensulfate, methyltrioctylammonium hydrogensulfate and the like are preferable. These quaternary ammonium hydrogen sulfates may be used alone or in combination of two or more. The amount to be used is selected from the range of 0.0001 to 10 mol%, preferably 0.01 to 5 mol%, based on the diolefin as a substrate.

The tungsten compound is a compound that generates a tungstate anion in water. For example, tungstic acid, tungsten trioxide, tungsten trisulfide, phosphotungstic acid, ammonium tungstate, potassium tungstate dihydrate, sodium tungstate diwater Examples of the hydrate include tungstic acid, tungsten trioxide, phosphotungstic acid, sodium tungstate dihydrate, and the like. The amount used is selected from the range of 0.0001 to 20 mol%, preferably 0.01 to 10 mol%, based on the diolefins of the substrate. It should be noted that this type of catalyst may be modified by using additives such as phosphoric acid, polyphosphoric acid, aminomethylphosphonic acid, sodium phosphate.

In the production method of the present invention, the reaction is usually performed in the range of 30 to 100 ° C, preferably in the range of 50 to 80 ° C.

The reaction time in the production method of the present invention depends on the reaction temperature and cannot be determined generally, but is usually in the range of 30 minutes to 12 hours, preferably in the range of 2 to 5 hours.

The diepoxy compound thus obtained has the general formula (A)

(In the formula, R ¹ and R ² are each independently the same or different, and are a hydrogen atom, a hydroxy group, a halogen atom, a carboxyl group, an alkyl group having 1 to 4 carbon atoms, an alkoxy group having 1 to 4 carbon atoms, carbon A cycloalkyl group having 3 to 7 carbon atoms, an aryl group, an aralkyl group, an acyl group or an acyloxy group, wherein R ³ and R ⁴ are independently the same or different, and an alkyl group having 1 to 4 carbon atoms or 3 carbon atoms; A cycloalkyl group, an aryl group, or an aralkyl group of ˜7).

Specific examples of the diepoxy compound include, for example, dimethyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate. , Diethyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate, dipropyl 1- (2- (3, 3-dimethyloxirane-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate, dibutyl 1- (2- (3,3-dimethyloxirane-2-yl) ethyl ) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate, diphenyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0 ] Heptane-3,4-dicarboxylate, dimethoxyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7 Xabicyclo [4.1.0] heptane-3,4-dicarboxylate, dimethyl 1- (2- (3,3-methylethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3 , 4-dicarboxylate, dimethyl 1- (2- (3,3-diethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate, ethyl methyl 1 -(2- (3,3-dimethyloxirane-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate, and the like.

  The diepoxy compound in the present invention is preferably dimethyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate, And diethyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate.

  The target diepoxy compound thus produced can be taken out by a usual method such as distillation after separating and concentrating the organic layer from the mixed solution after completion of the reaction.

  The solvent used in this reaction is selected from those which do not contain halogen and are not oxidized under the conditions of the present invention. Examples thereof include aromatic solvents such as toluene and xylene, hydrocarbon solvents such as hexane, heptane and cyclohexane, and ether solvents such as tetrahydrofuran and dioxane.

  In the production method of the present invention, the concentration of the diolefin as a substrate is usually 0.01 mol% or more, preferably 0.1 to 2.0 mol%, based on the solvent.

Next, the present invention will be described in detail with reference to examples.
Examples described below are examples of typical compounds for facilitating the understanding of the present invention, and the present invention is not limited thereto.

Example 1
In a test tube equipped with a magnetic stir bar, sodium tungstate dihydrate (11.8 mg, 0.0357 mmol), methyl trioctylammonium hydrogen sulfate (8.30 mg, 0.0178 mmol), 445 mg of 30% aqueous hydrogen peroxide solution, 3.9 mmol), dimethyl 4- (4-methyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate (500 mg, 1.78 mmol) and toluene (10 ml) until homogeneous solution The mixture was stirred at room temperature for 15 minutes (stirring speed: 1000 rpm). Then, the temperature was raised to 70 ° C. and reacted for 4.0 hours (stirring speed: 1000 rpm). The reaction solution was cooled to room temperature and then stirred for about 3 minutes while slowly dropping a saturated aqueous solution of sodium thiosulfate (5 ml) to completely stop the reaction. Thereafter, organic substances were extracted with ethyl acetate (10 ml × 5 times). After distilling off the solvent from the obtained solution, ¹ H-NMR was measured, and the conversion rate of dimethyl 4- (4-methyl-3-pentenyl) -4-cyclohexene-1,2-dicarboxylate as a raw material was 99. % Dimethyl 1- (2- (3,3-dimethyloxiran-2-yl) ethyl) -7-oxabicyclo [4.1.0] heptane-3,4-dicarboxylate which is a diepoxy compound The yield was 92% (internal standard: biphenyl).

Claims (2)

General formula (B)

(In the formula, R ¹ and R ² are each independently the same or different, and are a hydrogen atom, a hydroxy group, a halogen atom, a carboxyl group, an alkyl group having 1 to 4 carbon atoms, an alkoxy group having 1 to 4 carbon atoms, carbon A cycloalkyl group having 3 to 7 carbon atoms, an aryl group, an aralkyl group, an acyl group or an acyloxy group, wherein R ³ and R ⁴ are independently the same or different, and an alkyl group having 1 to 4 carbon atoms or 3 carbon atoms; -7 represents a cycloalkyl group, an aryl group or an aralkyl group.) By the oxidation reaction of a diolefin diester compound represented by the following general formula (A)

(In the formula, R ¹ and R ² are each independently the same or different, and are a hydrogen atom, a hydroxy group, a halogen atom, a carboxyl group, an alkyl group having 1 to 4 carbon atoms, an alkoxy group having 1 to 4 carbon atoms, carbon A cycloalkyl group having 3 to 7 carbon atoms, an aryl group, an aralkyl group, an acyl group or an acyloxy group, wherein R ³ and R ⁴ are independently the same or different, and an alkyl group having 1 to 4 carbon atoms or 3 carbon atoms; In the step of producing a diepoxy compound represented by -7, a hydrogen peroxide aqueous solution is used as an oxidizing agent and a tungsten compound and hydrogen sulfate quaternary are used as a catalyst. A method for producing diepoxy compounds in which ammonium is used to epoxidize two olefins. The process according to claim 1, wherein the reaction is carried out without using any halogen.