阅读说明：本技术 (甲基)丙烯酸酯的制备 (Preparation of (meth) acrylic esters ) 是由 M·特雷斯科 S·拜尔 T·舒茨 S·克里尔 于 2019-07-31 设计创作，主要内容包括：本发明涉及一种由(甲基)丙烯酸酐制备(甲基)丙烯酸酯的方法。(The invention relates to a method for producing (meth) acrylic esters from (meth) acrylic anhydride.)

1. A process for the preparation of (meth) acrylic esters, said process comprising at least the following step (a):

(a) reaction between a (meth) acrylic anhydride of formula (I) and a substrate in the presence of a first catalyst

Wherein R1 is a hydrogen atom or a methyl group;

thereby forming a product mixture comprising (meth) acrylate;

said method being characterized in that

The substrate is selected from primary, secondary, tertiary alcohols and phenols; and

the first catalyst comprises a magnesium salt or a salt of a rare earth element.

2. The process according to claim 1, wherein the first catalyst comprises a halide of magnesium or a rare earth element, a perchlorate of magnesium or a rare earth element, or a triflate of magnesium or a rare earth element, the first catalyst preferably being selected from the group consisting of magnesium bromide, magnesium iodide, magnesium chloride, lanthanum (III) triflate, yttrium (III) triflate, ytterbium (III) triflate and scandium (III) triflate.

3. The process according to claim 1 or 2, wherein the total amount of the first catalyst in step (a) is between 0.001 mol% and 10 mol%, more preferably between 0.01 mol% and 1.0 mol%, still more preferably between 0.1 mol% and 0.5 mol%, based on the amount of substrate.

4. The process according to one or more of claims 1 to 3, wherein the temperature is maintained during step (a) between 20 ℃ and 140 ℃, preferably between 40 ℃ and 110 ℃, more preferably between 60 ℃ and 90 ℃.

5. The process according to one or more of claims 1 to 4, wherein the substrate is selected from primary, secondary, tertiary alcohols and phenols having one or more hydroxyl groups, with primary, secondary and tertiary alcohols having one hydroxyl group being particularly preferred.

6. The process according to claim 5, wherein the molar ratio of (meth) acrylic anhydride to substrate in step (a) is between 5:1 and 1:5, preferably between 3:1 and 1:3, more preferably between 3:1 and 1:3, still more preferably between 2:1 and 1: 2.

7. The process according to one or more of claims 1 to 6, wherein the process further comprises the following steps (b) and (c) performed after step (a):

(b) adding a secondary alcohol to the product mixture obtained in step (a), thereby forming a product mixture comprising the (meth) acrylate and a (meth) acrylate of a secondary alcohol; and

(c) removing the (meth) acrylic acid ester of the auxiliary alcohol from the product mixture obtained in step (b), preferably by distillation;

wherein the secondary alcohol is a primary or secondary alcohol having a temperature at 10 ℃ of no more than 150 ℃, preferably no more than 120 ℃, more preferably no more than 80 ℃⁵Pa, wherein the auxiliary alcohol is preferably selected from methanol, ethanol, n-propanol, isopropanol or mixtures thereof, methanol being particularly preferred.

8. Use of magnesium salts or salts of rare earth elements as catalysts in reactions between (meth) acrylic anhydrides of formula (I) and substrates

Wherein R1 is a hydrogen atom or a methyl group;

the reaction produces a product mixture comprising (meth) acrylate, wherein

The substrate is selected from the group consisting of primary, secondary, tertiary alcohols and phenols.

Technical Field

The invention relates to a method for producing (meth) acrylic esters from (meth) acrylic anhydride.

Background

(meth) acrylates are commonly used as monomers for the preparation of various poly (meth) acrylates and corresponding copolymers. Accordingly, various methods for obtaining (meth) acrylic esters are known. These processes include inter alia transesterification reactions in which methyl methacrylate is reacted with an alcohol. Another common possibility is the acylation of alcohols with (meth) acrylic anhydride.

The process of acylating an alcohol with (meth) acrylic anhydride, particularly with methacrylic anhydride, is generally carried out in the presence of an acid, such as sulfuric acid. Under these conditions, unwanted reactions, such as the polymerization of anhydrides, often occur, so that the product yield of (meth) acrylates is only moderate. In addition, the preparation of (meth) acrylic esters of sterically hindered alcohols is known to suffer from low reaction yields, since these alcohols not only have low reactivity with (meth) acrylic anhydride, but also tend to undergo unwanted dehydration under the reaction conditions usually employed.

For these reasons, (meth) acrylic anhydride is generally used in large excess in order to achieve reasonable conversions of the sterically hindered alcohol and the phenol. This is disadvantageous from an economic and environmental point of view, since (meth) acrylic anhydride is rather expensive and recovery of the unreacted excess of (meth) acrylic anhydride is difficult.

In the past, considerable processes have been developed for acylating alcohols with non-polymerizable anhydrides, such as acetic anhydride. However, it is well known that these processes are generally ineffective with (meth) acrylic anhydride because the reactivity and chemical behavior of (meth) acrylic anhydride is significantly different from that of acetic anhydride.

US 4,540,743a describes the acylation of polyvinyl alcohol by esterifying the polyvinyl alcohol with activated (meth) acrylic anhydride in the presence of a tertiary amine. This procedure requires relatively large amounts of tertiary amine. Therefore, the tertiary amine needs to be separated from the product mixture in a separate washing step, which generates a considerable amount of aqueous waste.

Disclosure of Invention

In view of the above technical problems of the prior art, it is an object of the present invention to develop a more efficient industrially applicable process for preparing (meth) acrylic esters from (meth) acrylic anhydride. Such a method should ideally provide the following advantages:

high yield and high conversion of (meth) acrylate

Short reaction time

Low excess of (meth) acrylic anhydride

A low amount of acylation catalyst, which can be easily isolated from the resulting product, if desired.

In addition, the process should be suitable for the preparation of di-or poly (meth) acrylates on an industrial scale in an efficient and inexpensive manner.

The present invention is based on the surprising finding that activation of (meth) acrylic anhydride can be achieved in an efficient manner by using magnesium salts or salts of rare earth elements as catalysts.

Accordingly, one aspect of the present invention relates to a process for preparing a (meth) acrylate, the process comprising at least the following step (a):

(a) reaction between (meth) acrylic anhydride of formula (I) and a substrate in the presence of a magnesium salt or a salt of a rare earth element

Wherein R1 is a hydrogen atom or a methyl group,

thereby forming a product mixture comprising (meth) acrylate.

The terms "(meth) acrylate" and "(meth) acrylic" as used herein may refer to both acrylates and methacrylates. The (meth) acrylic anhydride of formula (I) may be acrylic anhydride (R1 is a hydrogen atom) or methacrylic anhydride (R1 is a methyl group).

The first catalyst used in step (a) catalyzes the reaction between the (meth) acrylic anhydride of formula (I) and the substrate. According to the invention, the first catalyst comprises a magnesium salt or a salt of a rare earth element.

The term "rare earth element" as used herein refers to an element selected from the group consisting of cerium, dysprosium, erbium, europium, gadolinium, holmium, lanthanum, lutetium, neodymium, praseodymium, promethium, samarium, scandium, terbium, thulium, ytterbium, and yttrium. In a particularly preferred embodiment, the term "rare earth element" refers to an element selected from lanthanum, ytterbium, yttrium and scandium.

In principle, essentially any magnesium salt or salt of the above-listed rare earth elements is suitable as first catalyst in the present invention. However, the catalytic activity of the first catalyst is particularly high if the salt is selected from the group consisting of fluoride, chloride, bromide, iodide, acetate, sulfate, perchlorate and triflate. In a particularly preferred embodiment, the salt may be selected from the group consisting of chloride, bromide, iodide and triflate.

Accordingly, the catalytic activity of the first catalyst is particularly high when the first catalyst comprises a halide of magnesium or a rare earth element, a perchlorate of magnesium or a rare earth element, or a triflate of magnesium or a rare earth element. In particular, the product yield of the (meth) acrylate formed in reaction step (a) is particularly high if the first catalyst is selected from the group consisting of magnesium bromide, magnesium iodide, magnesium chloride, magnesium bis- (trifluoromethanesulfonyl) imide, magnesium perchlorate, lanthanum (III) trifluoromethanesulfonate, ytterbium (III) trifluoromethanesulfonate, yttrium (III) trifluoromethanesulfonate and scandium (III) trifluoromethanesulfonate.

The first catalyst may be used in anhydrous form or as a hydrate.

Surprisingly, the reaction between the (meth) acrylic anhydride of formula (I) and the substrate in the reaction step (a) proceeds smoothly even if the first catalyst is present in a relatively low amount. Nevertheless, by using a higher amount of first catalyst, the reaction time during the reaction step (a) may be additionally reduced. The total amount of the first catalyst in step (a) is generally selected, depending on the reactivity of the substrate, to be between 0.001 mol% and 10 mol%, more preferably between 0.01 mol% and 1.0 mol%, still more preferably between 0.1 mol% and 0.5 mol%, based on the amount of substrate.

The reaction solvent used in step (a) is not particularly limited as long as the solvent cannot chemically react with the (meth) acrylic anhydride of formula (I) and has a boiling point that allows step (a) to be carried out at a desired temperature. Advantageously, however, step (a) is carried out in the absence of any solvent.

The order of addition of the reagents in step (a) is not particularly limited. Thus, in one embodiment, the first catalyst is first dispersed in the substrate, to which the (meth) acrylic anhydride of formula (I) is subsequently added. Alternatively, the first catalyst may be first dispersed in the (meth) acrylic anhydride of formula (I) and the substrate subsequently added to the resulting dispersion.

In some embodiments, it is also possible to first prepare a mixture of the (meth) acrylic anhydride of formula (I) and the substrate and to start the reaction by adding the first catalyst thereto. However, it is generally more difficult to use such procedures on an industrial scale.

The optimum reaction temperature during step (a) can be easily adjusted by the skilled person depending on the reactivity of the substrate and the (meth) acrylic anhydride of formula (I). Typically, the reaction temperature is maintained during step (a) between 20 ℃ and 140 ℃, preferably between 40 ℃ and 110 ℃, more preferably between 60 ℃ and 90 ℃.

Due to the high catalytic activity of the first catalyst, the reaction time of step (a) is typically between 10 minutes and 10 hours, typically between 30 minutes and 4 hours. As one skilled in the art will readily recognize, the reaction time of step (a) may also be adjusted by varying the reaction temperature and the amount of first catalyst.

Substrates suitable for use in the method of the invention are not particularly limited and may be selected from essentially any primary, secondary, tertiary and phenol. For example, in one embodiment of the invention, the substrate may be selected from primary, secondary, tertiary alcohols and phenols having one or more hydroxyl groups. For example, the substrate may advantageously be selected from primary, secondary and tertiary alcohols having one hydroxyl group. The use of these substrates leads favorably to the production of the corresponding (meth) acrylic monoesters in good chemical yields.

The molar ratio of (meth) acrylic anhydride to the substrate in step (a) is not particularly limited and may be adjusted according to the reactivity of the substrate and (meth) acrylic anhydride. For example, the molar ratio of (meth) acrylic anhydride to substrate in step (a) may be chosen between 5:1 and 1:5, preferably between 3:1 and 1:3, even more preferably between 2:1 and 1:2, even more preferably between 1.5:1 and 1: 1.5.

The reaction between the (meth) acrylic anhydride of formula (I) and the substrate in step (a) is generally carried out in the presence of a slight excess of (meth) acrylic anhydride, for example at least a 10 molar% excess or at least a 20 molar% excess, based on the amount of substrate. In order to separate the unreacted excess (meth) acrylic anhydride from the resulting (meth) acrylic ester, auxiliary alcohols may be added to the product mixture obtained in step (a). Under these conditions, a product mixture comprising the desired methacrylate and the methacrylate of the auxiliary alcohol is formed. Subsequently, the methacrylic acid esters of the auxiliary alcohols can be separated from this product mixture, usually by distillation.

Thus, in this embodiment, the process of the invention may be carried out as follows:

(a) reacting in the presence of a first catalyst a (meth) acrylic anhydride of the formula (I) below and a substrate, thereby forming a product mixture comprising a (meth) acrylate;

(b) adding a secondary alcohol to the product mixture obtained in step (a), thereby forming a product mixture comprising the (meth) acrylate and a (meth) acrylate of a secondary alcohol; and

(c) removing the (meth) acrylic acid ester of the auxiliary alcohol from the product mixture obtained in step (b).

The auxiliary alcohol is typically a primary or secondary alcohol. Since the auxiliary alcohol has high reactivity, it smoothly reacts with the (meth) acrylic anhydride of formula (I) that has not reacted after step (a), thereby forming a (meth) acrylic ester of the auxiliary alcohol. In order to facilitate the separation of the (meth) acrylic acid ester of the auxiliary alcohol by distillation in process step (c), the auxiliary alcohol preferably has a boiling point, measured at a pressure of 105Pa, of not more than 150 ℃, preferably not more than 120 ℃, more preferably not more than 80 ℃. For example, the auxiliary alcohol may advantageously be selected from methanol, ethanol, n-propanol, isopropanol or mixtures thereof, with methanol being particularly preferred.

Finally, another aspect of the invention is the use of a magnesium salt or a salt of a rare earth element as a catalyst in the reaction between (meth) acrylic anhydride of formula (I) and a substrate

Wherein R1 is a hydrogen atom or a methyl group;

the reaction produces a product mixture comprising (meth) acrylate, wherein

The substrate is selected from the group consisting of primary, secondary, tertiary alcohols and phenols.

The invention will be illustrated by the following examples, which are not intended to be limiting in any way.

Detailed Description

Examples

Examples 1-82 evaluation of catalytic Activity of first catalyst

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of menthol by methacrylic anhydride was studied.

Preparation of starting solutions of menthol and methacrylic anhydride

156 g (1.0 mol) of natural menthol and 161.9 g (1.05 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2.4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2, 2,6, 6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

General procedure for examples 1-67:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on menthol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 50 ℃ oil bath with an integrated magnetic stirrer for 3 hours and stirred.

The sample without any catalyst in a 50 ℃ oil bath (example 35) served as a reference sample as a reaction control, and another sample of the starting solution was kept at room temperature. After 3 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of examples 1-67 are summarized in Table 1 below:

TABLE 1 evaluation of catalytic Activity of the first catalyst when methacrylic anhydride was used

The data given in table 1 show that the various catalysts (lewis acids, bronsted acids, tertiary amines) commonly used for the acylation of alcohols with acetic anhydride are not suitable for (meth) acrylic anhydride. The use of these catalysts gave conversion of up to 18% under the reaction conditions tested.

Surprisingly, magnesium salts and salts of rare earth elements show significantly higher catalytic activity under the same reaction conditions.

The data in table 1 further show that the nature of the anion also greatly affects the catalytic activity of the tested salt. Contrary to the expectations of the inventors of the present invention, no correlation was found between the lewis acid strength of the anions of the tested salts and their catalytic activity. Magnesium halides and rare earth metal triflates surprisingly show the highest catalytic activity in acylation with (meth) acrylic anhydride. Perchlorates of the above metals also exhibit good catalytic activity.

Reference proportions 68-76 evaluation of the catalytic Activity of the first catalyst

As a reference example for evaluating the catalytic activity of the first catalyst, acylation of menthol by acetic anhydride was studied.

Preparation of starting solutions of menthol and methacrylic anhydride

37.8 grams (0.17 mole) of natural menthol and 161.9 grams (0.1785 mole) of acetic anhydride were combined. The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

General procedure for examples 68 to 76

A sample of 7 g stock solution was placed in a container havingPlug andmagnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on menthol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 50 ℃ oil bath with an integrated magnetic stirrer for 3 hours (unless otherwise indicated) and stirred.

After 3 hours, the content (% by area) of acetic acid, acetic anhydride, menthol and product was determined by gas chromatography. Based on these data, the reaction conversions based on acetic anhydride and on menthol were calculated.

The results of examples 68-76 are summarized in Table 2 below:

TABLE 2 evaluation of the catalytic Activity of the first catalyst when Using acetic anhydride

The data in Table 2 demonstrate that commonly used acylation catalysts, such as 4-dimethylaminopyridine, exhibit excellent catalytic activity when acetic anhydride is used. However, these catalysts surprisingly failed when methacrylic anhydride was used (see table 1 above). This indicates that the common general knowledge about the catalytic behavior of typical acylation catalysts is not applicable to acylation with (meth) acrylic anhydride.

Examples 77 to 95 evaluation of catalytic Activity of the first catalyst at 90 deg.C

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of menthol by methacrylic anhydride at 90 ℃ was investigated.

Preparation of starting solutions of menthol and methacrylic anhydride

156 g (1.0 mol) of natural menthol and 161.9 g (1.05 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2.4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2, 2,6, 6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

General procedure for examples 77-95:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on menthol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 90 ℃ oil bath with an integrated magnetic stirrer for 3 hours and stirred.

The sample without any catalyst in the oil bath at 90 ℃ (example 93) serves as a reference sample. After 3 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of examples 77-95 are summarized in Table 3 below:

TABLE 3 evaluation of the catalytic Activity of the first catalyst when methacrylic anhydride was used at 90 deg.C

The experimental data in table 3 confirm that the lanthanum (III) salt has excellent catalytic activity at 90 ℃, which is even higher than that of magnesium bromide at this temperature. The data also show that these catalysts can be used both as anhydrous salts and as hydrates without significant loss of catalytic activity.

In reference 93, the conversion in the absence of any catalyst was 38.90%. Surprisingly, the use of a strong lewis acid, such as zinc chloride (see example 94) did not result in an improvement of conversion levels of over 38.90%.

Examples 96 to 103 evaluation of the catalytic Activity of the first catalyst when Glycerol carbonate is used

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of glycerol carbonate by methacrylic anhydride at 80 ℃ was investigated.

Preparation of a stock solution of Glycerol carbonate and methacrylic anhydride

118 g (1.0 mol) of glycerol carbonate and 162.0 g (1.05 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2.4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2, 2,6, 6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

General procedure for examples 96 to 103:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mol% (unless otherwise indicated) of the first catalyst based on glycerol carbonate was added and the pressure tube was closed. Subsequently, the pressure tube was placed in an 80 ℃ oil bath with an integrated magnetic stirrer for 6 hours and stirred.

The sample without any catalyst in an oil bath at 80 ℃ (example 96) serves as a reference sample. After 6 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of examples 96-103 are summarized in Table 4 below:

TABLE 4 evaluation of the catalytic Activity of the first catalyst when methacrylic anhydride and Glycerol carbonate were used at 80 deg.C

The results in table 4 show that in the absence of any catalyst (reference 96), the conversion was as low as 6.00%. The use of known acylation catalysts, such as 4-dimethyl-aminopyridine (example 100) and zinc chloride (example 103) does not bring any improvement. In contrast, the product conversion in these examples is even lower than in the absence of any catalyst.

In the presence of zinc perchlorate (reference 99) or sulfuric acid (reference 102), unwanted polymer formation occurs. Thus, the desired product could not be detected.

Finally, the use of the catalyst according to the invention allows the preparation of the desired product in moderate to excellent yields.

Example 104-111 evaluation of catalytic Activity of the first catalyst Using isopropanol

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of isopropanol by methacrylic anhydride at 90 ℃ was investigated.

Preparation of starting solutions of isopropanol and methacrylic anhydride

30.1 g (0.50 mol) of isopropanol and 108.0 g (0.7 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2.4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2, 2,6, 6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

Example 104 general procedure of 111:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on isopropanol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 90 ℃ oil bath with an integrated magnetic stirrer for 6 hours and stirred.

The sample without any catalyst in an oil bath at 90 ℃ (example 104) serves as a reference sample. After 6 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of example 104-111 are summarized in table 5 below:

TABLE 5 evaluation of the catalytic Activity of the first catalyst at 90 ℃ Using methacrylic anhydride and isopropanol

The results in table 5 show that in the absence of any catalyst (reference 104), the conversion was 46.60%. The use of the known acylation catalyst 4-dimethylaminopyridine (reference 109) only brings about a modest improvement.

In the presence of zinc perchlorate (reference 108), unwanted polymer formation occurs and the desired product cannot be detected.

Example 112 evaluation of catalytic Activity of the first catalyst Using hexafluoroisopropanol 119

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of hexafluoroisopropanol by methacrylic anhydride at 90 ℃ was studied.

Preparation of a stock solution of hexafluoroisopropanol and methacrylic anhydride

50.4 g (0.30 mol) of hexafluoroisopropanol and 64.8 g (0.42 mol) of methacrylic anhydride are combined and stabilized with 2000ppm of 2.4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2.2.6.6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

Example 112 general procedure 119:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on hexafluoroisopropanol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 90 ℃ oil bath with an integrated magnetic stirrer for 6 hours and stirred.

The sample without any catalyst in the oil bath at 90 ℃ (reference example 112) served as a reference sample. After 6 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of example 112-119 are summarized in Table 6 below:

TABLE 6 evaluation of catalytic Activity of the first catalyst at 90 ℃ Using methacrylic anhydride and hexafluoroisopropanol

The results in table 6 show that in the absence of any catalyst (reference 112), the conversion was 43.80%.

In the presence of zinc perchlorate (reference example 116) andin the presence of M31 (reference 113), unwanted polymer formation occurred and the desired product could not be detected.

Example 120-127 evaluation of the catalytic Activity of the first catalyst Using t-Butanol

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of t-butanol by methacrylic anhydride at 90 ℃ was investigated.

Preparation of starting solutions of tert-butanol and methacrylic anhydride

37.1 g (0.50 mol) of tert-butanol and 107.9 g (0.70 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2, 4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2, 2,6, 6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

Example 137-general procedure of 127:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on t-butanol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 90 ℃ oil bath with an integrated magnetic stirrer for 6 hours and stirred.

The sample without any catalyst in the oil bath at 90 ℃ (reference example 120) serves as a reference sample. After 6 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of example 120-127 are summarized in Table 7 below:

TABLE 7 evaluation of catalytic Activity of the first catalyst at 90 ℃ Using methacrylic anhydride and t-Butanol

The results in table 7 show that in the absence of any catalyst (reference 120), the conversion was as low as 7.50%.

In the presence of zinc perchlorate (reference example 124) andin the presence of M31 (reference 121), unwanted polymer formation occurred. Thus, the desired product could not be detected.

The use of magnesium bromide (example 122) and magnesium perchlorate (example 123), i.e. the catalyst according to the invention, enables a significant improvement in the yield.

Example 128 evaluation of catalytic Activity of the first catalyst Using 4-hydroxybenzophenone

As a reference reaction for evaluating the catalytic activity of the first catalyst, acylation of 4-hydroxybenzophenone by methacrylic anhydride at 90 ℃ was investigated.

Preparation of a stock solution of 4-hydroxybenzophenone and methacrylic anhydride

3.35 g (0.017 mol) of 4-hydroxybenzophenone and 3.65 g (0.024 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2.4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2.2.6.6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

Example 128 general procedure of 137:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution 0.1 mole% (unless otherwise indicated) of the first catalyst based on t-butanol was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 90 ℃ oil bath with an integrated magnetic stirrer for 6 hours and stirred.

The sample without any catalyst in the oil bath at 90 ℃ (reference example 128) served as the reference sample. After 6 hours, the conversion and the product yield (% by area) were determined by gas chromatography.

The results of example 128-137 are summarized in Table 8 below:

TABLE 8 evaluation of the catalytic Activity of the first catalyst at 90 ℃ Using methacrylic anhydride and 4-hydroxybenzophenone

The results in table 8 show that in the absence of any catalyst (reference 128), the conversion is 30.9%.

In the presence of zinc perchlorate (reference numeral 133), unwanted polymer formation occurs. Thus, the desired product could not be detected.

The use of various catalysts according to the invention enables a significant improvement in the yield.

Example 138-155 catalytic Activity of different amounts of first catalyst

As a benchmark reaction for evaluating the catalytic activity of different amounts of the first catalyst, the acylation of menthol by methacrylic anhydride at 90 ℃ was investigated.

Preparation of starting solutions of menthol and methacrylic anhydride

78.1 g (0.50 mol) of natural menthol and 107.9 g (0.70 mol) of methacrylic anhydride were combined and stabilized with 2000ppm of 2, 4-dimethyl-6-tert-butylphenol and 1000ppm of hydroquinone monomethyl ether and 10ppm of 4-hydroxy-2, 2,6, 6-tetramethylpiperidin-1-oxyl (ppm based on the total mass of anhydride and alcohol). The resulting mixture was gently heated in the absence of any catalyst and a clear feedstock solution was obtained.

Example 138 general procedure 155:

a7.0 gram sample of the stock solution was placed in a container havingPlug and magnetic stirrer in a 15 ml pressure tube. To this solution the first catalyst was added and the pressure tube was closed. Subsequently, the pressure tube was placed in a 90 ℃ oil bath with an integrated magnetic stirrer and stirred.

The sample without any catalyst in the oil bath at 90 ℃ (reference example 138) served as a reference sample. After the times indicated in table 9, the conversion and product yield (area%) were determined by gas chromatography.

The results of example 138-155 are summarized in Table 9 below:

TABLE 9 evaluation of catalytic Activity of the first catalyst when methacrylic anhydride and menthol were used at 90 deg.C

The data in table 9 indicate that the optimum amount of the first catalyst is generally between about 0.1 mole% to about 0.5 mole% based on the amount of substrate.