WO2022158462A1 - (メタ)アクリル酸グリシジル組成物 - Google Patents
(メタ)アクリル酸グリシジル組成物 Download PDFInfo
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- WO2022158462A1 WO2022158462A1 PCT/JP2022/001689 JP2022001689W WO2022158462A1 WO 2022158462 A1 WO2022158462 A1 WO 2022158462A1 JP 2022001689 W JP2022001689 W JP 2022001689W WO 2022158462 A1 WO2022158462 A1 WO 2022158462A1
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- glycidyl
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- acrylate
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/12—Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
- C07D303/16—Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by esterified hydroxyl radicals
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/38—Compounds containing oxirane rings with hydrocarbon radicals, substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
- C07D303/40—Compounds containing oxirane rings with hydrocarbon radicals, substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals by ester radicals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
- C08F2/40—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation using retarding agents
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/10—Esters
- C08F20/26—Esters containing oxygen in addition to the carboxy oxygen
- C08F20/32—Esters containing oxygen in addition to the carboxy oxygen containing epoxy radicals
Definitions
- the present invention relates to a glycidyl (meth)acrylate composition. More particularly, the present invention relates to a glycidyl (meth)acrylate composition in which the phenol-based polymerization inhibitor contained in the glycidyl (meth)acrylate composition is resistant to deterioration and which can be stably stored for a long period of time. The present invention also provides a method for suppressing deactivation of a phenol-based polymerization inhibitor in a glycidyl (meth)acrylate resin composition.
- glycidyl (meth)acrylate refers to glycidyl acrylate or glycidyl methacrylate.
- a representative method for synthesizing glycidyl (meth)acrylate is to use epichlorohydrin as a raw material.
- the methods are roughly classified into the following two methods.
- the first is a method of synthesizing glycidyl (meth)acrylate by reacting epichlorohydrin and an alkali metal salt of (meth)acrylic acid in the presence of a catalyst (Patent Documents 1 and 2).
- the second is a method of synthesizing glycidyl (meth)acrylate by reacting epichlorohydrin and (meth)acrylic acid in the presence of a catalyst, followed by a ring closure reaction with an alkaline aqueous solution (Patent Document 3).
- a quaternary ammonium salt is used as the catalyst.
- 1,3-dichloropropanol is a reaction by-product during the synthesis of glycidyl (meth)acrylate. Since 1,3-dichloropropanol has a boiling point close to that of glycidyl methacrylate and is difficult to separate by distillation, reduction treatment using a quaternary ammonium salt as a catalyst is sometimes performed (Patent Document 4).
- quaternary ammonium salts are widely used in the production process of glycidyl (meth)acrylate.
- Non-Patent Document 1 describes that the addition reaction of phenol to epoxy groups proceeds in the presence of a quaternary ammonium salt.
- a phenol-based polymerization inhibitor such as p-methoxyphenol is used as a polymerization inhibitor for glycidyl (meth)acrylate. Therefore, if a quaternary ammonium salt used in the manufacturing process is mixed in the product, the phenol-based polymerization inhibitor reacts with the epoxy group of glycidyl (meth)acrylate during storage, resulting in a glycidyl (meth)acrylate composition. There is concern that the amount of the phenol-based polymerization inhibitor present therein may decrease over time, or that unintended polymerization may occur.
- the present invention provides a glycidyl (meth)acrylate composition in which the phenol-based polymerization inhibitor contained in the glycidyl (meth)acrylate composition is resistant to deterioration (deactivation) and can be stably stored for a long period of time. .
- the present invention also provides a method for suppressing deactivation of a phenol-based polymerization inhibitor in a glycidyl (meth)acrylate resin composition.
- the present invention is as follows, for example.
- ⁇ 1> Suppressing deactivation of a phenol-based polymerization inhibitor in a glycidyl (meth)acrylate composition, including adjusting the content of a quaternary ammonium salt in the glycidyl (meth)acrylate composition to 1.00 ppm or less Method.
- ⁇ 2> The method according to ⁇ 1>, wherein the quaternary ammonium salt is a tetraalkylammonium halide.
- ⁇ 3> The method according to ⁇ 2>, wherein the quaternary ammonium salt is tetramethylammonium chloride or triethylmethylammonium chloride.
- ⁇ 4> The phenol-based polymerization inhibitor according to any one of ⁇ 1> to ⁇ 3>, wherein p-methoxyphenol, hydroquinone, or Topanol A (2-(tert-butyl)-4,6-dimethylphenol).
- Method. ⁇ 5> The method according to any one of ⁇ 1> to ⁇ 4>, wherein glycidyl (meth)acrylate is glycidyl methacrylate.
- a glycidyl (meth)acrylate composition comprising glycidyl (meth)acrylate, a quaternary ammonium salt, and a phenolic polymerization inhibitor, wherein the content of the quaternary ammonium salt is 1.00 ppm or less.
- glycidyl (meth)acrylate composition according to ⁇ 7>, wherein the quaternary ammonium salt is tetramethylammonium chloride or triethylmethylammonium chloride.
- a phenol-based polymerization inhibitor according to any one of ⁇ 6> to ⁇ 8>, which is p-methoxyphenol, hydroquinone, or Topanol A (2-(tert-butyl)-4,6-dimethylphenol).
- a glycidyl (meth)acrylate composition ⁇ 10> The glycidyl (meth)acrylate composition according to any one of ⁇ 6> to ⁇ 9>, wherein the glycidyl (meth)acrylate is glycidyl methacrylate.
- a glycidyl (meth)acrylate composition in which a phenol-based polymerization inhibitor contained in the glycidyl (meth)acrylate composition is resistant to deterioration (deactivation) and can be stably stored for a long period of time. be able to.
- Glycidyl (meth)acrylate composition The glycidyl (meth)acrylate composition of the present invention contains glycidyl (meth)acrylate, a quaternary ammonium salt, and a phenolic polymerization inhibitor. Each component will be described below.
- Glycidyl (meth)acrylate refers to glycidyl acrylate and glycidyl methacrylate.
- glycidyl (meth)acrylate may be glycidyl acrylate.
- glycidyl (meth)acrylate may be glycidyl methacrylate.
- glycidyl (meth)acrylate is glycidyl methacrylate.
- Glycidyl (meth)acrylate can be produced by a known production method.
- a representative method for producing glycidyl (meth)acrylate includes a method using epichlorohydrin (hereinafter sometimes referred to as “EpCH”) as a raw material.
- EpCH epichlorohydrin
- a method of synthesizing glycidyl (meth)acrylate by reacting an alkali metal salt of acrylic acid in the presence of a catalyst Patent Documents 1 and 2), and epichlorohydrin and (meth)acrylic acid in the presence of a catalyst.
- Patent Document 3 quaternary ammonium salts are used as catalysts.
- TMAC tetramethylammonium chloride
- EMAC trimethylethylammonium chloride
- dimethyldiethylammonium chloride triethylmethyl tetraalkylammonium halides
- EMC ammonium chloride
- EMC trialkylbenzylammonium halides
- the quaternary ammonium salt may be one of the above, or any two or more of them may be used in combination. Chloride and trimethylbenzylammonium chloride are preferably used. The amount of the catalyst used is usually 0.01 to 1.5 mol % relative to (meth)acrylic acid.
- the synthesis solution contains a large amount of solids such as alkali chloride, which is approximately equimolar to the produced glycidyl (meth)acrylate, in addition to the quaternary ammonium salt as a catalyst.
- the synthesis reaction is carried out with excess EpCH. Therefore, usually after the completion of the synthesis, after removing the solid matter from the synthetic solution by a method such as filtration or washing, the unreacted surplus EpCH is recovered by distillation, and then the glycidyl (meth)acrylate is recovered by distillation. Common. EpCH recovered by distillation is recycled as a synthetic raw material.
- the process up to the removal of solids from the synthetic liquid is referred to as the synthesis process
- the liquid obtained by removing the solids from the synthetic liquid is referred to as the mother liquor
- the process after the removal of the solids is referred to as the distillation process.
- the distillation process may be either a batch process or a continuous process, and simple distillation, rectification, thin film distillation, etc. can be appropriately combined.
- the synthesis step is preferably carried out in the presence of an appropriate polymerization inhibitor, and known compounds such as phenol compounds, phenothiazine compounds, N-oxyl compounds, amine compounds, phosphorus compounds, sulfur compounds, and transition metal compounds can be used. , preferably they are also used in the distillation process.
- polymerization can be further prevented by supplying molecular oxygen as needed.
- a phenol-based polymerization inhibitor such as p-methoxyphenol is generally used as a polymerization inhibitor for glycidyl (meth)acrylate.
- 1,3-dichloropropanol (hereinafter sometimes referred to as "1,3-DCP") is present as an impurity in the obtained glycidyl (meth)acrylate. included. Since 1,3-DCP has a boiling point very close to that of glycidyl (meth)acrylate, separation by distillation is impractical. That is, when glycidyl (meth)acrylate is recovered after recovering EpCH in the distillation step as described above, almost the entire amount of 1,3-DCP produced in the synthesis step is recovered together with glycidyl (meth)acrylate. put away.
- the quaternary ammonium salts added in the purification step include tetraalkylammonium halides such as tetramethylammonium chloride, trimethylethylammonium chloride, dimethyldiethylammonium chloride, triethylmethylammonium chloride, and tetraethylammonium chloride; Examples include trialkylbenzylammonium halides such as triethylbenzylammonium chloride. Only one quaternary ammonium salt may be added, or two or more may be used in combination. Chloride and trimethylbenzylammonium chloride are preferably used.
- the quaternary ammonium salt to be added may be the same as or different from that used in the synthesis.
- the amount of the quaternary ammonium salt to be used is 0.001 to 1%, preferably 0.01 to 0.5%, more preferably 0.02 to 0.4% relative to the crude glycidyl (meth)acrylate. . If the amount is less than this, the reaction becomes slow, and if it is more than this, it is economically disadvantageous.
- the shape of the quaternary ammonium salt used in the synthesis process and purification process is not particularly limited. It may be in a powdery or granular solid state, or in an aqueous solution or in a slurry-dispersed state in glycidyl (meth)acrylate in the purification step. Granular or powdery ones are usually used.
- the method of adding the quaternary ammonium salt is also not particularly limited.
- a solid it may be charged into a reactor using a hopper or the like, and in the case of a purification step, crude glycidyl (meth)acrylate or the like may be washed away and added. Although it may be divided and added several times, it is usually added at once.
- Glycidyl (meth)acrylate used in the present invention preferably has a purity of 97% or higher, more preferably 98% or higher, still more preferably 99% or higher, and even more preferably 99.5% or higher. .
- the purity of glycidyl (meth)acrylate can be measured by a conventional method, such as gas chromatography (GC).
- Quaternary ammonium salts are those used as reaction catalysts in the production process of glycidyl (meth)acrylate and those added in the purification process, which are added to the glycidyl (meth)acrylate composition. may be present in the glycidyl (meth)acrylate composition so as to remain in the composition.
- Examples of quaternary ammonium salts that may be present in the glycidyl (meth)acrylate composition include tetraalkyl salts such as tetramethylammonium chloride, trimethylethylammonium chloride, dimethyldiethylammonium chloride, triethylmethylammonium chloride and tetraethylammonium chloride. ammonium halides; and trialkylbenzylammonium halides such as trimethylbenzylammonium chloride and triethylbenzylammonium chloride.
- the quaternary ammonium salt that may be present in the glycidyl (meth)acrylate composition may be one of the above or a combination of any two or more.
- preferred quaternary ammonium salts that may be present in the glycidyl (meth)acrylate composition are tetramethylammonium chloride, triethylmethylammonium chloride, tetraethylammonium chloride, triethylbenzylammonium chloride, and trimethylbenzylammonium chloride. is.
- said quaternary ammonium salt that may be present in the glycidyl (meth)acrylate composition is a tetraalkylammonium halide.
- said quaternary ammonium salt that may be present in the glycidyl (meth)acrylate composition is tetramethylammonium chloride or triethylmethylammonium chloride.
- the present inventors have found that quaternary ammonium salts that can remain in the glycidyl (meth)acrylate composition or in the glycidyl (meth)acrylate product are present in the glycidyl (meth)acrylate composition. It was found that the reaction with the inhibitor reduces the amount of the phenol-based polymerization inhibitor in the system, which impairs the long-term storage stability of the glycidyl (meth)acrylate composition. Therefore, the present invention ensures long-term storage stability of the glycidyl (meth)acrylate composition by adjusting the content of the quaternary ammonium salt in the glycidyl (meth)acrylate composition.
- the content of the quaternary ammonium salt present in the glycidyl (meth)acrylate composition of the present invention is preferably 1.00 ppm or less, more preferably 0.75 ppm or less, and even more preferably 0.75 ppm or less. 50 ppm or less. If the content of the quaternary ammonium salt present in the glycidyl (meth)acrylate composition of the present invention is within the above range, the reaction between the quaternary ammonium salt and the phenolic polymerization inhibitor is appropriately suppressed. be able to.
- Phenolic Polymerization Inhibitor is a polymerization inhibitor commonly used in the production of glycidyl (meth)acrylate, and is present in the produced glycidyl (meth)acrylate composition. .
- Phenolic polymerization inhibitors used in the production of glycidyl (meth)acrylate of the present invention include, for example, p-methoxyphenol (hereinafter sometimes referred to as “MQ”), hydroquinone, and 2,6-di-tert-butyl. -4-methylphenol, 2,2′-methylene-bis(4-methyl-6-tert-butylphenol), Topanol A (2-(tert-butyl)-4,6-dimethylphenol) and the like, It is not limited to these.
- the phenolic polymerization inhibitor is preferably p-methoxyphenol, hydroquinone or Topanol A (2-(tert-butyl)-4,6-dimethylphenol), p-methoxyphenol or Hydroquinone is more preferred, and p-methoxyphenol is most preferred.
- the phenol-based polymerization inhibitor used in the production of glycidyl (meth)acrylate is usually added in an amount in the range of 0.0005 to 0.01 equivalents relative to the amount of the (meth)acryloyl group.
- the content of the phenolic polymerization inhibitor present in the produced glycidyl (meth)acrylate composition is in the range of 20-200 ppm, preferably in the range of 20-150 ppm.
- the content of the quaternary ammonium salt in the glycidyl (meth)acrylate composition is preferably 1. It is adjusted to 00 ppm or less, more preferably 0.75 ppm or less, still more preferably 0.50 ppm or less. If the content of the quaternary ammonium salt present in the glycidyl (meth)acrylate composition of the present invention is adjusted within the above range, the reaction between the quaternary ammonium salt and the phenolic polymerization inhibitor is appropriately suppressed.
- the phenol-based polymerization in the glycidyl (meth)acrylate composition comprises adjusting the content of the quaternary ammonium salt in the glycidyl (meth)acrylate composition to 1.00 ppm or less. Methods are provided for inhibiting inhibitor deactivation. In a more preferred embodiment of the present invention, the phenol-based A method for suppressing deactivation of a polymerization inhibitor is provided.
- the phenol in the glycidyl (meth)acrylate composition comprises adjusting the content of the quaternary ammonium salt in the glycidyl (meth)acrylate composition to 0.50 ppm or less.
- a method for suppressing deactivation of a system polymerization inhibitor is provided.
- the quaternary ammonium salt is as described above. That is, in the method of suppressing deactivation of the phenol-based polymerization inhibitor in the glycidyl (meth)acrylate composition of the present invention, the quaternary ammonium salts include tetramethylammonium chloride, trimethylethylammonium chloride and dimethyldiethylammonium. tetraalkylammonium halides such as chloride, triethylmethylammonium chloride and tetraethylammonium chloride; and trialkylbenzylammonium halides such as trimethylbenzylammonium chloride and triethylbenzylammonium chloride.
- the quaternary ammonium salt may be used alone or in combination of two or more. Among the above, tetramethylammonium chloride, triethylmethylammonium chloride, tetraethylammonium chloride, and triethylbenzylammonium chloride are preferred. , and trimethylbenzylammonium chloride.
- said quaternary ammonium salt that may be present in the glycidyl (meth)acrylate composition is a tetraalkylammonium halide.
- said quaternary ammonium salt that may be present in the glycidyl (meth)acrylate composition is tetramethylammonium chloride or triethylmethylammonium chloride.
- the phenol-based polymerization inhibitor is as described above. That is, in the method of suppressing deactivation of the phenol-based polymerization inhibitor in the glycidyl (meth)acrylate composition of the present invention, examples of the phenol-based polymerization inhibitor include p-methoxyphenol (“MQ”), hydroquinone, 2,6-di-tert-butyl-4-methylphenol, 2,2′-methylene-bis(4-methyl-6-tert-butylphenol), Topanol A (2-(tert-butyl)-4,6- dimethylphenol), and the like, but are not limited to these.
- MQ p-methoxyphenol
- hydroquinone 2,6-di-tert-butyl-4-methylphenol
- Topanol A (2-(tert-butyl)-4,6- dimethylphenol
- the phenolic polymerization inhibitor is preferably p-methoxyphenol, hydroquinone or Topanol A (2-(tert-butyl)-4,6-dimethylphenol), p-methoxyphenol or Hydroquinone is more preferred, and p-methoxyphenol is most preferred.
- the phenol-based polymerization inhibitor used in the production of glycidyl (meth)acrylate is usually added in an amount in the range of 0.0005 to 0.01 equivalents relative to the amount of the (meth)acryloyl group.
- the content of the phenolic polymerization inhibitor present in the produced glycidyl (meth)acrylate composition is in the range of 20-200 ppm, preferably in the range of 20-150 ppm.
- the content of the quaternary ammonium salt present in the glycidyl (meth)acrylate composition is By adjusting the amount within a certain range, the reaction between the quaternary ammonium salt and the phenol-based polymerization inhibitor can be appropriately suppressed.
- a glycidyl (meth)acrylate composition is generally produced by purifying, by distillation, a reaction mixture obtained by reacting epichlorohydrin with (meth)acrylic acid or a metal salt of (meth)acrylic acid.
- the quaternary ammonium salt content in the glycidyl (meth)acrylate composition is adjusted by the amount of the quaternary ammonium salt used during production and the distillation method and conditions when distilling and recovering the glycidyl (meth)acrylate. do.
- the amount of the quaternary ammonium salt added during production is preferably 0.0001 to 0.01 equivalent to the amount of the (meth)acryloyl group.
- distillation methods include simple distillation and rectification, and the reflux ratio in rectification is preferably 0.1 to 3.0.
- Distillation conditions include, for example, temperature and pressure, and the temperature is preferably 40 to 120° C., and the pressure is preferably 0.05 to 10 kPaA.
- “Number of days required for 10% deterioration of the phenolic polymerization inhibitor” (unit: day) is the time until 10% of the phenolic polymerization inhibitor present in the produced glycidyl (meth)acrylate composition is deactivated. refers to the number of days In the method of the present invention, "the number of days required for 10% deterioration of the phenolic polymerization inhibitor” is preferably 20 days or more, more preferably 50 days or more, still more preferably 60 days or more, and most preferably. is 90 days or more.
- reaction rate constant (unit: day ⁇ 1 ) is the rate constant of deterioration of the phenol-based polymerization inhibitor, and refers to k in the following formula (1).
- ⁇ d[I]/dt k[I] (1)
- [I] is the concentration of the phenol-based polymerization inhibitor. Since the deterioration of the phenol-based polymerization inhibitor is due to the reaction with glycidyl (meth)acrylate, the concentration of glycidyl (meth)acrylate should be taken into consideration when calculating the reaction rate.
- the concentration of glycidyl (meth)acrylate was assumed to be constant.
- the “reaction rate constant” is preferably 5.3 ⁇ 10 ⁇ 3 day ⁇ 1 or less, more preferably 2.1 ⁇ 10 ⁇ 3 day ⁇ 1 or less, and still more preferably 1 .8 ⁇ 10 ⁇ 3 day ⁇ 1 or less, and most preferably 1.2 ⁇ 10 ⁇ 3 day ⁇ 1 or less. It can be said that deactivation of the phenol-based polymerization inhibitor in the glycidyl (meth)acrylate composition is appropriately suppressed when the "reaction rate constant" is within the above range.
- Example 1 0.25 ppm of triethylmethylammonium chloride ("EMAC”) was added to the test solution prepared in Reference Example 2, and the solution was stored at 25°C under normal pressure air atmosphere.
- MQ concentration was quantified in the same manner as in Reference Example 2, the MQ concentration at the start of the test was 102.4 ppm, whereas the MQ after storage for 14 days, 35 days, 56 days, 75 days, and 90 days
- the concentrations were 102.3 ppm, 101.7 ppm, 101.3 ppm, 100.2 ppm and 100.0 ppm, respectively.
- Example 2 0.50 ppm of triethylmethylammonium chloride ("EMAC”) was added to the test solution prepared in Reference Example 2, and the solution was stored at 25°C under normal pressure air atmosphere.
- MQ concentration was quantified in the same manner as in Reference Example 2, the MQ concentration at the start of the test was 102.4 ppm, whereas the MQ after storage for 14 days, 35 days, 56 days, 75 days, and 90 days
- the concentrations were 102.0 ppm, 101.0 ppm, 99.7 ppm, 97.6 ppm and 96.7 ppm, respectively.
- the reaction rate constant calculated by the same method as in Example 1 was 6.59 ⁇ 10 ⁇ 4 day ⁇ 1 , and the time required for MQ to degrade by 10% was 160 days.
- Example 3 0.75 ppm of triethylmethylammonium chloride ("EMAC”) was added to the test solution prepared in Reference Example 2, and the solution was stored at 25°C under normal pressure air atmosphere.
- MQ concentration was quantified in the same manner as in Reference Example 2, the MQ concentration at the start of the test was 102.4 ppm, whereas the MQ after storage for 14 days, 35 days, 56 days, 75 days, and 90 days The concentrations were 101.5 ppm, 99.3 ppm, 96.5 ppm, 92.7 ppm and 90.0 ppm, respectively.
- the reaction rate constant calculated by the same method as in Example 1 was 1.44 ⁇ 10 ⁇ 3 day ⁇ 1 , and the time required for MQ to degrade by 10% was 73 days.
- Example 4 1.00 ppm of triethylmethylammonium chloride (“EMAC”) was added to the test solution prepared in Reference Example 2, and the solution was stored at 25° C. under normal pressure air atmosphere.
- MQ concentration was quantified in the same manner as in Reference Example 2, the MQ concentration at the start of the test was 102.4 ppm, whereas the MQ after storage for 14 days, 35 days, 56 days, 75 days, and 90 days The concentrations were 100.9 ppm, 97.9 ppm, 93.5 ppm, 88.5 ppm and 84.9 ppm respectively.
- the reaction rate constant calculated by the same method as in Example 1 was 2.11 ⁇ 10 ⁇ 3 day ⁇ 1 , and the time required for MQ to degrade by 10% was 50 days.
- Example 5 To the test solution prepared in Reference Example 1, a predetermined amount of p-methoxyphenol (Fuji Film Wako Pure Chemical special grade reagent) and 1.00 ppm of tetramethylammonium chloride ("TMAC”) were added, and the mixture was heated at 25°C in normal pressure air. Stored under atmosphere.
- TMAC tetramethylammonium chloride
- the MQ concentration at the start of the test was 99.6 ppm
- the concentrations were 98.4 ppm, 97.7 ppm, 96.6 ppm, 95.2 ppm and 94.2 ppm, respectively.
- the reaction rate constant calculated by the same method as in Example 1 was 8.62 ⁇ 10 ⁇ 4 day ⁇ 1 , and the time required for MQ to degrade by 10% was 122 days.
- Example 6 A predetermined amount of p-methoxyphenol (special grade reagent of Fujifilm Wako Pure Chemical Industries) was added to GMA of Reference Example 1 to prepare a test solution. 1.00 ppm of triethylmethylammonium chloride (“EMAC”) was added to this test solution and stored at 25° C. under normal pressure air atmosphere.
- EMAC triethylmethylammonium chloride
- the MQ concentration at the start of the test was 50.1 ppm, whereas the MQ after storage for 10 days, 21 days, 32 days, 46 days, and 65 days
- the concentrations were 48.7 ppm, 48.0 ppm, 46.8 ppm, 45.0 ppm and 43.1 ppm, respectively.
- the reaction rate constant calculated by the same method as in Example 1 was 2.30 ⁇ 10 ⁇ 3 day ⁇ 1 , and the time required for MQ to degrade by 10% was 46 days.
- the phenol-based polymerization inhibitor contained in the glycidyl (meth)acrylate composition is resistant to deterioration and can be stably stored for a long period of time (meta ) is a glycidyl acrylate composition.
- the deterioration (deactivation) of the phenol-based polymerization inhibitor contained in the glycidyl (meth)acrylate composition can be appropriately suppressed.
- the glycidyl (meth)acrylate composition and method of the present invention contribute to ensuring long-term storage stability of the glycidyl (meth)acrylate composition.
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Abstract
Description
(メタ)アクリル酸グリシジル組成物中の第4級アンモニウム塩の含量を1.00ppm以下に調整することを含む、(メタ)アクリル酸グリシジル組成物中のフェノール系重合禁止剤の失活を抑制する方法。
<2>
前記第4級アンモニウム塩が、テトラアルキルアンモニウムハロゲニドである、<1>に記載の方法。
<3>
前記第4級アンモニウム塩が、テトラメチルアンモニウムクロリドまたはトリエチルメチルアンモニウムクロリドである、<2>に記載の方法。
<4>
前記フェノール系重合禁止剤が、p-メトキシフェノール、ヒドロキノン、又はトパノールA(2-(tert-ブチル)-4,6-ジメチルフェノール)である、<1>~<3>のいずれかに記載の方法。
<5>
(メタ)アクリル酸グリシジルが、メタクリル酸グリシジルである、<1>~<4>のいずれかに記載の方法。
<6>
(メタ)アクリル酸グリシジルと、第4級アンモニウム塩と、フェノール系重合禁止剤とを含む、(メタ)アクリル酸グリシジル組成物であって、前記第4級アンモニウム塩の含量が1.00ppm以下である、(メタ)アクリル酸グリシジル組成物。
<7>
前記第4級アンモニウム塩が、テトラアルキルアンモニウムハロゲニドである、<6>に記載の(メタ)アクリル酸グリシジル組成物。
<8>
前記第4級アンモニウム塩が、テトラメチルアンモニウムクロリドまたはトリエチルメチルアンモニウムクロリドである、<7>に記載の(メタ)アクリル酸グリシジル組成物。
<9>
前記フェノール系重合禁止剤が、p-メトキシフェノール、ヒドロキノン、又はトパノールA(2-(tert-ブチル)-4,6-ジメチルフェノール)である、<6>~<8>のいずれかに記載の(メタ)アクリル酸グリシジル組成物。
<10>
(メタ)アクリル酸グリシジルが、メタクリル酸グリシジルである、<6>~<9>のいずれかに記載の(メタ)アクリル酸グリシジル組成物。
本発明の(メタ)アクリル酸グリシジル組成物は、(メタ)アクリル酸グリシジルと、第4級アンモニウム塩と、フェノール系重合禁止剤とを含む。以下、各成分について説明する。
(メタ)アクリル酸グリシジルは、アクリル酸グリシジル及びメタクリル酸グリシジルを指す。本発明の一実施形態において、(メタ)アクリル酸グリシジルは、アクリル酸グリシジルであってよい。本発明の別の実施形態において、(メタ)アクリル酸グリシジルは、メタクリル酸グリシジルであってよい。本発明の好ましい実施形態において、(メタ)アクリル酸グリシジルは、メタクリル酸グリシジルである。
(式1) 1,3-DCP + GMA → EpCH + MACE
第4級アンモニウム塩は、(メタ)アクリル酸グリシジルの製造工程において反応触媒として用いられたもの及び精製工程で添加されたものが、(メタ)アクリル酸グリシジル組成物中に残存し得るために、(メタ)アクリル酸グリシジル組成物中に存在し得る。
フェノール系重合禁止剤は、(メタ)アクリル酸グリシジルの製造において一般的に用いられる重合禁止剤であり、製造された(メタ)アクリル酸グリシジル組成物中に存在する。
上述のように、本発明者らは、(メタ)アクリル酸グリシジル組成物中あるいは(メタ)アクリル酸グリシジル製品中に残存し得る第4級アンモニウム塩が、(メタ)アクリル酸グリシジル組成物中に存在するフェノール系重合禁止剤と反応することにより、系内のフェノール系重合禁止剤が減少することを見出した。本発明はまた、このような本発明者等の発見に基づき、(メタ)アクリル酸グリシジル組成物中の第4級アンモニウム塩の含量を調整することを含む、(メタ)アクリル酸グリシジル組成物中のフェノール系重合禁止剤の失活を抑制する方法を提供する。
-d[I]/dt=k[I] ・・・(1)
ここで、[I]はフェノール系重合禁止剤濃度である。なお、フェノール系重合禁止剤の変質は(メタ)アクリル酸グリシジルとの反応によるものであるため、本来は反応速度の算出の際に(メタ)アクリル酸グリシジルの濃度を考慮するべきであるが、(メタ)アクリル酸グリシジル組成物中に含まれる(メタ)アクリル酸グリシジルはフェノール系重合禁止剤に対して過剰であるため、(メタ)アクリル酸グリシジルの濃度は一定であるとした。
本発明の方法において、「反応速度定数」は、好ましくは5.3×10-3day-1以下であり、より好ましくは2.1×10-3day-1以下であり、更に好ましくは1.8×10-3day-1以下であり、最も好ましくは1.2×10-3day-1以下である。「反応速度定数」が上記の範囲にあれば、(メタ)アクリル酸グリシジル組成物中のフェノール系重合禁止剤の失活が適切に抑制されているといえる。
純度99.5%のメタクリル酸グリシジル(以下、「GMA」ということがある)40.0gと純水10.0gを混合し、ボルテクスミキサーで30秒間攪拌することでGMA中の塩成分を水相に溶解させた。前記混合物から水相を回収し、水相中のイオン成分を確認した。
カラム: Shodex IC YS-50(内径4.6mm、長さ125mm)
カラム温度:40℃
溶離液:0.2mmol/L硝酸水溶液
流速:0.8mL/min
検出器:電気伝導度検出器
試料注入量:100μL
カラム: 東ソー TSKgel IC-Anion-PW(内径4.6mm、長さ50mm)
カラム温度:40℃
溶離液:東ソー TSKgel eluent IC-Anion-A
流速:0.8mL/min
検出器:電気伝導度検出器
試料注入量:100μL
参考例1のGMAにp-メトキシフェノール(富士フィルム和光純薬特級試薬)を所定量添加して、試験液とした。試験液を25℃、常圧空気雰囲気下で保存して、MQ濃度の減少を確認した。GMA中のp-メトキシフェノール(MQ)の濃度は高速液体クロマトグラフを用いて以下の条件で定量した。
カラム:東ソー TSKgel ODS-120T(粒子径5μm、内径4.6mm、長さ25cm)
カラム温度:40℃
溶離液:アセトニトリル/純水/酢酸=700/300/1(体積比)
流速:0.8mL/min
検出器:紫外可視分光検出器(波長:285nm)
試料注入量:5μL
保持時間:MQ(4.5min)
参考例2で調製した試験液に、トリエチルメチルアンモニウムクロリド(「EMAC」)を0.25ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は102.4ppmであったのに対し、14日、35日、56日、75日、90日保存後のMQ濃度はそれぞれ、102.3ppm、101.7ppm、101.3ppm、100.2ppm、100.0ppmであった。
参考例2で調製した試験液に、トリエチルメチルアンモニウムクロリド(「EMAC」)を0.50ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は102.4ppmであったのに対し、14日、35日、56日、75日、90日保存後のMQ濃度はそれぞれ、102.0ppm、101.0ppm、99.7ppm、97.6ppm、96.7ppmであった。また、実施例1と同様の方法で算出した反応速度定数は6.59×10-4day-1であり、MQが10%変質するのに要する時間は160日であった。
参考例2で調製した試験液に、トリエチルメチルアンモニウムクロリド(「EMAC」)を0.75ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は102.4ppmであったのに対し、14日、35日、56日、75日、90日保存後のMQ濃度はそれぞれ、101.5ppm、99.3ppm、96.5ppm、92.7ppm、90.0ppmであった。また、実施例1と同様の方法で算出した反応速度定数は1.44×10-3day-1であり、MQが10%変質するのに要する時間は73日であった。
参考例2で調製した試験液に、トリエチルメチルアンモニウムクロリド(「EMAC」)を1.00ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は102.4ppmであったのに対し、14日、35日、56日、75日、90日保存後のMQ濃度はそれぞれ、100.9ppm、97.9ppm、93.5ppm、88.5ppm、84.9ppmであった。また、実施例1と同様の方法で算出した反応速度定数は2.11×10-3day-1であり、MQが10%変質するのに要する時間は50日であった。
参考例1で調製した試験液に、p-メトキシフェノール(富士フィルム和光純薬特級試薬)を所定量、テトラメチルアンモニウムクロリド(「TMAC」)を1.00ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は99.6ppmであったのに対し、10日、21日、32日、46日、65日保存後のMQ濃度はそれぞれ、98.4ppm、97.7ppm、96.6ppm、95.2ppm、94.2ppmであった。また、実施例1と同様の方法で算出した反応速度定数は8.62×10-4day-1であり、MQが10%変質するのに要する時間は122日であった。
参考例1のGMAにp-メトキシフェノール(富士フィルム和光純薬特級試薬)を所定量添加して、試験液とした。この試験液に、トリエチルメチルアンモニウムクロリド(「EMAC」)を1.00ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は50.1ppmであったのに対し、10日、21日、32日、46日、65日保存後のMQ濃度はそれぞれ、48.7ppm、48.0ppm、46.8ppm、45.0ppm、43.1ppmであった。また、実施例1と同様の方法で算出した反応速度定数は2.30×10-3day-1であり、MQが10%変質するのに要する時間は46日であった。
参考例1で調製した試験液に、p-メトキシフェノール(富士フィルム和光純薬特級試薬)を所定量、トリエチルメチルアンモニウムクロリド(「EMAC」)を5.00ppm添加して、25℃、常圧空気雰囲気下で保存した。参考例2と同様の方法でMQ濃度を定量したところ、試験開始時のMQ濃度は101.8ppmであったのに対し、15日、34日、49日、61日保存後のMQ濃度はそれぞれ、92.4ppm、77.0ppm、65.8ppm、58.2ppmであった。また、実施例1と同様の方法で算出した反応速度定数は9.32×10-3day-1であり、MQが10%変質するのに要する時間は11日であった。
EMAC:トリエチルメチルアンモニウムクロリド
TMAC:テトラメチルアンモニウムクロリド
MQ:p-メトキシフェノール
Claims (10)
- (メタ)アクリル酸グリシジル組成物中の第4級アンモニウム塩の含量を1.00ppm以下に調整することを含む、(メタ)アクリル酸グリシジル組成物中のフェノール系重合禁止剤の失活を抑制する方法。
- 前記第4級アンモニウム塩が、テトラアルキルアンモニウムハロゲニドである、請求項1に記載の方法。
- 前記第4級アンモニウム塩が、テトラメチルアンモニウムクロリドまたはトリエチルメチルアンモニウムクロリドである、請求項2に記載の方法。
- 前記フェノール系重合禁止剤が、p-メトキシフェノール、ヒドロキノン、又はトパノールA(2-(tert-ブチル)-4,6-ジメチルフェノール)である、請求項1~3のいずれかに記載の方法。
- (メタ)アクリル酸グリシジルが、メタクリル酸グリシジルである、請求項1~4のいずれかに記載の方法。
- (メタ)アクリル酸グリシジルと、第4級アンモニウム塩と、フェノール系重合禁止剤とを含む、(メタ)アクリル酸グリシジル組成物であって、前記第4級アンモニウム塩の含量が1.00ppm以下である、(メタ)アクリル酸グリシジル組成物。
- 前記第4級アンモニウム塩が、テトラアルキルアンモニウムハロゲニドである、請求項6に記載の(メタ)アクリル酸グリシジル組成物。
- 前記第4級アンモニウム塩が、テトラメチルアンモニウムクロリドまたはトリエチルメチルアンモニウムクロリドである、請求項7に記載の(メタ)アクリル酸グリシジル組成物。
- 前記フェノール系重合禁止剤が、p-メトキシフェノール、ヒドロキノン、又はトパノールA(2-(tert-ブチル)-4,6-ジメチルフェノール)である、請求項6~8のいずれかに記載の(メタ)アクリル酸グリシジル組成物。
- (メタ)アクリル酸グリシジルが、メタクリル酸グリシジルである、請求項6~9のいずれかに記載の(メタ)アクリル酸グリシジル組成物。
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63255273A (ja) * | 1987-04-13 | 1988-10-21 | Osaka Yuki Kagaku Kogyo Kk | アクリル酸グリシジルまたはメタクリル酸グリシジルの精製方法 |
| JPH07118251A (ja) * | 1993-04-06 | 1995-05-09 | Nippon Oil & Fats Co Ltd | (メタ)アクリル酸グリシジルの製造法 |
| JPH07309854A (ja) * | 1994-05-20 | 1995-11-28 | Mitsubishi Gas Chem Co Inc | グリシジルアクリレートまたはグリシジルメタクリレートの精製方法 |
| JP2000212177A (ja) * | 1999-01-20 | 2000-08-02 | Mitsubishi Gas Chem Co Inc | (メタ)アクリル酸グリシジルの精製法 |
| JP2010018538A (ja) * | 2008-07-10 | 2010-01-28 | Nippon Kayaku Co Ltd | エポキシ化合物の製造方法 |
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| JP4662026B2 (ja) * | 2004-12-08 | 2011-03-30 | 三菱瓦斯化学株式会社 | メタクリル酸グリシジルの製造方法 |
| JP4666139B2 (ja) * | 2005-01-12 | 2011-04-06 | 三菱瓦斯化学株式会社 | メタクリル酸グリシジルの精製方法 |
| JP5999342B2 (ja) * | 2012-10-10 | 2016-09-28 | 三菱瓦斯化学株式会社 | メタクリル酸グリシジルの製造方法 |
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Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63255273A (ja) * | 1987-04-13 | 1988-10-21 | Osaka Yuki Kagaku Kogyo Kk | アクリル酸グリシジルまたはメタクリル酸グリシジルの精製方法 |
| JPH07118251A (ja) * | 1993-04-06 | 1995-05-09 | Nippon Oil & Fats Co Ltd | (メタ)アクリル酸グリシジルの製造法 |
| JPH07309854A (ja) * | 1994-05-20 | 1995-11-28 | Mitsubishi Gas Chem Co Inc | グリシジルアクリレートまたはグリシジルメタクリレートの精製方法 |
| JP2000212177A (ja) * | 1999-01-20 | 2000-08-02 | Mitsubishi Gas Chem Co Inc | (メタ)アクリル酸グリシジルの精製法 |
| JP2010018538A (ja) * | 2008-07-10 | 2010-01-28 | Nippon Kayaku Co Ltd | エポキシ化合物の製造方法 |
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| US20240140924A1 (en) | 2024-05-02 |
| JPWO2022158462A1 (ja) | 2022-07-28 |
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