WO2017043416A1 - 2,4,6-トリス(2-ヒドロキシ-3-メチル-4-アルコキシフェニル)-1,3,5-トリアジン化合物、及び2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンの製造方法 - Google Patents
2,4,6-トリス(2-ヒドロキシ-3-メチル-4-アルコキシフェニル)-1,3,5-トリアジン化合物、及び2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンの製造方法 Download PDFInfo
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- WO2017043416A1 WO2017043416A1 PCT/JP2016/075705 JP2016075705W WO2017043416A1 WO 2017043416 A1 WO2017043416 A1 WO 2017043416A1 JP 2016075705 W JP2016075705 W JP 2016075705W WO 2017043416 A1 WO2017043416 A1 WO 2017043416A1
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- compound
- tris
- triazine
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- methyl
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- 0 Cc(c(O)c(cc1)-c2nc(-c(ccc(O*)c3C)c3O)nc(-c(ccc(O*)c3C)c3O)n2)c1O* Chemical compound Cc(c(O)c(cc1)-c2nc(-c(ccc(O*)c3C)c3O)nc(-c(ccc(O*)c3C)c3O)n2)c1O* 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/14—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with hydrogen or carbon atoms directly attached to at least one ring carbon atom
- C07D251/24—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with hydrogen or carbon atoms directly attached to at least one ring carbon atom to three ring carbon atoms
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/28—Only halogen atoms, e.g. cyanuric chloride
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- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B5/00—Optical elements other than lenses
- G02B5/30—Polarising elements
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- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B1/00—Optical elements characterised by the material of which they are made; Optical coatings for optical elements
- G02B1/10—Optical coatings produced by application to, or surface treatment of, optical elements
- G02B1/14—Protective coatings, e.g. hard coatings
Definitions
- the present invention relates to 2,4,6-tris (2-hydroxy-3-methyl-4-alkoxyphenyl) -1,3,5-triazine compound useful as an ultraviolet absorber, and 2,4 as a raw material thereof.
- the present invention relates to a method for producing 6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine.
- UV absorbers with excellent absorption ability in various wavelength ranges are light-resistant. Used for improvement.
- 2,4,6-tris (2-hydroxy-3-methyl-4-alkoxyphenyl) -1,3,5-triazine compound is an ultraviolet absorber excellent in ultraviolet absorbing ability in a long wavelength region. Therefore, it is expected to be used in applications requiring absorption ability in a long wavelength region such as a polarizer protective film.
- 2,4,6-tris (2-hydroxy-3-methyl-4-alkoxyphenyl) -1,3,5-triazine compound 2,4,6-tris (2,4-dihydroxy) is used.
- a method is known in which a reaction between -3-methylphenyl) -1,3,5-triazine and an alkyl halide is produced using dimethylformamide as a solvent and potassium carbonate as a base (Patent Document 1).
- the 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine can be produced by reacting cyanuric chloride with 2-methylresorcinol by using aluminum chloride.
- cyanuric chloride cyanuric chloride
- 2-methylresorcinol 2-methylresorcinol
- Patent Document 2 a method of producing chlorobenzene as a solvent and cyclopentylmethyl ether as an additive
- Patent Document 3 a method of producing using sulfolane as a solvent
- JP 2004-160883 A JP 2009-292754 A JP 2009-292753 A
- An object of the present invention is to provide a production method capable of improving yield and quality in the production of 1,5-triazine compounds. Further, in the production of 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine represented by the formula (1), the yield and quality are improved. It is in providing the manufacturing method which can be performed.
- the method further includes the step of producing the compound (1) by reacting cyanuric chloride with 2-methylresorcinol in the presence of a Lewis acid and an ester compound as an additive.
- the production method according to any one of [5].
- ester compound is at least one selected from the group consisting of ethyl acetate, isopropyl acetate, and hexyl acetate.
- ester compound is at least one selected from the group consisting of ethyl acetate, isopropyl acetate, and hexyl acetate.
- the manufacturing method of the polarizer protective film characterized by including the process of shape
- a method for producing a polarizing plate comprising a step of laminating a polarizer protective film produced by the method described in [10] above on at least one surface of a polarizer.
- the yield of the 2,4,6-tris (2-hydroxy-3-methyl-4-alkoxyphenyl) -1,3,5-triazine compound represented by the formula (3), and Quality can be improved. Furthermore, the yield and quality of 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine represented by the formula (1) can be improved. .
- a reaction solvent and an ester compound as an additive are added to cyanuric chloride for temperature control, and then Lewis acid and 2-methylresorcinol are added to carry out the reaction.
- the reaction solvent is not particularly limited as long as it does not affect the reaction, and specifically, for example, tetrahydrofuran, methyltetrahydrofuran, diethyl ether, 1,4-dioxane, methyl tert-butyl ether, ethylene glycol dimethyl ether, etc.
- Ether solvents such as acetonitrile and propionitrile
- aliphatic hydrocarbon solvents such as pentane, hexane, heptane and methylcyclohexane
- aromatic hydrocarbon solvents such as benzene, toluene, xylene, ethylbenzene and mesitylene
- Ketone solvents such as acetone, methyl ethyl ketone and methyl isobutyl ketone
- Halogen solvents such as methylene chloride, 1,2-dichloroethane and chlorobenzene
- Sulfoxide solvents such as dimethyl sulfoxide and sulfolane N, N-dimethylformamide, N, N-dimethylacetamide, N, N-diethylacetamide, N-methyl-2-pyrrolidone, N-ethyl-2-pyrrolidone, N-methyl- ⁇ -caprolactam, hexamethyl phosphoric
- halogen solvents such as methylene chloride, 1,2-dichloroethane, chlorobenzene
- sulfoxide solvents such as dimethyl sulfoxide and sulfolane
- N N-dimethylformamide, N, N-dimethylacetamide, N, N-diethylacetamide
- Amide solvents such as methyl-2-pyrrolidone, N-ethyl-2-pyrrolidone, N-methyl- ⁇ -caprolactam and hexamethylphosphoramide
- urea solvents such as dimethylpropylene urea, more preferably chlorobenzene, Sulfolane, N, N-dimethylformamide, N, N-dimethylacetamide.
- the upper limit is preferably 100 times weight, more preferably 50 times weight, with respect to 1 part by weight of the cyanuric chloride. Yes, particularly preferably 20 times the weight.
- the lower limit is preferably 0.1 times the weight, more preferably 0.5 times the weight, and particularly preferably 1 times the weight with respect to 1 part by weight of the cyanuric chloride.
- a particularly preferred solvent is chlorobenzene.
- chlorobenzene is 80 weight or less with respect to 1 weight part of cyanuric chloride, More preferably, it is 40 weight or less, Most preferably, it is 20 weight or less. Although a minimum is not specifically limited, Preferably it is 2 weight or more, More preferably, it is 5 weight or more, Most preferably, it is 10 weight or more.
- ester compounds are most suitable. Since the ester compound has an appropriate coordination ability and can appropriately control the reactivity of the Lewis acid, the yield and purity of the compound (1) are improved.
- the ester compound as the additive is not particularly limited, and examples thereof include formic acid ester, acetic acid ester, propionic acid ester, butyric acid ester, isobutyric acid ester, benzoic acid ester, malonic acid ester, and lactone. Further, C 1-6 alkyl ester, C 3-6 cycloalkyl ester, C 7-12 alkyl ester, C 6-12 aryl ester, C 6-12 aryl-C 1-6 alkyl ester and the like can be mentioned.
- the amount of the ester compound used is not particularly limited, but is preferably 60 parts by weight or less, more preferably 30 parts by weight or less, and particularly preferably 15 parts by weight or less with respect to 1 part by weight of cyanuric chloride. Although a minimum is not specifically limited, Preferably it is 0.01 weight part or more, More preferably, it is 0.1 weight part or more, Most preferably, it is 1 weight part or more.
- the Lewis acid used in the present invention is not particularly limited as long as it promotes the reaction according to the present invention.
- the amount of the Lewis acid used is not particularly limited, but it is preferably 8 mol times or less, more preferably 4 mol times or less, and particularly preferably 2 mol times or less with respect to 1 mol of cyanuric chloride. Although a minimum is not specifically limited, Preferably it is 0.2 mol times or more, More preferably, it is 0.5 mol times or more, Most preferably, it is 1 mol times or more.
- the amount of 2-methylresorcinol used is not particularly limited, but is preferably 16 mol times or less, more preferably 8 mol times or less, and particularly preferably 4 mol times or less with respect to 1 mol of cyanuric chloride. Although a minimum is not specifically limited, Preferably it is 0.7 mol times or more, More preferably, it is 1.5 mol times or more, Most preferably, it is 3 mol times or more.
- the addition form of the Lewis acid and 2-methylresorcinol is not particularly limited, but may be added in a solid state or in a state dissolved or suspended in a solvent.
- the temperature may be adjusted once.
- the said temperature should just be set suitably, it can be 20 degreeC or more and 80 degrees C or less, for example.
- the reaction temperature in this step is not particularly limited, but is preferably not higher than the boiling point of the reaction solvent, more preferably not higher than 80 ° C., particularly preferably not higher than 50 ° C. Although a minimum is not specifically limited, Preferably it is more than melting
- the order of addition of the reagents in this step is not particularly limited, but a Lewis acid may be added to a solution containing cyanuric chloride, a reaction solvent, and an ester compound, followed by addition of 2-methylresorcinol, or cyanuric chloride. Further, 2-methylresorcinol may be added to the solution to which the reaction solvent and the ester compound have been added, and then Lewis acid may be added. In addition, Lewis acid and 2-methylresorcinol may be added simultaneously.
- a general post-treatment after the reaction.
- an inert solvent such as toluene is added, the temperature is raised, and hydrochloric acid is added to hydrolyze excess Lewis acid.
- water is distilled off by heating distillation, the solid precipitated by cooling is filtered off, and the obtained solid is washed sequentially with toluene, water, and the like, whereby the crude product of the compound (1) is obtained. obtain.
- the crude body may be reslurried with water or the like and then filtered to remove the remaining aluminum and acidic components to increase the purity.
- the amount of an inert solvent such as toluene used for the treatment after the reaction is not particularly limited, but is preferably 60 parts by weight or less, more preferably 30 parts by weight or less, particularly preferably 1 part by weight of cyanuric chloride. 15 parts by weight or less. Although a minimum is not specifically limited, Preferably it is 1 weight part or more, More preferably, it is 2 weight part or more, Most preferably, it is 5 weight part or more.
- the concentration of hydrochloric acid used for the treatment after the reaction is not particularly limited, but is preferably 35 wt% or less, more preferably 30 wt% or less, and particularly preferably 20 wt% or less with respect to the entire reaction solution. Although a minimum is not specifically limited, Preferably it is 5 wt% or more, More preferably, it is 10 wt% or more, Most preferably, it is 15 wt% or more.
- the amount of hydrochloric acid used is not particularly limited, but is, for example, 16 mol times or less, preferably 8 mol times or less, and more preferably 4 mol times or less with respect to 1 mol of cyanuric chloride. Although a minimum is not specifically limited, For example, it is 0.7 mol times or more, Preferably it is 1.5 mol times or more, More preferably, it is 3 mol times or more.
- the addition temperature of the hydrochloric acid is not particularly limited, but is preferably not more than the boiling point of the reaction solvent, more preferably not more than 150 ° C., particularly preferably not more than 100 ° C. Although a minimum is not specifically limited, Preferably it is more than melting
- the temperature at which the solid is precipitated by cooling is not particularly limited, but is preferably 70 ° C. or less, more preferably 50 ° C. or less, and particularly preferably 30 ° C. or less.
- the lower limit is not particularly limited, but is preferably not less than the melting point of the reaction solvent, more preferably not less than ⁇ 40 ° C., particularly preferably not less than ⁇ 20 ° C.
- the solid separation method is not particularly limited, and the target solid can be obtained by a method such as vacuum filtration, pressure filtration, or centrifugation.
- 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine represented by the formula (1) is added to 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine represented by the formula (1).
- an alkylating agent is further added to carry out the reaction.
- 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine compound is converted into 2,4,6-tris (2-hydroxy-
- the solubility is lowered and precipitates, so that there is an advantage that no further reaction proceeds.
- the compound (1) used in this step may be a free form, a salt with an acid such as hydrochloride, hydrobromide, sulfate, methanesulfonate, or a lithium salt, sodium salt, potassium salt, etc. Any of the alkali metal salts may be used. Further, the usage form of the compound (1) may be a dry crystal, a wet crystal, or an extraction solution.
- the alcohol is not particularly limited.
- the said alcohol or water may be used independently and may use 2 or more types together.
- an alcohol aqueous solution may be used.
- the mixing ratio of water and alcohol in the aqueous alcohol solution may be adjusted as appropriate.
- the concentration of the alcohol can be about 5 wt% or more and 95 wt% or less.
- the amount of the alcohol or water used is not particularly limited, but is preferably 60 parts by weight or less, more preferably 30 parts by weight or less, and particularly preferably 15 parts by weight or less with respect to 1 part by weight of the compound (1). It is. Although a minimum is not specifically limited, Preferably it is 0.2 weight part or more, More preferably, it is 0.5 weight part or more, Most preferably, it is 1 weight part or more.
- the alcohol or water also serves as a reaction solvent, it is not particularly necessary to add an additional solvent, but an additional solvent may be further added for the purpose of improving liquid properties. In addition, the addition of an additional solvent may improve the yield.
- the additional solvent is not particularly limited as long as it does not affect the reaction, and specifically includes, for example, tetrahydrofuran, methyltetrahydrofuran, diethyl ether, 1,4-dioxane, methyl tert-butyl ether, ethylene glycol dimethyl ether and the like.
- Ether solvents such as acetonitrile and propionitrile; ester solvents such as ethyl acetate, n-propyl acetate and isopropyl acetate; aliphatic hydrocarbon solvents such as pentane, hexane, heptane and methylcyclohexane; benzene, Aromatic hydrocarbon solvents such as toluene, xylene, ethylbenzene, mesitylene; ketone solvents such as acetone, methyl ethyl ketone, methyl isobutyl ketone; halogen solvents such as methylene chloride, 1,2-dichloroethane; Sulfoxide solvents such as sulfoxide; N, N-dimethylformamide, N, N-dimethylacetamide, N, N-diethylacetamide, N-methyl-2-pyrrolidone, N-ethyl-2-pyr
- the mixing ratio is not particularly limited.
- the amount of the additional solvent used is not particularly limited and may be appropriately adjusted.
- the ratio of alcohol and water is about 1% by volume or more and 95% by volume or less with respect to the total amount of alcohol, water and additional solvent.
- the proportion of the additional solvent is preferably 2% by volume or more, more preferably 5% by volume or more, further preferably 10% by volume, more preferably 70% by volume or less or 60% by volume or less, and 50% by volume or less or 30 volume% is more preferable, and 20 volume% or less is still more preferable.
- the base is not particularly limited, but is preferably an alkali metal hydroxide, alkali metal alkoxide, alkali metal carbonate, alkali metal bicarbonate, alkaline earth metal hydroxide, alkaline earth metal carbonate, alkaline earth.
- Metallic hydrogen carbonates more preferably potassium hydroxide, potassium alkoxide, potassium carbonate, potassium hydrogen carbonate, and particularly preferably potassium carbonate.
- the amount of the base used is not particularly limited, but is preferably 12 mol times or less, more preferably 6 mol times or less, and particularly preferably 3 mols per 1 mol of the compound (1). Is less than double. Although it does not specifically limit as a minimum, Preferably it is 0.5 mol times or more, More preferably, it is 1 mol times or more, Especially preferably, it is 2 mol times or more.
- the alkylating agent used in this reaction is represented by the formula (2).
- the order of addition of the compound (1), alcohol or water, base, additional solvent and alkylating agent (2) in this step is not particularly limited, but the alkylating agent (2) is preferably added last.
- R represents a C 1-10 alkyl group, C 1-10 straight chain alkyl group, C 1-10 branched chain alkyl group, may be any of C 3-10 cycloalkyl groups.
- An ethyl group, an n-propyl group, an n-butyl group, an n-pentyl group, or an n-hexyl group is preferable, and an n-butyl group or an n-hexyl group is more preferable.
- X represents a leaving group, preferably a halogen atom or a sulfonyloxy group, more preferably a bromine atom, an iodine atom, or a methanesulfonyloxy group.
- the amount of the alkylating agent (2) used is not particularly limited, but is preferably 20 mol times or less, more preferably 10 mol times or less, and particularly preferably 1 mol of the compound (1). Is 5 mole times or less. Although it does not specifically limit as a minimum, Preferably it is 2 mol times or more, More preferably, it is 3 mol times or more, Especially preferably, it is 4 mol times or more.
- the reaction temperature in this step is not particularly limited, but is preferably not higher than the boiling point of the reaction solvent, more preferably not higher than 200 ° C., particularly preferably not higher than 150 ° C. Although a minimum is not specifically limited, Preferably it is more than melting
- the solid is precipitated by adding an acid to neutralize the reaction solution and cooling. By filtering and washing this, 2,4,6-tris (2-hydroxy-3-methyl-4-alkoxyphenyl) -1,3,5-triazine compound (3), which is the target product, is obtained.
- the acid used for the neutralization is not particularly limited, but preferably a mineral acid such as hydrogen chloride, hydrogen bromide, sulfuric acid and nitric acid; ammonium salts such as ammonium chloride, ammonium sulfate and ammonium acetate; trifluoromethanesulfonic acid and paratoluene Sulfonic acids such as sulfonic acid and methanesulfonic acid, more preferably hydrogen chloride, sulfuric acid, and ammonium chloride, and particularly preferably ammonium chloride. These acids may be used as they are or as an aqueous solution.
- a mineral acid such as hydrogen chloride, hydrogen bromide, sulfuric acid and nitric acid
- ammonium salts such as ammonium chloride, ammonium sulfate and ammonium acetate
- trifluoromethanesulfonic acid and paratoluene Sulfonic acids such as sulfonic acid and methanesulfonic acid,
- the amount of the acid used is not particularly limited, but is preferably 20 moles or less, more preferably 10 moles or less, and particularly preferably 5 moles or less, per mole of the compound (1). It is. Although it does not specifically limit as a minimum, Preferably it is 1 mol times or more, More preferably, it is 2 mol times or more, Especially preferably, it is 4 mol times or more. Further, the degree of neutralization may be adjusted as appropriate. For example, the pH can be adjusted to 6.0 or more and 8.0 or less. In an excessively acidic state, the compound (1) may become a salt to increase the solubility and may be difficult to precipitate as a solid. On the other hand, in an excessive basic state, a salt corresponding to the used base may be precipitated.
- the temperature at which the solid is precipitated is not particularly limited, but is preferably 70 ° C. or less, more preferably 50 ° C. or less, and particularly preferably 30 ° C. or less.
- the lower limit is not particularly limited, but is preferably not less than the melting point of the reaction solvent, more preferably not less than ⁇ 40 ° C., particularly preferably not less than ⁇ 20 ° C.
- the solid separation method is not particularly limited, but the target solid can be obtained by a method such as vacuum filtration, pressure filtration, or centrifugation.
- the compound (3) which is the target product, has sufficient purity to exhibit its function as it is, but if further improvement in purity is desired, recrystallization may be performed as necessary.
- the solvent used for recrystallization is preferably tetrahydrofuran, ethyl acetate, toluene, dimethylformamide, or water, and more preferably ethyl acetate.
- a polarizer protective film can be produced using the compound (3) produced by the method of the present invention, and further a polarizing plate can be produced. Specifically, at least the compound (3) produced by the method of the present invention is mixed with a thermoplastic resin to prepare a thermoplastic resin composition, and the thermoplastic resin composition is further formed into a film. Thus, a polarizer protective film can be produced.
- the polarizer protective film is a film that protects the polarizer from ultraviolet rays or the like in the polarizing plate.
- a well-known thing can be used as a thermoplastic resin used for manufacture of a polarizer protective film. Examples thereof include thermoplastic cellulose resins such as triacetyl cellulose; polyester resins such as polyethylene terephthalate; poly (meth) acrylic acid resins.
- the thermoplastic resin composition to be used may be heated to the melting temperature or higher and melt kneaded with at least the compound (3).
- the thermoplastic resin composition for example, fillers, antioxidants, thermal degradation inhibitors, light stabilizers, lubricants, mold release agents, polymer processing aids, antistatic agents, flame retardants, dyes and pigments, Light diffusing agents, organic dyes, matting agents, impact modifiers, foaming agents, fillers, phosphors and the like may be added.
- the thermoplastic resin composition may be formed into a polarizer protective film by forming into a film using, for example, a solution casting method, a melt extrusion method, a calendar method, a compression molding method, or the like. Further, uniaxial stretching or biaxial stretching may be performed.
- the thickness of the film may be adjusted as appropriate, and can be, for example, about 10 ⁇ m or more and 300 ⁇ m or less.
- a polarizing plate can be produced by laminating the polarizer protective film on at least one surface of the polarizer.
- a general polarizer may be used.
- a uniaxially stretched film obtained by adsorbing a dichroic substance such as iodine or a dichroic dye on a hydrophilic film such as a polyvinyl alcohol film can be used.
- the thickness of the polarizer is not particularly limited, but can be, for example, about 1 ⁇ m or more and 100 ⁇ m or less.
- the said polarizer protective film and polarizer can be laminated
- reaction conversion rate to 2,4,6-tris (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine The following reaction conversion rate and purity were calculated by the following formula from each peak area area of the high performance liquid chromatography chart.
- impurities other than the disubstituted product [2-chloro-4,6-di (2,4-dihydroxy-3-methylphenyl) -1,3,5-triazine] Since the amount produced is extremely small, it is not considered in the calculation formula.
- ⁇ Purity> The purity of the target product was calculated from the following calculation formula from the HPLC chart. ⁇ (Peak area area of target) / [(total peak area area) ⁇ (peak area area of blank measurement)] ⁇ ⁇ 100
- Example 1 Triarylation Step Cyanuric chloride (20.00 g, 108.5 mmol), chlorobenzene (369.60 g, 18.48 wt / wt), ethyl acetate (180.00 g, 9.00 wt / wt) were added to add 40 The temperature was adjusted to ° C. Aluminum chloride (21.70 g, 1.50 equivalent) was added over 10 minutes using a solid inlet tube, followed by 2-methylresorcinol (47.14 g, 3.50 equivalent) over 30 minutes. “Wt / wt” means the weight ratio to cyanuric chloride. When reacted at 40 ° C. for 25 hours, the reaction conversion rate was 97%.
- Example 2 to 15 Triarylation Step The procedure of Example 1 was followed except that the additive, reaction temperature and reagent amount were as described in Table 1. The results are shown in Table 1. In addition, none of the compound (4) was detected.
- Comparative Example 1 Use of CPME in Triarylation Step Cyanuric chloride (2.50 g, 13.6 mmol), 2-methylresorcinol (5.91 g, 3.50 equivalent), aluminum chloride (2.72 g, 1.50 equivalent) ), Chlorobenzene (46.20 g, 18.48 wt / wt) and cyclopentyl methyl ether (2.45 g, 0.98 wt / wt, CPME) were added and reacted at 80 ° C. for 2 hours.
- Comparative Examples 4 to 15 Examination of additives in the triarylation step The procedure of Comparative Example 3 was followed except that the additives were changed. When an ether solvent, nitrile solvent, amide solvent, ketone solvent, sulfoxide solvent is used as an additive, or when no additive is used, the liquid property deteriorates, the reaction is poor, or the reaction conversion rate is low. Each became a problem.
- Examples 16 to 18 Examination of Additives in Triarylation Step When an ester solvent was used as an additive, the liquid properties were good and the reaction conversion rate was equal to or higher than that of Comparative Example 2. The results of Comparative Examples 2 to 15 and Examples 16 to 18 are shown in Table 2. In the table, regarding the liquid properties, when the viscosity of the reaction solution is excessively increased and stirring becomes difficult, the result is “bad”, and when the viscosity of the reaction solution does not increase excessively and stirring can be continued. “Good”.
- Example 19 Reaction using alcohol and water as reaction solvent in the trialkylation step
- the compound (1) 25.87 g, 57.82 mmol
- ethanol 170.74 g, 6.60 wt / wt
- the temperature was adjusted to ° C.
- Potassium carbonate (19.18 g, 2.40 equivalents) and hexyl bromide (42.00 g, 4.40 equivalents) were added, the temperature was adjusted to 76 ° C., and the mixture was reacted for 40 hours under reflux.
- Examples 20 to 29 Trialkylation step The procedure of Example 19 was followed except that the reaction solvent, alkylating agent, reaction temperature, and amount of reaction solvent were as shown in Table 3. The results are shown in Table 3. In the table, “DMA” represents N, N-dimethylacetamide.
- the compound (3) (2.10 g, 67%, yield: purity 98.9 area%, the compound (7), and the compound (8) are not detected).
- the yield of the compound (5) was 14%, and the whole amount was removed in the crystallization mother liquor.
- the yield was reduced, and impurities were produced and mixed into the target compound (3).
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Abstract
Description
で表される不純物が副生し、収率及び品質が大きく低下するという課題を認めた。
で表される不純物が副生し、やはり収率及び品質を大きく低下するという課題を認めた。
以下、本発明を示す。
で表される2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンと、一般式(2):RX[式中、RはC1-10アルキル基を表し、Xは脱離基を表す]で表されるアルキル化剤とを、アルコール又は水を含む溶媒中、塩基の存在下で反応させる工程を含むことを特徴とする、下記一般式(3):
[式中、Rは前記と同義を示す]で表される2,4,6-トリス(2-ヒドロキシ-3-メチル-4-アルコキシフェニル)-1,3,5-トリアジン化合物の製造方法。
で表される2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンの製造方法。
少なくとも熱可塑性樹脂と前記化合物(3)とを混合し、熱可塑性樹脂組成物を得る工程、および、
前記熱可塑性樹脂組成物をフィルム状に成形する工程を含むことを特徴とする、偏光子保護フィルムの製造方法。
まず、下記反応スキームで表される2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンの製造方法について説明する。
前記ルイス酸の使用量としては、特に限定されないが、塩化シアヌル1モルに対して、好ましくは8モル倍以下、更に好ましくは4モル倍以下、特に好ましくは2モル倍以下である。下限は、特に限定されないが、好ましくは0.2モル倍以上、更に好ましくは0.5モル倍以上、特に好ましくは1モル倍以上である。
固体の分離方法としては、特に限定されないが、例えば減圧濾過、加圧濾過、又は遠心分離等の方法により、目的物の固体を取得することができる。
続いて、下記反応スキームで表される2,4,6-トリス(2-ヒドロキシ-3-メチル-4-アルコキシフェニル)-1,3,5-トリアジン化合物の製造方法について説明する。
本工程に使用する前記化合物(1)はフリー体でもよいし、塩酸塩、臭化水素酸塩、硫酸塩、メタンスルホン酸塩等の酸との塩、若しくはリチウム塩、ナトリウム塩、カリウム塩等のアルカリ金属塩のいずれであってもよい。また、前記化合物(1)の使用形態としては、乾燥結晶でもよいし、湿結晶、若しくは抽出溶液のいずれであってもよい。
偏光子保護フィルムの製造に用いられる熱可塑性樹脂としては、公知のものを用いることができる。例えば、トリアセチルセルロースなどの熱可塑性セルロース系樹脂;ポリエチレンテレフタレートなどのポリエステル系樹脂;ポリ(メタ)アクリル酸系樹脂などを挙げることができる。
本実施例において、化合物の収率及び品質は、高速液体クロマトグラフィーを用いて分析した。また、純度(area%)は、溶媒ピーク及びシステム由来の波形の乱れに起因するピーク形状(以下、「ブランク」という)を差し引いた後の全ピーク面積に対する対象物の面積をいう。また、各不純物量(area%)は、対象物の面積に対する各不純物の面積をいう。
カラム: Senshu Pal PEGASIL ODS
4.6mmI.D.×250mm
カラム温度: 40℃
流速: 0.8mL/min
検出波長: 345nm
移動相A: 蒸留水
移動相B: テトラヒドロフラン
注入量: 10μL
グラジエントパターン
0.00分 移動相A:移動相B=50:50
5.00分 移動相A:移動相B=50:50
25.00分 移動相A:移動相B=25:75
30.00分 移動相A:移動相B=25:75
30.01分 移動相A:移動相B=50:50
40.00分 STOP
カラム: Senshu Pal PEGASIL ODS
4.6mmI.D.×250mm
カラム温度: 40℃
流速: 0.8mL/min
検出波長: 345nm
移動相A: 蒸留水
移動相B: テトラヒドロフラン
注入量: 10μL
グラジエントパターン
0.00分 移動相A:移動相B=35:65
30.00分 移動相A:移動相B=25:75
35.00分 移動相A:移動相B=20:80
45.00分 移動相A:移動相B=20:80
45.01分 移動相A:移動相B=35:65
55.00分 STOP
以下の反応変換率及び純度は、高速液体クロマトグラフィーチャートの各ピークエリア面積より、以下の式により算出した。また、反応変換率の計算において、二置換体[2-クロロ-4,6-ジ(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジン]以外の不純物に関しては、その生成量が極微量であるため、計算式で考慮していない。
{[2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンのピークエリア面積]/[2-クロロ-4,6-ジ(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンのピークエリア面積+2,4,6-トリス(2,4-ジヒドロキシ-3-メチルフェニル)-1,3,5-トリアジンのピークエリア面積)]}×100
同様に、二置換体[2-(2,4-ジヒドロキシ-3-メチルフェニル)-4,6-ジ(2-ヒドロキシ-3-メチル-4-ヘキシルオキシフェニル)-1,3,5-トリアジン]以外の不純物に関しては、その生成量が極微量であるため、計算式で考慮していない。
{[2,4,6-トリス(2-ヒドロキシ-3-メチル-4-ヘキシルオキシフェニル)-1,3,5-トリアジンのピークエリア面積)]/[2-(2,4-ジヒドロキシ-3-メチルフェニル)-4,6-ジ(2-ヒドロキシ-3-メチル-4-ヘキシルオキシフェニル)-1,3,5-トリアジンのピークエリア面積+2,4,6-トリス(2-ヒドロキシ-3-メチル-4-ヘキシルオキシフェニル)-1,3,5-トリアジンのピークエリア面積)]}×100
目的物の純度は、HPLCチャートから、以下の計算式から算出した。
{(目的物のピークエリア面積)/[(全ピークエリア面積)-(ブランク測定のピークエリア面積)]}×100
塩化シアヌル(20.00g,108.5mmol)、クロロベンゼン(369.60g,18.48wt/wt)、酢酸エチル(180.00g,9.00wt/wt)を加えて40℃に温調した。固体導入管を用いて塩化アルミニウム(21.70g,1.50当量)を10分かけて加えた後、2-メチルレゾルシノール(47.14g,3.50当量)を30分かけて加えた。なお、「wt/wt」は塩化シアヌルに対する重量比を意味する。40℃で25時間反応させたところ、反応変換率は97%であった。トルエン(217.40g,10.87wt/wt)を加えた後、80℃まで昇温した。18wt%塩酸(85.90g,3.80当量)を加えて86℃まで昇温して塩化アルミニウムの分解を1時間かけて行った後、加熱蒸留による脱水を4時間行った。25℃まで冷却後、ブフナー漏斗にて濾過を行い、前記化合物(1)の粗体を取得した。得られた粗体を水(660.00g,33.00wt/wt)でリスラリーした後、ブフナー漏斗にて濾過を行い、前記化合物(1)を取得した(収率93%,純度96.9area%,前記化合物(4)は不検出)。
添加剤、反応温度および試剤量を表1に記載の通りとした以外は、前記実施例1の操作に従った。結果を表1に示す。尚、前記化合物(4)はいずれも不検出であった。
塩化シアヌル(2.50g,13.6mmol)、2-メチルレゾルシノール(5.91g,3.50当量)、塩化アルミニウム(2.72g,1.50当量)、クロロベンゼン(46.20g,18.48wt/wt)、シクロペンチルメチルエーテル(2.45g,0.98wt/wt,CPME)を加えて80℃で2時間反応させた。80℃において18wt%塩酸(10.76g,3.8当量)を加えて90℃まで昇温し、塩化アルミニウムの分解を1時間かけて行った後、トルエン(27.18g,10.87wt/wt)を加えて還流脱水を2時間行った。25℃まで冷却後、ブフナー漏斗にて濾過を行い、前記化合物(1)(3.88g,収率64%、純度80.9area%、前記化合物(4)を14.7area%含有)を取得した。このように、添加剤としてシクロペンチルメチルエーテルを用いた場合には、不純物である前記化合物(4)が生成し、目的化合物の収率と純度が低下してしまった。
塩化シアヌル(15.00g,81.34mmol)、クロロベンゼン(277.2g,18.48wt/wt)、シクロペンチルメチルエーテル(14.70g,0.98wt/wt)を加えて25℃に温調した。固体導入管を用いて塩化アルミニウム(16.27g,1.50当量)を1時間かけて加えた後、2-メチルレゾルシノール(35.34g,3.50当量)を1時間かけて加えた。25℃で18時間反応させたところ、下記式(6):
で表される反応中間体が残存し、反応変換率は93%であった。続いて比較例1と同様の後処理を実施し、前記化合物(30.28g,収率83%,純度88.6area%,前記化合物(4)を4.3area%含有)を取得した。
塩化シアヌル(0.50g,2.7mmol)、クロロベンゼン(9.24g,18.48wt/wt)、ジブチルエーテル(0.49g,0.98wt/wt)を加えて25℃に温調した。塩化アルミニウム(0.54g,1.5当量)を加えた後、2-メチルレゾルシノール(1.18g,3.50当量)を加えて25℃で反応させたところ、液性状の悪化により攪拌困難となった。尚、反応変換率は62%であった。
添加剤を変更した以外は前記比較例3の操作に従った。添加剤としてエーテル系溶媒、ニトリル系溶媒、アミド系溶媒、ケトン系溶媒、スルホキシド系溶媒を用いた場合、又は添加剤なしの場合には、液性状の悪化、反応不良、又は反応変換率が低いことがそれぞれ問題となった。
添加剤としてエステル系溶媒を用いた場合、液性状は良好であり、反応変換率も比較例2と同等以上であった。
上記比較例2~15、実施例16~18の結果を表2に示す。表中、液性状に関して、反応溶液の粘度が過度に上昇して攪拌が困難となった場合を「悪い」とし、反応溶液の粘度が過度に上昇せず攪拌の継続が可能であった場合を「良好」としている。
前記化合物(1)(25.87g,57.82mmol)、エタノール(170.74g,6.60wt/wt)を加えて22℃に温調した。炭酸カリウム(19.18g,2.40当量)、ヘキシルブロマイド(42.00g,4.40当量)を加えて76℃に温調し、還流下で40時間反応させた。水(170.74g,6.6wt/wt)、塩化アンモニウム(14.85g,4.80当量)を添加して中和し、25℃まで冷却すると固体が析出した。これを濾過、洗浄することにより前記化合物(3)の粗体を取得した。粗体に酢酸エチル(150.00g,5.00wt/wt)を加えて57℃で溶解した後、1℃まで冷却して15時間熟成した。これを濾過、洗浄することにより、前記化合物(3)を取得した(32.74g,81%、純度99.0area%,後記化合物(7)及び後記化合物(8)はいずれも不検出)。尚、前記化合物(5)の収率は2%であり、晶析母液に全量除去された。
反応溶媒、アルキル化剤、反応温度、反応溶媒量を表3に記載の通りとした以外は前記実施例19の操作に従った。結果を表3に示す。なお、表中、「DMA」はN,N-ジメチルアセトアミドを示す。
前記化合物(1)(1.00g,2.23mmol)、炭酸カリウム(0.556g,1.80当量)、N,N-ジメチルホルムアミド(5.27g,5.27wt/wt)を加えて90℃に温調した。ここに、ヘキシルブロマイド(1.22g,3.30当量)を加えて90℃で2時間反応させた。反応液を25℃まで冷却した後、クロロホルム(16.54g,16.54wt/wt)、水(5.59g,5.59wt/wt)を加えて生成物を有機層に抽出した。当該有機層を無水硫酸ナトリウムで乾燥した後、溶媒を留去して固相を得た。当該固相を酢酸エチルから再結晶することにより、前記化合物(3)(1.00g,収率:64%,純度94.8area%、前記化合物(7)を1.06area%含有,前記化合物(8)を3.93area%含有)。このように、反応溶媒としてN,N-ジメチルホルムアミドのみを用いた場合には、収率が低下し、また、不純物が生成して目的化合物(3)に混入した。
前記化合物(1)(2.00g,4.47mmol)、炭酸カリウム(1.48g,2.4当量)、N,N-ジメチルホルムアミド(10.54g,5.27wt/wt)を加えて60℃に温調した。ここに、ヘキシルブロマイド(3.25g,4.4当量)を加えて60℃で23時間反応させた。酢酸エチル(33.08g,16.54wt/wt)、水(15.52g,7.76wt/wt)を加え、75℃まで冷却した後、生成物を有機層に抽出し、有機層を更に水(4.00g,2wt/wt)で洗浄した。当該有機層の溶媒を留去して固相を得た。当該固相に酢酸エチル(28.92g,14.46wt/wt)を加えて75℃で溶解した後、0℃まで冷却して1時間熟成した。これを分離、乾燥することにより、前記化合物(3)(2.10g,67%,収率:純度98.9area%,前記化合物(7),及び前記化合物(8)はいずれも不検出)。尚、前記化合物(5)の収率は14%であり、晶析母液に全量除去された。このように、反応溶媒としてN,N-ジメチルホルムアミドのみを用いた場合には、収率が低下し、また、不純物が生成して目的化合物(3)に混入した。
Claims (11)
- Rがヘキシル基、又はブチル基である、請求項1に記載の製造方法。
- Xが臭素原子、ヨウ素原子、又はメタンスルホニルオキシ基である、請求項1、又は2に記載の製造方法。
- 前記アルコールが、エタノール、1-プロパノール、2-プロパノール、1-ブタノール及び1-ヘキサノールからなる群より選ばれる少なくとも1種である、請求項1~3のいずれかに記載の製造方法。
- さらに、前記反応の後に酸水溶液を添加して反応液を中和することにより前記化合物(3)を固体として取得する工程を含む、請求項1~4のいずれかに記載の製造方法。
- さらに、ルイス酸、及び添加剤としてエステル化合物の存在下、塩化シアヌルと2-メチルレゾルシノールとを反応させることにより、前記化合物(1)を製造する工程を含む、請求項1~5のいずれかに記載の製造方法。
- 前記エステル化合物が、酢酸エチル、酢酸イソプロピル、酢酸ヘキシルからなる群より選ばれる少なくとも1種である、請求項6に記載の製造方法。
- 前記エステル化合物が、酢酸エチル、酢酸イソプロピル、酢酸ヘキシルからなる群より選ばれる少なくとも1種である、請求項8に記載の製造方法。
- 請求項1~7のいずれかの方法により前記化合物(3)を製造する工程、
少なくとも熱可塑性樹脂と前記化合物(3)とを混合し、熱可塑性樹脂組成物を得る工程、および、
前記熱可塑性樹脂組成物をフィルム状に成形する工程を含むことを特徴とする、偏光子保護フィルムの製造方法。 - 偏光子の少なくとも一方の面に、請求項10に記載の方法で製造された偏光子保護フィルムを積層する工程を含むことを特徴とする、偏光板の製造方法。
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US20180305325A1 (en) | 2018-10-25 |
CN108026055B (zh) | 2021-06-15 |
EP3348549B1 (en) | 2020-06-17 |
EP3348549A4 (en) | 2019-07-10 |
CN108026055A (zh) | 2018-05-11 |
JP6890092B2 (ja) | 2021-06-18 |
EP3348549A1 (en) | 2018-07-18 |
JPWO2017043416A1 (ja) | 2018-06-28 |
US10351538B2 (en) | 2019-07-16 |
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