JP2000226449A - Production of alkyl-substituted phenol polymer - Google Patents

Abstract

PROBLEM TO BE SOLVED: To obtain a phenol polymer having high heat stability, freed from a gel insoluble in a solvent, and reduced in discoloration by polymerizing an alkyl-substituted phenol in the presence of oxygen and a copper/tridentate ligand catalyst. SOLUTION: An alkyl-substituted phenol represented by formula I is polymerized in the presence of oxygen and a copper complex catalyst comprising a copper atom and a tridentate ligand in which the coordinated atoms are nitrogen atoms. In formula I, R1 to R3 are each independently hydrogen, an alkyl or a substituted alkyl; at least either of R1 and R2 is an alkyl or a substituted alkyl; at least either of R2 and R3 is hydrogen; and R1 and R2 may be combined with each other to form a ring. A copper complex catalyst represented by formula II is desirable. In formula II, R4s, which may be the same as or different from each other, are each a hydrocarbon group, a substituted hydrocarbon group, or hydrogen, R5s, which may be the same as or different from each other, are each a divalent hydrocarbon group or a substituted hydrocarbon group; X is a counter ion; and n is the number of Xs and suitably determined according to the valence of the copper and the valance of X.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

[0001] The present invention relates to a method for producing an alkyl-substituted phenol polymer.

[0002]

2. Description of the Related Art A method of oxidatively polymerizing 2,6-disubstituted phenols using a copper catalyst is disclosed in JP-B-36-1869.
Numerous methods are known, such as Japanese Patent Publication No. 2 (1994), and it is widely known that 2,6-disubstituted phenol polymers exhibit high heat resistance. J. Am. Chem. Soc. 81, 6335-6336 (1959) discloses a synthesis example of a polymer of an alkyl-substituted phenol, 2,6-dimethylphenol, Macromolecules, 2, 107-108.
(1969) reports a synthesis example of a polymer of 2,6-diphenylphenol which is an aryl-substituted phenol. However, alkyl substitution to phenol is generally much easier than aryl substitution, and alkyl-substituted phenolic polymers are more economically advantageous in terms of monomer cost.

[0003] On the other hand, for alkyl-substituted phenols in which at least one ortho position is a hydrogen atom, a method of carrying out oxygen oxidation polymerization using a copper catalyst is known. For example, as an oxidation polymerization catalyst for 2,5-dimethylphenol,
Ecletica Quim., 1 as a copper / bidentate amine ligand catalyst
8, 93-100 (1993) reports a copper / tetramethylethylenediamine catalyst. As a copper / monodentate amine ligand catalyst, Polymer, 20 (8), 995-1002 (1979)
Dimethylpyridine catalyst, Chem. Prum., 22 (9), 451-454
(1972) added a copper / monoalkylamine catalyst to Polimery, 1
4 (11), 535-538 (1969) report a copper / dialkylamine catalyst. However, the polymers obtained by the methods using these catalysts have a problem that they have low thermal stability, contain a gel component insoluble in a solvent, and are colored.

[0004] The present inventors have disclosed in Japanese Patent Application Laid-Open No. 10-1681.
No. 80, in the production of poly (2-phenyl-1,4-phenylene oxide) by oxidative polymerization of 2-phenylphenol, which is an aryl-substituted phenol having one hydrogen atom at the ortho position, the coordination atom is nitrogen. A method of polymerizing in a specific reaction solvent and at a specific reaction temperature using a copper complex catalyst comprising a tridentate ligand as an atom and a copper atom is disclosed. However, in this method using 2-phenylphenol, a copper / bidentate ligand catalyst (Japanese Unexamined Patent Publication No.
The heating of the polymer to 100 ° C. to 400 ° C. using either the 168179 example 2) or the copper / tridentate catalyst (Example 1 of JP-A-10-168180). Weight loss or thermal stability was substantially similar.

[0005]

SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a polymer having high heat stability, containing no gel insoluble in a solvent, and having low coloration, using a low-cost alkyl-substituted phenol. Is to provide.

[0006]

The present inventors have conducted intensive studies to achieve the above-mentioned object. As a result, surprisingly, in the case of an alkyl-substituted phenol, the copper-substituted phenol is surprisingly different from the case of an aryl-substituted phenol. Using a / tridentate ligand catalyst results in a 10% higher heating weight loss temperature, no gel content, and less coloring than using a conventional copper / bidentate ligand catalyst or copper / monodentate ligand catalyst. Finding that a polymer can be produced,
The present invention has been completed.

That is, the present invention provides an alkyl-substituted phenol represented by the following general formula (I) in the presence of a copper complex catalyst comprising a tridentate ligand in which oxygen and a coordinating atom are a nitrogen atom and a copper atom. A method for producing an alkyl-substituted phenol polymer characterized by polymerizing

[0008]

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[0009] (wherein, R ¹ to R ³ are each independently a hydrogen atom, an alkyl group or a substituted alkyl group, at least one of R ¹ and R ² is an alkyl or substituted alkyl group, R ² or R ^At least one of ³ is a hydrogen atom, and R ¹ and R ² may form a ring.).

[0010]

BEST MODE FOR CARRYING OUT THE INVENTION The alkyl-substituted phenol used in the present invention is an alkyl-substituted phenol represented by the above general formula (I). R ^{1 to} R ^{3 in} the general formula (I) are each independently a hydrogen atom, an alkyl group or a substituted alkyl group, and at least one of R ¹ and R ² is an alkyl group or a substituted alkyl group; ² or R
^At least one of ³ is a hydrogen atom. In addition,
R ¹ and R ² may form a ring. The alkyl group in R ¹ to R ³ in the general formula (I), if not form a ring with R ¹ and R ^2, preferably an alkyl having 1 to 20 carbon atoms and more preferably having 1 to 20 carbon atoms Groups. Specifically, methyl, ethyl, n-propyl, iso-propyl, n-butyl, iso-butyl, t-butyl, pentyl, cyclopentyl,
Hexyl group, cyclohexyl group, heptyl group, octyl group, nonyl group, decyl group, dodecyl group, and octadecyl group are exemplified. When R ¹ and R ² form a ring, 5-7
And R ¹ and R ² are a — (CH ₂ ) ₃ — group or — (CH ₂ )
More preferably, it is a ₄ -group.

Examples of the substituted alkyl group represented by R ^{1 to} R ³ in the general formula (I) include the above-mentioned alkyl groups substituted with an aryl group, a halogen atom, an alkoxy group, etc. 20 substituted alkyl groups,
More preferably, a substituted alkyl group having 1 to 1 carbon atoms is used. Specific examples include a benzyl group, a phenylethyl group, a pentafluorobenzyl group, a trifluoromethyl group, a methoxyethyl group, and a (methoxyethoxy) ethoxy group. R ^{1 to} R ^{3 in} the general formula (I) are each independently preferably a hydrogen atom or an alkyl group having 1 to 12 carbon atoms, more preferably a hydrogen atom or an alkyl group having 1 to 6 carbon atoms. It is.

In the present invention, the alkyl-substituted phenol can be used alone or as a mixture as a starting material. Further, the alkyl-substituted phenol can be used as a mixture with phenol and / or 4-phenoxyphenol. The copper complex catalyst used in the present invention is a copper complex catalyst comprising a tridentate ligand, which is a nitrogen atom, and a copper atom.

The tridentate ligand in the copper complex catalyst used in the present invention is a tridentate ligand whose coordinating atom is a nitrogen atom. In the present invention, the term “ligand” refers to a chemical dictionary (first edition,
(Tokyo Kagaku Dojin, 1989) refers to a molecule or ion bound to a certain atom by a coordination bond. The atoms directly involved in the bond are called coordinating atoms. A tridentate ligand is a ligand having three coordinating atoms. A catalyst comprising a bidentate or monodentate ligand in which the coordinating atom is a nitrogen atom and a copper atom is not preferred because the resulting alkylphenol polymer has a low 10% heating loss temperature.

The tridentate ligand used in the present invention is not particularly limited, except that the coordinating atom is a nitrogen atom. Specific examples of such tridentate ligands include diethylenetriamine, bis (2-pyridylmethyl) amine, bis (2-pyridylethyl) amine, bis (2-imidazolylmethyl) amine, bis (2-oxazolylmethyl) ) Amine, bis (2
-Thiazolylmethyl) amine, N- (2-pyridylmethylidene) -N- (2-pyridylmethyl) amine, 2,
2 ′: 6 ′, 2 ″ -terpyridine, 3- (2-pyridylmethylimino) -2-butanone oxime, tris (2-
Pyridyl) methane, tris (2-imidazolyl) methane, tris (1-pyrazolyl) methane, tris (1-pyrazolyl) phosphate, tris (1-pyrazolyl) borate, 1,4,7-triazacyclononane, or the like, or Derivatives thereof can be mentioned. The valence of the copper atom in the copper complex catalyst used in the present invention is 0 to 3, but preferably 1 or 2.

In the copper complex catalyst used in the present invention, the ratio of the tridentate ligand to the copper atom is not particularly limited. Is preferably one or more. More preferably 1 to 3,
More preferably, it is one.

In the copper complex catalyst used in the present invention, the structure other than the ligand and the copper atom is not particularly limited as long as the catalytic activity is not deactivated. In the copper complex catalyst of the present invention, a solvent or the like may be coordinated in the raw material of the complex, the synthesis process and / or the oxidative polymerization process.

In some cases, the copper complex catalyst used in the present invention needs a counter ion for maintaining electrical neutrality. As the counter anion, a conjugated base of Bronsted acid is usually used, and specific examples include fluoride ion, chloride ion, bromide ion, iodide ion,
Sulfate, nitrate, carbonate, perchlorate, tetrafluoroborate, hexafluorophosphate, methanesulfonate, trifluoromethanesulfonate, toluenesulfonate, acetate, trifluoroacetate, propion Acid ions, benzoate ions, hydroxide ions, oxide ions, methoxide ions, ethoxide ions and the like can be mentioned. As the counter anion, preferably chloride ion, bromide ion, iodide ion, sulfate ion, nitrate ion, acetate ion, hydroxide ion or methoxide ion, more preferably chloride ion, bromide ion, sulfate ion or It is a nitrate ion. As the counter cation, a cation such as an alkali metal or an alkaline earth metal can be appropriately used.

The copper complex catalyst used in the present invention is preferably a copper complex represented by the following general formula (II).

[0019]

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(Wherein, R ⁴ represents a hydrocarbon group, a substituted hydrocarbon group or a hydrogen atom, and all R ⁴ may be the same or different. R ⁵ is a divalent hydrocarbon group or a substituted hydrocarbon group) represents a group, all of R ⁵ is optionally be the same or different .X is a counter anion, n represents a number of X, it is suitably determined by the valence of copper and X.)

The hydrocarbon group represented by R ⁴ in the general formula (II) may be an alkyl group having 1 to 20 carbon atoms, an aralkyl group having 7 to 20 carbon atoms or 6 to 20 carbon atoms.
Are preferred, specifically, a methyl group, an ethyl group, a n-propyl group, an iso-propyl group, an n-butyl group, an iso-butyl group, a t-butyl group, a 1-pentyl group, and a 3-pentyl group , Cyclopentyl group, hexyl group,
Cyclohexyl group, octyl group, decyl group, 4-methylcyclohexyl group, 4-t-butylcyclohexyl group,
3,5-dimethylcyclohexyl group, benzyl group, 2-
Examples include a phenylethyl group, a 1-phenylethyl group, a phenyl group, a 1-naphthyl group, and a 2-naphthyl group.

The substituted hydrocarbon group for R ⁴ in the general formula (II) is the above-mentioned preferred hydrocarbon group substituted with a halogen atom, an alkoxy group, a disubstituted amino group and the like. Examples include a phenylmethyl group, a methoxyethyl group, a diphenylaminopropyl group and the like.

R ^{4 in the} general formula (II) is preferably a hydrocarbon group, more preferably an alkyl group having 1 to 20 carbon atoms or an aralkyl group having 7 to 20 carbon atoms.
Alkyl groups having 2 to 12 carbon atoms are more preferred.

The divalent hydrocarbon group represented by R ⁵ in the general formula (II) includes an alkylene group having 1 to 20 carbon atoms, a cycloalkylene group having 3 to 20 carbon atoms or a cycloalkylene group having 6 to 20 carbon atoms. An arylene group is preferable, and specific examples include a methylene group, an ethylene group, a 1,2-propylene group, a 1,3-propylene group, a 2,4-butylene group,
4-dimethyl-2,4-butylene group, 1,2-diphenyl-1,2-ethylene, 1,2-cyclopentylene group,
Examples thereof include a 1,2-cyclohexylene group and a 1,2-phenylene group.

The divalent substituted hydrocarbon group represented by R ⁵ in the general formula (II) is the above-mentioned preferred divalent hydrocarbon group substituted with a halogen atom, an alkoxy group, a disubstituted amino group and the like. For example, tetrafluoro-1,2-
Examples thereof include an ethylene group, a 4,5-dimethoxy-1,2-phenylene group, and a 4-dimethylamino-1,2-phenylene group.

R ^{5 in the} general formula (II) is preferably a divalent hydrocarbon group, more preferably an alkylene group having 1 to 20 carbon atoms or a cycloalkylene group having 3 to 20 carbon atoms. Alkylene groups of numbers 2 to 6 are more preferred, and ethylene groups are particularly preferred.

In the general formula (II), the valence of copper is 1
Or 2, X is a counter anion, and n is the number of Xs, determined by the valence of copper.

In the general formula (II), the structure other than the above is not particularly limited as long as the catalyst ability is not deactivated. The transition metal complex catalyst used in the present invention includes
A solvent or the like may be coordinated in the raw material of the complex, in the synthesis process and / or the oxidative coupling reaction process.

The copper complex used in the present invention can be synthesized by, for example, a method of mixing a tridentate ligand compound and a copper compound in an appropriate solvent. As the transition metal compound, a Bronsted acid salt of a transition metal or the like is appropriately used. As the tridentate ligand compound, a commercially available product can be used as appropriate, and is described in J. Chem. Soc. Dalton Trans., 83 (199
3). And J. Am. Chem. Soc., 8865, 117 (1995). As the copper complex, a complex synthesized in advance can be used, but the complex may be formed in a reaction system.

In the present invention, the catalysts can be used alone or as a mixture. In the present invention, the catalyst can be used in any amount, but generally, the amount of the transition metal compound is preferably 0.001 to 50 mol%, more preferably 0.01 to 10 mol%, based on the phenolic starting material. Is more preferred.

In the catalyst used in the present invention, when the copper valence of the copper complex is divalent and has a conjugate base of an acid stronger than phenol as a counter ion, the copper complex catalyst is deactivated. It is preferable that a base not to be present coexist with the counter ion in an amount of 1/4 equivalent or more during the polymerization. Examples of such bases include hydroxides, oxides, alkoxides of alkali metals or alkaline earth metals such as sodium hydroxide, potassium hydroxide, calcium oxide, sodium methoxide, sodium ethoxide; methylamine, ethylamine, Amines such as propylamine, butylamine, dibutylamine and triethylamine; and pyridines such as pyridine, 2-methylpyridine, 2,6-dimethylpyridine and 2,6-diphenylpyridine. It is more preferable that alkoxides, amines or pyridines coexist with the counter ion in an amount of 1/4 equivalent or more, and it is even more preferable that the substituted pyridines coexist in an amount of 1/2 equivalent or more.

In the present invention, the oxidizing agent is oxygen, which may be a mixture with an inert gas or air. The amount of oxygen to be used is usually at least an equivalent or a large excess with respect to the phenolic starting material.

Although the reaction of the present invention can be carried out in the absence of a reaction solvent, it is generally preferable to use a solvent. The solvent is not particularly limited as long as it is inert to the phenolic starting material and liquid at the reaction temperature. Preferred examples of the solvent include aromatic hydrocarbons such as benzene, toluene and xylene; linear and cyclic aliphatic hydrocarbons such as heptane and cyclohexane; halogenated hydrocarbons such as chlorobenzene, dichlorobenzene and dichloromethane; acetonitrile , Nitriles such as benzonitrile; methanol, ethanol, n-
Alcohols such as propyl alcohol and iso-propyl alcohol; ethers such as dioxane, tetrahydrofuran and ethylene glycol dimethyl ether;
Amides such as N-dimethylformamide and N-methylpyrrolidone; nitro compounds such as nitromethane and nitrobenzene; and water. Aromatic hydrocarbons, chain and cyclic aliphatic hydrocarbons, halogenated hydrocarbons, nitriles, ethers or nitro compounds are more preferred, and aromatic hydrocarbons or halogenated hydrocarbons are more preferred. These are used alone or as a mixture.

When the solvent is used, it is used in such a ratio that the concentration of the phenolic starting material is preferably 0.5 to 50% by weight, more preferably 1 to 30% by weight.
The reaction temperature for carrying out the present invention is not particularly limited as long as the reaction medium is in a liquid state. If no solvent is used, a temperature above the melting point of the phenolic starting material is required. A preferred temperature range is from 0 ° C to 200 ° C, more preferably from 0 ° C to 150 ° C, even more preferably from 0 ° C to 100 ° C.
° C. The reaction time varies depending on reaction conditions such as the reaction temperature, but is usually 1 hour or more, preferably 3 to 300 hours. In the present invention, the intended alkyl-substituted phenol polymer can be separated by a usual method. For example, a method in which a poor solvent for a polymer such as methanol or hexane is added to the reaction mixture in a large excess, the precipitated polymer is filtered, washed with the poor solvent, and then dried. The polymer obtained by the method of the present invention has the following repeating unit.

[0035]

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(In the formula, R ^{1 to} R ³ have the same meanings as described above.)

[0037]

The present invention will be described in more detail with reference to the following examples, but the scope of the present invention is not limited by these examples.

(I) Analysis Conversion of alkyl-substituted phenol (Conv.): 15 m of reaction mixture containing diphenyl ether as internal standard substance
g, acidified by adding a small amount of concentrated hydrochloric acid,
2 g of methanol was added to obtain a measurement sample. This sample was subjected to high performance liquid chromatography (pump: SC8020 system manufactured by Tosoh Corporation, detector: PD- manufactured by Tosoh Corporation)
8020, detection wavelength: 278 nm, column: ODS-AM manufactured by YMC, developing solvent: methanol / water = 68: 32
38 minutes after the start, the concentration was changed to 100/0, and then kept until 50 minutes.), And diphenyl ether was quantified as an internal standard.

Yield (%): After completion of the polymerization, a large excess of methanol or a methanol / water mixed solvent was added to the reaction mixture, and the precipitated polymer was dissolved in methanol or methanol / water.
Washed thoroughly with a water mixed solvent. The yield is the ratio of the methanol-insoluble component thus obtained. However, the case where the yield is lower than the conversion rate is considered to be due to the fact that many polymers are soluble in methanol. Solubility of 2,5-dimethylphenol polymer: 1 mg of polymer was added to 1,2-
To 1 ml of dichlorobenzene (abbreviated as oDCB), add 15 ml
The presence or absence of an insoluble portion (referred to as gel content) when heated to 0 ° C. was observed.

Number average molecular weight (Mn) and weight average molecular weight (Mw) of the polymer: The polymer was analyzed by gel permeation chromatography, and the weight average molecular weight (Mw) and number average molecular weight (Mn) were measured as standard polystyrene equivalent values. . 2,
For 5-dimethylphenol polymer, Polymer Labo
RatLab's PL-GPC210 system enables PolymerLab
oratories Plgel 10um MIXED-B (3 columns) and 1,2-dichlorobenzene (containing 2,6-di-t-butyl-4-methylphenol 0.01% w / v) as a developing solvent.
The measurement was performed at 0 ° C. For other alkyl-substituted phenolic polymers, pump: SC8020 system manufactured by Tosoh Corporation, detector: RI-8020 manufactured by Tosoh Corporation, column:
Tosoh TSKGELα-M 2 bottles, developing solvent: 0.4
The measurement was performed at 60 ° C. using N, N-dimethylformamide containing wt% LiCl.

10% loss on heating of polymer (Td10): T
In a G analysis (TG-DTA2000S manufactured by MAC SCIENCE), the temperature was raised from room temperature to 500 ° C. at a rate of 10 ° C./min in an argon atmosphere, and a temperature at which a 10% weight loss was observed was measured.

(Ii) Oxidative Polymerization of Alkylphenols Example 1 In a 25 ml two-necked round bottom flask equipped with a magnetic stirrer,
A 2 L rubber balloon filled with oxygen was attached, and the inside of the flask was replaced with oxygen. To this, Cu (Cl2) (1,4,7-triisopropyl-
1,4,7-triazacyclononane) (J. Am. Chem. Soc., 12
0, 8529, (1995). Abbreviated as Cu (tacn). ) 0.006
mmol, 2,5-dimethylphenol1.2mmol
And 2,6-diphenylpyridine 0.06 mmol as a base
Was dissolved in 2.4 g of toluene. This is 4
It was kept warm at 0 ° C. and stirred vigorously. After 72 hours, a few drops of concentrated hydrochloric acid were added to make the mixture acidic, and then 25 ml of methanol was added.
The precipitated polymer was collected by filtration. After washing three times with 10 ml of methanol and drying under reduced pressure at 60 to 100 ° C. for 6 hours, a white polymer was obtained. This polymer was poly (2,5-dimethyl-1,4-phenylene oxide). Table 1 shows the analysis results of the polymer.

[0043]

[Table 1]

Example 2 A white polymer was obtained in the same manner as in Example 1 except that the amount of Cu (tacn) was 0.06 mmol, the amount of 2,6-diphenylpyridine was 0.6 mmol, and the reaction time was 24 hours. Was. Table 1 shows the results.

Comparative Examples 1 to 4 A brownish polymer was obtained in the same manner as in Example 2 except that the catalyst and the reaction time were changed as shown in Table 1. Table 1 shows the results. For the catalyst, Cu (tmed) is Cu ₂ (C
l) ₂ (OH) ₂ (N, N, N ', N "-tetramethylethylenediamine) ₂
CuCl / 2,6-Me ₂ Py is CuCl / 2,6-dimethylpyridine (1/3 mol / mol), and CuCl / n-Pr ₂ NH is CuCl / di-
n-butylamine (1/12 mol / mol) and CuCl ₂ /
c-HexNH ₂ is CuCl ₂ .2H ₂ O / cyclohexylamine (1 /
16 mol / mol).

As described above, from Examples 1 and 2 and Comparative Examples 1-4,
The method using a copper complex catalyst of a tridentate ligand has a higher 10% weight loss temperature (Td10) of the obtained polymer than the method of using a copper complex catalyst of a bidentate and monodentate ligand, and has a higher gel content and It is clear that the coloring is reduced.

Examples 3 to 7 Polymers were obtained in the same manner as in Example 1 except that the alkyl-substituted phenol and the reaction time were as shown in Table 2. Table 2 shows the results.

[0048]

[Table 2]

Example 8 A 2 L rubber balloon filled with oxygen was attached to a 25 ml two-necked round bottom flask equipped with a magnetic stirrer, and the inside of the flask was replaced with oxygen. To this, 0.006 mmol of Cu (tacn) was added, and 1.2 mmol of 2-t-butylphenol and 0.06 mmol of 2,6-diphenylpyridine as a base dissolved in 2.4 g of toluene were added. This was kept warm at 40 ° C. and stirred vigorously. After 163 hr, a few drops of concentrated hydrochloric acid were added to make the mixture acidic, and then methanol 25 ml and water 3 ml
Was added, and the precipitated polymer was collected by filtration. Methanol 10m
1 ml of water and 1 ml of water.
After drying under reduced pressure for an hour, a polymer was obtained. Table 2 shows the analysis results of the polymer.

[0050]

As described above, in the oxygen oxidation polymerization of an alkyl-substituted phenol, the thermal stability is improved by using a copper complex catalyst comprising a tridentate ligand in which the coordinating atom is a nitrogen atom and a copper atom. It is possible to obtain a poly (alkyl-substituted-1,4-phenylene oxide) polymer which is excellent, has high solubility in a solvent, and has no coloring.

 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Kiyoshi Fujisawa 4-201-706, Azuma, Tsukuba-shi, Ibaraki Prefecture (72) Inventor Yoshihiko Morooka 2-41-21 Fujigaoka, Aoba-ku, Yokohama-shi, Kanagawa 404 Tokyo Institute of Technology 404 (72) Inventor Shiro Kobayashi 1-1-1 Higashi, Tsukuba City, Ibaraki Pref. F-Term (in reference) 4M005 AA26 BB04

Claims (2)

[Claims] 1. An alkyl-substituted phenol represented by the following general formula (I) is polymerized in the presence of a copper complex catalyst comprising a tridentate ligand in which oxygen and a coordinating atom are a nitrogen atom and a copper atom. A method for producing an alkyl-substituted phenol polymer, characterized by the following. Embedded image (Wherein, R ^{1 to} R ³ are each independently a hydrogen atom, an alkyl group or a substituted alkyl group, at least one of R ¹ and R ² is an alkyl group or a substituted alkyl group, and at least one of R ² or R ³ One is a hydrogen atom, and R ¹ and R ² may form a ring.) 2. The method for producing an alkyl-substituted phenol polymer according to claim 1, wherein the copper complex catalyst is represented by the following general formula (II). Embedded image (In the formula, R ⁴ represents a hydrocarbon group, a substituted hydrocarbon group or a hydrogen atom, and all R ⁴ may be the same or different from each other. R ⁵ represents a divalent hydrocarbon group or a substituted hydrocarbon group. Wherein all R ^{5 's} may be the same or different, X is a counter anion, and n is the number of X, which is appropriately determined by the valences of copper and X.)