JPS642577B2 - - Google Patents

Info

Publication number
JPS642577B2
JPS642577B2 JP56123792A JP12379281A JPS642577B2 JP S642577 B2 JPS642577 B2 JP S642577B2 JP 56123792 A JP56123792 A JP 56123792A JP 12379281 A JP12379281 A JP 12379281A JP S642577 B2 JPS642577 B2 JP S642577B2
Authority
JP
Japan
Prior art keywords
formula
benzene
reaction
propyl
product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP56123792A
Other languages
Japanese (ja)
Other versions
JPS5824531A (en
Inventor
Haruhisa Harada
Hiroshi Maki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP56123792A priority Critical patent/JPS5824531A/en
Publication of JPS5824531A publication Critical patent/JPS5824531A/en
Publication of JPS642577B2 publication Critical patent/JPS642577B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、種々の高性能熱可塑性重合体、界面
活性剤、樹脂改質剤、安定剤などの製造用原料と
して有用な二価フエノール誘導体とその製造法に
関するものである。
[Detailed Description of the Invention] <Industrial Application Field> The present invention provides dihydric phenol derivatives useful as raw materials for producing various high-performance thermoplastic polymers, surfactants, resin modifiers, stabilizers, etc. and its manufacturing method.

<従来の技術> ビスフエノール類が種々の高性能熱可塑性重合
体、例えばポリカーボネート、ポリエステル、エ
ポキシ樹脂などの重要な出発原料であることは、
一般に良く知られている。
<Prior Art> Bisphenols are important starting materials for various high-performance thermoplastic polymers, such as polycarbonates, polyesters, and epoxy resins.
generally well known.

しかし、ビスフエノール類を用いた重合体は用
途によつてはさらに耐熱性接着性能のより一層の
向上が望まれている。
However, polymers using bisphenols are desired to have further improved heat-resistant adhesive performance depending on the application.

又、レゾルシン、カテコールなどの二価フエノ
ール化合物あるいはそれらの誘導体は、ゴムの無
毒性加硫促進剤として幅広く用いられているが、
性能のより一層の向上が望まれている。
In addition, divalent phenol compounds such as resorcinol and catechol, or their derivatives, are widely used as non-toxic vulcanization accelerators for rubber.
Further improvements in performance are desired.

<発明が解決しようとする課題> この様な現状に鑑み、本発明者らは二価フエノ
ール系の化合物について鋭意検討した結果、新規
な二価フエノール誘導体を提供することを目的と
する。
<Problems to be Solved by the Invention> In view of the current situation, the present inventors have conducted intensive studies on divalent phenol-based compounds, and as a result, it is an object of the present invention to provide a novel divalent phenol derivative.

<課題を解決するための手段> 即ち本発明は 構造式 又は であらわされる二価フエノール誘導体とその製造
法、即ちレゾルシン又はカテコールと、 式(B) 及び式(C) 及び式(D) (式(B),(C)及び(D)において、ベンゼン核の置換
基は、ベンゼン核の1,3位又は1,4位に位置
する) からなる群から選んだ化合物とを酸性縮合剤の存
在下−20〜100℃の温度で反応させ、反応混合物
から前記の二価フエノール(A―1),(A―2),
(A―3)又は(A―4)を回収することを特徴
とする二価フエノール誘導体の製造法に関するも
のである。
<Means for solving the problem> That is, the present invention has the following structural formula: or A divalent phenol derivative represented by the formula (B) and its production method, that is, resorcinol or catechol, and the formula (B) and formula (C) and formula (D) (In formulas (B), (C) and (D), the substituents on the benzene nucleus are located at the 1, 3 or 1, 4 positions of the benzene nucleus) with an acidic condensing agent. The above dihydric phenols (A-1), (A-2),
The present invention relates to a method for producing a divalent phenol derivative, which comprises recovering (A-3) or (A-4).

式(B)の化合物の具体例は1,3―ジイソプロペ
ニルベンゼン、1,4―ジイソプロペニルベンゼ
ンである。
Specific examples of the compound of formula (B) are 1,3-diisopropenylbenzene and 1,4-diisopropenylbenzene.

式(C)の化合物の具体例は3―(2―ヒドロキシ
―2―プロピル)―イソプロペニルベンゼン、4
―(2―ヒドロキシ―2―プロピル)―イソプロ
ペニルベンゼンである。
Specific examples of the compound of formula (C) are 3-(2-hydroxy-2-propyl)-isopropenylbenzene, 4
-(2-hydroxy-2-propyl)-isopropenylbenzene.

式(D)の化合物の具体例は1,3―ジ(2―ヒド
ロキシ―2―プロピル)ベンゼン、1,4―ジ
(2―ヒドロキシ―2―プロピル)―ベンゼンで
ある。
Specific examples of the compound of formula (D) are 1,3-di(2-hydroxy-2-propyl)benzene and 1,4-di(2-hydroxy-2-propyl)-benzene.

また、これら式(B),(C),(D)からなる群から選ば
れる化合物の製法は特に限定はされないが、工業
的に一般的な製法は 式(E) (式(E)において、ベンゼン核の置換基は、ベン
ゼン核の1,3位又は1,4位に位置する)であ
らわされる炭化水素化合物の脱水素によつて得ら
れる式(B)の化合物、あるいは空気酸化によつて得
ることのできる。
In addition, the manufacturing method of the compound selected from the group consisting of formulas (B), (C), and (D) is not particularly limited, but the industrially common manufacturing method is formula (E). (In formula (E), the substituents on the benzene nucleus are located at the 1, 3 or 1, 4 positions of the benzene nucleus.) A compound of formula (B) obtained by dehydrogenation of a hydrocarbon compound represented by , or by air oxidation.

式(F) (式(F)において、ベンゼン核の置換基は、ベン
ゼン核の1,3位又は1,4位に位置する) 及び/又は式(G) (式(G)において、ベンゼン核の置換基は、ベン
ゼン核の1,3位又は1,4位に位置する) であらわされるヒドロペルオキシドの亜硫酸ソー
ダ、水素等の還元処理によつて得られる式(D)の化
合物、あるいは式(D)であらわされる化合物を酸触
媒の存在下、脱水して得られる式(B),(C)の化合物
として製造し得る。
Formula (F) (In formula (F), the substituents on the benzene nucleus are located at the 1, 3 or 1, 4 positions of the benzene nucleus) and/or formula (G) (In formula (G), the substituents on the benzene nucleus are located at the 1, 3 or 1, 4 positions of the benzene nucleus.) Formula obtained by reducing hydroperoxide with sodium sulfite, hydrogen, etc. Compounds of formula (B) and (C) can be produced by dehydrating the compound of (D) or the compound of formula (D) in the presence of an acid catalyst.

これらの化合物は、1,3―ジ置換体の範囲
内、あるいは1,4―ジ置換体の範囲内で単独で
も、2つ以上の混合物として反応に供することが
できる。
These compounds can be subjected to the reaction in the range of 1,3-disubstituted products or 1,4-disubstituted products, singly or as a mixture of two or more.

さらに、これらの化合物は、1,3―ジ置換
体、1,4―ジ置換体の2つ以上の混合物として
供し、反応させた後目的反応生成物の物性(例え
ば融点など)の違いを利用し、目的反応生成物を
各々分離し、製造することも可能である。
Furthermore, these compounds are provided as a mixture of two or more of the 1,3-disubstituted product and the 1,4-disubstituted product, and after the reaction, the difference in physical properties (such as melting point) of the desired reaction product can be utilized. However, it is also possible to separate and produce each desired reaction product.

本発明の実施に於いてレゾルシン、又はカテコ
ールは、通常式(B),(C),(D)であらわされる化合物
1モル当り、2.0〜10倍モル量、好ましくは、2.0
〜6倍モル量と、化学量論量もしくはそれ以上、
過剰に用いられる。
In carrying out the present invention, resorcinol or catechol is usually used in a molar amount of 2.0 to 10 times, preferably 2.0 times, per mole of the compound represented by formula (B), (C), or (D).
~6 times the molar amount and the stoichiometric amount or more,
Used in excess.

酸性縮合剤としては通常の硫酸、塩酸、塩化水
素ガス、三弗化ホウ素、弗化水素、トリフルオル
酢酸、酸性白土、酸性イオン交換樹脂等を用いる
ことができる。
As the acidic condensing agent, common sulfuric acid, hydrochloric acid, hydrogen chloride gas, boron trifluoride, hydrogen fluoride, trifluoroacetic acid, acid clay, acidic ion exchange resin, etc. can be used.

この縮合反応を助ける意味で、硫化水素、メル
カプタン類、チオフエノール類等“S”化合物を
併用すればなお効率良く反応を行なわせることが
できる。
In order to assist this condensation reaction, the reaction can be carried out more efficiently if "S" compounds such as hydrogen sulfide, mercaptans, and thiophenols are used in combination.

反応を円滑に行なわせるために適当な有機溶剤
例えば、ベンゼン、トルエン、クロルベンゼンな
どを溶媒として用いることも可能である。
In order to carry out the reaction smoothly, it is also possible to use a suitable organic solvent such as benzene, toluene, chlorobenzene, etc. as a solvent.

反応温度は通常−20〜100℃の範囲で行なわれ
る。
The reaction temperature is usually in the range of -20 to 100°C.

反応圧力は通常は大気圧下で行なうことができ
るが、酸性縮合剤が気体である場合は加圧下で行
なわれる。又反応で水が生成する場合酸性縮合剤
が水で希釈されるのでその効能を持続させるため
に生成する水を反応系外へ除去する意味で減圧下
で行なうこともできる。この時、有機溶媒を共存
させ、減圧共沸下で水を除去することも可能であ
る。
The reaction pressure can usually be carried out under atmospheric pressure, but when the acidic condensing agent is a gas, it is carried out under increased pressure. Furthermore, when water is produced in the reaction, since the acidic condensing agent is diluted with water, the reaction can be carried out under reduced pressure in order to remove the produced water from the reaction system in order to maintain its effectiveness. At this time, it is also possible to coexist an organic solvent and remove water under reduced pressure and azeotropy.

本発明の二価フエノール誘導体は、反応混合物
から固体として、析出、あるいは、有機溶剤を用
いた場合は有機層の冷却により、固体として析出
し粗生成物として回収し得る。
The dihydric phenol derivative of the present invention can be precipitated as a solid from the reaction mixture, or when an organic solvent is used, can be precipitated as a solid and recovered as a crude product by cooling the organic layer.

この粗生成物を通常の方法で例えば、温水洗
浄、あるいは蒸留などの方法で未反応のレゾルシ
ン又はカテコールを除去した後、水、アルコー
ル、酢酸、クロロホルム、ベンゼン、トルエンな
ど、あるいはこれらの混合物のごとき溶剤から再
結晶すると高純度の固体として回収し得る。
After removing unreacted resorcin or catechol from this crude product by a conventional method such as hot water washing or distillation, it is treated with water, alcohol, acetic acid, chloroform, benzene, toluene, etc., or a mixture thereof. It can be recovered as a highly pure solid by recrystallization from a solvent.

以下に実施例により本発明をさらに詳細に説明
するが、本発明の範囲はこれらによつて制限をう
けるものではない。
The present invention will be explained in more detail with reference to Examples below, but the scope of the present invention is not limited thereby.

実施例 1 500mlガラス製3ツ口フラスコにレゾルシン33
g(0.3モル)、1,3―ジ(2―ヒドロキシ―2
―プロピル)ベンゼン19.4g(0.1モル)、ベンゼ
ン100ml、濃塩酸100mlを仕込み、かくはんしつつ
5℃で15時間反応を行なつた。
Example 1 Resorcinol 33 in a 500ml glass three-necked flask
g (0.3 mol), 1,3-di(2-hydroxy-2
19.4 g (0.1 mol) of benzene (propyl), 100 ml of benzene, and 100 ml of concentrated hydrochloric acid were charged, and the reaction was carried out at 5°C for 15 hours with stirring.

反応終了後、黄土色の油層を分離し、熱炭酸ソ
ーダ水溶液で中和した。中和終了後、油層中に含
れている未反応のレゾルシンを熱水洗浄で除去
し、油層を氷水浴で冷却した。冷却により淡黄土
色の固体が析出し、ロ過分離で淡黄土色の粉末を
得た。ベンゼン再結晶により融点104〜107℃の白
色の結晶を91%の収率で得た。
After the reaction was completed, the ocher oil layer was separated and neutralized with hot aqueous sodium carbonate solution. After the neutralization was completed, unreacted resorcin contained in the oil layer was removed by washing with hot water, and the oil layer was cooled in an ice water bath. A pale ocher solid was precipitated by cooling, and a pale ocher powder was obtained by filtration. White crystals with a melting point of 104-107°C were obtained by benzene recrystallization in a yield of 91%.

この製造法、及び生成物の赤外吸収スペクト
ル、NMRスペクトル、マススペクトル、元素分
析に基づいて、この生成物は、 式 であらわされる分子量378の1,3―ジ〔2―
(2,4―ジヒドロキシフエニル)―2―プロピ
ル〕ベンゼンであることが確認された。
Based on this manufacturing method and the infrared absorption spectrum, NMR spectrum, mass spectrum, and elemental analysis of the product, this product has the formula 1,3-di[2-
It was confirmed to be (2,4-dihydroxyphenyl)-2-propyl]benzene.

実施例 2 500mlガラス製3ツ口フラスコにレゾルシン33
g(0.3モル)、1,4―ジ―(2―ヒドロキシ―
2―プロピル)ベンゼン19.4g(0.1モル)、ベン
ゼン100ml、濃塩酸100mlを仕込み、かくはんしつ
つ5℃で15時間反応を行なつた。
Example 2 Resorcinol 33 in a 500ml glass three-necked flask
g (0.3 mol), 1,4-di-(2-hydroxy-
19.4 g (0.1 mol) of 2-propyl)benzene, 100 ml of benzene, and 100 ml of concentrated hydrochloric acid were charged, and the reaction was carried out at 5° C. for 15 hours with stirring.

反応終了後、黄褐色の油層を分離し、熱炭酸ソ
ーダ水溶液で中和した。中和終了後、油層中に含
まれている未反応のレゾルシンを熱水洗浄で除去
し、油層を氷水浴で冷却した。冷却により淡黄褐
色の固体が析出し、ロ過分離で淡黄褐色の粉末を
得た。メタノール再結晶により融点135〜139℃の
白色の結晶を87%の収率で得た。
After the reaction was completed, the yellowish brown oil layer was separated and neutralized with a hot aqueous solution of sodium carbonate. After the neutralization was completed, unreacted resorcin contained in the oil layer was removed by washing with hot water, and the oil layer was cooled in an ice water bath. A light yellowish brown solid was precipitated by cooling, and a light yellowish brown powder was obtained by filtration. White crystals with a melting point of 135-139°C were obtained by methanol recrystallization in a yield of 87%.

この製造法、及び生成物の赤外吸収スペクト
ル、NMRスペクトル、マススペクトル、元素分
析に基づいて、この生成物は、 式 であらわされる分子量378の1,4―ジ〔2―
(2,4―ジヒドロキシフエニル)―2―プロピ
ル〕ベンゼンであることが確認された。
Based on this manufacturing method and the infrared absorption spectrum, NMR spectrum, mass spectrum, and elemental analysis of the product, this product has the formula 1,4-di[2-
It was confirmed to be (2,4-dihydroxyphenyl)-2-propyl]benzene.

実施例 3 500mlのガラス製3ツ口フラスコにカテコール
33g(0.3モル)、ベンゼン100ml、濃塩酸50mlを
仕込み、40℃に維持した。そこへ、1,3―ジイ
ソプロペニルベンゼンと、3―(2―ヒドロキシ
―2―プロピル)イソプロペニルベンゼンの混合
物16g(合計で0.1モル)を徐々に添加した。8
時間の反応後には赤褐色の油層が分離した。
Example 3 Catechol in a 500ml glass three neck flask
33 g (0.3 mol), 100 ml of benzene, and 50 ml of concentrated hydrochloric acid were charged, and the temperature was maintained at 40°C. 16 g (0.1 mol in total) of a mixture of 1,3-diisopropenylbenzene and 3-(2-hydroxy-2-propyl)isopropenylbenzene was gradually added thereto. 8
After an hour of reaction, a reddish-brown oil layer separated.

この油層を分取し、熱炭酸ソーダ水溶液で中和
し、中和終了後、油層中に含まれている未反応の
カテコールを熱水洗浄で除去した。油層の冷却で
析出物を認め、過することによつて淡褐色の固
型物を得た。
This oil layer was separated and neutralized with a hot aqueous solution of sodium carbonate. After neutralization, unreacted catechol contained in the oil layer was removed by washing with hot water. A precipitate was observed when the oil layer was cooled, and a pale brown solid was obtained by filtering.

クロロホルム再結晶により、融点133〜137℃の
白色の結晶を81%の収率で得た。
White crystals with a melting point of 133-137°C were obtained by chloroform recrystallization in a yield of 81%.

この製造法、及び生成物の赤外吸収スペクト
ル、NMRスペクトル、マススペクトル、元素分
析にもとづいて、この生成物は、 式 であらわされる分子量378の、1,3―ジ〔2―
(3,4―ジヒドロキシフエニル)―2―プロピ
ル〕ベンゼンであることが確認された。
Based on this manufacturing method and the infrared absorption spectrum, NMR spectrum, mass spectrum, and elemental analysis of the product, this product has the formula 1,3-di[2-
It was confirmed to be (3,4-dihydroxyphenyl)-2-propyl]benzene.

実施例 4 500mlガラス製3ツ口フラスコにカテコール33
g(0.3モル)、1,4―ジ(2―ヒドロキシ―2
―プロピル)ベンゼン19.4g(0.1モル)、ベンゼ
ン100ml、濃塩酸100mlを仕込み、かくはんしつつ
5℃で15時間反応を行なつた。反応終了後、結晶
の析出が認められた。水層を除去後、油層と結晶
を熱炭酸ソーダ水溶液で中和し、続いて熱水洗浄
で未反応のカテコールを除去した。続いて、氷水
浴で冷却し結晶の析出を完全にし、過すること
によつて乳白色の粉末を得た。ベンゼン再結晶に
より、融点192〜198℃の白色の結晶を78%の収率
で得た。
Example 4 Catechol 33 in a 500ml glass three neck flask
g (0.3 mol), 1,4-di(2-hydroxy-2
19.4 g (0.1 mol) of benzene (propyl), 100 ml of benzene, and 100 ml of concentrated hydrochloric acid were charged, and the reaction was carried out at 5°C for 15 hours with stirring. After the reaction was completed, precipitation of crystals was observed. After removing the aqueous layer, the oil layer and crystals were neutralized with a hot aqueous solution of sodium carbonate, and then unreacted catechol was removed by washing with hot water. Subsequently, the mixture was cooled in an ice-water bath to completely precipitate crystals, and filtered to obtain a milky white powder. Benzene recrystallization gave white crystals with a melting point of 192-198°C in a yield of 78%.

この製造法、及び生成物の赤外吸収スペクト
ル、NMRスペクトル、マススペクトル、元素分
析にもとづいて、この生成物は、 式 であらわされる分子量378の1,4―ジ〔2―
(3,4―ジヒドロキシフエニル)―2―プロピ
ル)ベンゼンであることが確認された。
Based on this manufacturing method and the infrared absorption spectrum, NMR spectrum, mass spectrum, and elemental analysis of the product, this product has the formula 1,4-di[2-
It was confirmed to be (3,4-dihydroxyphenyl)-2-propyl)benzene.

<発明の効果> 本発明によつて新規な二価フエノール誘導体を
得ることができた。
<Effects of the Invention> A novel dihydric phenol derivative could be obtained by the present invention.

Claims (1)

【特許請求の範囲】 1 構造式 又は、 であらわされる二価フエノール誘導体。 2 レゾルシン又はカテコールと 式(B) 及び式(C) 及び式(D) (式(B),(C)及び(D)において、ベンゼン核の置換
基は、ベンゼン核の1,3位又は1,4位に位置
する)からなる群から選んだ化合物とを酸性縮合
剤の存在下−20〜100℃の温度で反応させ、反応
混合物から構造式 又は であらわされる二価フエノール誘導体を回収する
ことを特徴とする二価フエノール誘導体の製造
法。
[Claims] 1. Structural formula Or A divalent phenol derivative represented by 2 Resorcinol or catechol and formula (B) and formula (C) and formula (D) (In formulas (B), (C) and (D), the substituents on the benzene nucleus are located at the 1, 3 or 1, 4 positions of the benzene nucleus) with an acidic condensing agent. The structural formula or A method for producing a divalent phenol derivative, which comprises recovering a divalent phenol derivative represented by:
JP56123792A 1981-08-06 1981-08-06 Novel dihydric phenol derivative and its preparation Granted JPS5824531A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56123792A JPS5824531A (en) 1981-08-06 1981-08-06 Novel dihydric phenol derivative and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56123792A JPS5824531A (en) 1981-08-06 1981-08-06 Novel dihydric phenol derivative and its preparation

Publications (2)

Publication Number Publication Date
JPS5824531A JPS5824531A (en) 1983-02-14
JPS642577B2 true JPS642577B2 (en) 1989-01-18

Family

ID=14869414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56123792A Granted JPS5824531A (en) 1981-08-06 1981-08-06 Novel dihydric phenol derivative and its preparation

Country Status (1)

Country Link
JP (1) JPS5824531A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55500140A (en) * 1978-02-24 1980-03-13
US4614826A (en) * 1983-02-28 1986-09-30 Mitsui Petrochemical Industries, Ltd. Polyglycidyl ethers of polynuclear polyhydric phenols
JPS59157040A (en) * 1983-02-28 1984-09-06 Mitsui Petrochem Ind Ltd Polynucleus polyhydric phenol and its preparation
JPH0688953B2 (en) * 1985-11-15 1994-11-09 三井石油化学工業株式会社 Method for producing 2- (aminoaryl) -2- (hydroxyaryl) alkane

Also Published As

Publication number Publication date
JPS5824531A (en) 1983-02-14

Similar Documents

Publication Publication Date Title
KR870001382B1 (en) Process for preparing triazine derivatives
US20210171457A1 (en) Process for making diaryl sulfones
JPH0114212B2 (en)
JPS642577B2 (en)
JP6016303B2 (en) Method for producing xanthene compound having fluorene skeleton
JP4596680B2 (en) Bisthiophenol fluorenes and method for producing the same
JPS58121230A (en) Novel alkyl disubstituted phenol derivative and its preparation
JP4438465B2 (en) Method for producing tetrakis (4-hydroxyphenyl) ethane compound
JPS5813528A (en) Novel phenolic compound and its preparation
JP3275186B2 (en) Method for producing fully-nuclear alkyl-substituted trisphenol derivatives
JP2840372B2 (en) Method for producing hydroxyarylamine compound
JPH0244821B2 (en)
JPS5818331A (en) Novel phenolic compound and its preparation
JPS58121231A (en) Novel cresol derivative and its preparation
CN107011124B (en) Production method of trisphenol compound
JP3337326B2 (en) Process for producing bis (hydroxyaryl) pentanoic acids
JP5572430B2 (en) Process for producing 9,9-bis (4-hydroxyphenyl) fluorenes
JP6665292B2 (en) Method for producing 1,1,2,2-tetrakis (4-hydroxyphenyl) ethane compound
JPH037241A (en) Novel dihydroxy compound and preparation thereof
JP4145082B2 (en) Substituted phenols
GILMAN et al. Alkylation and Related Reactions of Dibenzo-p-dioxin
JPH0816075B2 (en) Process for producing p, p&#39;-biphenol
JP4077887B2 (en) Process for producing 2,2-bis (hydroxyaryl) propionic acids
JPS6121549B2 (en)
JP2005023022A (en) Method for producing high-purity 1,1-bis(4-hydroxyphenyl)cyclohexanes