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JPH0322376B2 - - Google Patents
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JPH0322376B2 - - Google Patents

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Publication number
JPH0322376B2
JPH0322376B2 JP57073203A JP7320382A JPH0322376B2 JP H0322376 B2 JPH0322376 B2 JP H0322376B2 JP 57073203 A JP57073203 A JP 57073203A JP 7320382 A JP7320382 A JP 7320382A JP H0322376 B2 JPH0322376 B2 JP H0322376B2
Authority
JP
Japan
Prior art keywords
biphenol
reaction
butyl
tetra
temperature
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 - Lifetime
Application number
JP57073203A
Other languages
Japanese (ja)
Other versions
JPS58189127A (en
Inventor
Hiroshi Uchida
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP57073203A priority Critical patent/JPS58189127A/en
Publication of JPS58189127A publication Critical patent/JPS58189127A/en
Publication of JPH0322376B2 publication Critical patent/JPH0322376B2/ja
Granted legal-status Critical Current

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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)

Description

【発明の詳細な説明】 本発明はP,P′−ビフエノールの製造に関す
る。更に詳しくは3,5、3′,5′−テトラ−t−
ブチル−4,4′−ビフエノールを脱ブチルして
P,P′−ビフエノールを製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the production of P,P'-biphenol. More specifically, 3,5,3',5'-tetra-t-
This invention relates to a method for producing P,P'-biphenol by removing butyl from butyl-4,4'-biphenol.

P,P′−ビフエノールは樹脂の酸化安定剤、染
料中間体、およびポリカーボネート、ポリエポキ
サイド、ポリエステル、ポリスルホンなどの合成
樹脂の原料となり、特に優れた耐熱性を有するこ
とから、各方面から注目されている。上記原料と
してのP,P′−ビフエノールは、ポリマーの物性
を十分に生かすために純度の高いものが要求され
ているが、P,P′−ビフエノールのもつている性
質のために重合原料として使用に適する純度の高
い精製品を得ることは非常に難かしい。
P,P'-biphenol is used as an oxidation stabilizer for resins, as a dye intermediate, and as a raw material for synthetic resins such as polycarbonate, polyepoxide, polyester, and polysulfone, and is attracting attention from various quarters because it has particularly excellent heat resistance. There is. P,P'-biphenol as the above raw material is required to be highly pure in order to fully utilize the physical properties of the polymer, but due to the properties of P,P'-biphenol it is used as a polymerization raw material. It is very difficult to obtain refined products with high purity suitable for.

従来、3,5、3′,5′−テトラ−t−ブチルビ
フエノールを脱ブチル化してP,P′−ビフエノー
ルを得る方法としてはアルミニウムアルコキシド
触媒が有効であることが知られているが、この触
媒は生成したP,P′−ビフエノールとの分離に非
常に問題がある。
Conventionally, it has been known that aluminum alkoxide catalysts are effective as a method for debutylating 3,5,3',5'-tetra-t-butylbiphenol to obtain P,P'-biphenol. This catalyst is very problematic in its separation from the P,P'-biphenol formed.

また無溶媒、無触媒で脱アルキルする方法(特
開昭55−92332、UCC)が知られているが、この
方法では250〜500℃という高温が要求され実際的
でない。
Furthermore, a method of dealkylating without a solvent and without a catalyst is known (Japanese Patent Application Laid-Open No. 55-92332, UCC), but this method requires a high temperature of 250 to 500°C and is not practical.

またP,P′−ビフエノールは高融点、高沸点物
質であるため蒸留操作によつて精製することは実
際上不可能に近い。またP,P′−ビフエノールは
溶剤に比較的溶け難いため再結晶に際して多量の
溶媒又は特殊な操作が必要となり経済的でなく、
反応混合物から直接高純度のP,P′−ビフエノー
ルを分離することが望まれている。
Furthermore, since P,P'-biphenol is a substance with a high melting point and a high boiling point, it is virtually impossible to purify it by distillation. In addition, since P,P'-biphenol is relatively difficult to dissolve in solvents, a large amount of solvent or special operations are required for recrystallization, which is not economical.
It is desired to separate highly pure P,P'-biphenol directly from the reaction mixture.

本発明者は、上記事情を考慮して鋭意研究を進
めた結果本発明を完成するに到つた。
The present inventor has completed the present invention as a result of intensive research in consideration of the above circumstances.

すなわち、本発明では3,5、3′,5′−テトラ
−t−ブチル−4,4′−ビフエノールをフエノー
ルまたは1〜3の低級アルキル基又は低級アルコ
キシ基で置換されたフエノールを溶媒とし、触媒
として硫酸またはスルホン酸の存在下に120〜150
℃の温度で脱ブチル化し、引続き溶媒の融点〜80
℃の温度にてP,P′−ビフエノールの結晶を上述
の1〜3の低級アルキル基又は低級アルコキシ基
で置換されたフエノールとしては具体的には例え
ば、o−、m−又はp−クレゾール;2−、3−
又は4−エチルフエノール;2−、3−又は4−
t−ブチルフエノール;2,3−、2,4−、
2,5−、2,6−、3,4−又は3,5−ジメ
チルフエノール;2,3−2,4−、2,5−、
2,6−、3,4−又は3,5−ジ−t−ブチル
フエノール;アニソール又はo−、m−又はp−
メトキシフエノール;2−、3−又は4−エトキ
シフエノール等が挙げられる。これらのうち、本
発明の方法に於ける溶媒としては、特に、フエノ
ール、クレゾールが好ましいものと言える。ま
た、触媒のスルホン酸としてはメチルスルホン
酸、エチルスルホン酸、フエニルスルホン酸、ト
ルエンスルホン酸等のアルキル又はアリールスル
ホン酸が挙げられるが、好ましくは硫酸触媒が良
い。
That is, in the present invention, phenol or phenol substituted with 1 to 3 lower alkyl groups or lower alkoxy groups is used as a solvent for 3,5,3',5'-tetra-t-butyl-4,4'-biphenol, 120-150 in the presence of sulfuric acid or sulfonic acid as catalyst
Debutylated and subsequently melting point of the solvent at a temperature of ~80 °C
Specific examples of the phenol obtained by substituting P,P'-biphenol crystals with the above-mentioned 1 to 3 lower alkyl groups or lower alkoxy groups at a temperature of °C include o-, m- or p-cresol; 2-, 3-
or 4-ethylphenol; 2-, 3- or 4-
t-butylphenol; 2,3-, 2,4-,
2,5-, 2,6-, 3,4- or 3,5-dimethylphenol; 2,3-2,4-, 2,5-,
2,6-, 3,4- or 3,5-di-t-butylphenol; anisole or o-, m- or p-
Methoxyphenol; 2-, 3- or 4-ethoxyphenol, and the like. Among these, phenol and cresol are particularly preferred as solvents in the method of the present invention. Further, examples of the sulfonic acid of the catalyst include alkyl or aryl sulfonic acids such as methylsulfonic acid, ethylsulfonic acid, phenylsulfonic acid, and toluenesulfonic acid, but preferably a sulfuric acid catalyst is used.

反応条件としては必ずしも厳密な制限はない
が、一般に以下の如き範囲で行うのが適当であ
る。反応温度:120〜250℃、好ましくは180〜200
℃、溶媒使用量(重量):原料と同量乃至10倍程
度、好ましくは1.5〜2.0倍、触媒量(重量):原
料に対して0.01〜20%、好ましくは0.1〜5.0%、
反応時間:1〜数時間、但し、これらの条件は一
つの目安であり、必要に応じて適宜加減すること
が望ましい。
Although there are no strict limitations on the reaction conditions, it is generally appropriate to carry out the reaction within the following ranges. Reaction temperature: 120-250℃, preferably 180-200℃
°C, amount of solvent used (weight): the same amount to about 10 times that of the raw material, preferably 1.5 to 2.0 times, amount of catalyst (weight): 0.01 to 20%, preferably 0.1 to 5.0% based on the raw material,
Reaction time: 1 to several hours, however, these conditions are only a guideline, and it is desirable to adjust them as necessary.

反応によつて原料テトラ−t−ブチルビフエノ
ールのt−ブチル基が脱離してビフエノールが得
られ、また、脱離したt−ブチル基はイソブテン
として回収される。この際、溶媒として用いたフ
エノール又は置換フエノール類は、その一部が原
料からのt−ブチル基にてアルキル化(トランス
アルキレーシヨン)され、反応条件によつてはそ
の割合はt−ブチル基を基準として40%程度にも
なるが、反応時間を長くすることによりトランス
アルキレーシヨンの割合は減少しイソブテンとし
て回収されるものの割合が増加する。
Through the reaction, the t-butyl group of the raw material tetra-t-butylbiphenol is eliminated to obtain biphenol, and the eliminated t-butyl group is recovered as isobutene. At this time, a portion of the phenol or substituted phenols used as a solvent is alkylated (transalkylation) with t-butyl groups from the raw materials, and depending on the reaction conditions, the proportion of t-butyl groups may vary. However, by increasing the reaction time, the proportion of transalkylation decreases and the proportion of isobutene recovered increases.

反応終了後反応液を冷却すると目的物である
P,P′−ビフエノールの結晶が析出するが、この
とき反応液の温度を溶媒の融点以上で好ましくは
80℃以下に保ち、生成物を濾取すれば容易に高純
度の目的物を得ることができる。この場合、80℃
以上の温度でもP,P′−ビフエノールの結晶を得
ることは可能であるが、目的物の溶解度が高くな
るために回収率が低下し効率が良くない。また、
逆に温度が低過ぎると溶媒のフエノール又は置換
フエノール類が凝固して分離が出来なくなつた
り、トランスアルキル化されたフエノール又は置
換フエノール類が析出して純度低下を招く等の不
都合がある。好適な温度については溶媒の種類に
よつて凝固点(融点)や目的物の溶解性が異なる
ため一律には規定し得ないが、一例を示せばフエ
ノール溶媒の場合には50〜80℃、クレゾール溶媒
の場合には40〜80℃程度が適当である。尚、反応
液からのP,P′−ビフエノールの析出は急速に行
うよりも比較的時間をかけてゆつくりと行つた方
が良く、また、不純物の混入を避けるには上記範
囲内であつて且成可く定温に保つて析出させ、更
にその温度を維持して濾過することが望ましい。
When the reaction solution is cooled after the completion of the reaction, crystals of P,P'-biphenol, which is the target product, are precipitated, but at this time, the temperature of the reaction solution is preferably kept above the melting point of the solvent
By keeping the temperature below 80°C and collecting the product by filtration, the target product of high purity can be easily obtained. In this case, 80℃
Although it is possible to obtain crystals of P,P'-biphenol even at temperatures above, the solubility of the target substance increases, resulting in a lower recovery rate and poor efficiency. Also,
On the other hand, if the temperature is too low, there are disadvantages such as the phenol or substituted phenols in the solvent coagulate and separation becomes impossible, or transalkylated phenols or substituted phenols precipitate, resulting in a decrease in purity. Suitable temperatures cannot be uniformly defined because the freezing point (melting point) and solubility of the target substance vary depending on the type of solvent, but as an example, 50 to 80°C for phenol solvents and 50 to 80°C for cresol solvents. In this case, a temperature of about 40 to 80°C is appropriate. It should be noted that it is better to precipitate P,P'-biphenol from the reaction solution slowly over a relatively long period of time rather than rapidly, and to avoid contamination with impurities, the precipitation should be within the above range. It is desirable to precipitate by keeping the temperature at a constant temperature, and then filter it while maintaining that temperature.

このP,P′−t−ビフエノールの回収率は溶媒
の種類、量、濾過の温度によつて微妙に影響する
が55〜84%の間である。析出分離したP,P′−ビ
フエノールの結晶は充分に高純度のものである
が、場合により若干着色していることがあるた
め、必要に応じてトルエンやベンゼンのような芳
香族炭化水素等でよく洗浄することにより、薄い
ピンク色がとれ、ほぼ純白のP,P′−ビフエノー
ルを得ることが出来る。このものはガスクロマト
グラフ分析によつて純度が測定されるが99%以上
である。
The recovery rate of P,P'-t-biphenol varies slightly depending on the type and amount of solvent and the temperature of filtration, but is between 55 and 84%. Although the precipitated and separated crystals of P,P'-biphenol are of sufficiently high purity, they may be slightly colored in some cases, so if necessary, they may be treated with an aromatic hydrocarbon such as toluene or benzene. By washing thoroughly, the pale pink color is removed and almost pure white P,P'-biphenol can be obtained. The purity of this product is determined by gas chromatography and is over 99%.

また熱時濾過した濾液に特殊な操作をせずに原
料である3,5、3′,5′−テトラ−t−ブチル−
4,4′−ビフエノールを入れ上記操作と同様な操
作を行なうことにより、脱ブチル化反応を繰返し
行なうことが出来る。この場合の熱時濾過の濾液
はP,P′−ビフエノールの飽和溶液であるので、
加えた3,5、3′,5′−テトラ−t−ブチル−
4,4′−ビフエノールに対してほぼ定量的にP,
P′ビフエノールが得られる。
In addition, the raw material 3,5,3',5'-tetra-t-butyl-3,5,3',5'-tetra-t-butyl-
By adding 4,4'-biphenol and performing the same operation as above, the debutylation reaction can be repeated. In this case, the filtrate of hot filtration is a saturated solution of P,P'-biphenol, so
Added 3,5,3',5'-tetra-t-butyl-
Almost quantitatively P for 4,4'-biphenol,
P'biphenol is obtained.

次に実施例を示して本発明をさらに詳しく説明
する。
Next, the present invention will be explained in more detail by showing examples.

〔実施例 1〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール2.8g(7.04mmol)、フエノール
12.84g、硫酸2滴を50mlフラスコに入れマグネ
チツクスターラーで撹拌しながら150℃で5時間
反応させた。反応終了後70℃まで反応混合物を冷
却し、この温度で2時間結晶を析出させた。結晶
を析出させた後70℃で熱時濾過しP,P′−ビフエ
ノールの粗成物を得た。このものをトルエンで洗
浄することによりP,P′−ビフエノール0.83g
(4.46mmol、収率63%)を得た。色は白色で、純
度はガスクロマトグラフ分析の結果99%以上であ
つた。
[Example 1] 3,5,3',5'-tetra-t-butyl-4,
4′-biphenol 2.8g (7.04mmol), phenol
12.84g and 2 drops of sulfuric acid were placed in a 50ml flask and reacted at 150°C for 5 hours while stirring with a magnetic stirrer. After the reaction was completed, the reaction mixture was cooled to 70°C, and crystals were precipitated at this temperature for 2 hours. After crystals were precipitated, they were filtered while hot at 70°C to obtain a crude product of P,P'-biphenol. By washing this material with toluene, 0.83g of P,P'-biphenol was obtained.
(4.46 mmol, yield 63%) was obtained. The color was white, and the purity was 99% or more as a result of gas chromatography analysis.

〔実施例 2〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール2.27g(5.54mmol)、p−t−
ブチルフエノール9.22g、硫酸2滴を50mlフラス
コに入れマグネチツクスターラーで撹拌しながら
200℃で3時間反応させた。反応終了後70℃まで
反応混合物を冷却し、この温度で2時間保持し結
晶を析出させた。この後70℃で熱時濾過し、分離
した結晶をトルエンで洗浄することにより白色の
P,P′ビフエノール0.743g(3.99mmol、収率72
%)を得た。純度は、ガスクロマトグラフ分析の
結果99%以上であつた。
[Example 2] 3,5,3',5'-tetra-t-butyl-4,
4'-biphenol 2.27g (5.54mmol), p-t-
Put 9.22g of butylphenol and 2 drops of sulfuric acid into a 50ml flask and stir with a magnetic stirrer.
The reaction was carried out at 200°C for 3 hours. After the reaction was completed, the reaction mixture was cooled to 70°C and maintained at this temperature for 2 hours to precipitate crystals. After this, 0.743 g (3.99 mmol, yield 72
%) was obtained. The purity was 99% or more as a result of gas chromatography analysis.

〔実施例 3〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール80.45g(0.196mmol)、フエノ
ール160.44g、硫酸0.1mlを300mlの2口フラスコ
に入れ、窒素を吹込みながら180℃で5時間反応
させた。反応終了後、反応溶液を60℃に冷却し2
時間結晶を析出させ、熱時濾過しP,P′−ビフエ
ノールを得た。このものをトルエンで洗浄し直空
乾燥し、P,P′−ビフエノール28.63g
(0.154mol、収率78.5%)を得た。純度はガスク
ロマトグラフ分析によつて測定した結果99%以上
であつた。
[Example 3] 3,5,3',5'-tetra-t-butyl-4,
80.45 g (0.196 mmol) of 4'-biphenol, 160.44 g of phenol, and 0.1 ml of sulfuric acid were placed in a 300 ml two-necked flask, and reacted at 180° C. for 5 hours while blowing nitrogen. After the reaction was completed, the reaction solution was cooled to 60°C and
Crystals were precipitated over time and filtered while hot to obtain P,P'-biphenol. This product was washed with toluene and dried directly in the air, and 28.63 g of P,P'-biphenol was obtained.
(0.154 mol, yield 78.5%) was obtained. The purity was determined to be 99% or more by gas chromatography analysis.

〔実施例 4〕 実施例3における熱時濾過の濾液に3,5、
3′,5′−テトラ−t−ブチル−4,4′−ビフエノ
ール50.60g(0.123mol)を入れ、300mlの2口フ
ラスコで窒素を吹込みながら200℃で2時間反応
させた。反応混合物を60℃に冷却し、2時間結晶
を析出させ60℃で熱濾過し分離した結晶をトルエ
ンで洗浄した後乾燥しP,P′−ビフエノール
22.87g(0.123mol、収率99.9%)を得た。純度
はガスクロマトグラフ分析を行なつた結果99%以
上であつた。
[Example 4] In the filtrate of hot filtration in Example 3, 3,5,
50.60 g (0.123 mol) of 3',5'-tetra-t-butyl-4,4'-biphenol was added and reacted in a 300 ml two-necked flask at 200°C for 2 hours while blowing nitrogen. The reaction mixture was cooled to 60°C, crystals were precipitated for 2 hours, filtered hot at 60°C, the separated crystals were washed with toluene and dried to give P,P'-biphenol.
22.87g (0.123mol, yield 99.9%) was obtained. The purity was 99% or higher as determined by gas chromatography analysis.

〔実施例 5〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール2.062g(5.02mmol)、o−クレ
ゾール10.042g、硫酸1滴を50mlフラスコに入れ
マグネチツクスターラーで撹拌しながら170℃で
3時間反応させた。反応終了後50℃まで反応混合
物を冷却し、2時間結晶を析出させ50℃で熱時濾
過した。この結晶をトルエンで洗浄した後乾燥
し、P,P′−ビフエノール0.830g
(4.46mmol88.8%)を得た。純度はガスクロマト
グラフ分析を行なつた結果99%以上であつた。
[Example 5] 3,5,3',5'-tetra-t-butyl-4,
2.062 g (5.02 mmol) of 4'-biphenol, 10.042 g of o-cresol, and 1 drop of sulfuric acid were placed in a 50 ml flask and reacted at 170° C. for 3 hours while stirring with a magnetic stirrer. After the reaction was completed, the reaction mixture was cooled to 50°C, crystals were precipitated for 2 hours, and filtered while hot at 50°C. After washing the crystals with toluene and drying them, 0.830 g of P,P'-biphenol was obtained.
(4.46mmol88.8%) was obtained. The purity was 99% or higher as determined by gas chromatography analysis.

〔実施例 6〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール10.04g(25.33mmol)、アニソ
ール50.02g、硫酸0.5gを100mlフラスコに入れ、
マグネチツクスターラーで撹拌しながら170℃で
6時間反応させた。反応終了後50℃まで反応混合
物を冷却し、実施例5と同様の操作でP,P′−ビ
フエノール4.32g(23.2mmol91.6%)を得た。純
度はガスクロマトグラフ分析により99%以上であ
つた。
[Example 6] 3,5,3',5'-tetra-t-butyl-4,
Put 10.04 g (25.33 mmol) of 4′-biphenol, 50.02 g of anisole, and 0.5 g of sulfuric acid into a 100 ml flask.
The mixture was reacted at 170°C for 6 hours while stirring with a magnetic stirrer. After the reaction was completed, the reaction mixture was cooled to 50°C, and the same procedure as in Example 5 was carried out to obtain 4.32 g (23.2 mmol 91.6%) of P,P'-biphenol. The purity was 99% or more by gas chromatography analysis.

〔実施例 7〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール10.1647g(24.8mmol)、p−メ
トキシフエノール49.9811g、硫酸0.1mlを100ml
フラスコに入れマグネチツクスターラーで撹拌し
ながら150℃で1時間反応させた。反応終了後80
℃に冷却し、この温度で2時間結晶を析出させ、
熱時濾過し、P,P′−ビフエノールを得た。この
ものをトルエンで洗浄し、真空乾燥し、P,P′−
ビフエノール2.91g(15.6mmol収率63.0%)を得
た。〔実施例 8〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール14.048g(34.2mmol)、1,3
−ジメトキシベンゼン48.364g、硫酸1.0mlを100
mlフラスコに入れマグネチツクスターラーで撹拌
しながら170℃で2時間反応させた。反応終了後
50℃に冷却し、実施例5と同様な操作でP,P′−
ビフエノール5.16g(27.7mmol、収率81.0%)を
得た。
[Example 7] 3,5,3',5'-tetra-t-butyl-4,
100ml of 4′-biphenol 10.1647g (24.8mmol), p-methoxyphenol 49.9811g, sulfuric acid 0.1ml
The mixture was placed in a flask and reacted at 150°C for 1 hour while stirring with a magnetic stirrer. 80 minutes after the reaction
℃ and allowed to precipitate crystals at this temperature for 2 hours,
The mixture was filtered while hot to obtain P,P'-biphenol. This material was washed with toluene, dried in vacuum, and P,P'-
2.91 g (15.6 mmol yield 63.0%) of biphenol was obtained. [Example 8] 3,5,3',5'-tetra-t-butyl-4,
4′-biphenol 14.048g (34.2mmol), 1,3
- 48.364 g of dimethoxybenzene, 1.0 ml of sulfuric acid in 100 g
The mixture was placed in a ml flask and reacted at 170°C for 2 hours while stirring with a magnetic stirrer. After the reaction
Cool to 50°C and perform the same operation as in Example 5 to prepare P, P'-
5.16 g (27.7 mmol, yield 81.0%) of biphenol was obtained.

〔実施例 9〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール2.25g(5.49mmol)、フエノー
ル8.20g、p−トルエンスルホン酸0.21gを50ml
フラスコに入れ、マグネチツクスターラーで撹拌
しながら、160℃で3時間反応させた。反応終了
後60℃まで反応混合物を冷却し、この温度で2時
間保持し、結晶を析出させた。この後60℃で熱時
濾過し、分離した結晶をトルエンで洗浄し、白色
のP,P′−ビフエノール0.87g(4.67mmol、収
率85%)を得た。純度はガスクロマトグラフ分析
の結果99%以上であつた。
[Example 9] 3,5,3',5'-tetra-t-butyl-4,
50 ml of 4′-biphenol 2.25 g (5.49 mmol), phenol 8.20 g, p-toluenesulfonic acid 0.21 g
The mixture was placed in a flask and reacted at 160°C for 3 hours while stirring with a magnetic stirrer. After the reaction was completed, the reaction mixture was cooled to 60°C and maintained at this temperature for 2 hours to precipitate crystals. Thereafter, it was filtered while hot at 60°C, and the separated crystals were washed with toluene to obtain 0.87 g (4.67 mmol, yield 85%) of white P,P'-biphenol. The purity was 99% or higher as determined by gas chromatography analysis.

〔実施例 10〕 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノール2.22g(5.41mmol)フエノール
7.03g、メタンスルホン酸3滴、フエノール7.03
gを用い上記の方法と同様な操作で白色のP,
P′−ビフエノール0.85g(4.54mmol収率84%)
を得た。純度はガスクロマトグラフ分析の結果99
%以上であつた。
[Example 10] 3,5,3',5'-tetra-t-butyl-4,
4'-biphenol 2.22g (5.41mmol) phenol
7.03g, 3 drops of methanesulfonic acid, phenol 7.03
Using g, white P,
P'-biphenol 0.85g (4.54mmol yield 84%)
I got it. Purity is 99% as a result of gas chromatography analysis
% or more.

Claims (1)

【特許請求の範囲】[Claims] 1 3,5、3′,5′−テトラ−t−ブチル−4,
4′−ビフエノールをフエノールまたは1〜3の低
級アルキル基もしくは低級アルコキシ基で置換さ
れたフエノールを溶媒に用い、触媒として硫酸ま
たはスルホン酸の存在下に120〜250℃の温度で脱
ブチル化してP,P′−ビフエノールを生成せしめ
た後、溶媒の融点〜80℃の温度で濾過してP,
P′−ビフエノールを分離することを特徴とした
P,P′−ビフエノールの製造法。
1 3,5,3',5'-tetra-t-butyl-4,
4′-biphenol is debutylated at a temperature of 120 to 250°C in the presence of sulfuric acid or sulfonic acid as a catalyst using phenol or phenol substituted with 1 to 3 lower alkyl groups or lower alkoxy groups as a solvent to obtain P. , P'-biphenol is produced, and then filtered at a temperature between the melting point of the solvent and 80°C to produce P,
A method for producing P,P'-biphenol, which comprises separating P'-biphenol.
JP57073203A 1982-04-30 1982-04-30 Preparation of p,p-biphenol Granted JPS58189127A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57073203A JPS58189127A (en) 1982-04-30 1982-04-30 Preparation of p,p-biphenol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57073203A JPS58189127A (en) 1982-04-30 1982-04-30 Preparation of p,p-biphenol

Publications (2)

Publication Number Publication Date
JPS58189127A JPS58189127A (en) 1983-11-04
JPH0322376B2 true JPH0322376B2 (en) 1991-03-26

Family

ID=13511348

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57073203A Granted JPS58189127A (en) 1982-04-30 1982-04-30 Preparation of p,p-biphenol

Country Status (1)

Country Link
JP (1) JPS58189127A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63119432A (en) * 1986-11-07 1988-05-24 Kureha Chem Ind Co Ltd Production of 4,4-dihydroxybiphenyl
JP2524594B2 (en) * 1987-06-02 1996-08-14 三菱化学株式会社 Method for producing high-purity 4,4'-biphenol
JP2829869B2 (en) * 1989-09-05 1998-12-02 三菱化学株式会社 Method for producing 4,4'-dihydroxybiphenyl
KR20030074736A (en) * 2001-01-31 2003-09-19 스미또모 가가꾸 고교 가부시끼가이샤 Process for production of 4,4'-biphenol
JP5230226B2 (en) * 2008-03-07 2013-07-10 富士フイルム株式会社 Carbonate purification method and production method

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