JPS58109435A - Preparation of m-alkylhydroxybenzene - Google Patents

Preparation of m-alkylhydroxybenzene

Info

Publication number
JPS58109435A
JPS58109435A JP56210285A JP21028581A JPS58109435A JP S58109435 A JPS58109435 A JP S58109435A JP 56210285 A JP56210285 A JP 56210285A JP 21028581 A JP21028581 A JP 21028581A JP S58109435 A JPS58109435 A JP S58109435A
Authority
JP
Japan
Prior art keywords
alkylbenzene
acid
sulfuric acid
alkylhydroxybenzene
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.)
Granted
Application number
JP56210285A
Other languages
Japanese (ja)
Other versions
JPH0234929B2 (en
Inventor
Mitsuhiro Wada
光弘 和田
Seiji Maki
牧 征二
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.)
Taoka Chemical Co Ltd
Original Assignee
Taoka 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 Taoka Chemical Co Ltd filed Critical Taoka Chemical Co Ltd
Priority to JP56210285A priority Critical patent/JPS58109435A/en
Priority to DE8282306320T priority patent/DE3262826D1/en
Priority to US06/444,696 priority patent/US4475002A/en
Priority to EP82306320A priority patent/EP0080880B1/en
Publication of JPS58109435A publication Critical patent/JPS58109435A/en
Publication of JPH0234929B2 publication Critical patent/JPH0234929B2/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)

Abstract

PURPOSE:To suppress the side reactions such as disulfonation, dealkylation, etc. in the preparation of substantially pure m-alkylhydroxybenzene from alkylbenzene through alkylbenzenesulfonic acid, by carrying out the reaction in the presence of a specific amount of inorganic salt such as Glauber salt. CONSTITUTION:Alkylbenzene or alkylbenzenesulfonic acid mixture is heated at 150-210 deg.C in the presence of sulfuric acid. The above reaction is carried out in the presence of 1-5mol% inorganic salt (preferably Glauber salt) based on charged sulfuric acid to obtain alkylbenzene-sulfonic acid having high m-isomer content. The alkylbenzene sulfonic acids other than m-isomer are selectively hydrolyzed, and the unhydrolyzed alkylbenzenesulfonic acid is subjected to caustic alkali fusion to obtain m-alkylhydroxybenzene.

Description

【発明の詳細な説明】 本発明は、m−アルキルヒドロキシベンゼン類の合理的
かつ経済的製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a rational and economical method for producing m-alkylhydroxybenzenes.

アルキルベンゼンからアルキルベンゼンスルホン酸を経
て実質的に純粋なm−アルキルベンゼン3−7837、
特公昭43−9713、特開昭49−110638等に
記載された技術として公知である。それらの内容は次の
工程から成っている。
Substantially pure m-alkylbenzene 3-7837 from alkylbenzene via alkylbenzene sulfonic acid,
This is known as a technique described in Japanese Patent Publication No. 43-9713, Japanese Patent Application Laid-open No. 49-110638, etc. Their content consists of the following steps:

(A)アルキルベンゼンを低温で硫酸によりスルホン化
して得たアルキルベンゼンスルホン酸混合物を硫酸の存
在下、150〜210℃の範囲の温度で加熱するか、ま
たはアルキルベンゼンヲ硫酸によって150〜210℃
の範囲の温度に保持することによって、m一体含量の多
いアルキルベンゼンスルホン酸a合物をm、 (B)6フルキルベンゼンスルホン酸混合物に水、好ま
しくは水蒸気を接触させてm一体以外のアルキルベンゼ
ンスルホン酸を選択的に加水分解してアルキルベンゼン
と硫酸にし、アルキルベンゼンは水と共沸させて系外に
除く。
(A) An alkylbenzene sulfonic acid mixture obtained by sulfonating alkylbenzene with sulfuric acid at low temperature is heated at a temperature in the range of 150 to 210°C in the presence of sulfuric acid, or the alkylbenzene is heated to 150 to 210°C with sulfuric acid.
By keeping the alkylbenzenesulfonic acid compound a having a high content of m at a temperature in the range of m, (B) contacting the 6-flukylbenzenesulfonic acid mixture with water, preferably water vapor, to form an alkylbenzenesulfone other than m. The acid is selectively hydrolyzed into alkylbenzene and sulfuric acid, and the alkylbenzene is azeotroped with water and removed from the system.

(C)加水分解を受けなかっだm−アルキルベンゼンス
ルボン酸をアルカリ塩化し、次いで(D)苛性的にアル
カリ融解してm−アルキルヒドロキシベンゼンlJる。
(C) The m-alkylbenzenesulfonic acid that has not undergone hydrolysis is converted into an alkali salt, and then (D) the m-alkylhydroxybenzene is dissolved in a caustic solution.

応の中で、工程A1すなわちスルホン化および異性化は
反応温度が高い程m一体が増加する。しかしながら特に
190℃近辺から急激に酸化、分解が進み、脱アルキル
やタール化が現われスルホン化物は黒色タール状になっ
て使用に堪えなくなる。
In step A1, ie, sulfonation and isomerization, the higher the reaction temperature, the more m-integrity increases. However, oxidation and decomposition proceed rapidly especially from around 190° C., dealkylation and tarring appear, and the sulfonated product becomes black tar-like and becomes unusable.

工程Bの加水分解も高温かつ長時間を要して行なわれる
ので副反応が起りやすい。そのために最終製品の純度や
品質の低下、あるいは収率の減少が避けられない。
Hydrolysis in step B is also carried out at high temperatures and over a long period of time, so side reactions are likely to occur. As a result, a decrease in the purity and quality of the final product or a decrease in yield is unavoidable.

本発明人らは、か\る従来法の欠点を改良すべく研究を
重ねた結果、70〜80%の高濃度硫酸中で150〜2
10℃に加熱する異性化および硫酸モル比が増大する加
水分解中に起きるジスルホン化、脱アルキル化、スルホ
ン酸分解等の副反応を抑制するために特定量の芒硝を存
在させておくことが有効であることを見出し本発明を完
成するに到った。
As a result of repeated research to improve the drawbacks of the conventional method, the inventors of the present invention discovered that 150 to 2
It is effective to have a specific amount of Glauber's salt present in order to suppress side reactions such as disulfonation, dealkylation, and sulfonic acid decomposition that occur during isomerization when heated to 10°C and hydrolysis when the sulfuric acid molar ratio increases. They found that this is the case and completed the present invention.

すなわち本発明は、アルキルベンゼン、またはアルキル
ベンゼンスルホン酸混合物を、硫酸および仕込硫酸モル
の1〜5%の無機塩の存在下に体含量の多いアルキルベ
ンゼンスルホン酸ヲ得、m一体重外のアルキルベンゼン
スルホン酸ヲ選択的に加水分解した後、加水分解を受け
なかったアルキルヘンセンスルホン酸を苛性的に融解す
ることを特徴とするm−アルキルヒドロキシベンゼンの
製造方法である。
That is, the present invention prepares an alkylbenzene or an alkylbenzene sulfonic acid mixture in the presence of sulfuric acid and an inorganic salt of 1 to 5% of the mol of sulfuric acid charged to obtain an alkylbenzene sulfonic acid with a high body content. This is a method for producing m-alkylhydroxybenzene, which comprises selectively hydrolyzing and then causticly melting the alkylhensene sulfonic acid that has not undergone hydrolysis.

本発明に使用するに適したアルキルベンゼンとしては、
例tばトルエン、エチルベンゼン、イソプロピルベンゼ
ン、キシレン等であって、異性化、または加水分解等に
よってm−異性体を得ることができるアルキルベンゼン
類である。
Alkylbenzenes suitable for use in the present invention include:
Examples include toluene, ethylbenzene, isopropylbenzene, xylene, etc., which are alkylbenzenes whose m-isomer can be obtained by isomerization, hydrolysis, or the like.

本発明におけるアルキルベンゼンと硫酸との反応は、こ
の種技術において知られた前述の如き条件下に行なうこ
とができる。以下にエチルベンゼンを例にとって本発明
の詳細な説明する。後述の実施例1の方法によりエチル
ベンゼンをMIIJの硫酸によりスルホン化、異性化す
る際、芒硝の添加、無添加による反応生成物の組成を測
定し、その百分率を表1に示した。次いでそれぞれの反
応組成物を実施例1に準じて加水分解し、得られた組成
物の組成比を表■に示した。さらにそれぞれの加水分解
組成物を実施例1の方法に準じて苛性融解、中和、蒸留
後得られた組成物の組成および組成比率を表■に示した
The reaction of alkylbenzene and sulfuric acid in the present invention can be carried out under the conditions known in the art and as described above. The present invention will be explained in detail below using ethylbenzene as an example. When ethylbenzene was sulfonated and isomerized with MIIJ sulfuric acid according to the method of Example 1 described later, the composition of the reaction product with and without the addition of Glauber's salt was measured, and the percentages are shown in Table 1. Next, each reaction composition was hydrolyzed according to Example 1, and the composition ratios of the resulting compositions are shown in Table 3. Further, each hydrolyzed composition was subjected to caustic melting, neutralization, and distillation according to the method of Example 1, and the compositions and composition ratios of the obtained compositions are shown in Table 2.

表  1 異性化終了時の組成および比率(%) 表  ■ 表  ■1 a )収1はエチルフェノールの対消費エチルベンゼン
収率を示した。
Table 1 Composition and ratio (%) at the end of isomerization Table ■Table ■1 a) Yield 1 shows the yield of ethylbenzene relative to the consumption of ethylphenol.

表1〜■の組成物の組成比率から、芒硝添加のない場合
は好ましくない副反応によりベンゼンスルホン酸、トル
エンスルホン酸および不明成分が多く、エチルフェノー
ルの純度および収率も低く、芒硝敞を増してゆくと、こ
れらの副反応が抑制され、純度および収率も高くなるこ
とが明らかである。芒硝の添加量は仕込硫酸モルに対し
て1〜5%がよく、1%以下では効果が乏しく、5%以
内で充分であって5%以上は不必要である。またかかる
芒硝添加の効果は芒硝の添加をスルホン化の当初から行
なっておくだけでなく、スルホン化後、異性化前に行な
ってもよく、加水分解時の安定性だけを目的とするなら
ば加水分解直前に添加することによっても効果は変らな
い。いずれの場合も得られたm−アルキルベンゼンスル
ホン酸は従来から行なわれている方法よ・りも非常に効
率よく精製出来、アルカリ融解工程を経て、高純度のm
−アルキルヒドロキシベンゼン類とする事が出来る。
From the composition ratios of the compositions in Tables 1 to ■, it can be seen that without the addition of Glauber's salt, there are many benzenesulfonic acids, toluenesulfonic acids, and unknown components due to unfavorable side reactions, the purity and yield of ethylphenol is low, and the concentration of Glauber's salt increases. It is clear that as the process progresses, these side reactions are suppressed and the purity and yield are also increased. The amount of Glauber's salt to be added is preferably 1 to 5% based on the mole of sulfuric acid charged. If it is less than 1%, the effect is poor, and if it is less than 5%, it is sufficient, and if it is more than 5%, it is unnecessary. Furthermore, the effect of adding mirabilite can be achieved not only by adding mirabilite from the beginning of sulfonation, but also by adding mirabilite after sulfonation and before isomerization. Even if it is added just before decomposition, the effect remains the same. In either case, the obtained m-alkylbenzenesulfonic acid can be purified much more efficiently than the conventional method, and after undergoing an alkaline melting process, it can be purified to a highly pure m-alkylbenzenesulfonic acid.
-Can be made into alkylhydroxybenzenes.

本発明の製造方法によって、20o℃以上の高温でもア
ルキルベンゼンスルホン酸の酸化分解を顕著に抑制し、
その結果、高温かつ長時間のスルホン化、異性化、加水
分解反応が可能になり、m−棒金はが98%を超すとド
ロキシベンゼンヲ収率よく得られるようになった。
By the production method of the present invention, the oxidative decomposition of alkylbenzenesulfonic acid is significantly suppressed even at high temperatures of 20oC or higher,
As a result, high-temperature and long-term sulfonation, isomerization, and hydrolysis reactions became possible, and when the m-rod exceeded 98%, droxybenzene could be obtained in good yield.

以下に本発明方法を実施例によって説明するが本発明は
この実施例によって限定されるものではない。
The method of the present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples.

実施例 1 98%i酸1200yを21!四ツロフラスコに仕込み
、無水芒硝20pを撹拌しながら添加し、次いで848
yのエチルベンゼンを1時間を要して滴下する。徐々に
加熱昇温し、2時間を要し留出水を抜きながら200℃
にする。同温度で4時間加熱撹拌し、異性化する。次に
内温を170℃迄降温し、同温度で撹拌下に2600 
meの水を12時間を要して連続的に滴下し加水分解を
行なう。
Example 1 98% i acid 1200y 21! Pour into a Yotsuro flask, add 20p of anhydrous sodium sulfate with stirring, and then
Add y of ethylbenzene dropwise over a period of 1 hour. Gradually raise the temperature to 200℃ while removing distilled water for 2 hours.
Make it. Heat and stir at the same temperature for 4 hours to isomerize. Next, the internal temperature was lowered to 170℃, and at the same temperature it was heated to 2600℃ with stirring.
Me water was continuously added dropwise over a period of 12 hours to carry out hydrolysis.

420pのエチルベンゼンが回収された。反応液に47
%苛性ソーダを加えてpH8まで中和、80℃で熱時芒
硝を戸別し、母液を563yの苛性ソーダと83yの苛
性カリを21溶融釜に330℃の温度で加熱溶融してい
る混合物中に滴下する。
420p of ethylbenzene was recovered. 47 to the reaction solution
% caustic soda to neutralize it to pH 8, heat it at 80°C, pour the mother liquor into a mixture of 563y of caustic soda and 83y of caustic potash, which is heated and melted in a 21 melting pot at a temperature of 330°C.

滴下後、内容物の温度を330℃から340℃に昇温し
、340℃で60分撹拌保持した。得られた融解反応物
を2000meの水に溶解し、35%塩酸でpH7,2
に中和する。
After the dropwise addition, the temperature of the contents was raised from 330°C to 340°C, and stirred and held at 340°C for 60 minutes. The obtained molten reaction product was dissolved in 2000me water, and the pH was adjusted to 7.2 with 35% hydrochloric acid.
to neutralize.

生成したフェノール類をエーテルで抽出、蒸留を行なっ
て純度92.8%の粗m−エチルフェノールを得た。分
留により98%純度のm−エチルフェノール335gを
得た。収率は消費エチルベンゼンに対して68%であっ
た。
The produced phenols were extracted with ether and distilled to obtain crude m-ethylphenol with a purity of 92.8%. 335 g of m-ethylphenol with a purity of 98% was obtained by fractional distillation. The yield was 68% based on consumed ethylbenzene.

実施例 2 98%硫酸600yを11フラスコに仕込み、撹拌しな
がら無水芒硝34y(添加率4%)を加える。次いでエ
チルベンゼン424yを30分を要して庄原し、徐々に
加熱昇温する。2時間を要し留出水を抜きながら200
℃にする。同温度で4時間加熱撹拌し異性化する。以下
、実施例−1と同様に後処理し、93.8%の粗m−エ
チルフェノールを得た。分留により純度98.2%のも
の1789が得られた。対消費エチルベンゼン収率は7
2%であった。
Example 2 600 y of 98% sulfuric acid is charged into a flask No. 11, and 34 y of anhydrous sodium sulfate (addition rate: 4%) is added while stirring. Next, ethylbenzene 424y was added to the mixture for 30 minutes, and the temperature was gradually increased. It took 2 hours and 200 yen while draining the distillate water.
℃. The mixture is heated and stirred at the same temperature for 4 hours for isomerization. Thereafter, post-treatment was carried out in the same manner as in Example-1 to obtain 93.8% crude m-ethylphenol. Fractional distillation yielded 1789 with a purity of 98.2%. Yield of ethylbenzene based on consumption is 7
It was 2%.

実施例 3 98%硫酸1090yを21!フラスコに仕込み、撹拌
しながら無水芒硝317;’(添加率2%)を加える。
Example 3 98% sulfuric acid 1090y 21! Charge the mixture into a flask, and add anhydrous Glauber's Salt 317;' (addition rate: 2%) while stirring.

続いてトルエン503yを滴下し、2時間をかけて19
5℃迄昇温する。195℃で4時間加熱撹拌して異性化
を行なう。次に165℃迄降温後、同温度を保ちながら
水1000+++eを一定速度で10時間を要し連続的
に滴下する。加水分解を受けだp−)ルエンスルホン酸
はトルエンと硫酸に戻り、水との共沸によりトルエンは
系外に留出する。回収されたトルエン//″1216y
であった。
Next, 503y of toluene was added dropwise, and 19g was added over 2 hours.
Raise the temperature to 5℃. Isomerization is carried out by heating and stirring at 195° C. for 4 hours. Next, after the temperature was lowered to 165°C, 1000+++e of water was continuously added dropwise at a constant rate over a period of 10 hours while maintaining the same temperature. The hydrolyzed p-)luenesulfonic acid returns to toluene and sulfuric acid, and toluene is distilled out of the system by azeotropy with water. Recovered toluene //''1216y
Met.

加水分解後のトルエンスルホン酸を苛性ソーダで中和し
、苛性融解、抽出、分留を行ない純度98%のm−クレ
ゾール242yを得た。
The toluenesulfonic acid after hydrolysis was neutralized with caustic soda, followed by caustic melting, extraction, and fractional distillation to obtain m-cresol 242y with a purity of 98%.

実施例 4 98%硫酸1700yを317ラスコに仕込み、撹拌し
ながら無水芒硝75g!(添加率3%)を加え、次いで
メタキシレン1100 ?li!fi下、2.5時間を
要して180℃迄昇温する。その後175〜180℃で
3時間保温し異性化を行なう。150℃迄降温し、水7
00meを同温度で3時間かけて連続的に滴下して加水
分解を行なった。加水分解により水蒸気と共に留出する
メタキシレンは水と分離して270y回収された。加水
分解後の残液3100y中に含まれるキシレンスルホン
酸を常法により中和し、苛性融解を行ない、3,5−キ
シレノール707yを得た。純度97%であった。
Example 4 Pour 1700y of 98% sulfuric acid into a 317 lasco, and add 75g of anhydrous sodium sulfate while stirring! (addition rate: 3%) and then meta-xylene 1100? li! It takes 2.5 hours to raise the temperature to 180° C. under fi. Thereafter, the mixture is kept at 175 to 180°C for 3 hours to perform isomerization. The temperature drops to 150℃, water 7
Hydrolysis was carried out by continuously dropping 00me at the same temperature over 3 hours. Meta-xylene distilled out together with water vapor due to hydrolysis was separated from water and recovered for 270y. Xylene sulfonic acid contained in the residual liquid 3100y after hydrolysis was neutralized by a conventional method and caustic melting was performed to obtain 3,5-xylenol 707y. The purity was 97%.

特許出願人 田岡化学工業株式会社 −11完− 228−Patent applicant: Taoka Chemical Industry Co., Ltd. -11 completed- 228-

Claims (1)

【特許請求の範囲】[Claims] 1、 アルキルベンゼン、またはアルキルベンゼンスル
ホン酸混合物を、硫酸および仕込硫酸モルの1〜5%の
無機塩の存在下に150〜210℃の範囲の温度で加熱
して、m一体含量の多いアルキルベンゼンスルホン酸を
得、m一体以外のアルキルベンゼンスルホン酸を選択的
に加水分解した後、加水分解を受け々かったアルキルベ
ンゼンスルホン酸を苛性的に融解することを特徴とする
m−アルキルヒドロキシベンゼンの製造方法
1. An alkylbenzene or alkylbenzene sulfonic acid mixture is heated in the presence of sulfuric acid and an inorganic salt of 1 to 5% of the mol of sulfuric acid charged at a temperature in the range of 150 to 210°C to produce an alkylbenzene sulfonic acid with a high monomer content. A method for producing m-alkylhydroxybenzene, which comprises selectively hydrolyzing alkylbenzene sulfonic acids other than m-monomers, and then causticly melting alkylbenzene sulfonic acids that have not undergone hydrolysis.
JP56210285A 1981-11-27 1981-12-23 Preparation of m-alkylhydroxybenzene Granted JPS58109435A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP56210285A JPS58109435A (en) 1981-12-23 1981-12-23 Preparation of m-alkylhydroxybenzene
DE8282306320T DE3262826D1 (en) 1981-11-27 1982-11-26 Process for preparing m-alkylhydroxybenzene
US06/444,696 US4475002A (en) 1981-11-27 1982-11-26 Process for preparing m-alkylhydroxybenzene
EP82306320A EP0080880B1 (en) 1981-11-27 1982-11-26 Process for preparing m-alkylhydroxybenzene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56210285A JPS58109435A (en) 1981-12-23 1981-12-23 Preparation of m-alkylhydroxybenzene

Publications (2)

Publication Number Publication Date
JPS58109435A true JPS58109435A (en) 1983-06-29
JPH0234929B2 JPH0234929B2 (en) 1990-08-07

Family

ID=16586862

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56210285A Granted JPS58109435A (en) 1981-11-27 1981-12-23 Preparation of m-alkylhydroxybenzene

Country Status (1)

Country Link
JP (1) JPS58109435A (en)

Also Published As

Publication number Publication date
JPH0234929B2 (en) 1990-08-07

Similar Documents

Publication Publication Date Title
Snyder et al. The preparation of 3, 3′-dibromobiphenyl and its conversion to organometallic compounds
US3579537A (en) Process for separation of sultones from alkenyl sulfonic acids
US2126648A (en) Process of producing halogenated phenols
JPS58109435A (en) Preparation of m-alkylhydroxybenzene
JPS5943935B2 (en) Method for producing 4,4'-dihydroxydiphenyl
JPH0229057B2 (en) MMARUKIRUHIDOROKISHIBENZENNOSEIZOHOHO
US3309409A (en) Purification of acidic chlorophenylsulfones
JPH029012B2 (en)
RU2041197C1 (en) Process for preparing 1,1-bis-(chlorophenyl)-2,2,2- trichloroethanol
JPS643176B2 (en)
WO1991004245A1 (en) Process for preparing 4,4'-dihydroxydiphenyl sulfone
US4130581A (en) Preparing J acid by fusion using phenolic fluxing agent
US1915925A (en) Process of making resorcinol
EP0080880B1 (en) Process for preparing m-alkylhydroxybenzene
JPH0229056B2 (en) MMARUKIRUHIDOROKISHIBENZENNOSEIZOHOHO
SU40359A1 (en) Method for producing phenolphthalein
US1988156A (en) Process for the preparation of phenols
US1308757A (en) Alexis c
EP0694516B1 (en) Process of selective desulfonation
JP2956960B2 (en) Method for producing m-hydroxyalkylbenzene
US1750299A (en) Production of acyl resorcinols
JPH0234928B2 (en) MMARUKIRUHIDOROKISHIBENZENNOSEIZOHOHO
US1992167A (en) Process for the manufacture of phenols from alkali arylsulphonates
JPH01500672A (en) Improvement of manufacturing method of diarylsulfones
SU556725A3 (en) The method of obtaining a mixture of benzenedisulphonic acid and benzene monosulphonic acid or toluene monosulphonic acid