JPS6160645A - Production of sulfonyl dibenzoic acid - Google Patents

Production of sulfonyl dibenzoic acid

Info

Publication number
JPS6160645A
JPS6160645A JP59180324A JP18032484A JPS6160645A JP S6160645 A JPS6160645 A JP S6160645A JP 59180324 A JP59180324 A JP 59180324A JP 18032484 A JP18032484 A JP 18032484A JP S6160645 A JPS6160645 A JP S6160645A
Authority
JP
Japan
Prior art keywords
cobalt
reaction
bromine
acetic acid
amount
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.)
Pending
Application number
JP59180324A
Other languages
Japanese (ja)
Inventor
Tadamitsu Kiyoura
清浦 忠光
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP59180324A priority Critical patent/JPS6160645A/en
Publication of JPS6160645A publication Critical patent/JPS6160645A/en
Pending 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 obtain the titled compound useful as a raw material of polyamide resin, in high yield, by oxidizing diarylsulfone with molecular oxygen in acetic acid solvent, while keeping the ratio of the cobalt catalyst to bromine and the concentration of the catalyst in acetic solvent at specific levels. CONSTITUTION:The objective compound of formula I can be produced by oxidizing the diarylsulfone of formula I with molecular oxygen in acetic acid solvent using a catalyst comprising cobalt and bromine. The amount of the cobalt is 0.2-3wt% in terms of metallic cobalt based on the acetic acid, and the amount of bromine is 1-1.5 equivalent per 1 equivalent of cobalt. The reaction can be carried out under extermely mild conditions, i.e. at about 100 deg.C and atmospheric pressure - about 10kg/cm<2> pressure. The objective compound can be produced in a short reaction time, in high yield, safely and economically in an industrial scale. The reaction liquid can be recycled to the oxidation reaction system after separating the objective compound therefrom and adding diarylsulfone thereto.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はスルホニルジ安息香酸の製造法、より詳細には
、酢酸溶媒中でジアリルスルホンを分子状酸素で酸化し
てスルホニルジ安息香酸を製造する方法に関するもので
ある。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for producing sulfonyl dibenzoic acid, and more specifically, a method for producing sulfonyl dibenzoic acid by oxidizing diallylsulfone with molecular oxygen in an acetic acid solvent. It's about how to do it.

スルホニルジ安息香酸は、ポリアミド樹脂の原料として
有用なものである。
Sulfonyl dibenzoic acid is useful as a raw material for polyamide resins.

スルホニルジ安息香酸な用いて製造したポリアミドは強
度、耐熱性等に優れた性質を示めす。
Polyamide produced using sulfonyl dibenzoic acid exhibits excellent properties such as strength and heat resistance.

(従来技術およびその問題点) ジアリルスルホンを酢酸溶媒中で分子状酸素により酸化
してスルホニルジ安息香酸な製造する方法には、コバル
ト塩を触媒とし、加圧下130°Cで反応させ86%の
収率で目的物を得る方法(FRL507,996;CA
70286571)、 QBI、005,231;CA
6317983e )、あるいはコバルトの有機酸塩と
メチルエチルケトンとを用い、105℃、300psI
gで反応させる方法(US 3.676.488 、C
A77101.202n; US 3,692,828
、CA77151685t )等が知られている。
(Prior art and its problems) A method for producing sulfonyl dibenzoic acid by oxidizing diallyl sulfone with molecular oxygen in an acetic acid solvent involves using a cobalt salt as a catalyst and reacting at 130°C under pressure to obtain 86% Method for obtaining the desired product in high yield (FRL507,996; CA
70286571), QBI, 005,231; CA
6317983e) or using cobalt organic acid salt and methyl ethyl ketone at 105°C and 300 psI.
(US 3.676.488, C
A77101.202n; US 3,692,828
, CA77151685t), etc. are known.

しかしながら、上記した既存のジアリルスルホンを酸化
しスルホニルジ安息香酸な得る方法は、反応に要する時
間が長い、反応をかなりの加圧下で実施する必要がある
、収率もあまり優れたものではない等の欠点があり、工
業的にスルホニルジ安息香酸を安価に製造する方法とし
て満足できる方法ではない。
However, the existing method described above to obtain sulfonyl dibenzoic acid by oxidizing diallyl sulfone requires a long reaction time, the reaction must be carried out under considerable pressure, and the yield is not very good. This method is not satisfactory as a method for industrially producing sulfonyl dibenzoic acid at low cost.

本発明の目的とするところは、前述の既存合成法のよう
な欠点の無い、工業的に安価なスルホニルジ安息香酸の
製造法を提供することにある。
An object of the present invention is to provide an industrially inexpensive method for producing sulfonyl dibenzoic acid that does not have the drawbacks of the existing synthetic methods described above.

(問題点を解決するための手段) 本発明者はジアリルスルホンの酢酸溶媒中での酸化反応
に関して種々研究した結果、用いるコバルト触媒と臭素
との割合および酢酸溶媒中の触媒濃度をある一定範囲に
保つと極めて温和な反応条件でも酸化反応が速みやかに
進行することを見出し、本発明を完成するに至った。
(Means for Solving the Problems) As a result of various studies on the oxidation reaction of diallylsulfone in an acetic acid solvent, the present inventor determined that the ratio of the cobalt catalyst to bromine used and the catalyst concentration in the acetic acid solvent should be within a certain range. The present inventors have discovered that when maintained, the oxidation reaction proceeds rapidly even under extremely mild reaction conditions, leading to the completion of the present invention.

すなわち、本発明の要旨とするところは、ジアリルスル
ホンを分子状敢素で酸化しスルホニルジ安息香酸を製造
するに際し、酢酸溶媒中で触媒と。
That is, the gist of the present invention is to oxidize diallyl sulfone with molecular hydrogen to produce sulfonyl dibenzoic acid using a catalyst in an acetic acid solvent.

して用いるコバルト塩のコバルト金属で表わしたコバル
トの使用量を酢酸に対し0.2〜3 wt%の範囲とし
、臭素の使用竜をコバルトと当量乃至当量の1.5倍量
の範囲で反応させること忙ある。
The amount of cobalt expressed as cobalt metal in the cobalt salt used as a cobalt salt is in the range of 0.2 to 3 wt% relative to acetic acid, and the amount of bromine used is in the range of an equivalent amount to 1.5 times the equivalent amount of cobalt. I'm busy making things happen.

本発明の方法は出発物質として、 CH3−1ジーS02ξC113で表わされるジアリル
スルホンを用いる。
The method of the invention uses diallylsulfone represented by CH3-1S02ξC113 as a starting material.

通常、3,3−ジメチルジフェニルスルホン、3゜4−
ジメチルジフェニルスルホンまたは4,4−ジメチルジ
フェニルスルホン等の化合物が多用される。
Usually, 3,3-dimethyldiphenylsulfone, 3゜4-
Compounds such as dimethyldiphenylsulfone or 4,4-dimethyldiphenylsulfone are frequently used.

これらの化合物は、例えば、トルエンスルホニルクロラ
イドをトルエンとルイス酸触媒の存在下で反応させる、
あるいはトルエンスルホン酸とトルエンをメタンスルホ
ン酸溶媒中で脱水剤の存在下に縮合させる等の方法で製
造することが出来る。
These compounds can be prepared, for example, by reacting toluene sulfonyl chloride with toluene in the presence of a Lewis acid catalyst.
Alternatively, it can be produced by a method such as condensing toluenesulfonic acid and toluene in a methanesulfonic acid solvent in the presence of a dehydrating agent.

本発明の反応は、液状の低級カルボン酸溶媒中で実施す
る。低級カルボン酸溶媒としてはとくに酢酸が好ましい
The reaction of the present invention is carried out in a liquid lower carboxylic acid solvent. Acetic acid is particularly preferred as the lower carboxylic acid solvent.

溶媒の使用量はジアリルスルホン九対して1〜20倍量
、好ましくは2〜10倍量である。
The amount of the solvent used is 1 to 20 times, preferably 2 to 10 times the amount of diallylsulfone 9.

本発明の反応に用いる触媒は、コバルトの塩であって、
有機または無機のコバルト塩が用いられる。これらのコ
バルト塩のうちでは、酢酸コバルト、プロピオン酸コバ
ルト、安息香酸コバルトマたはナフテン酸コバルト等が
多用される。
The catalyst used in the reaction of the present invention is a cobalt salt,
Organic or inorganic cobalt salts are used. Among these cobalt salts, cobalt acetate, cobalt propionate, cobalt benzoate, cobalt naphthenate, etc. are often used.

コバルトの原子価は、通常、反応液忙仕込む際は2価の
コバルト塩が多用される。触媒の使用竜としては、コバ
ルト塩中のコバルト金属で表わしたコバルトの竜が酢酸
等の有機酸溶媒忙対し0.2〜3 wt%の範囲が適し
ている。コバルトの量が0.2wt%に満たないと反応
の速度は極端に低下し、反応が実質的に進行し難(なる
。コバルトの量が上記の3wt%付近で反応の速度はは
y飽和値に達し、3wt%を越えても反応はさらに速み
やかに進行しなくなる。またコバルト濃度をこれ以上増
加することは、反応後の処理行程でのコバルトの損失が
増大する等の点で好ましくない。
Regarding the valence of cobalt, divalent cobalt salts are usually used frequently when preparing a reaction solution. The amount of cobalt expressed as cobalt metal in the cobalt salt is preferably in the range of 0.2 to 3 wt% when used in an organic acid solvent such as acetic acid. If the amount of cobalt is less than 0.2 wt%, the reaction rate will be extremely low and it will be difficult for the reaction to actually proceed. If the cobalt concentration exceeds 3 wt%, the reaction will not proceed any more rapidly.Increasing the cobalt concentration any further is not preferable because the loss of cobalt in the post-reaction treatment process will increase. .

コバルト塩と共に臭素を触媒として使用する。Bromine is used as a catalyst along with a cobalt salt.

臭素としては無水の臭化水素酸、分子状臭素、臭゛、化
物が使用されるが、通常、無水臭化水素が多用される。
As bromine, anhydrous hydrobromic acid, molecular bromine, bromine, and compounds are used, but anhydrous hydrogen bromide is usually used.

無水の臭化水素酸を酢酸等の有機酸中に溶解せしめたも
の力板触媒液の調製の際に便利である。臭素の使用量は
、使用するコバルト原子と当世乃至当世の1.5倍量の
範囲が好ましい。
A solution prepared by dissolving anhydrous hydrobromic acid in an organic acid such as acetic acid is useful for preparing a plate catalyst solution. The amount of bromine used is preferably in the range of 1.5 times the amount of cobalt atoms used in the present day or the amount in the present day.

臭素の使用量がコバルトと当量未満であると、触媒活性
が低く、反応の速度が低下する。また漠素素を当量の1
.5倍を越えて増加しても反応速度の増加は飽和値に達
し、臭素の損失になり好ましくない。
If the amount of bromine used is less than the equivalent amount of cobalt, the catalyst activity will be low and the reaction rate will be reduced. Also, the equivalent of 1
.. Even if the amount is increased by more than 5 times, the increase in reaction rate will reach a saturation value, resulting in loss of bromine, which is not preferable.

本発明の方法で用いる酸化剤は、分子状の酸素であって
、酸素ガスまたは空気が用いられる。酸素ガスを反応に
使用する際には、反応を常圧または微加圧(1,1〜x
、5ky/i)で反応は充分な速さで進行する。また、
酸化剤として空気を用いる場合でも常圧で反応が進行す
るが、通常は2〜7時程度の加圧下に反応を実施する場
合が多い。
The oxidizing agent used in the method of the present invention is molecular oxygen, and oxygen gas or air is used. When using oxygen gas in the reaction, the reaction may be carried out at normal pressure or slightly pressurized (1,1~x
, 5ky/i), the reaction proceeds at a sufficient rate. Also,
Although the reaction proceeds at normal pressure even when air is used as the oxidizing agent, the reaction is usually carried out under pressure of about 2 to 7 hours.

反応を実施する際の温度は90〜130℃、通常は10
0〜110℃の温度範囲が多用される。上述のよ5K、
本発明の方法では、反応温度が100℃前後、反応に要
する圧力も常圧乃至数kg/−と温和であり、工業的に
反応を実施する際に極めて安全で、装置も簡略とするこ
とが出来る。
The temperature at which the reaction is carried out is 90-130°C, usually 10°C.
A temperature range of 0 to 110°C is frequently used. The above-mentioned 5K,
In the method of the present invention, the reaction temperature is around 100°C, and the pressure required for the reaction is mild, ranging from normal pressure to several kg/-, making it extremely safe to carry out the reaction industrially, and requiring simple equipment. I can do it.

反応に要する時間は、反応を回分式で実施した場合で例
示すれば、1〜10時間の範囲であり、通常、常圧酸素
で反応を実施する場合は、2〜6時間である。
The time required for the reaction is, for example, in the range of 1 to 10 hours when the reaction is carried out batchwise, and is usually 2 to 6 hours when the reaction is carried out in normal pressure oxygen.

反応が進行し目的物のスルホニルジ安息香酸が生成する
と反応液中に固体として析出する。ジアリルスルホンの
一方のみが、酸化されたスルホニルモノ安息香酸は大部
分が反応液中に溶解している。したがって、反応を充分
に進行させ、析出した固体を反応液から戸別し、洗滌す
るのみで目的物を単離出来る。目的物を単離後の反応液
は、ふた〜び、ジアリルスルホンを添加し繰返し酸化反
応を実施することが出来る。
As the reaction progresses and the target product, sulfonyl dibenzoic acid, is produced, it is precipitated as a solid in the reaction solution. Most of the sulfonyl monobenzoic acid, in which only one of the diallylsulfones has been oxidized, is dissolved in the reaction solution. Therefore, the target product can be isolated by simply allowing the reaction to proceed sufficiently, separating the precipitated solid from the reaction solution, and washing it. After isolation of the target product, diallylsulfone can be added to the reaction solution again to carry out the oxidation reaction repeatedly.

(実施列) 以下、実施例圧より本発明を説明する。(Implementation row) The present invention will be explained below using examples.

実施例−1 パラトルエンスルホン酸−水塩およびこれと等モルのト
ルエンを五酸化溝を添加したメタンスA/ホン酸溶媒中
に加え、25℃で20時間反応させルジ7・ニルスルホ
ン(MP、155℃>’+収率9゜チで得た。
Example-1 Para-toluenesulfonic acid hydrate and an equimolar amount of toluene were added to a methane A/phonic acid solvent to which a pentoxide groove was added, and the mixture was reacted at 25°C for 20 hours. ℃>'+Yield: 9°C.

内容11の五ツロフラスコに撹拌棒、温度計、還流冷却
器、酸素吹込管を付けたものを反応器とした。
A reactor was prepared by adding a stirring rod, a thermometer, a reflux condenser, and an oxygen blowing tube to a five-tube flask as described in Item 11.

酢酸5009 VC”h酸=’ ハルト(Co(CI−
I3COO)2 ・4l−50) 159 (0,06
モル)(酢酸中金属コバルトとして0.71 wt%に
相当)、無水臭化水素酸4.859 (0,075モル
)を含有する酢酸溶液16.2gを添加した。ついで4
.4−ジメチルジフェニルスルホン 73.89 (0
,3モル) ヲ添加り、 、Fjt応器外器外部イルバ
スで加熱し溶液を105°Cとした。よく攪拌しながら
、常圧酸素ガスを吹込み反応開始した。反応液温は11
2℃まで上昇し、反応開始1.5時、間で白色の固体が
析出し出した。更に2時間半反応を続行後、酸素の吸込
みを中止し、反応器を50’Cまで冷却してから、生成
した白色沈澱を戸別した。
Acetic acid 5009 VC"h acid=' Hult (Co(CI-
I3COO)2 ・4l-50) 159 (0,06
16.2 g of an acetic acid solution containing 4.859 (0,075 mol) of hydrobromic anhydride was added. Then 4
.. 4-Dimethyldiphenylsulfone 73.89 (0
, 3 mol) was added, and the solution was heated to 105°C in an air bath outside the reactor. While stirring well, normal pressure oxygen gas was blown in to start the reaction. The reaction solution temperature is 11
The temperature rose to 2°C, and a white solid precipitated out 1.5 hours after the start of the reaction. After continuing the reaction for an additional 2 and a half hours, the oxygen suction was stopped, the reactor was cooled to 50'C, and the white precipitate formed was removed from the house.

戸別した沈澱を、酢酸、次いで温水で充分に洗滌し10
0℃で減圧下に乾燥し、白色粉末84,5り(収率92
チ)を得た。白色粉末の元素分析値お実施例−2 実施例−1と同様の方法と反応条件で3,4−ジメチル
ジフェニルスルホンの酸化反応を実施した。反応開始2
時間で白色固体の析出が認められた。合計6時間反応を
続行後、冷却し、析出した沈澱をF別洗滌し、白色粉末
76.29 (82%収率)を得た。取得した粉末は元
素分析値およびIRスペクトルヨリジフェニルスルホン
−3,4−ジカルボン酸と同定された。
The precipitate separated from each house was thoroughly washed with acetic acid and then with warm water for 10 minutes.
Dry under reduced pressure at 0°C to give a white powder of 84.5 ml (yield: 92
h) was obtained. Elemental Analysis Values of White Powder Example-2 An oxidation reaction of 3,4-dimethyldiphenylsulfone was carried out using the same method and reaction conditions as in Example-1. Reaction start 2
Precipitation of a white solid was observed over time. After continuing the reaction for a total of 6 hours, it was cooled, and the precipitate precipitated was washed separately with F to obtain 76.29 g of white powder (82% yield). The obtained powder was identified by elemental analysis and IR spectrum as yolidiphenylsulfone-3,4-dicarboxylic acid.

実施例−3 実施例−1と同様の反応方法で、使用する容器を300
−のフラスコとし、酢酸溶媒150−を用いて反応させ
た。
Example-3 Using the same reaction method as in Example-1, the container used was
A reaction was carried out using an acetic acid solvent of 150- in a flask containing -.

用いる触媒量を種々に変えて、酸化反応により消失する
、4.4−ジメチルジフェニルスルホンの濃度をガスク
ロマトグラフィーで追跡した。
The amount of catalyst used was varied and the concentration of 4,4-dimethyldiphenylsulfone that disappeared through the oxidation reaction was monitored by gas chromatography.

得られた結果を表−1に示めした。なおコバルトと臭素
は当量使用した。
The results obtained are shown in Table-1. Note that cobalt and bromine were used in equivalent amounts.

表−1 実施例−4 実施例3と同様の方法でコバルト濃度1.QNvt%と
し、添加する無水臭化水素酸の濃度を変えて、原料の消
失速度を追跡した。
Table-1 Example-4 Cobalt concentration 1. QNvt% and the concentration of added hydrobromic anhydride was varied to track the rate of disappearance of the raw material.

得られた結果を表−2に示めす。The results obtained are shown in Table-2.

(発明の効果) 本発明の方法によれば、反応温度を100℃前後、反応
圧力を常圧乃至10に9/d程度の極めて温和な条件で
反応を実施出来、反応時間も短縮され、更に収率も高く
、二条的に有利にスルホニルジ安息香酸な製造出来る。
(Effects of the Invention) According to the method of the present invention, the reaction can be carried out under very mild conditions such as a reaction temperature of around 100°C and a reaction pressure of about 9/d to normal pressure, and the reaction time is shortened. The yield is also high, and sulfonyl dibenzoic acid can be produced advantageously in two steps.

Claims (1)

【特許請求の範囲】 1)一般式▲数式、化学式、表等があります▼で表わさ
れるジ アリルスルホンを分子状酸素で酸化して、一般式▲数式
、化学式、表等があります▼で表わされる、スル ホニルジ安息香酸を製造するに際し、酢酸溶媒中でコバ
ルトと臭素から構成される触媒を使用し、コバルト金属
で表わしたコバルトの使用量を酢酸に対し0.2〜3w
t%の範囲とし、臭素の使用量をコバルトと当量乃至当
量の1.5倍量の範囲で反応させることを特徴とするス
ルホニルジ安息香酸の製造法。
[Claims] 1) Diallylsulfone represented by the general formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ is oxidized with molecular oxygen to produce a compound represented by the general formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ When producing sulfonyl dibenzoic acid, a catalyst composed of cobalt and bromine is used in an acetic acid solvent, and the amount of cobalt expressed as cobalt metal is 0.2 to 3 w per acetic acid.
A method for producing sulfonyl dibenzoic acid, characterized in that the amount of bromine used is in the range of an equivalent amount to 1.5 times the equivalent amount of cobalt.
JP59180324A 1984-08-31 1984-08-31 Production of sulfonyl dibenzoic acid Pending JPS6160645A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59180324A JPS6160645A (en) 1984-08-31 1984-08-31 Production of sulfonyl dibenzoic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59180324A JPS6160645A (en) 1984-08-31 1984-08-31 Production of sulfonyl dibenzoic acid

Publications (1)

Publication Number Publication Date
JPS6160645A true JPS6160645A (en) 1986-03-28

Family

ID=16081216

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59180324A Pending JPS6160645A (en) 1984-08-31 1984-08-31 Production of sulfonyl dibenzoic acid

Country Status (1)

Country Link
JP (1) JPS6160645A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63170351A (en) * 1987-01-06 1988-07-14 New Japan Chem Co Ltd Production of aromatic polycarboxylic acids

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63170351A (en) * 1987-01-06 1988-07-14 New Japan Chem Co Ltd Production of aromatic polycarboxylic acids

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