JPS62255454A - Production of 2-(4,4'-bis(dimethylamino)-benzohydryl)-5-dimethylaminobenz-oic acid - Google Patents

Production of 2-(4,4'-bis(dimethylamino)-benzohydryl)-5-dimethylaminobenz-oic acid

Info

Publication number
JPS62255454A
JPS62255454A JP61097376A JP9737686A JPS62255454A JP S62255454 A JPS62255454 A JP S62255454A JP 61097376 A JP61097376 A JP 61097376A JP 9737686 A JP9737686 A JP 9737686A JP S62255454 A JPS62255454 A JP S62255454A
Authority
JP
Japan
Prior art keywords
acid
bis
benzohydryl
dimethylamino
average particle
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
JP61097376A
Other languages
Japanese (ja)
Other versions
JPH0333150B2 (en
Inventor
Yoshiharu Fujino
藤野 義治
Hajime Kawai
初 河合
Katsuhiko Tsunemitsu
恒光 克彦
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.)
Yamada Chemical Co Ltd
Original Assignee
Yamada 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 Yamada Chemical Co Ltd filed Critical Yamada Chemical Co Ltd
Priority to JP61097376A priority Critical patent/JPS62255454A/en
Publication of JPS62255454A publication Critical patent/JPS62255454A/en
Publication of JPH0333150B2 publication Critical patent/JPH0333150B2/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 obtain the titled compound useful as a synthetic intermediate for pigment for recording material in high quality and yield, by adding tetramethyl-4,4'-diaminobenzhydrol to an aqueous solution of a mineral acid having a specific pH and containing m-dimethylaminobenzoic acid. CONSTITUTION:Tetramethyl-4,4'-diaminobenzhydrol having an average particle diameter of <=50mu is added as slowly as possible to an aqueous solution of a mineral acid such as hydrochloric acid, sulfuric acid, etc., of 1.5-3.0pH, preferably 2.0-3.0pH containing m-dimethylaminobenzoic acid having an average particle diameter of <=30mu and the components are made to react with each other at 50-100 deg.C to obtain the objective compond. The reaction system is preferably added with a surfactant (e.g. polyoxyethylene alkyl ether) to effect uniform dispersion of the reaction mixture.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 2−(”4.41−ビス(ジメチルアミノ)−ベンゾヒ
ドリル]−5−ジメチルアミノ安息香酸(以下LCと略
称する)は、感圧複写紙、感熱記録紙等の記録材料用色
素として広く一般に用いられている3、3−ビス(4−
ジメチルアミノフェニル)−6−シメチルアミノフタリ
ド(以下cvLと略称する)の中間体として極めて重要
な化合物である。本発明は、その改良された製造法に関
するものである。
Detailed Description of the Invention [Industrial Field of Application] 2-("4.41-bis(dimethylamino)-benzohydryl]-5-dimethylaminobenzoic acid (hereinafter abbreviated as LC) is used for pressure-sensitive copying paper. , 3,3-bis(4-
It is an extremely important compound as an intermediate of dimethylaminophenyl)-6-dimethylaminophthalide (hereinafter abbreviated as cvL). The present invention relates to an improved method of manufacturing the same.

〔従来の技術と発明が解決しようとする問題点〕従来か
らLCの合成法としては、コージメチルアミノ安息香酸
(以下DA BAと略称する)とテトラメチル4,41
−ジアミノベンズヒドロール(以下MHと略称する)と
を硫酸水溶液中で反応させる方法(米国特許第5842
105号)、及びDABAの硫酸水溶液中にMHの硫酸
水溶液を滴下する方法(ドイツ公開第215648号)
があるが、いずれの方法も反応中での分解副生成物が多
く、収率及び品質は極めて低い。一般にLCを酸化して
合成されるCvTJの収率と品質は、LCの品質に大き
く左右されることが知られておシ、通常酸化する前KL
Cを単離、精製することがおこなわれる。例えば、芳香
族炭化水素、又は水下混合性アルカンとの混合物を用い
て処理する方法(特開昭53−115740)があるが
、溶剤の回収が煩雑であシ、処理中にI、Oの損失が大
きい等の欠点がある。本発明は、これら欠点を改良し高
品質のLCを高収率で合成する製造法を提供するもので
ある。
[Prior art and problems to be solved by the invention] Conventionally, as a method for synthesizing LC, kodimethylaminobenzoic acid (hereinafter abbreviated as DA BA) and tetramethyl 4,41
- A method of reacting diaminobenzhydrol (hereinafter abbreviated as MH) in an aqueous sulfuric acid solution (US Pat. No. 5842)
105), and a method of dropping a sulfuric acid aqueous solution of MH into a sulfuric acid aqueous solution of DABA (German Publication No. 215648).
However, both methods produce many decomposition by-products during the reaction, and the yield and quality are extremely low. It is known that the yield and quality of CvTJ, which is generally synthesized by oxidizing LC, is greatly affected by the quality of LC.
C is isolated and purified. For example, there is a method of treatment using aromatic hydrocarbons or mixtures with water-miscible alkanes (Japanese Unexamined Patent Publication No. 53-115740), but the recovery of the solvent is complicated and I and O are removed during the treatment. It has drawbacks such as large losses. The present invention aims to improve these drawbacks and provide a manufacturing method for synthesizing high-quality LC in high yield.

〔問題を解決するための手段〕[Means to solve the problem]

本発明者等は、従来の合成法の欠点を改良すべく鋭意研
究した結果、本発明の改良された製造法によシ極めて高
品質のTJCが高収率で得られることを見い出した。す
なわちDAEAを含むPHHI3.5−3.0の鉱酸水
溶液中にMHを加えることを特徴とするLCの製造法で
ある。ここで使用される鉱酸としては、塩酸及び硫酸が
挙げられる。又DABAの平均粒子径としては30ミク
ロン以下がよく、MHの平均粒子径としては50ミクロ
ン以下がよい。反応温度は50−100℃が好ましく、
MHはできるだけゆつくシと加えるのが有利である。又
反応混合物を均一に分散させるため界面活性剤、例えば
ポリオキシエチレンアルキルエーテル等の添加は効果的
である。
As a result of intensive research aimed at improving the drawbacks of conventional synthesis methods, the present inventors have discovered that extremely high quality TJC can be obtained in high yield by the improved production method of the present invention. That is, the method for producing LC is characterized in that MH is added to an aqueous mineral acid solution containing DAEA and having a PHHI of 3.5 to 3.0. Mineral acids used here include hydrochloric acid and sulfuric acid. Further, the average particle diameter of DABA is preferably 30 microns or less, and the average particle diameter of MH is preferably 50 microns or less. The reaction temperature is preferably 50-100°C,
It is advantageous to add MH as slowly as possible. Additionally, it is effective to add a surfactant such as polyoxyethylene alkyl ether to uniformly disperse the reaction mixture.

〔作用と発明の効果〕[Action and effect of invention]

本発明の改良された製造法が従来の欠点をなくし、高品
質のLCを高収率で得る上において極めて優れているこ
とを以下に説明する。すなわち本発明は、鉱酸水溶液、
好ましくは硫酸水溶液のPHHI35−3.0、好まし
くは2.0−3.0において最適反応条件となシ、反応
は非常に促進され分解副生成物も少い。このPH価にお
いて生成するI、Cは余シ溶解せず、DABA及びME
tはよく溶解する。このなめ加えられたMHは、速やか
に溶解しDAEAと反応する。又反応溶液中に懸濁して
いるDAEAは、反応によシ生成したI、Oの析出に伴
って速やかに溶解し反応液のpiはほぼ一定に保たれる
。この結果LCが円滑に生成され高収率で目的物が得ら
れる。又上記PHにおいては、 DABA及びMEt中
の不純物や反応中の分解副生成物がよく溶解するため反
応後析出したLCt−55過、水洗するのみではとんど
完全にこれらを除去することができ高品質のLCがえら
れる。
It will be explained below that the improved manufacturing method of the present invention eliminates the conventional drawbacks and is extremely superior in obtaining high quality LC in high yield. That is, the present invention provides a mineral acid aqueous solution,
The optimum reaction conditions are preferably a PHHI of 35-3.0, preferably 2.0-3.0 of the sulfuric acid aqueous solution, the reaction is very accelerated and there are few decomposition by-products. I and C produced at this pH value do not dissolve, and DABA and ME
t dissolves well. This added MH quickly dissolves and reacts with DAEA. Furthermore, DAEA suspended in the reaction solution is rapidly dissolved as I and O produced by the reaction are precipitated, and the pi of the reaction solution is kept almost constant. As a result, LC is smoothly generated and the target product can be obtained in high yield. Furthermore, at the above pH, impurities in DABA and MEt and decomposition by-products during the reaction dissolve well, so they cannot be completely removed by simply filtering through LCt-55 and washing with water, which precipitate after the reaction. High quality LC can be obtained.

次に実施例を挙げて具体的に説明する0〔実施例〕 実施例 1゜ DABA 177 y (平均粒子径30ミクロン以下
で純粋なりAEA 173gを含む)を4.9%(以下
重量部)硫酸水溶液500g1Ic加え、次いでスコア
ロールナ100(花王アトラス社製)1Fを添加し、攪
拌下IC70℃でMH2B4g(平均粒子径50ミクロ
ン以下で純粋なMH2709を含む)と水500ゴの混
合物を10時間で加えた。反応終了後反応物を濾過し、
濾過残渣を中性まで水洗し乾燥粗生成物391 g(理
論量の92%のLCを含む)を得た。
Next, examples will be specifically explained.0 [Example] Example 1゜DABA 177y (pure with an average particle size of 30 microns or less and containing 173 g of AEA) was added to 4.9% (hereinafter parts by weight) sulfuric acid. Add 500g of an aqueous solution, then add 1F of Scorerolna 100 (manufactured by Kao Atlas Co., Ltd.), and add a mixture of 4g of MH2B (contains pure MH2709 with an average particle size of 50 microns or less) and 500g of water at IC 70°C under stirring for 10 hours. added. After the reaction is completed, the reaction product is filtered,
The filter residue was washed with water to neutrality to obtain 391 g of dry crude product (containing 92% of the theoretical amount of LC).

実施例 2゜ MH284f(平均粒子径50ミクロン以下で純粋なM
H270fを含む)を、Mu31og(平均粒子径10
ミクロン以下で純粋なMH270fを含む)に代える以
外は、実施例1と全く同様の操作をおこない乾燥粗生成
物3s7F(理論量の90%のI、Cを含む)を得た。
Example 2゜MH284f (pure M with an average particle size of 50 microns or less)
H270f), Mu31og (average particle size 10
A dry crude product 3s7F (containing 90% of the theoretical amount of I and C) was obtained by carrying out exactly the same operation as in Example 1, except for replacing with MH270f (containing 90% of the theoretical amount of I and C).

実施例 3゜ のLCを含む)を得た。Example 3゜ (containing LC) was obtained.

実施例 4゜ 実施例1の硫酸水溶液の代シに9.8%硫酸水溶液む)
を得た。
Example 4゜9.8% sulfuric acid aqueous solution was used instead of the sulfuric acid aqueous solution of Example 1)
I got it.

実施例 5゜ 1aaMtの割合で10時間かけて空気を導入した。反
応終了後反応物を濾過し、濾過残渣を中性迄水洗して乾
燥粗生成物4o6p(理論量の94%のCVLを含む)
を得た。このものは極めて高い品質のCVLであった。
Example 5 Air was introduced at a rate of 1 aaMt over 10 hours. After the completion of the reaction, the reaction product was filtered, and the filter residue was washed with water until neutral to give a dry crude product 4o6p (containing 94% of the theoretical amount of CVL).
I got it. This was CVL of extremely high quality.

Claims (4)

【特許請求の範囲】[Claims] (1)m−ジメチルアミノ安息香酸を含むPH価1.5
−3.0の鉱酸水溶液中にテトラメチル−4,4^1−
ジアミノベンズヒドロールを加えることを特徴とする2
−〔4,4^1−ビス(ジメチルアミノ)−ベンゾヒド
リル〕−5−ジメチルアミノ安息香酸の製造法。
(1) PH value 1.5 containing m-dimethylaminobenzoic acid
-Tetramethyl-4,4^1- in mineral acid aqueous solution of -3.0
2 characterized by adding diaminobenzhydrol
- [4,4^1-bis(dimethylamino)-benzohydryl]-5-dimethylaminobenzoic acid production method.
(2)鉱酸として硫酸を用いることを特徴とする特許請
求の範囲第1項に記載の2−〔4,4^1−ビス(ジメ
チルアミノ)−ベンゾヒドリル〕−5−ジメチルアミノ
安息香酸の製造法。
(2) Production of 2-[4,4^1-bis(dimethylamino)-benzohydryl]-5-dimethylaminobenzoic acid according to claim 1, characterized in that sulfuric acid is used as the mineral acid. Law.
(3)m−ジメチルアミノ安息香酸の平均粒子径を30
ミクロン以下とする特許請求の範囲第2項に記載の2−
〔4,4^1−ビス(ジメチルアミノ)−ベンゾヒドリ
ル〕−5−ジメチルアミノ安息香酸の製造法。
(3) The average particle diameter of m-dimethylaminobenzoic acid is 30
2- as set forth in claim 2, which is less than microns;
A method for producing [4,4^1-bis(dimethylamino)-benzohydryl]-5-dimethylaminobenzoic acid.
(4)テトラメチル−4,4^1−ジアミノベンズヒド
ロールの平均粒子径を50ミクロン以下とする特許請求
の範囲第2項又は第3項に記載の2−〔4,4^1−ビ
ス(ジメチルアミノ)ベンゾヒドリル〕−5−ジメチル
アミノ安息香酸の製造法。
(4) 2-[4,4^1-bis according to claim 2 or 3, wherein the average particle diameter of tetramethyl-4,4^1-diaminobenzhydrol is 50 microns or less A method for producing (dimethylamino)benzohydryl]-5-dimethylaminobenzoic acid.
JP61097376A 1986-04-25 1986-04-25 Production of 2-(4,4'-bis(dimethylamino)-benzohydryl)-5-dimethylaminobenz-oic acid Granted JPS62255454A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61097376A JPS62255454A (en) 1986-04-25 1986-04-25 Production of 2-(4,4'-bis(dimethylamino)-benzohydryl)-5-dimethylaminobenz-oic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61097376A JPS62255454A (en) 1986-04-25 1986-04-25 Production of 2-(4,4'-bis(dimethylamino)-benzohydryl)-5-dimethylaminobenz-oic acid

Publications (2)

Publication Number Publication Date
JPS62255454A true JPS62255454A (en) 1987-11-07
JPH0333150B2 JPH0333150B2 (en) 1991-05-16

Family

ID=14190793

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61097376A Granted JPS62255454A (en) 1986-04-25 1986-04-25 Production of 2-(4,4'-bis(dimethylamino)-benzohydryl)-5-dimethylaminobenz-oic acid

Country Status (1)

Country Link
JP (1) JPS62255454A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0373151A2 (en) * 1987-05-18 1990-06-13 Yamada Chemical Co., Ltd. Process for producing 2-(4,4'-bis-(dimethylamino)-benzhydryl)-5-dimethyl-aminobenzoic acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0373151A2 (en) * 1987-05-18 1990-06-13 Yamada Chemical Co., Ltd. Process for producing 2-(4,4'-bis-(dimethylamino)-benzhydryl)-5-dimethyl-aminobenzoic acid

Also Published As

Publication number Publication date
JPH0333150B2 (en) 1991-05-16

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