JPS588373B2 - Production method of quinizarin (1,4-dihydroxyanthraquinone) - Google Patents
Production method of quinizarin (1,4-dihydroxyanthraquinone)Info
- Publication number
- JPS588373B2 JPS588373B2 JP14080777A JP14080777A JPS588373B2 JP S588373 B2 JPS588373 B2 JP S588373B2 JP 14080777 A JP14080777 A JP 14080777A JP 14080777 A JP14080777 A JP 14080777A JP S588373 B2 JPS588373 B2 JP S588373B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- quinizarin
- phthalic anhydride
- chlorophenol
- sulfuric acid
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C46/00—Preparation of quinones
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
染料製造の重要な中間体であるキニザリンは工業的には
Ullmanns Encyklop.Ndie
dertechnischen Chem ie ,
3版(1953)第3巻、第669〜670頁に記載の
方法に従い硫酸中で硼酸の存在下で、あるいはドイツ特
許公開第2014566号明細書に従い硼酸と3ハロゲ
ン化硼素および(または)3ハロゲン化硼素の錯化合物
の存在下で、温度170〜210℃における無水フタル
酸とp−クロロフェノールとの反応により製造する。DETAILED DESCRIPTION OF THE INVENTION Quinizarin, an important intermediate in dye production, is commercially available from Ullmanns Encyclop. Ndie
Dertechnischen Chemie,
in the presence of boric acid in sulfuric acid according to the method described in 3rd edition (1953), volume 3, pages 669-670, or with boron trihalide and/or trihalogen according to DE 2014566 A1. It is produced by the reaction of phthalic anhydride and p-chlorophenol at a temperature of 170 to 210°C in the presence of a boron complex.
そのキニザリンは溶融物の水による稀釈ならびに沈澱す
る反応生成物の分離により、場合によってはアルカリ性
剤での処理と酸化剤の存在下で単離する。The quinizarin is isolated by dilution of the melt with water and separation of the precipitated reaction product, optionally after treatment with an alkaline agent and in the presence of an oxidizing agent.
この技術と方法とにより得られる1・4−ジヒドロキシ
アントラキノンは生成温度が低けれハ低いだけ、そして
硫酸濃度が高げれば高いだけより純粋である。The 1,4-dihydroxyanthraquinone obtained by this technique and method is purer at lower production temperatures and purer at higher sulfuric acid concentrations.
しかしこの反応は、180℃で行なうと非常に遅いので
経済的に問題があり、また妥当な反応速度である200
℃では生成物の純度に不満足な点が残る。However, this reaction is very slow when carried out at 180°C, which poses an economic problem;
℃, the purity of the product remains unsatisfactory.
より高い濃度の硫酸で反応を行うと反応生成物の純度は
上昇はするが収率が低下する。Performing the reaction with a higher concentration of sulfuric acid increases the purity of the reaction product but reduces the yield.
硫酸濃度が低下すればする程使用する酸の量は多くなる
。The lower the sulfuric acid concentration, the greater the amount of acid used.
いずれの場合も多量の廃硫酸が生じ、その中和による処
理とその際生成する多量の塩の除去とは生態学的にも経
済上でも重大なこととなる。In either case, a large amount of waste sulfuric acid is generated, and its treatment by neutralization and the removal of the large amount of salts produced during this process are ecologically and economically important.
驚くべきことに、より高い反応温度でより高濃度の硫酸
を本質的により少量適用すると廃硫酸は少くとも50%
減少し、1・4−ジヒドロキシーアントラキノンは少く
とも公知の方法と同様のよい収率ならびに純度で得られ
ることが見出された。Surprisingly, applying essentially smaller amounts of highly concentrated sulfuric acid at higher reaction temperatures reduces waste sulfuric acid by at least 50%.
It has been found that 1,4-dihydroxy-anthraquinone can be obtained in good yields and purity at least as good as the known method.
その新規の方法はp−クロロフェノールと無水フタル酸
との反応を少くとも25%の発煙硫酸中で3酸化硼素の
存在下に温度180〜220℃有利には200〜210
℃で加圧せず、連続的にまたは不連続的に行なうことか
らなる。The new process involves the reaction of p-chlorophenol with phthalic anhydride in at least 25% oleum in the presence of boron trioxide at a temperature of 180-220°C, preferably 200-210°C.
It consists of carrying out continuously or discontinuously at ℃ without applying pressure.
得られた反応生成物は所望の場合は公知の方法でアルカ
リ性剤を用い、場合によっては酸化剤の存在下で後処理
することができる。The reaction product obtained can, if desired, be worked up in known manner using alkaline agents and optionally in the presence of oxidizing agents.
両方の出発物質は化学量論量で反応させてもよい。Both starting materials may be reacted in stoichiometric amounts.
しかし安価な無水フタル酸を化学量論量より1.5倍ま
で特には1.3倍まで過剰に適用するのが有利である。However, it is advantageous to apply the inexpensive phthalic anhydride in an excess of up to 1.5 times, especially up to 1.3 times, the stoichiometric amount.
通常その反応は35%発煙硫酸として発煙硫酸対ソタル
酸重量比1:1〜4:1有利には1.1〜1.5:1,
そして3酸化硼素対無水フタル酸比1:2〜1:4で行
なう。Usually the reaction is carried out using 35% oleum in a weight ratio of fuming sulfuric acid to sotalic acid of 1:1 to 4:1, preferably 1.1 to 1.5:1.
The ratio of boron trioxide to phthalic anhydride is 1:2 to 1:4.
使用する発煙硫酸の濃度は臨界的なものではなく約70
%にすることもできる。The concentration of fuming sulfuric acid used is not critical and is about 70
It can also be expressed as a percentage.
前記の新規の方法は例えば少くとも25%発煙硫酸中で
かきまぜながら100〜150℃有利には120〜13
0℃で3酸化硼素を加えて行なう。The new process is carried out for example at 100 DEG -150 DEG C., preferably at 120 DEG-13 DEG C., while stirring in at least 25% oleum.
Boron trioxide is added at 0°C.
ついで130〜150℃で無水フタル酸を、それからp
−クロロフェノールを加え、そこでその反応混合物をよ
く混合しながら180〜220℃有利には200〜21
0℃に加熱し、6〜15時間この反応温度に保つ。Then phthalic anhydride at 130-150°C, then p
- add the chlorophenol and then heat the reaction mixture to 180-220° C., advantageously 200-210° C., with good mixing;
Heat to 0°C and keep at this reaction temperature for 6-15 hours.
反応終了後160〜170℃に冷却し、この熱い反応混
合物を全体に対し4〜5倍量の水中にあけ、2〜5時間
かきまぜながら還流冷却の下に温度100℃までで処理
する。After the reaction is completed, the mixture is cooled to 160-170°C, and the hot reaction mixture is poured into 4-5 times the amount of water, and treated under reflux cooling for 2-5 hours at a temperature of up to 100°C.
その後生成物を熱時ろ過し、場合によっては弱アルカリ
性薬剤を適用して中性になるまで洗浄し、乾燥する。The product is then filtered hot, optionally washed until neutral with the application of a weakly alkaline agent, and dried.
製造される粗キニザリン1k9当りの廃硫酸の量は従来
技術( Ullmanns Encyklop!di
e dert.echnischen Chemi
e, 4版第7巻604頁1973年参照)の水準に
従えば5. 3 kgであるのに対し、本発明の新規方
法によれば僅に1. 7 kgが生ずるにすぎない。The amount of waste sulfuric acid per 1k9 of crude quinizarin produced is determined by the conventional technology (Ullmanns Encyklop! di
e dert. echnischen Chemi
e, 4th edition, Vol. 7, p. 604, 1973). 3 kg, compared to only 1.3 kg according to the new method of the present invention. Only 7 kg is produced.
例
500mlのスルホン化フラスコ中に硫酸1水和物1
2 4.5 9−6 8mlを入れ、62%発煙硫酸1
44L?=72mlを加えると、温度が45〜50゜C
まで上昇する。Example 1 sulfuric acid monohydrate in a 500 ml sulfonation flask
2 4.5 9-6 Add 8ml of 62% oleum 1
44L? = When 72ml is added, the temperature becomes 45-50°C.
rises to.
そこで3酸化硼素50gをかきませながら入れると温度
120〜125℃まで上昇する。Then, when 50 g of boron trioxide is added while stirring, the temperature rises to 120-125°C.
それには約20分間必要である。乳状の溶液が生成する
。This requires approximately 20 minutes. A milky solution forms.
フラスコ内容物を150℃に加熱し、それから130〜
150℃で始めに無水フタル酸160gついでp−クロ
ロフェノール104gを入れる。The flask contents were heated to 150°C, then 130~
At 150 DEG C., 160 g of phthalic anhydride and then 104 g of p-chlorophenol were added.
そこで反応混合物を205±2℃に加熱し、14時間こ
の温度に保つ。The reaction mixture is then heated to 205±2° C. and kept at this temperature for 14 hours.
反応終了後160〜170℃に冷却し、反応物を水20
00ml中に入れ、それから4時間かきまぜながら還流
して煮沸する。After the reaction was completed, the reaction product was cooled to 160-170°C and diluted with 20% water.
00ml and then boiled under reflux with stirring for 4 hours.
その後熱時吸引涙過し、温水で中性になるまで洗浄し、
真空中60〜70℃で乾燥する。After that, when hot, suction the tears, wash with warm water until neutral,
Dry in vacuo at 60-70°C.
『粗キニザリン』(約90%)170〜175gを得る
。170-175 g of "crude quinizarin" (approximately 90%) is obtained.
『粗キニザリン』収率は理論値の90%(p−クロロフ
ェノールで計算して)である。The "crude quinizarin" yield is 90% of theory (calculated with p-chlorophenol).
『粗キニザリン』を公知の精製操作すなわち昇華、再結
晶あるいはアルカリ性剤、例えば希水酸化ナトリウム溶
液または重炭酸ナトリウム水溶液による処理あるいは炭
酸ナトリウムまたはアンモニア(その際、酸化剤例えば
次亜塩素酸ナトリウムまたは塩素酸ナトリウムを加える
こともできる)による処理にかげる。The "crude quinizarin" can be purified by known purification operations such as sublimation, recrystallization or treatment with alkaline agents such as dilute sodium hydroxide solution or aqueous sodium bicarbonate solution or with sodium carbonate or ammonia (in which case oxidizing agents such as sodium hypochlorite or chlorine). (sodium acid may be added).
こうして理論値(p−クロロフェノールで計算して)の
80%またはそれ以上の『純キニザリン』収率を得る。A yield of "pure quinizarin" of 80% or more of the theoretical value (calculated with p-chlorophenol) is thus obtained.
Claims (1)
くとも25%の発煙硫酸中で3酸化硼素の存在下で温度
180〜220℃で行なうことを特徴とする無水フタル
酸とp−クロロフェノールとの反応によるキニザリンの
製法。 2 反応を200〜210℃で行なう前項1に記載の方
法。 3p−クロロフェノールと無水フタル酸とを化学量論比
1:1〜]:1.5で使う前項1または2に記載の方法
。 4 発煙硫酸と無水フタル酸とを重量比1:1〜4:1
で使う前項1〜3のいずれかに記載の方法。 5 3酸化硼素と無水フタル酸とを重量比1:2〜1:
4で使う前項1〜4のいずれかに記載の方法。[Claims] 1. Phthalic anhydride, characterized in that the reaction between phthalic anhydride and p-chlorophenol is carried out in at least 25% oleum in the presence of boron trioxide at a temperature of 180 to 220°C. A method for producing quinizarin by the reaction of and p-chlorophenol. 2. The method according to item 1, wherein the reaction is carried out at 200 to 210°C. 3. The method according to item 1 or 2 above, wherein 3p-chlorophenol and phthalic anhydride are used in a stoichiometric ratio of 1:1 to ]:1.5. 4 The weight ratio of oleum and phthalic anhydride is 1:1 to 4:1.
The method described in any one of the preceding sections 1 to 3 used in . 5 Boron trioxide and phthalic anhydride in a weight ratio of 1:2 to 1:
4. The method described in any one of 1 to 4 above.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH000016471/76 | 1976-12-30 | ||
CH1647176 | 1976-12-30 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5384956A JPS5384956A (en) | 1978-07-26 |
JPS588373B2 true JPS588373B2 (en) | 1983-02-15 |
Family
ID=4417674
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14080777A Expired JPS588373B2 (en) | 1976-12-30 | 1977-11-25 | Production method of quinizarin (1,4-dihydroxyanthraquinone) |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS588373B2 (en) |
DE (1) | DE2758397C2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0226388Y2 (en) * | 1986-01-09 | 1990-07-18 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2830554A1 (en) * | 1978-07-12 | 1980-01-24 | Bayer Ag | METHOD FOR PRODUCING CHINIZARINE |
EP0038777B1 (en) * | 1980-04-22 | 1983-10-05 | Ciba-Geigy Ag | Process for the preparation of oh or chloro derivatives of quinizarine bisubstituted in position 5 and 8 |
CN111763142B (en) * | 2020-07-03 | 2023-03-24 | 浙江亿得新材料股份有限公司 | Synthesis of orange intermediate |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE568311C (en) * | 1929-06-04 | 1933-01-17 | Ici Ltd | Process for the preparation of oxyanthraquinone derivatives |
US2445538A (en) * | 1946-04-13 | 1948-07-20 | Allied Chem & Dye Corp | Manufacture of quinizarine |
-
1977
- 1977-11-25 JP JP14080777A patent/JPS588373B2/en not_active Expired
- 1977-12-28 DE DE19772758397 patent/DE2758397C2/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0226388Y2 (en) * | 1986-01-09 | 1990-07-18 |
Also Published As
Publication number | Publication date |
---|---|
DE2758397A1 (en) | 1978-07-13 |
DE2758397C2 (en) | 1983-08-04 |
JPS5384956A (en) | 1978-07-26 |
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