JP3289338B2 - Norcamphor manufacturing method - Google Patents

Norcamphor manufacturing method

Info

Publication number
JP3289338B2
JP3289338B2 JP28873792A JP28873792A JP3289338B2 JP 3289338 B2 JP3289338 B2 JP 3289338B2 JP 28873792 A JP28873792 A JP 28873792A JP 28873792 A JP28873792 A JP 28873792A JP 3289338 B2 JP3289338 B2 JP 3289338B2
Authority
JP
Japan
Prior art keywords
norcamphor
added
hypochlorite
norbornanol
mixture
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 - Fee Related
Application number
JP28873792A
Other languages
Japanese (ja)
Other versions
JPH06135881A (en
Inventor
勲 栗本
靜一 甲斐
和憲 岩倉
正好 南井
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP28873792A priority Critical patent/JP3289338B2/en
Publication of JPH06135881A publication Critical patent/JPH06135881A/en
Application granted granted Critical
Publication of JP3289338B2 publication Critical patent/JP3289338B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、医薬等の中間体として
有用なノルカンファーの製造法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a process for producing norcamphor useful as an intermediate for pharmaceuticals and the like.

【0002】[0002]

【従来の技術】ノルボルナノールを次亜塩素酸塩により
酸化してノルカンファーを得る方法として、ジクロルメ
タンまたは酢酸エチル中で硫酸水素テトラブチルアンモ
ニウムの存在下、次亜塩素酸ナトリウム水溶液もしくは
次亜塩素酸カリウム水溶液によりノルボルナノールを酸
化する方法(Tetrahedron Lett., 20, 1641(1976) およ
びIsr. J. Chem., 26, 229(1985))が知られている。
2. Description of the Related Art As a method for obtaining norcamphor by oxidizing norbornanol with hypochlorite, an aqueous solution of sodium hypochlorite or potassium hypochlorite in dichloromethane or ethyl acetate in the presence of tetrabutylammonium hydrogen sulfate is used. A method of oxidizing norbornanol with an aqueous solution (Tetrahedron Lett., 20, 1641 (1976) and Isr. J. Chem., 26, 229 (1985)) is known.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
方法では、収率が低く、副反応が起きるために生成物の
ノルカンファーの純度が低いという問題があり、工業的
に必ずしも満足し得るものではなかった。本発明の目的
は、このような問題を解決するノルカンファーの製造法
を提供することにある。
However, in the above-mentioned method, there is a problem that the yield is low and the purity of the norcamphor product is low due to a side reaction, which is not necessarily industrially satisfactory. Did not. An object of the present invention is to provide a method for producing norcamphor which solves such a problem.

【0004】[0004]

【課題を解決するための手段】すなわち、本発明は、ノ
ルボルナノールと次亜塩素酸塩とを炭化水素溶媒中、
水、第4級アンモニウム塩および酸の存在下に反応させ
ることを特徴とするノルカンファーの製造法を提供する
ものである。
That is, the present invention relates to a method for preparing norbornanol and hypochlorite in a hydrocarbon solvent,
It is intended to provide a process for producing norcamphor characterized by reacting in the presence of water, a quaternary ammonium salt and an acid.

【0005】本発明で用いられる原料のノルボルナノー
ルは、exo体あるいはendo体のいずれであっても
よく、それらの混合物であってもよい。また、それらの
光学活性体であってもよい。
[0005] The raw material norbornanol used in the present invention may be either an exo form or an endo form, or a mixture thereof. Moreover, those optically active substances may be used.

【0006】本発明で用いられる次亜塩素酸塩として
は、例えば、次亜塩素酸ナトリウム、次亜塩素酸カリウ
ム、次亜塩素酸カルシウム等があげられるが、これらの
中でも特に次亜塩素酸ナトリウムが好ましい。これらの
次亜塩素酸塩の使用形態としては、固体、水溶液等が例
示されるが、次亜塩素酸ナトリウム、次亜塩素酸カリウ
ムの無水物は不安定であるので、これらを使用する場合
には、水溶液で使用することが好ましい。これらの使用
量は、原料のノルボルナノールに対して1〜10当量、
好ましくは1.1〜3当量の範囲である。
[0006] Examples of the hypochlorite used in the present invention include sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, etc. Among them, sodium hypochlorite is particularly preferable. Is preferred. Examples of the form of use of these hypochlorites include solids, aqueous solutions, and the like.However, anhydrous sodium hypochlorite and potassium hypochlorite are unstable. Is preferably used in an aqueous solution. These are used in an amount of 1 to 10 equivalents to the raw material norbornanol,
Preferably it is in the range of 1.1 to 3 equivalents.

【0007】第4級アンモニウム塩としては、例えば、
臭化テトラブチルアンモニウム、硫酸水素テトラブチル
アンモニウム、塩化トリオクチルメチルアンモニウム、
塩化ベンジルトリメチルアンモニウム、塩化ベンジルト
リエチルアンモニウム、塩化ベンジルトリブチルアンモ
ニウム、塩化N−オクチルピリジニウム、塩化N−ラウ
リルピリジニウム等があげられるが、これらの中でも臭
化テトラブチルアンモニウムが特に好ましい。これらの
第4級アンモニウムの使用量は、原料のノルボルナノー
ルに対して0.01〜2当量、好ましくは0.05〜1
当量の範囲である。これらの第4級アンモニウム塩を用
いない場合には、原料のノルボルナノールの消失に長時
間を必要とし、また、目的とするノルカンファーの収率
も低く、好ましくない。
As the quaternary ammonium salt, for example,
Tetrabutylammonium bromide, tetrabutylammonium hydrogen sulfate, trioctylmethylammonium chloride,
Examples thereof include benzyltrimethylammonium chloride, benzyltriethylammonium chloride, benzyltributylammonium chloride, N-octylpyridinium chloride, and N-laurylpyridinium chloride. Of these, tetrabutylammonium bromide is particularly preferred. These quaternary ammoniums are used in an amount of 0.01 to 2 equivalents, preferably 0.05 to 1 equivalent, based on the raw material norbornanol.
The range of equivalents. When these quaternary ammonium salts are not used, it takes a long time to eliminate norbornanol as a raw material, and the yield of the desired norcamphor is low, which is not preferable.

【0008】本発明で用いられる酸として、具体的に
は、硫酸あるいは塩酸等が例示される。これらの使用量
は、原料のノルボルナノールに対して0.5〜10当
量、好ましくは、1〜5当量の範囲である。
[0008] Specific examples of the acid used in the present invention include sulfuric acid and hydrochloric acid. The amount of these used is in the range of 0.5 to 10 equivalents, preferably 1 to 5 equivalents to norbornanol as a raw material.

【0009】溶媒として使用される炭化水素としては、
例えば、ベンゼン、トルエン、キシレン等の芳香族炭化
水素、ヘキサン、ヘプタン、シクロヘキサン等の脂肪族
炭化水素の単独もしくは混合物が例示され、それらの使
用量は、特に制限されない。
The hydrocarbon used as a solvent includes:
For example, an aromatic hydrocarbon such as benzene, toluene, xylene and the like, and an aliphatic hydrocarbon such as hexane, heptane and cyclohexane, alone or in a mixture, are exemplified, and the use amount thereof is not particularly limited.

【0010】水の使用量は、反応に用いる次亜塩素酸塩
を溶解できる量であれば充分であるが、上限については
特に制限されない。また、次亜塩素酸塩を水溶液として
使用する場合には、さらに追加の水を使用する必要はな
いが、場合によっては、更に水を追加しても差し支えな
い。
[0010] The amount of water used is sufficient as long as it can dissolve the hypochlorite used in the reaction, but the upper limit is not particularly limited. When hypochlorite is used as an aqueous solution, it is not necessary to use additional water, but in some cases, additional water may be added.

【0011】反応温度は、通常、0〜100℃、好まし
くは、0〜50℃の範囲である。反応時間は、次亜塩素
酸塩あるいは第4級アンモニウム塩の種類によって異な
り、特に制限されず、原料のノルボルナノールの消失を
もって反応終了とする。
[0011] The reaction temperature is usually in the range of 0 to 100 ° C, preferably 0 to 50 ° C. The reaction time varies depending on the type of hypochlorite or quaternary ammonium salt, and is not particularly limited. The reaction is terminated when the raw material norbornanol disappears.

【0012】反応終了後、未反応の次亜塩素酸塩をチオ
硫酸ナトリウム等の還元剤で分解した後、通常の後処理
操作、例えば、抽出、分液、濃縮等の操作を行うことに
より、目的のノルカンファーを得ることができる。この
ものは、特に精製操作を行わなくても充分に高い純度を
持っているが、場合によっては、昇華、水蒸気蒸留等の
操作で更に精製することもできる。
After completion of the reaction, unreacted hypochlorite is decomposed with a reducing agent such as sodium thiosulfate, and then subjected to ordinary post-treatment operations, for example, extraction, liquid separation, and concentration. The desired norcamphor can be obtained. This product has a sufficiently high purity without performing any refining operation. However, in some cases, it can be further purified by an operation such as sublimation or steam distillation.

【0013】[0013]

【発明の効果】本発明により、医薬等の中間体として有
用なノルカンファーが、高純度で工業的に有利に製造す
ることができる。この化合物は、例えば、J. Med. Che
m., 31,1847(1988) に記載のトロンボキサンA2 受容体
拮抗剤の中間体として、好適に利用することができる。
Industrial Applicability According to the present invention, norcamphor useful as an intermediate for a drug or the like can be industrially advantageously produced with high purity. This compound is, for example, J. Med. Che
m., 31, 1847 (1988) can be suitably used as an intermediate of the thromboxane A2 receptor antagonist.

【0014】[0014]

【実施例】以下、実施例により本発明をさらに詳細に説
明するが、本発明はこれらにより限定されるものではな
い。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the invention is limited thereto.

【0015】実施例1 撹拌装置、温度計、滴下ロートおよびコンデンサーを装
着した4つ口フラスコに(±)−exo−ノルボルナノ
ール11.2gと臭化テトラブチルアンモニウム3.2
gを仕込み、トルエン300mlを加え、溶解した後、
25%硫酸水120gを加えた。この混合物に20〜2
5℃で12%次亜塩素酸ナトリウム水溶液80.6gを
3時間かけて滴下し、滴下終了後、同温で5時間撹拌し
た。
Example 1 In a four-necked flask equipped with a stirrer, thermometer, dropping funnel and condenser, (±) -exo-norbornanol 11.2 g and tetrabutylammonium bromide 3.2 were added.
g, and after adding and dissolving 300 ml of toluene,
120 g of 25% aqueous sulfuric acid was added. 20 to 2
At 5 ° C., 80.6 g of a 12% aqueous solution of sodium hypochlorite was added dropwise over 3 hours. After completion of the addition, the mixture was stirred at the same temperature for 5 hours.

【0016】反応終了後、反応混合物に次亜塩素酸ナト
リウムの黄色が消失するまでチオ硫酸ナトリウムを加え
た後、分液し、有機層を飽和重曹水、飽和食塩水の順で
洗浄し、さらに濃縮して純度99.2%の(±)−ノル
カンファー10.7gを得た。
After completion of the reaction, sodium thiosulfate was added to the reaction mixture until the yellow color of sodium hypochlorite disappeared, and the mixture was separated. The organic layer was washed with saturated aqueous sodium hydrogen carbonate and saturated brine in that order. It was concentrated to obtain 10.7 g of (±) -norcamphor having a purity of 99.2%.

【0017】このものを昇華精製し、純度100%の
(±)−ノルカンファー8.3gを得た。
This was purified by sublimation to obtain 8.3 g of (±) -norcamphor having a purity of 100%.

【0018】実施例2 撹拌装置、温度計、滴下ロートおよびコンデンサーを装
着した4つ口フラスコに(±)−exo−ノルボルナノ
ール11.2gと臭化テトラブチルアンモニウム3.2
gを仕込み、ヘキサン300mlを加え、溶解した後、
35%塩酸水100gを加えた。この混合物に20〜2
5℃で12%次亜塩素酸ナトリウム水溶液80.6gを
3時間かけて滴下し、滴下終了後、同温で3時間撹拌し
た。
Example 2 In a four-necked flask equipped with a stirrer, thermometer, dropping funnel and condenser, (±) -exo-norbornanol 11.2 g and tetrabutylammonium bromide 3.2 were added.
g, 300 ml of hexane was added and dissolved,
100 g of 35% hydrochloric acid was added. 20 to 2
At 5 ° C., 80.6 g of a 12% aqueous solution of sodium hypochlorite was added dropwise over 3 hours. After completion of the addition, the mixture was stirred at the same temperature for 3 hours.

【0019】反応終了後、反応混合物に次亜塩素酸ナト
リウムの黄色が消失するまでチオ硫酸ナトリウムを加え
た後、分液した。水層をトルエン100mlで抽出、分
液し、得られたトルエン層を先の有機層と合わせ、これ
を飽和重曹水、飽和食塩水の順で洗浄し、さらに濃縮し
て純度98.9%の(±)−ノルカンファー10.2g
を得た。
After completion of the reaction, sodium thiosulfate was added to the reaction mixture until the yellow color of sodium hypochlorite disappeared, and the mixture was separated. The aqueous layer was extracted with 100 ml of toluene and separated, and the obtained toluene layer was combined with the organic layer, washed with a saturated aqueous solution of sodium bicarbonate and a saturated saline solution in that order, and further concentrated to a purity of 98.9%. (±) -Norcamphor 10.2g
I got

【0020】実施例3 撹拌装置、温度計、滴下ロートおよびコンデンサーを装
着した4つ口フラスコに(1S,2S,4R)−ノルボ
ルナノール11.2g(光学純度98%ee)と臭化テ
トラブチルアンモニウム3.2gを仕込み、トルエン3
00mlを加え、溶解した後、25%硫酸水120gを
加えた。この混合物に20〜25℃で12%次亜塩素酸
ナトリウム水溶液80.6gを3時間かけて滴下し、滴
下終了後、同温で5時間撹拌した。
Example 3 In a four-necked flask equipped with a stirrer, a thermometer, a dropping funnel and a condenser, 11.2 g of (1S, 2S, 4R) -norbornanol (98% ee in optical purity) and tetrabutylammonium bromide 3 were added. .2 g and toluene 3
After adding and dissolving 00 ml, 120 g of 25% sulfuric acid aqueous solution was added. To this mixture, 80.6 g of a 12% aqueous sodium hypochlorite solution was added dropwise at 20 to 25 ° C. over 3 hours, and after completion of the addition, the mixture was stirred at the same temperature for 5 hours.

【0021】反応終了後、反応混合物に次亜塩素酸ナト
リウムの黄色が消失するまでチオ硫酸ナトリウムを加え
た後、分液し、有機層を飽和重曹水、飽和食塩水の順で
洗浄し、さらに濃縮して純度99.3%の(1S,4
R)−ノルカンファー10.8g(光学純度98%)を
得た。
After completion of the reaction, sodium thiosulfate was added to the reaction mixture until the yellow color of sodium hypochlorite disappeared, and the mixture was separated. The organic layer was washed with saturated aqueous sodium hydrogen carbonate and saturated brine in that order. Concentrate to 99.3% purity (1S, 4
10.8 g of R) -norcamphor (98% optical purity) was obtained.

【0022】実施例4 実施例3で原料として用いた(1S,2S,4R)−ノ
ルボルナノールに代えて、(±)−endo−ノルボル
ナノールを用いる以外は、実施例3と同様にして、反応
および後処理を行い、純度99.1%の(±)−ノルカ
ンファー10.7gを得た。
Example 4 The reaction and reaction were carried out in the same manner as in Example 3 except that (±) -endo-norbornanol was used in place of (1S, 2S, 4R) -norbornanol used as a raw material in Example 3. After the treatment, 10.7 g of (±) -norcamphor having a purity of 99.1% was obtained.

【0023】実施例5〜8 実施例3で原料として用いた(1S,2S,4R)−ノ
ルボルナノールに代えて、(±)−exo−ノルボルナ
ノールを用い、第4級アンモニウム塩として用いた臭化
テトラブチルアンモニウムに代えて、表1に記載の各種
の第4級アンモニウム塩を用いる以外は、実施例3と同
様にして、反応および後処理を行い、(±)−ノルカン
ファーを得た。結果を表1に示す。
Examples 5 to 8 Instead of (1S, 2S, 4R) -norbornanol used as a raw material in Example 3, (±) -exo-norbornanol was used and tetrabromide used as a quaternary ammonium salt was used. The reaction and post-treatment were carried out in the same manner as in Example 3 except that various quaternary ammonium salts shown in Table 1 were used instead of butylammonium to obtain (±) -norcamphor. Table 1 shows the results.

【0024】[0024]

【表1】 [Table 1]

【0025】比較例1 撹拌装置、温度計、滴下ロートおよびコンデンサーを装
着した4つ口フラスコに(±)−exo−ノルボルナノ
ール11.2gを仕込み、トルエン300mlを加え、
溶解した後、25%硫酸水120gを加えた。この混合
物に20〜25℃で12%次亜塩素酸ナトリウム水溶液
80.6gを3時間かけて滴下し、滴下終了後、同温で
35時間撹拌した。反応終了後、反応混合物に次亜塩素
酸ナトリウムの黄色が消失するまでチオ硫酸ナトリウム
を加えた後、分液し、有機層を飽和重曹水、飽和食塩水
の順で洗浄し、さらに濃縮して純度47.3%の(±)
−ノルカンファー10.1gを得た。
Comparative Example 1 In a four-necked flask equipped with a stirrer, a thermometer, a dropping funnel and a condenser, 11.2 g of (±) -exo-norbornanol was charged, and 300 ml of toluene was added.
After dissolution, 120 g of 25% aqueous sulfuric acid was added. To this mixture, 80.6 g of a 12% aqueous solution of sodium hypochlorite was added dropwise at 20 to 25 ° C over 3 hours, and after the addition was completed, the mixture was stirred at the same temperature for 35 hours. After completion of the reaction, sodium thiosulfate was added to the reaction mixture until the yellow color of sodium hypochlorite disappeared, and the mixture was separated. The organic layer was washed with saturated aqueous sodium hydrogen carbonate and saturated brine in this order, and further concentrated. 47.3% purity (±)
-10.1 g of norcamphor was obtained.

【0026】比較例2 撹拌装置、温度計、滴下ロートおよびコンデンサーを装
着した4つ口フラスコに(±)−exo−ノルボルナノ
ール11.2gと臭化テトラブチルアンモニウム3.2
gを仕込み、酢酸エチル300mlを加え、溶解した
後、25%硫酸水120gを加えた。この混合物に20
〜25℃で12%次亜塩素酸ナトリウム水溶液80.6
gを3時間かけて滴下し、滴下終了後、同温で7時間撹
拌した。反応終了後、反応混合物に次亜塩素酸ナトリウ
ムの黄色が消失するまでチオ硫酸ナトリウムを加えた
後、分液し、有機層を飽和重曹水、飽和食塩水の順で洗
浄し、さらに濃縮して純度78.7%の(±)−ノルカ
ンファー10.0gを得た。
Comparative Example 2 In a four-necked flask equipped with a stirrer, thermometer, dropping funnel and condenser, (±) -exo-norbornanol 11.2 g and tetrabutylammonium bromide 3.2 were added.
g, 300 ml of ethyl acetate was added and dissolved, and 120 g of 25% aqueous sulfuric acid was added. 20 to this mixture
80.6% aqueous solution of sodium hypochlorite at ~ 25 ° C
g was added dropwise over 3 hours, and after completion of the addition, the mixture was stirred at the same temperature for 7 hours. After completion of the reaction, sodium thiosulfate was added to the reaction mixture until the yellow color of sodium hypochlorite disappeared, and the mixture was separated. The organic layer was washed with saturated aqueous sodium hydrogen carbonate and saturated brine in this order, and further concentrated. 10.0 g of (±) -norcamphor having a purity of 78.7% was obtained.

【0027】比較例3 撹拌装置、温度計、滴下ロートおよびコンデンサーを装
着した4つ口フラスコに(±)−exo−ノルボルナノ
ール11.2gと臭化テトラブチルアンモニウム3.2
gを仕込み、ジクロルメタン300mlを加え、溶解し
た後、25%硫酸水120gを加えた。この混合物に2
0〜25℃で12%次亜塩素酸ナトリウム水溶液80.
6gを3時間かけて滴下し、滴下終了後、同温で5時間
撹拌した。反応終了後、反応混合物に次亜塩素酸ナトリ
ウムの黄色が消失するまでチオ硫酸ナトリウムを加えた
後、分液し、有機層を飽和重曹水、飽和食塩水の順で洗
浄し、さらに濃縮して純度83.6%の(±)−ノルカ
ンファー9.9gを得た。
Comparative Example 3 In a four-necked flask equipped with a stirrer, a thermometer, a dropping funnel and a condenser, 11.2 g of (±) -exo-norbornanol and 3.2 g of tetrabutylammonium bromide were added.
g, 300 ml of dichloromethane was added and dissolved, and then 120 g of 25% aqueous sulfuric acid was added. 2 in this mixture
80. 12% aqueous sodium hypochlorite solution at 0-25 ° C
6 g was added dropwise over 3 hours, and after completion of the addition, the mixture was stirred at the same temperature for 5 hours. After completion of the reaction, sodium thiosulfate was added to the reaction mixture until the yellow color of sodium hypochlorite disappeared, and the mixture was separated. The organic layer was washed with saturated aqueous sodium hydrogen carbonate and saturated brine in this order, and further concentrated. 9.9 g of (±) -norcamphor having a purity of 83.6% was obtained.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 南井 正好 大阪府高槻市塚原2丁目10番1号 住友 化学工業株式会社内 (56)参考文献 特開 昭61−225148(JP,A) 特開 昭62−228037(JP,A) (58)調査した分野(Int.Cl.7,DB名) C07C 45/30 C07C 49/433 C07C 49/437 B01J 31/02 102 C07B 61/00 300 ──────────────────────────────────────────────────続 き Continuation of front page (72) Inventor Masayoshi Minami 2-10-1, Tsukahara, Takatsuki-shi, Osaka Sumitomo Chemical Co., Ltd. (56) References JP-A-61-225148 (JP, A) JP-A Sho 62-228037 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C07C 45/30 C07C 49/433 C07C 49/437 B01J 31/02 102 C07B 61/00 300

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ノルボルナノールと次亜塩素酸塩とを炭化
水素溶媒中、水、第4級アンモニウム塩および酸の存在
下に反応させることを特徴とするノルカンファーの製造
法。
1. A process for producing norcamphor, comprising reacting norbornanol and hypochlorite in a hydrocarbon solvent in the presence of water, a quaternary ammonium salt and an acid.
【請求項2】次亜塩素酸塩が次亜塩素酸ナトリウムであ
る請求項1に記載の製造法。
2. The method according to claim 1, wherein the hypochlorite is sodium hypochlorite.
【請求項3】第4級アンモニウム塩が臭化テトラブチル
アンモニウムである請求項1または2に記載の製造法。
3. The method according to claim 1, wherein the quaternary ammonium salt is tetrabutylammonium bromide.
【請求項4】酸が硫酸または塩酸である請求項1、2ま
たは3に記載の製造法。
4. The method according to claim 1, wherein the acid is sulfuric acid or hydrochloric acid.
JP28873792A 1992-10-27 1992-10-27 Norcamphor manufacturing method Expired - Fee Related JP3289338B2 (en)

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JP3289338B2 true JP3289338B2 (en) 2002-06-04

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EP0924180A4 (en) * 1996-07-02 2005-04-20 Toray Finechemicals Co Ltd Processes for the preparation of optically active ketones
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