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JPH0369903B2 - - Google Patents
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JPH0369903B2 - - Google Patents

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Publication number
JPH0369903B2
JPH0369903B2 JP57023091A JP2309182A JPH0369903B2 JP H0369903 B2 JPH0369903 B2 JP H0369903B2 JP 57023091 A JP57023091 A JP 57023091A JP 2309182 A JP2309182 A JP 2309182A JP H0369903 B2 JPH0369903 B2 JP H0369903B2
Authority
JP
Japan
Prior art keywords
sulfuric acid
sulfate
amount
crystals
solvent
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 - Lifetime
Application number
JP57023091A
Other languages
Japanese (ja)
Other versions
JPS58140081A (en
Inventor
Yukio Suzuki
Haruki Morino
Juji Funaki
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 JP57023091A priority Critical patent/JPS58140081A/en
Publication of JPS58140081A publication Critical patent/JPS58140081A/en
Publication of JPH0369903B2 publication Critical patent/JPH0369903B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、式() で示されるトリアゾリルスチリルケトン誘導体、
すなわち1−(2,4−ジクロロフエニル)−4,
4−ジメチル−2−(1,2,4−トリアゾール
−1−イル)−1−ペンテン−3−オンの幾何異
性体の混合物からの幾何異性体の分離方法に関す
る。 式()で示されるトリアゾリルスチリルケト
ン誘導体は、それ自身殺菌剤として有利である
(特開昭53−130661号公報)が、それを還元する
ことにより得られる式() で示されるトリアゾリルスチリルカルビノール誘
導体、すなわち1−(2,4−ジクロロフエニル)
−2−(1,2,4−トリアゾール−1−イル)−
4,4−ジメチル−1−ペンテン−3−オール
は、殺菌剤、除草剤、植物生長調節剤として有用
であり、特にそのE体はそのZ体よりも効力が優
れていることが知られている(特開昭54−41875
号、55−124771号、56−25105号公報)。 ところで式()のトリアゾリルスチリルケト
ン誘導体(以下、特にことわらない限り、式
()のトリアゾリルスチリルケトン誘導体のE
体、Z体およびE、Z混合物をそれぞれE体、Z
体およびE/Z体と称する)を得る方法として、
たとえば下記のような方法がある。 (1) E/Z体またはZ体を光によつてE体に異性
化する(特開昭55−147265号公報)。 (2) E/Z体をクロマトグラフイーによつて分離
する(特開昭55−147265号公報)。 (3) E/Z体からZ体のみを結晶として析出さ
せ、母液部からE体に富む混合物を得る。必要
によりZ体はE/Z体に異性化する(特開昭56
−140978号公報等)。 しかしながら、前記(1)の方法は光反応装置など
の特殊な装置が必要となる。(2)の方法は工業的な
方法として困難な点が多い。(3)の方法は母液から
E体を回収することになり、E体の含有率を余り
高くできないし、また原料E/Z体中の不純物を
除できない等の欠点がある。 本発明者らは、これらの欠点を克服するために
鋭意研究を行ない、E/Z体からE体の硫酸塩の
みを選択的に晶出させうることを見出し、さらに
これを分離取得した後、分解することにより高純
度のE体が得られることを見出し、さらに種々の
検討を加え、本発明に到達した。 すなわち、本発明は、式()で示されるトリ
アゾリルスチリルケトン誘導体のE/Z体を、溶
媒中において硫酸と反応させ、該誘導体のE体の
硫酸塩として析出させ、分離取得した後、該硫酸
塩を分離してE体を得ることを特徴とするトリア
ゾリルスチリルケトン誘導体の幾何異性体の分離
方法である。 本発明方法において用いる硫酸の濃度が稀薄す
ぎると硫酸塩の析出量が減少したり、場合によつ
ては全く析出しなくなることから、硫酸の濃度は
通常40%以上、好ましくは50〜98%、より好まし
くは90〜98%である。 また、硫酸の使用量は、純分換算でE/Z体の
E体含有量に対して通常0.5〜3倍モルの範囲で
あるが、硫酸量、殊に高濃度の硫酸量が多過ぎる
とZ体の硫酸塩の析出も随伴し易くなることか
ら、より好ましくは0.95〜1.2倍モルの範囲であ
る。 本発明方法において用いられる溶媒としては、
不活性溶媒であれば特に限定されるものではない
が、好ましいものとして非プロトン性有機溶媒が
あげられ、たとえばベンゼン、トルエン、キシレ
ン等の芳香族炭化水素、塩化メチレン、クロロホ
ルム、四塩化炭素、ジクロロエタン、トリクレ
ン、パークレン、モノクロロベンゼン、ジクロロ
ベンゼン等のハロゲン化炭化水素、酢酸エチル、
ギ酸エチル等のエステル系溶媒、ジエチルエーテ
ル、テトラヒドロフラン等のエーテル系溶媒、ヘ
キサン、ヘプタン、オクタン、石油エーテル、リ
グロイン、シクロヘキサン、メチルシクロヘキサ
ン等の脂肪族または脂環族炭化水素、アセトン、
メチルエチルケトン、メチルイソブチルケトン、
シクロヘキサノン等のケトン系溶媒、アセトニト
リル、プロピオニトリル等のニトリル系溶媒ある
いはこれらの混合溶媒などが例示される。ことに
芳香族炭化水素およびハロゲン化炭化水素が好適
に用いられる。溶媒の使用量はその種類、晶析温
度によつて変わりうるので一概には決められない
が、通常は原料のE/Z体に対し、0.5重量倍か
ら20重量倍の範囲である。 本発明方法において、E体の硫酸塩の析出は、
通常自然に開始されるので、その種晶の接種は必
須ではないが、より確実を期するために接種して
もよい。この種晶は硫酸と原料E/Z体の混合後
でもよいし、混合前のE/Z体溶液に加えてもよ
い。 反応温度または晶析温度は溶媒の沸点以下であ
つて、かつ異性化等の副反応を伴なわない温度で
実施されるが、好ましくは0℃〜80℃で行なわれ
る。 反応溶液からE体の硫酸塩を分離するには、た
とえば過、遠心分離、デカンテーシヨンなど通
常の方法を用いることにより行なわれる。 上記のようにして得られたE体の硫酸塩からE
体を回収するには、通常、水と混和せず、かつE
体を溶かす溶媒、たとえばトルエン、クロロベン
ゼン、酢酸エチル、エーテル、四塩化炭素等の存
在下、大過剰の水と該硫酸塩とを混合することに
よつて硫酸塩が分解され、油層から高純度のE体
が回収される。このとき、水層中に炭酸ナトリウ
ム、重炭酸ナトリウム、水酸化ナトリウム、アン
モニアなどの塩基を硫酸に対し過剰に存在させて
もよい。また、水以外にも過剰量の含水のメタノ
ール、酢酸等のプロトン性溶媒あるいはアミン等
の塩基でも該硫酸塩を分解することができる。 なお、本発明方法によつてE体硫酸塩を除去し
たあとの母液中には、Z体が多く含まるが、水洗
等によつて硫酸を除いたのち、これはたとえば特
開昭56−140978号公報等に示されている方法によ
り、E/Z体に異性化させたのち、再び本発明方
法に用いることができるし、または該母液に過剰
モルの硫酸、より好ましくはさらにZ体硫酸塩の
種晶を加えることにより、Z体の硫酸塩を析出さ
せることもできる。 以下、具体的な例をもつて本発明を説明するが
当然ながら、本発明はこれらの例に限られるもの
ではない。なお、E/Z体はE体とZ体の比率を
表わす。 参考例 1 E体1gをトルエン10gに溶解し、20℃に保温
し、撹拌下に濃硫酸0.165c.c.を添加した。2時間
撹拌したのち過した。少量のトルエンで結晶を
洗浄したのち、結晶を真空乾燥した。 結晶収量 1.27g 融 点 205.5〜207℃ 元素分析量 C(%) H(%) N(%) 42.8 4.1 9.8 元素分析量 S(%) Cl(%) 7.5 16.9 参考例 2 Z体1gをトルエン10gに溶解し、20℃に保温
撹拌下に濃硫酸0.083c.c.を滴下した。そののち12
℃に冷却し、6時間後に結晶を取し、少量のト
ルエンで洗浄したのち、真空乾燥した。 結晶収量 0.62g 融 点 117.5〜118℃ 元素分析量 C(%) H(%) N(%) 43.0 4.2 9.9 元素分析量 S(%) Cl(%) 7.4 17.1 実施例 1 E/Z体(純度96.8%、E/Z43.0/57.0)8.11
gをトルエン80gに溶解し、20℃で濃硫酸1.22g
を滴下した。4.5時間、20℃に保温撹拌後取し、
ヘキサン10c.c.で結晶を洗つたのち結晶を真空乾燥
した。 結晶収量 4.23g 融 点 197〜205℃ 次にこの結晶1gに10%重炭酸ナトリウム水溶
液4c.c.、トルエン20c.c.および水20c.c.を加え、室温
(20〜5℃)で、結晶が消失するまで撹拌したの
ち水層を分離し、油層を2回水洗後濃縮した。得
られた結晶は0.76g(原料のE/Z体に対し通算
で40%)、E/Zは96.0/4.0であつた。 実施例 2〜6 実施例1で用いたE/Z体を同量用いて、溶
媒、温度、時間をかえた以外は実施例1と同様に
してE体の分離を行なつた。
The present invention is based on the formula () A triazolyl styryl ketone derivative represented by
That is, 1-(2,4-dichlorophenyl)-4,
The present invention relates to a method for separating geometric isomers of 4-dimethyl-2-(1,2,4-triazol-1-yl)-1-penten-3-one from a mixture of geometric isomers. The triazolyl styryl ketone derivative represented by the formula () is itself advantageous as a bactericide (Japanese Unexamined Patent Publication No. 130661/1983), but the triazolyl styryl ketone derivative represented by the formula () obtained by reducing it is A triazolylstyryl carbinol derivative represented by, i.e. 1-(2,4-dichlorophenyl)
-2-(1,2,4-triazol-1-yl)-
4,4-Dimethyl-1-penten-3-ol is useful as a fungicide, herbicide, and plant growth regulator, and it is known that its E form is particularly more effective than its Z form. (Unexamined Japanese Patent Publication No. 54-41875)
No. 55-124771, Publication No. 56-25105). By the way, the triazolyl styryl ketone derivative of formula () (hereinafter, unless otherwise specified, E of the triazolyl styryl ketone derivative of formula ())
E body, Z body, and E, Z mixture are respectively E body and Z body.
(referred to as the body and the E/Z body),
For example, there are the following methods. (1) Isomerizing the E/Z form or the Z form to the E form using light (Japanese Patent Application Laid-open No. 147265/1983). (2) Separate the E/Z form by chromatography (Japanese Patent Application Laid-open No. 147265/1983). (3) Only the Z form is precipitated as crystals from the E/Z form, and a mixture rich in the E form is obtained from the mother liquor. If necessary, the Z form is isomerized into the E/Z form (Japanese Patent Application Laid-open No. 1983
−140978, etc.). However, method (1) above requires a special device such as a photoreaction device. Method (2) has many difficulties as an industrial method. Method (3) involves recovering the E form from the mother liquor, and has disadvantages such as not being able to increase the content of the E form too much, and impurities in the raw material E/Z form being unable to be removed. In order to overcome these drawbacks, the present inventors conducted intensive research and found that it was possible to selectively crystallize only the sulfate of the E form from the E/Z form, and after separating and obtaining it, It was discovered that highly pure E-isomer can be obtained by decomposition, and after further various studies, the present invention was arrived at. That is, in the present invention, the E/Z form of the triazolyl styryl ketone derivative represented by the formula () is reacted with sulfuric acid in a solvent, precipitated as a sulfate salt of the E form of the derivative, and then separated and obtained. This is a method for separating geometric isomers of triazolyl styryl ketone derivatives, which is characterized by separating the sulfate to obtain the E form. If the concentration of sulfuric acid used in the method of the present invention is too dilute, the amount of sulfate precipitated will decrease, or in some cases will not precipitate at all. More preferably it is 90-98%. In addition, the amount of sulfuric acid used is usually in the range of 0.5 to 3 times the mole of the E form of the E/Z form in pure terms, but if the amount of sulfuric acid, especially the amount of highly concentrated sulfuric acid, is too large, The amount is more preferably in the range of 0.95 to 1.2 times the mole since the Z-form sulfate is likely to be accompanied by precipitation. The solvent used in the method of the present invention is
Although not particularly limited as long as it is an inert solvent, preferred examples include aprotic organic solvents, such as aromatic hydrocarbons such as benzene, toluene, and xylene, methylene chloride, chloroform, carbon tetrachloride, and dichloroethane. , halogenated hydrocarbons such as trichrene, perchrene, monochlorobenzene, dichlorobenzene, ethyl acetate,
Ester solvents such as ethyl formate, ether solvents such as diethyl ether and tetrahydrofuran, aliphatic or alicyclic hydrocarbons such as hexane, heptane, octane, petroleum ether, ligroin, cyclohexane, and methylcyclohexane, acetone,
Methyl ethyl ketone, methyl isobutyl ketone,
Examples include ketone solvents such as cyclohexanone, nitrile solvents such as acetonitrile and propionitrile, and mixed solvents thereof. Aromatic hydrocarbons and halogenated hydrocarbons are particularly preferably used. The amount of solvent to be used cannot be determined unconditionally as it varies depending on the type and crystallization temperature, but it is usually in the range of 0.5 times to 20 times the weight of the E/Z form of the raw material. In the method of the present invention, the precipitation of E-form sulfate is as follows:
Inoculation of seed crystals is not essential since it usually starts naturally, but may be done to ensure greater certainty. This seed crystal may be added after mixing the sulfuric acid and the raw material E/Z form, or may be added to the E/Z form solution before mixing. The reaction temperature or crystallization temperature is below the boiling point of the solvent and is carried out at a temperature that does not involve side reactions such as isomerization, preferably at 0°C to 80°C. The E-form sulfate can be separated from the reaction solution by using conventional methods such as filtration, centrifugation, and decantation. From the sulfate of E form obtained as above, E
To recover the body, it is usually immiscible with water and E
By mixing the sulfate with a large excess of water in the presence of a solvent that dissolves the sulfate, such as toluene, chlorobenzene, ethyl acetate, ether, carbon tetrachloride, etc., the sulfate is decomposed and a highly purified product is extracted from the oil layer. Body E is recovered. At this time, a base such as sodium carbonate, sodium bicarbonate, sodium hydroxide, or ammonia may be present in excess of sulfuric acid in the aqueous layer. In addition to water, the sulfate can be decomposed using an excessive amount of water-containing protic solvents such as methanol or acetic acid, or bases such as amines. Note that the mother liquor after removing E-form sulfate by the method of the present invention contains a large amount of Z-form, but after removing sulfuric acid by washing with water etc. After isomerizing to the E/Z form by the method shown in the above publication, it can be used again in the method of the present invention, or an excess molar amount of sulfuric acid, more preferably, a Z form sulfate is further added to the mother liquor. Z-form sulfate can also be precipitated by adding seed crystals. Hereinafter, the present invention will be explained using specific examples, but it goes without saying that the present invention is not limited to these examples. Note that E/Z body represents the ratio of E body and Z body. Reference Example 1 1 g of Form E was dissolved in 10 g of toluene, kept at 20°C, and 0.165 cc of concentrated sulfuric acid was added while stirring. The mixture was stirred for 2 hours and then filtered. After washing the crystals with a small amount of toluene, the crystals were vacuum dried. Crystal yield 1.27g Melting point 205.5-207℃ Elemental analysis amount C(%) H(%) N(%) 42.8 4.1 9.8 Elemental analysis amount S(%) Cl(%) 7.5 16.9 Reference example 2 1g of Z-isomer was mixed with 10g of toluene 0.083 cc of concentrated sulfuric acid was added dropwise while stirring while keeping the mixture at 20°C. then 12
The crystals were collected after 6 hours, washed with a small amount of toluene, and then dried in vacuum. Crystal yield 0.62g Melting point 117.5-118℃ Elemental analysis amount C(%) H(%) N(%) 43.0 4.2 9.9 Elemental analysis amount S(%) Cl(%) 7.4 17.1 Example 1 E/Z form (purity 96.8%, E/Z43.0/57.0) 8.11
Dissolve g in 80 g of toluene and add 1.22 g of concentrated sulfuric acid at 20℃.
was dripped. After stirring and keeping warm at 20℃ for 4.5 hours, take it out.
After washing the crystals with 10 c.c. of hexane, the crystals were vacuum dried. Crystal yield: 4.23 g Melting point: 197-205°C Next, 4 c.c. of a 10% aqueous sodium bicarbonate solution, 20 c.c. of toluene and 20 c.c. of water were added to 1 g of this crystal, and at room temperature (20-5°C), After stirring until the crystals disappeared, the aqueous layer was separated, and the oil layer was washed twice with water and concentrated. The obtained crystals were 0.76 g (40% in total based on the E/Z form of the raw material), and the E/Z was 96.0/4.0. Examples 2 to 6 Using the same amount of the E/Z form used in Example 1, the E form was separated in the same manner as in Example 1, except that the solvent, temperature, and time were changed.

【表】【table】

【表】 実施例 7 実施例1で用いたE/Z体8.11gをモノクロル
ベンゼン20gに溶解した。30℃に保温して、濃硫
酸1.22gを滴下したのち、同温度で、5時間撹拌
後過した。結晶はモノクロルベンゼン20c.c.で洗
浄したのち真空乾燥した。収量は4.29gであつ
た。 この結晶1gをジメチルホルムアミド2c.c.に溶
解し、トルエン20c.c.および水20c.c.を加えたのちよ
く混合し、水層を分離した。油層をさらに2回水
洗したのち濃縮し、E体(E/Z、97.3/2.7)
0.77gを得た。 実施例 8 実施例7の濃硫酸1.22gに代えて80%硫酸3.07
gを用いたほかは実施例7と全く同様に行なつ
た。得られた結晶は4.58gでこの結晶1gを分解
して得たE体の収量は0.71g、E/Zは96.7/3.3
であつた。なおこの塩は3.5%の水分を有してお
り、融点は188〜193℃であつた。 実施例 9 実施例7の濃硫酸に代えて50%硫酸2.45gを用
いたほかは全く同様に行なつた。得られた塩は
3.35g、この結晶1gを分解して得たE体は0.62
g(E/Z100.0/0.0)であつた。また、この塩
は8.4%の水を含んでおり、融点は158〜165℃で
あつた。 実施例 10 粗製E/Z体(純度84.4%、E/Z30.6/69.4)
2gを5gのモノクロロベンゼンに溶解し、
0.072c.c.の濃硫酸を添加した。E体硫酸塩結晶
(実施例1と同様にして得たもの)を微量接種し
たのち、27〜32℃で4時間撹拌し過した。得ら
れた結晶は0.504g、これを分解して得たE体は
0.384gで、その純度は97.6%、E/Z99.1/0.9で
あつた。 一方、この母液から回収されたトリアゾリルス
チリルケトン誘導体1.566gは、純度82.4%、
E/Z9.5/90.5であつた。これを1gとり、モノ
クロロベンゼン3.2gに溶解して、濃硫酸0.136c.c.
を30℃で加え、4時間撹拌したのち、過、少量
のモノクロロベンゼンで洗浄して結晶0.915gを
得た。この結晶を全量分解して、0.7g(純度
95.2%、E/Z9.9/90.1)を回収した。 実施例 11 実施例7で得た硫酸塩2gにトルエン5c.c.およ
び水10c.c.を加え、40℃で30分間撹拌したところ、
結晶はほぼ消失しさらに30分間撹拌後、水層を分
離し、水10c.c.で2回洗浄したのち、油層を濃縮し
た。1.481gのE体を得た。 実施例 12 実施例7において、濃硫酸1.22gに代えて濃硫
酸2.45gを用いたほかは同様に行なつた。得られ
た塩は4.68g、この結晶1gを分解してE/Zが
97.7/2.3であるE体を得た。 比較例 1 実施例12において、濃硫酸を滴下終了したの
ち、参考例1で得たE体の硫酸塩および参考例2
で得たZ体硫酸塩各々約1mgを添加したほかは同
様に行なつた。得られた結晶は7.60g、この結晶
1gを分解したところ、E/Zが60.8/39.2の
E/Z体であつた。
[Table] Example 7 8.11 g of the E/Z substance used in Example 1 was dissolved in 20 g of monochlorobenzene. After keeping the temperature at 30°C, 1.22 g of concentrated sulfuric acid was added dropwise, and the mixture was stirred at the same temperature for 5 hours and then filtered. The crystals were washed with 20 c.c. of monochlorobenzene and then dried in vacuum. The yield was 4.29g. 1 g of this crystal was dissolved in 2 c.c. of dimethylformamide, 20 c.c. of toluene and 20 c.c. of water were added and mixed well, and the aqueous layer was separated. After washing the oil layer twice with water, it was concentrated to obtain E form (E/Z, 97.3/2.7).
0.77g was obtained. Example 8 80% sulfuric acid 3.07 g instead of 1.22 g of concentrated sulfuric acid in Example 7
The same procedure as in Example 7 was carried out except that g was used. The obtained crystal was 4.58 g, and the yield of E form obtained by decomposing 1 g of this crystal was 0.71 g, and E/Z was 96.7/3.3.
It was hot. Note that this salt had a water content of 3.5% and a melting point of 188-193°C. Example 9 The same procedure as in Example 7 was repeated except that 2.45 g of 50% sulfuric acid was used instead of concentrated sulfuric acid. The obtained salt is
3.35g, the E form obtained by decomposing 1g of this crystal is 0.62
g (E/Z100.0/0.0). Additionally, this salt contained 8.4% water and had a melting point of 158-165°C. Example 10 Crude E/Z form (purity 84.4%, E/Z30.6/69.4)
Dissolve 2g in 5g of monochlorobenzene,
0.072 cc of concentrated sulfuric acid was added. After inoculating a small amount of E-form sulfate crystals (obtained in the same manner as in Example 1), the mixture was stirred at 27 to 32°C for 4 hours. The obtained crystal is 0.504g, and the E form obtained by decomposing it is
It weighed 0.384 g, and its purity was 97.6%, E/Z 99.1/0.9. On the other hand, 1.566 g of triazolyl styryl ketone derivative recovered from this mother liquor had a purity of 82.4%.
It was E/Z9.5/90.5. Take 1g of this, dissolve it in 3.2g of monochlorobenzene, and add 0.136cc of concentrated sulfuric acid.
was added at 30°C, stirred for 4 hours, and washed with filtrate and a small amount of monochlorobenzene to obtain 0.915 g of crystals. The entire amount of this crystal was decomposed and 0.7g (purity
95.2%, E/Z9.9/90.1) was recovered. Example 11 5 c.c. of toluene and 10 c.c. of water were added to 2 g of the sulfate obtained in Example 7, and the mixture was stirred at 40°C for 30 minutes.
The crystals almost disappeared, and after further stirring for 30 minutes, the aqueous layer was separated, washed twice with 10 c.c. of water, and then the oil layer was concentrated. 1.481 g of E form was obtained. Example 12 The same procedure as in Example 7 was carried out except that 2.45 g of concentrated sulfuric acid was used instead of 1.22 g of concentrated sulfuric acid. The obtained salt was 4.68g, and 1g of this crystal was decomposed to give E/Z.
An E-body with a ratio of 97.7/2.3 was obtained. Comparative Example 1 In Example 12, after finishing dropping concentrated sulfuric acid, the E-form sulfate obtained in Reference Example 1 and Reference Example 2 were added.
The same procedure was followed except that about 1 mg of each of the Z-isomer sulfates obtained in (1) was added. The obtained crystal was 7.60 g, and when 1 g of this crystal was decomposed, it was found to be an E/Z form with E/Z of 60.8/39.2.

Claims (1)

【特許請求の範囲】 1 式 で示されるトリアゾリルスチリルケトン誘導体の
幾何異性体混合物を、溶媒中において硫酸と反応
させ、該誘導体のE体の硫酸塩を結晶として析出
させ、分離取得した後、これを分解することを特
徴とする該トリアゾリルスチリルケトン誘導体の
E体の分離方法。 2 硫酸が40%以上の硫酸である特許請求の範囲
第1項に記載の方法。 3 硫酸が90%以上の硫酸である特許請求の範囲
第1項または第2項に記載の方法。 4 硫酸を該トリアゾリルスチリルケトン誘導体
のE体に対して、0.5〜3倍モル用いる特許請求
の範囲第1項、第2項または第3項に記載の方
法。 5 硫酸を該トリアゾリルスチリルケトン誘導体
のE体に対して、0.95〜1.2倍モル用いる特許請
求の範囲第1項、第2項、第3項または第4項に
記載の方法。 6 溶媒が非プロトン性不活性溶媒である特許請
求の範囲第1項、第2項、第3項、第4項または
第5項に記載の方法。 7 溶媒が芳香族炭化水素またはハロゲン化炭化
水素である特許請求の範囲第6項に記載の方法。
[Claims] 1 formula A mixture of geometric isomers of a triazolyl styryl ketone derivative represented by is reacted with sulfuric acid in a solvent to precipitate the sulfate of the E form of the derivative as crystals, and after separating and obtaining it, it is decomposed. A method for separating the E form of the triazolyl styryl ketone derivative. 2. The method according to claim 1, wherein the sulfuric acid is 40% or more sulfuric acid. 3. The method according to claim 1 or 2, wherein the sulfuric acid is 90% or more sulfuric acid. 4. The method according to claim 1, 2 or 3, in which sulfuric acid is used in an amount of 0.5 to 3 times the mole of the E-form of the triazolyl styryl ketone derivative. 5. The method according to claim 1, 2, 3, or 4, in which sulfuric acid is used in an amount of 0.95 to 1.2 times the mole of E-form of the triazolyl styryl ketone derivative. 6. The method according to claim 1, 2, 3, 4 or 5, wherein the solvent is an aprotic inert solvent. 7. The method according to claim 6, wherein the solvent is an aromatic hydrocarbon or a halogenated hydrocarbon.
JP57023091A 1982-02-15 1982-02-15 Separation of geometric isomer of triazolyl styryl ketone derivative Granted JPS58140081A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57023091A JPS58140081A (en) 1982-02-15 1982-02-15 Separation of geometric isomer of triazolyl styryl ketone derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57023091A JPS58140081A (en) 1982-02-15 1982-02-15 Separation of geometric isomer of triazolyl styryl ketone derivative

Publications (2)

Publication Number Publication Date
JPS58140081A JPS58140081A (en) 1983-08-19
JPH0369903B2 true JPH0369903B2 (en) 1991-11-05

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62178575A (en) * 1986-01-31 1987-08-05 Sumitomo Chem Co Ltd Production of e-isomer of triazolylstyryl ketone derivative
JPS62226966A (en) * 1986-03-28 1987-10-05 Sumitomo Chem Co Ltd Production of e-isomer of triazole derivative
JP4892821B2 (en) * 2004-09-30 2012-03-07 大日本印刷株式会社 Epalrestat manufacturing method
JP4892915B2 (en) * 2005-10-04 2012-03-07 大日本印刷株式会社 Epalrestat manufacturing method

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55147265A (en) * 1979-04-05 1980-11-17 Sumitomo Chem Co Ltd Triazole geometrical isomer compound and its preparation
JPS56140978A (en) * 1980-04-07 1981-11-04 Sumitomo Chem Co Ltd Preparation of triazole geometrical isomeric mixture

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