JP2001081073A - Production of phthalimide derivative - Google Patents

Production of phthalimide derivative

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Publication number
JP2001081073A
JP2001081073A JP25685399A JP25685399A JP2001081073A JP 2001081073 A JP2001081073 A JP 2001081073A JP 25685399 A JP25685399 A JP 25685399A JP 25685399 A JP25685399 A JP 25685399A JP 2001081073 A JP2001081073 A JP 2001081073A
Authority
JP
Japan
Prior art keywords
solvent
phthalimide derivative
phthalic anhydride
phthalimide
general formula
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
JP25685399A
Other languages
Japanese (ja)
Inventor
Tatsumi Nuno
辰巳 布
Susumu Otsuka
大塚  晋
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 JP25685399A priority Critical patent/JP2001081073A/en
Publication of JP2001081073A publication Critical patent/JP2001081073A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To produce a phthalimide derivative good in purity in high yield without scaling due to deposited crystals by reacting phthalic anhydride with specific aminoalcohols in the presence of an organic solvent, adding the resultant reactional liquid to a crystallizing solvent and crystallizing the compound. SOLUTION: Phthalic anhydride is reacted with aminoalcohols represented by the formula H2N-(CH2)n-OH (n is 2-4) in a molar amount of preferably 0.95-2 times based on the phthalic anhydride in the presence of an organic solvent in a weight of preferably 1-10 times based on the phthalic anhydride while removing water formed as a by-product to the outside of the reactional system to provide a reactional liquid containing a phthalimide derivative represented by the formula. The resultant reactional liquid is then added to a crystallizing solvent in a weight of preferably 0.5-10 times based on the phthalic anhydride and crystallized to thereby afford the objective compound. The organic solvent and the crystallizing solvent are preferably an aromatic hydrocarbon-based solvent, an aliphatic hydrocarbon-based solvent, an ethereal solvent and a mixed solvent thereof. The reactional temperature is preferably 80-150 deg.C and the crystallizing temperature is preferably -10 to +65 deg.C.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、フタルイミド誘導
体の改良された製造方法に関する。
The present invention relates to an improved method for producing a phthalimide derivative.

【0002】[0002]

【従来の技術】一般式(2) (式中、nは2〜4の整数を表わす。)で示されるフタ
ルイミド誘導体は、医薬、農薬等の製造中間体として幅
広く使用されている。
2. Description of the Related Art General formula (2) (In the formula, n represents an integer of 2 to 4.) The phthalimide derivative represented by the formula (1) is widely used as an intermediate for producing pharmaceuticals, agricultural chemicals and the like.

【0003】かかる一般式(2)で示されるフタルイミ
ド誘導体の製造方法としては、例えば無水フタル酸と一
般式(1) (式中、nは上記と同一の意味を表わす。)で示される
アミノアルコール類を、疎水性有機溶媒中、還流条件下
で反応させる方法(例えばJ.Org.Chem.,
,1244(1979)等)が知られており、通常得
られた一般式(2)で示されるフタルイミド誘導体を含
む反応液を冷却して、該フタルイミド誘導体を結晶化さ
せていた。
As a method for producing the phthalimide derivative represented by the general formula (2), for example, phthalic anhydride and the general formula (1) (Wherein, n represents the same meaning as described above) by reacting an amino alcohol represented by the formula (1) in a hydrophobic organic solvent under reflux conditions (for example, J. Org. Chem., 4) .
4 , 1244 (1979)), and the phthalimide derivative is crystallized by cooling a reaction solution containing a phthalimide derivative represented by the general formula (2), which is usually obtained.

【0004】しかしながら、かかる方法では、該フタル
イミド誘導体の結晶によるスケーリングが激しく、操作
性の面で問題があった。さらに、該フタルイミド誘導体
の収率も低く、不純物が該フタルイミド誘導体の結晶へ
かみ込み易いため、該フタルイミド誘導体の結晶の純度
も低く、再結晶等のさらなる精製処理が必要である等の
問題があった。
[0004] However, in such a method, the phthalimide derivative is greatly scaled by crystals, and there is a problem in operability. Furthermore, the yield of the phthalimide derivative is low, and impurities are easily infiltrated into the crystals of the phthalimide derivative. Therefore, the purity of the crystals of the phthalimide derivative is low, and further purification such as recrystallization is required. Was.

【0005】[0005]

【発明が解決しようとする課題】このような状況の下、
本発明者らは、上記一般式(2)で示されるフタルイミ
ド誘導体を操作性よく、かつ収率および純度よく製造す
る方法について鋭意検討したところ、無水フタル酸と一
般式(1)で示されるアミノアルコール類を、有機溶媒
の存在下に、副生する水を反応系外に除去しながら反応
させて、上記一般式(2)で示されるフタルイミド誘導
体を含む反応液を得、該反応液を晶析溶媒に加えること
により、析出した結晶によるスケーリングもなく、純度
のよい上記一般式(2)で示されるフタルイミド誘導体
の結晶が収率よく容易に得られることを見出し、本発明
に至った。
SUMMARY OF THE INVENTION Under such circumstances,
The present inventors have conducted intensive studies on a method for producing the phthalimide derivative represented by the above general formula (2) with good operability and high yield and purity, and found that phthalic anhydride and an amino compound represented by the general formula (1) were obtained. The alcohol is reacted in the presence of an organic solvent while removing by-produced water out of the reaction system to obtain a reaction solution containing the phthalimide derivative represented by the general formula (2), and the reaction solution is crystallized. The present inventors have found that by adding to a precipitation solvent, high-purity phthalimide derivative crystals represented by the above general formula (2) can be easily obtained in good yield without scaling due to precipitated crystals, and the present invention has been accomplished.

【0006】[0006]

【課題を解決するための手段】すなわち、本発明は、無
水フタル酸と一般式(1) (式中、nは2〜4の整数を表わす。)で示されるアミ
ノアルコール類を、有機溶媒の存在下に、副生する水を
反応系外に除去しながら反応させて、一般式(2) (式中、nは前記と同一の意味を表わす。)で示される
フタルイミド誘導体を含む反応液を得、該反応液を晶析
溶媒に加えて、一般式(2)で示されるフタルイミド誘
導体を結晶化させることを特徴とするフタルイミド誘導
体の製造方法を提供するものである。
That is, the present invention relates to phthalic anhydride and a compound represented by the general formula (1): (Wherein, n represents an integer of 2 to 4), and reacted in the presence of an organic solvent while removing by-produced water out of the reaction system to obtain a compound represented by the general formula (2) ) (Wherein, n represents the same meaning as described above), and a reaction solution containing a phthalimide derivative represented by the following formula is obtained. The reaction solution is added to a crystallization solvent to crystallize the phthalimide derivative represented by the general formula (2). It is intended to provide a method for producing a phthalimide derivative, characterized in that

【0007】[0007]

【発明の実施の形態】一般式(1) で示されるアミノアルコール類の式中、nは2〜4の整
数を表わし、かかるアミノアルコール類としては、モノ
エタノールアミン、3−アミノ−1−プロパノール、4
−アミノ−1−ブタノールが挙げられる。
DETAILED DESCRIPTION OF THE INVENTION General formula (1) In the formula of amino alcohols represented by, n represents an integer of 2 to 4, and examples of such amino alcohols include monoethanolamine, 3-amino-1-propanol,
-Amino-1-butanol.

【0008】かかるアミノアルコール類の使用量は、無
水フタル酸に対して、通常0.9モル倍以上、好ましく
は0.95モル倍以上であり、その上限は特にないが、
経済的な面を考慮して、通常2モル倍以下である。
The amount of the amino alcohol to be used is usually 0.9 mole times or more, preferably 0.95 mole times or more with respect to phthalic anhydride, and there is no particular upper limit.
In consideration of economical aspects, it is usually 2 mole times or less.

【0009】有機溶媒としては、例えば芳香族炭化水素
系溶媒、脂肪族炭化水素系溶媒、エーテル系溶媒等およ
びこれらの混合溶媒が挙げられる。芳香族炭化水素系溶
媒としては、例えばトルエン、キシレン、クロロベンゼ
ン等が、脂肪族炭化水素系溶媒としては、例えばヘキサ
ン、ヘプタン、オクタン、シクロペンタン、シクロヘキ
サン等が、エーテル系溶媒としては、例えばジエチルエ
ーテル、ジイソプロピルエーテル等が挙げられる。
The organic solvent includes, for example, aromatic hydrocarbon solvents, aliphatic hydrocarbon solvents, ether solvents and the like, and mixed solvents thereof. As aromatic hydrocarbon solvents, for example, toluene, xylene, chlorobenzene, etc., as aliphatic hydrocarbon solvents, for example, hexane, heptane, octane, cyclopentane, cyclohexane, etc., as ether solvents, for example, diethyl ether , Diisopropyl ether and the like.

【0010】その使用量は、無水フタル酸に対して、通
常0.5重量倍以上、好ましくは1重量倍以上である。
その上限は特にないが、それが多すぎると容積効率が悪
くなるため、実用的には10重量倍以下である。
The amount of the phthalic anhydride to be used is usually 0.5 times by weight or more, preferably 1 time by weight or more.
There is no particular upper limit, but if it is too large, the volumetric efficiency will deteriorate, so that it is practically 10 times or less by weight.

【0011】反応温度は、有機溶媒の使用量等にもよる
が、通常80〜150℃の範囲である。
The reaction temperature is usually in the range of 80 to 150 ° C., although it depends on the amount of the organic solvent used and the like.

【0012】本反応は、通常無水フタル酸、一般式
(1)で示されるアミノアルコール類および有機溶媒を
混合し、所定温度に加熱することにより行われるが、反
応の進行に伴い、水が副生してくるため、副生する水を
反応系外に除去しながら反応を実施することが重要であ
る。
This reaction is usually carried out by mixing phthalic anhydride, an amino alcohol represented by the general formula (1) and an organic solvent and heating the mixture to a predetermined temperature. Therefore, it is important to carry out the reaction while removing by-product water out of the reaction system.

【0013】かくして一般式(2)で示されるフタルイ
ミド誘導体を含む反応液が得られ、該反応液を晶析溶媒
に加えて、一般式(2)で示されるフタルイミド誘導体
を結晶化させるが、かかる方法により、フタルイミド誘
導体の結晶のスケーリングは見られず、操作性よく、高
収率で高純度の一般式(2)で示されるフタルイミド誘
導体の結晶が得られる。
Thus, a reaction solution containing the phthalimide derivative represented by the general formula (2) is obtained, and the reaction solution is added to a crystallization solvent to crystallize the phthalimide derivative represented by the general formula (2). According to the method, scaling of the crystal of the phthalimide derivative is not observed, and the crystal of the phthalimide derivative represented by the general formula (2) is obtained with high operability, high yield, and high purity.

【0014】晶析溶媒としては、例えば芳香族炭化水素
系溶媒、脂肪族炭化水素系溶媒、エーテル系溶媒等およ
びこれらの混合溶媒が挙げられ、それぞれ上記したもの
と同様のものが挙げられ、必ずしも上記反応で使用した
溶媒と同じ溶媒を用いる必要はないが、溶媒回収等を考
慮すると、上記反応で使用した有機溶媒と同一のものを
用いることが好ましい。
Examples of the crystallization solvent include, for example, aromatic hydrocarbon solvents, aliphatic hydrocarbon solvents, ether solvents and the like, and mixed solvents thereof. Although it is not necessary to use the same solvent as that used in the above reaction, it is preferable to use the same organic solvent as used in the above reaction in consideration of solvent recovery and the like.

【0015】晶析溶媒の使用量は、上記反応で用いた有
機溶媒の使用量にもよるが、析出したフタルイミド誘導
体の結晶のスラリー性等を考慮して、無水フタル酸に対
して、通常0.5重量倍以上であり、その上限は特にな
いが、あまり多すぎると容積効率が悪くなるため、実用
的には10重量倍以下である。
Although the amount of the crystallization solvent depends on the amount of the organic solvent used in the above reaction, it is usually 0 to phthalic anhydride in consideration of the slurry property of the precipitated phthalimide derivative crystals. It is not less than 0.5 times by weight, and there is no particular upper limit. However, if it is too much, the volumetric efficiency is deteriorated.

【0016】一般式(2)で示されるフタルイミド誘導
体を含む反応液は、通常反応終了後そのまま晶析溶媒に
加えられるが、該反応液を、一般式(2)で示されるフ
タルイミド誘導体の結晶が析出しない程度に冷却した後
加えてもよい。該反応液は、一括で晶析溶媒に加えても
よいが、好ましくは連続的または間欠的に晶析溶媒に加
えられる。
The reaction solution containing the phthalimide derivative represented by the general formula (2) is usually added to the crystallization solvent as it is after the completion of the reaction, and the reaction solution is mixed with the phthalimide derivative crystal represented by the general formula (2). It may be added after cooling to such an extent that precipitation does not occur. The reaction solution may be added all at once to the crystallization solvent, but is preferably added continuously or intermittently to the crystallization solvent.

【0017】結晶化温度は、あまり高いと結晶化しにく
く、あまり低いと実用的ではないため、通常−10〜6
5℃の範囲である。
If the crystallization temperature is too high, crystallization is difficult, and if it is too low, it is not practical.
It is in the range of 5 ° C.

【0018】かくして下記一般式(2) (式中、nは上記と同一の意味を表わす。)で示される
フタルイミド誘導体の結晶が得られ、これをそのまま取
り出してもよいし、さらに冷却して、さらに多くの結晶
を析出させた後取り出してもよい。
Thus, the following general formula (2) (In the formula, n represents the same meaning as described above.) A crystal of the phthalimide derivative represented by the following formula is obtained, and this crystal may be taken out as it is, or further cooled to precipitate more crystals, and then taken out. You may.

【0019】かかる一般式(2)で示されるフタルイミ
ド誘導体としては、N−(2−ヒドロキシエチル)フタ
ルイミド、N−(3−ヒドロキシプロピル)フタルイミ
ド、N−(4−ヒドロキシブチル)フタルイミドが挙げ
られる。
Examples of the phthalimide derivative represented by the general formula (2) include N- (2-hydroxyethyl) phthalimide, N- (3-hydroxypropyl) phthalimide, and N- (4-hydroxybutyl) phthalimide.

【0020】[0020]

【発明の効果】本発明の方法によれば、無水フタル酸と
アミノアルコール類を、有機溶媒の存在下に、副生する
水を反応系外に除去しながら反応させて、目的とするフ
タルイミド誘導体を含む反応液を得、該反応液を晶析溶
媒に加えることより、該フタルイミド誘導体の結晶によ
るスケーリングがなく、高収率で、高純度の結晶を得る
ことができる。
According to the method of the present invention, the desired phthalimide derivative is obtained by reacting phthalic anhydride and amino alcohols in the presence of an organic solvent while removing by-product water out of the reaction system. By obtaining a reaction solution containing the phthalimide derivative and adding the reaction solution to a crystallization solvent, high-purity crystals can be obtained in high yield without scaling by the crystals of the phthalimide derivative.

【0021】[0021]

【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、本発明はこれら実施例により限定されるもの
ではない。なお、得られたフタルイミド誘導体の純度
は、高速液体クロマトグラフィ分析により求めた。
EXAMPLES The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. In addition, the purity of the obtained phthalimide derivative was determined by high performance liquid chromatography analysis.

【0022】実施例1 攪拌装置、脱水還流装置および温度計を取り付けた4ッ
口フラスコに、無水フタル酸267gおよびトルエン2
97gを仕込み、内温89℃まで昇温した。モノエタノ
ールアミン110gを1時間かけて滴下した後、副生す
る水を反応系外へ除去しながら、内温89〜119℃で
8時間攪拌、保持し、N−(2−ヒドロキシエチル)フ
タルイミドを含む反応液を得た。攪拌装置および温度計
を取り付けた別の4ッ口フラスコに、トルエン423g
を仕込み、内温18℃まで冷却した。この冷トルエン
に、先に得た反応液を、内温18〜22℃で、2時間か
けて滴下した後、30分攪拌、保持した。結晶のスケー
リングは見られなかった。析出した結晶を濾過し、乾燥
し、N−(2−ヒドロキシエチル)フタルイミド340
gを得た。純度:99.3重量%。収率:97.2%。
Example 1 267 g of phthalic anhydride and 2 parts of toluene were placed in a four-necked flask equipped with a stirrer, a dehydrating reflux device and a thermometer.
97 g was charged and the internal temperature was raised to 89 ° C. After dropwise adding 110 g of monoethanolamine over 1 hour, the mixture was stirred and maintained at an internal temperature of 89 to 119 ° C. for 8 hours while removing by-produced water to the outside of the reaction system, to remove N- (2-hydroxyethyl) phthalimide. A reaction solution was obtained. 423 g of toluene was placed in another four-necked flask equipped with a stirrer and a thermometer.
And cooled to an internal temperature of 18 ° C. The reaction solution obtained above was dropped into this cold toluene at an internal temperature of 18 to 22 ° C. over 2 hours, and then stirred and held for 30 minutes. No crystal scaling was seen. The precipitated crystals are filtered, dried, and N- (2-hydroxyethyl) phthalimide 340
g was obtained. Purity: 99.3% by weight. Yield: 97.2%.

【0023】実施例2 攪拌装置、脱水還流装置および温度計を取り付けた4ッ
口フラスコに、無水フタル酸267gおよびトルエン5
53gを仕込み、内温99℃まで昇温した。モノエタノ
ールアミン110gを1時間かけて滴下した後、副生す
る水を反応系外へ除去しながら、還流条件下で10時間
攪拌、保持し、N−(ヒドロキシエチル)フタルイミド
を含む反応液を得た。攪拌装置および温度計を取り付け
た別の4ッ口フラスコに、トルエン533gを仕込み、
内温2℃まで冷却した。この冷トルエンに、先に得た反
応液を、内温60℃以下で、10分かけて滴下した後、
内温23℃で30分攪拌、保持した。結晶のスケーリン
グは見られなかった。析出した結晶を濾過し、乾燥し、
N−(2−ヒドロキシエチル)フタルイミド332gを
得た。純度:99.3重量%。収率:94.9%。
Example 2 A four-necked flask equipped with a stirrer, a dehydrating reflux device and a thermometer was charged with 267 g of phthalic anhydride and toluene 5
53 g was charged and the internal temperature was raised to 99 ° C. After dropwise adding 110 g of monoethanolamine over 1 hour, the reaction solution containing N- (hydroxyethyl) phthalimide was obtained by stirring and maintaining under reflux conditions for 10 hours while removing by-product water from the reaction system. Was. In another four-necked flask equipped with a stirrer and a thermometer, 533 g of toluene was charged,
It was cooled to an internal temperature of 2 ° C. The reaction solution obtained above was dropped into the cold toluene at an internal temperature of 60 ° C. or lower over 10 minutes,
The mixture was stirred and maintained at an internal temperature of 23 ° C. for 30 minutes. No crystal scaling was seen. The precipitated crystals are filtered, dried,
332 g of N- (2-hydroxyethyl) phthalimide were obtained. Purity: 99.3% by weight. Yield: 94.9%.

【0024】比較例1 攪拌装置および温度計を取り付けた4ッ口フラスコに、
無水フタル酸146gおよびトルエン210gを仕込
み、内温100℃以下で、モノエタノールアミン60g
を1時間かけて滴下した。その後内温90℃で10時間
攪拌、保持した。その後、内温5℃まで3時間かけて冷
却したところ、析出した結晶のスケーリングが見られ
た。同温度で30分攪拌、保持した後、析出した結晶を
濾過し、乾燥し、N−(2−ヒドロキシエチル)フタル
イミド187gを得た。純度:89.9重量%。収率:
88.5%。
Comparative Example 1 In a four-necked flask equipped with a stirrer and a thermometer,
146 g of phthalic anhydride and 210 g of toluene were charged, and at an internal temperature of 100 ° C. or less, 60 g of monoethanolamine was added.
Was added dropwise over 1 hour. Thereafter, the mixture was stirred and maintained at an internal temperature of 90 ° C. for 10 hours. Thereafter, when the internal temperature was cooled down to 5 ° C. over 3 hours, scaling of precipitated crystals was observed. After stirring and maintaining at the same temperature for 30 minutes, the precipitated crystals were filtered and dried to obtain 187 g of N- (2-hydroxyethyl) phthalimide. Purity: 89.9% by weight. yield:
88.5%.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】無水フタル酸と一般式(1) (式中、nは2〜4の整数を表わす。)で示されるアミ
ノアルコール類を、有機溶媒の存在下に、副生する水を
反応系外に除去しながら反応させて、一般式(2) (式中、nは前記と同一の意味を表わす。)で示される
フタルイミド誘導体を含む反応液を得、該反応液を晶析
溶媒に加えて、一般式(2)で示されるフタルイミド誘
導体を結晶化させることを特徴とするフタルイミド誘導
体の製造方法。
(1) phthalic anhydride and a compound represented by the general formula (1): (Wherein, n represents an integer of 2 to 4), and reacted in the presence of an organic solvent while removing by-produced water out of the reaction system to obtain a compound represented by the general formula (2) ) (Wherein, n represents the same meaning as described above), and a reaction solution containing a phthalimide derivative represented by the following formula is obtained. The reaction solution is added to a crystallization solvent to crystallize the phthalimide derivative represented by the general formula (2). A method for producing a phthalimide derivative.
【請求項2】有機溶媒が、芳香族炭化水素系溶媒、脂肪
族炭化水素系溶媒、エーテル系溶媒およびこれらの混合
溶媒である請求項1に記載のフタルイミド誘導体の製造
方法。
2. The method for producing a phthalimide derivative according to claim 1, wherein the organic solvent is an aromatic hydrocarbon solvent, an aliphatic hydrocarbon solvent, an ether solvent, or a mixed solvent thereof.
【請求項3】晶析溶媒が、芳香族炭化水素系溶媒、脂肪
族炭化水素系溶媒、エーテル系溶媒およびこれらの混合
溶媒である請求項1に記載のフタルイミド誘導体の製造
方法。
3. The method for producing a phthalimide derivative according to claim 1, wherein the crystallization solvent is an aromatic hydrocarbon solvent, an aliphatic hydrocarbon solvent, an ether solvent, or a mixed solvent thereof.
【請求項4】反応温度が、80〜150℃である請求項
1に記載のフタルイミド誘導体の製造方法。
4. The method for producing a phthalimide derivative according to claim 1, wherein the reaction temperature is 80 to 150 ° C.
【請求項5】結晶化温度が、−10〜65℃である請求
項1に記載のフタルイミド誘導体の製造方法。
5. The method for producing a phthalimide derivative according to claim 1, wherein the crystallization temperature is from -10 to 65 ° C.
JP25685399A 1999-09-10 1999-09-10 Production of phthalimide derivative Pending JP2001081073A (en)

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Country Status (1)

Country Link
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Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
JPN6010007952, HAMILTON,R. et al, "A convenient synthesis of N−protected diphenyl phosphonate ester analogs of ornithine, lysine and ho", Tetrahedron Letters, 1993, Vol.34, No.17, p.2847−50 *
JPN6010007955, 社団法人日本化学会 編, 実験化学講座 22 有機合成 IV −酸・アミノ酸・ペプチド−, 1992, 第4版, p.217−218, 丸善株式会社 *
JPN6010007961, 緒方章, 化学実験操作法 上巻, 1963, 第27版, p.371−397, 株式会社南江堂 *

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