JP3298158B2 - Carbamate compound and method for producing the same - Google Patents

Carbamate compound and method for producing the same

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Publication number
JP3298158B2
JP3298158B2 JP17813892A JP17813892A JP3298158B2 JP 3298158 B2 JP3298158 B2 JP 3298158B2 JP 17813892 A JP17813892 A JP 17813892A JP 17813892 A JP17813892 A JP 17813892A JP 3298158 B2 JP3298158 B2 JP 3298158B2
Authority
JP
Japan
Prior art keywords
type
ipc
isopropyl
diethoxyphenyl
carbamate
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
JP17813892A
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Japanese (ja)
Other versions
JPH0625141A (en
Inventor
美秀 森
敏朗 大石
清 山科
義孝 平生
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
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Sumitomo Chemical Co Ltd
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Priority to JP17813892A priority Critical patent/JP3298158B2/en
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

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、新規な結晶構造のイソ
プロピル N−(3,4−ジエトキシフェニル)カーバ
メート(以下、IPCと称する。)およびその製造方
法、特に製剤性に優れた結晶構造のIPCを選択的に製
造する方法に関する。IPCはベンツイミダゾール耐性
灰色かび病菌などに卓効を有する殺菌性化合物として知
られている。
BACKGROUND OF THE INVENTION The present invention relates to a novel crystal structure of isopropyl N- (3,4-diethoxyphenyl) carbamate (hereinafter referred to as IPC) and a method for producing the same, particularly a crystal structure excellent in pharmaceutical properties. And a method for selectively producing IPC. IPC is known as a bactericidal compound having an excellent effect on benzimidazole-resistant gray mold and the like.

【0002】[0002]

【従来の技術】IPCは、通常、ベンゼン、トルエン等
の有機溶媒中で3,4−ジエトキシアニリンとイソプロ
ピルクロロホーメートを反応させた後、不純物、溶媒等
を除去して得られる(特開昭58-74652号、特開昭58- 12
6856号、特開昭59- 204165号)。こうして得られるIP
Cを殺菌剤として使用するに際しては、通常、これを担
体と混合し、例えば粉剤、水和剤、フロアブル剤、乳剤
等に製剤化して用いられる。
2. Description of the Related Art IPC is usually obtained by reacting 3,4-diethoxyaniline with isopropyl chloroformate in an organic solvent such as benzene or toluene, and then removing impurities, a solvent, etc. 58-74652, JP-A-58-12
No. 6856, JP-A-59-204165). IP obtained in this way
When C is used as a fungicide, it is usually mixed with a carrier and formulated into, for example, powders, wettable powders, flowables, emulsions and the like.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、前記で
得られるIPCは製剤化工程およびその製剤品に於い
て、粉砕性、凝集性、固結性等の点で充分なものとは言
い難く、本発明者はかかる問題のないIPCを取得する
ことを目的として鋭意検討した結果、IPCには数種の
結晶構造があることを見出すと共に、溶融状態のIPC
を2℃/分以下の速度で冷却して結晶化させると、前記
目的に合致した結晶構造を有するIPCを得ることがで
きることを見出し、本発明に至った。
However, the IPC obtained as described above is not sufficient in terms of pulverizability, cohesion, consolidation, etc. in the preparation process and its preparations. As a result of intensive studies for the purpose of obtaining an IPC free from such a problem, the inventor has found that the IPC has several types of crystal structures,
Was found to be able to obtain an IPC having a crystal structure that meets the above-mentioned object by cooling at a rate of 2 ° C./min or less for crystallization.

【0004】[0004]

【課題を解決するための手段】すなわち本発明は、X線
回折(CuKα:λ=1.5412Å)において2θが
10.6°及び12.2°に特有の回折ピークを有する
製剤化に優れたIPC及び溶融状態のIPCを1分間
℃以下の速度で冷却し、結晶を析出させることに
製剤化に優れた該IPCの製造方法を提供するものであ
る。
That is, the present invention is excellent in the preparation of a preparation having specific diffraction peaks at 2θ of 10.6 ° and 12.2 ° in X-ray diffraction (CuKα: λ = 1.5412 °). IPC and IPC molten to 1 minute
2 ℃ cooled at a rate, there is provided a method for producing superior the IPC to by that formulation to precipitate crystals.

【0005】以下に本発明につき説明する。本発明者は
IPCを種々の条件下に結晶化し、X線、DSC、I
R、MS、NMR、GC、LC等の装置を用いて分析し
鋭意検討の結果、IPCには4種類の存在形態が存在す
ることを見出した。即ち、X線回折(CuKα:λ=
1.5412Å)において2θが、10.6°及び1
2.2°に特性ピークを有するもの(以下、A型結晶と
称する)、15.3°に特性ピークを有するもの(以
下、B型結晶と称する)、16.9°に特性ピークを有
するもの(以下、C型結晶と称する)および非晶型の4
種類である。
Hereinafter, the present invention will be described. The present inventors have crystallized IPC under various conditions, and have obtained X-ray, DSC, I
As a result of intensive analysis by analyzing using an apparatus such as R, MS, NMR, GC, LC, etc., it was found that there are four types of existence forms in IPC. That is, X-ray diffraction (CuKα: λ =
1.5412 °), 2θ is 10.6 ° and 1
One having a characteristic peak at 2.2 ° (hereinafter referred to as A-type crystal), one having a characteristic peak at 15.3 ° (hereinafter referred to as B-type crystal), and one having a characteristic peak at 16.9 ° (Hereinafter referred to as C-type crystal) and amorphous 4
Kind.

【0006】図1にIPCのA型結晶、B型結晶、C型
結晶及び非晶型のX線回析パターンを示す。図中、横軸
は回折角の2倍(2θ)、縦軸は反射強度を表す。図中
に矢印で示すように、各結晶構造は各々特有な反射ピー
クを有し、A型結晶は2θが10.6°及び12.2
°、B型結晶は2θが15.3°、C型結晶は2θが1
6.9°に特有の回折ピークを有する。表1にA型、B
型及びC型の各結晶の回折ピークの値を示す。
FIG. 1 shows X-ray diffraction patterns of A-type crystal, B-type crystal, C-type crystal and amorphous type of IPC. In the figure, the horizontal axis represents twice the diffraction angle (2θ), and the vertical axis represents the reflection intensity. As shown by arrows in the figure, each crystal structure has a unique reflection peak, and the A-type crystal has 2θ of 10.6 ° and 12.2.
°, B type crystal has 2θ of 15.3 °, and C type crystal has 2θ of 1
It has a unique diffraction peak at 6.9 °. Table 1 shows types A and B
The values of the diffraction peaks of the crystals of type C and type C are shown.

【0007】[0007]

【表1】 [Table 1]

【0008】これら結晶型のうちA型及びB型は熱処理
しても結晶構造に変化は見られないが、C型は熱処理に
より結晶構造が一部A型に変わる。又、非晶型は常法で
得られるIPCを液体窒素等で超急冷した時のみ現れ、
常温で容易にC型に変わる。
[0008] Among these crystal types, A-type and B-type do not show any change in the crystal structure even when heat-treated, but the C-type partially changes to the A-type by heat-treatment. In addition, the amorphous type appears only when IPC obtained by a conventional method is ultra-quenched with liquid nitrogen or the like,
It easily changes to C-type at room temperature.

【0009】図2にIPCのA型結晶、B型結晶、C型
結晶及び非晶型の熱処理前後のX線回折パターンを示
す。A型、B型及びC型は70℃で24時間、非晶型は
20℃で15分間加熱した。この図でA型及びB型では
熱処理前後にX線回折パターンに変化は見られないが、
C型では熱処理後一部A型の回折パターンが見られる。
さらに非晶型はC型に変わっていることがわかる。
FIG. 2 shows X-ray diffraction patterns of A-type crystal, B-type crystal, C-type crystal and amorphous type of IPC before and after heat treatment. Types A, B and C were heated at 70 ° C. for 24 hours, and amorphous types were heated at 20 ° C. for 15 minutes. In this figure, there is no change in the X-ray diffraction pattern before and after the heat treatment in the A type and the B type,
In the case of the C type, a diffraction pattern of the A type is partially observed after the heat treatment.
Further, it can be seen that the amorphous type has been changed to the C type.

【0010】ところで、IPCのベンツイミダゾール耐
性灰色かび病菌などに対する殺菌活性に関しては、結晶
構造による差異はないものの、その製剤性については、
結晶構造の影響が大きく、後述するようにA型結晶は粉
砕性、凝集性、固結性等の点で極めて優れるが、B型及
びC型ではこれらの点で十分とは言えない。なお、A型
結晶のIPCに3〜5%程度のB型が混入していても実
用上の製剤性に問題は生じない。
The bactericidal activity of IPC against benzimidazole-resistant Botrytis cinerea is not affected by the crystal structure.
The crystal structure is greatly affected, and as will be described later, the A-type crystal is extremely excellent in terms of pulverizability, cohesiveness, consolidation and the like, but the B-type and C-type crystals are not sufficient in these respects. Even if about 3 to 5% of type B is mixed in the IPC of the type A crystal, there is no problem in practical formulation.

【0011】このような結晶構造のIPCの取得法にお
いて、溶融IPCの冷却速度の違いによってA型、B
型、C型、A型+B型およびB型+C型の結晶構造のI
PCが得られ、冷却速度を増すにつれて、A型からA型
+B型、B型、B型+C型、C型へと得られる結晶構造
が変わる。A型、B型およびC型の結晶構造のIPC
は、溶融IPCを各々約2℃/分以下、約2.5〜10
℃/分および約12℃/分以上で冷却、結晶化させるこ
とにより得ることができる。
In the method of obtaining IPC having such a crystal structure, A-type and B-type are obtained depending on the cooling rate of the molten IPC.
Type, C type, A type + B type and B type + C type crystal structure I
As PC is obtained and the cooling rate is increased, the crystal structure obtained from type A to type A + B, type B, type B + C, and type C changes. A, B and C crystal structures IPC
Is about 2 ° C./min or less, about 2.5-10
It can be obtained by cooling and crystallizing at a temperature of at least about 12 ° C./min.

【0012】製剤化に優れたA型結晶のIPCは、溶融
IPCを約2℃/分以下の冷却速度で冷却し、結晶化さ
せることにより得られる。かかる方法を工業的に実施す
るに際しては、例えば溶融IPCをドラムドライヤー
(ドラム型固化器)を用いてフレーク化する方法を採用
するこができる。この場合、比較的高温のドラム冷却水
を用い、溶融IPCの冷却速度を約2℃/分以下に保持
することが重要である。かかる冷却水の温度は、ドラム
ドライヤーの大きさ、ドラムの回転速度、溶融温度等に
よっても多少異なるが、例えばIPCの溶融温度が11
5〜125℃、ドラム回転速度が1rpmの場合、ドラ
ム冷却水温度を65℃以上にすることによって十分目的
を達成できる。またベルト型固化器を用い、溶融IPC
の冷却速度を約2℃/分以下に保持することによりドラ
ム型固化器と同様にA型結晶のIPCを得ることができ
る。
[0012] The IPC of type A crystal excellent in formulation can be obtained by cooling the molten IPC at a cooling rate of about 2 ° C / min or less and crystallization. When such a method is industrially performed, for example, a method in which molten IPC is flaked using a drum dryer (drum-type solidifier) can be employed. In this case, it is important to use relatively high-temperature drum cooling water and to maintain the cooling rate of the molten IPC at about 2 ° C./min or less. The temperature of the cooling water slightly varies depending on the size of the drum dryer, the rotation speed of the drum, the melting temperature, and the like.
When the temperature is 5 to 125 ° C. and the drum rotation speed is 1 rpm, the object can be sufficiently achieved by setting the temperature of the drum cooling water to 65 ° C. or higher. In addition, using a belt-type solidifier,
By keeping the cooling rate at about 2 ° C./min or less, IPC of A-type crystal can be obtained as in the case of the drum-type solidifier.

【0013】また、滴下造粒器を用い、溶融IPCを水
中に滴下して、冷却、結晶化する方法も採用し得るが、
この場合も水温を上げて溶融IPCの冷却速度を約2℃
/分以下に保持する必要がある。例えば、溶融IPCの
温度が100〜130℃の場合、液滴の大きさにもよる
が、通常、水温を40℃以上に保った温水中に滴下する
ことによってA型結晶のIPCを得ることができる。
Further, a method of cooling and crystallizing the molten IPC by dripping the molten IPC into water using a dropping granulator can also be adopted.
Also in this case, the water temperature is raised and the cooling rate of the molten IPC is set to about 2 ° C.
/ Min. For example, when the temperature of the molten IPC is 100 to 130 ° C., although it depends on the size of the droplet, it is usually possible to obtain the IPC of the A-type crystal by dropping it into hot water whose water temperature is maintained at 40 ° C. or higher. it can.

【0014】これらの方法に於いて、溶融IPCの温度
は、IPCの劣化の観点から100〜130℃が好まし
く、また、必要に応じ、かかる溶融IPCにジオクチル
スルホコハク酸ソーダなどの界面活性剤を添加すること
もできる。
In these methods, the temperature of the molten IPC is preferably from 100 to 130 ° C. from the viewpoint of deterioration of the IPC, and if necessary, a surfactant such as sodium dioctyl sulfosuccinate may be added to the molten IPC. You can also.

【0015】[0015]

【発明の効果】本発明により、製剤性に優れた結晶構造
のIPCを効率良く製造できる。
According to the present invention, it is possible to efficiently produce IPC having a crystal structure excellent in formulation properties.

【0016】[0016]

【実施例】以下、製造例および製剤性試験を挙げて本発
明をより詳細に説明するが、本発明はこれらによって何
ら限定されるものではない。
The present invention will be described in more detail with reference to the following Preparation Examples and Formulation Tests, but the present invention is not limited thereto.

【0017】製造例1 IPC各5gをガラス管に入れ、それぞれ130℃で3
0分加熱溶融後、1〜1.3℃/分、2.5〜3℃/分
および12〜15℃/分の条件で冷却し、結晶化させ
た。その結果それぞれ、ほぼA型、B型およびC型の結
晶構造のIPCが生成していた。
Production Example 1 5 g of each IPC was placed in a glass tube, and each was placed at 130 ° C. for 3 g.
After heating and melting for 0 minutes, the mixture was cooled and crystallized under the conditions of 1 to 1.3 ° C / minute, 2.5 to 3 ° C / minute, and 12 to 15 ° C / minute. As a result, IPCs of almost A-type, B-type, and C-type crystal structures were generated, respectively.

【0018】製造例2 IPC10kgをスチームで115〜120℃に加熱、
溶融後、ドラムドライヤー(ドラム大きさ:200mm
φ×300mml)を用い、ドラム回転数1rpmでフ
レーク化し、ドラムドライヤーの冷却水温度と得られる
IPC結晶中のA型結晶の生成割合との関係について調
べた。図4に用いた装置の概要を、図5に結果を示す。
なお、A型結晶の生成割合は、X線回折図での2θ=1
2.2°、15.3°、16.9°の面積強度を各々I
a、Ib、Icとして次式に従って計算した。 A型結晶の割合(%)=〔1.998(Ia−0.876 Ic) ×100
〕÷〔1.998(Ia−0.876 Ic) +2.357 Ib+13.274Ic〕 上式で係数0.876は2θ=12.3°に現れるC型
のピークの割合である。図5よりドラム冷却水を65℃
以上(冷却速度の推算値約2℃/分以下)にすることに
よりA型の結晶構造のIPCが得られることがわかる。
Production Example 2 10 kg of IPC was heated to 115 to 120 ° C. with steam.
After melting, a drum dryer (drum size: 200 mm
(φ × 300 mml), flakes were formed at a drum rotation speed of 1 rpm, and the relationship between the cooling water temperature of the drum dryer and the generation rate of A-type crystals in the obtained IPC crystals was examined. FIG. 4 shows the outline of the apparatus used, and FIG. 5 shows the results.
The generation rate of the A-type crystal was 2θ = 1 in the X-ray diffraction diagram.
2.2 °, 15.3 °, 16.9 ° area intensity of I
a, Ib, and Ic were calculated according to the following equations. A-type crystal ratio (%) = [1.998 (Ia−0.876 Ic) × 100
] [1.998 (Ia-0.876 Ic) + 2.357 Ib + 13.274 Ic] In the above equation, the coefficient 0.876 is the ratio of the C-type peak appearing at 2θ = 12.3 °. As shown in FIG.
It can be seen that IPC having an A-type crystal structure can be obtained by making the above (the estimated cooling rate is about 2 ° C./min or less).

【0019】製造例3 スチームで110℃に加熱溶融したIPC7.8kg
を、界面活性剤としてジオクチルスルホコハク酸ソーダ
の4%水溶液をIPC1kgあたり0.04kgを加え
た45〜50℃の温水30.3kg中に滴下後、30℃
に冷却し晶析した。その後、濾過、乾燥し、A型の結晶
のIPC7.4kgを得た。
Production Example 3 7.8 kg of IPC heated and melted at 110 ° C. with steam
Was dropped into 30.3 kg of hot water of 45 to 50 ° C. to which 0.04 kg of a 4% aqueous solution of sodium dioctyl sulfosuccinate was added as a surfactant per 1 kg of IPC.
And crystallized. Thereafter, the mixture was filtered and dried to obtain 7.4 kg of A-type crystals of IPC.

【0020】製造例4 130℃に加熱溶融したIPC2gを20℃の水100
gに滴下し、結晶を析出させた。得られた結晶はC型で
あった。
Production Example 4 2 g of IPC heated and melted at 130.degree.
g, to precipitate crystals. The obtained crystals were of the C type.

【0021】製剤性試験例1 製造例1に準じて製造したA型、B型、C型のIPCの
結晶について、各々の水和剤としての粉砕性、凝集性お
よび固結性について試験した。粉砕性については、IP
C26部にホワイトカーボン5部およびソルポール50
50(分散剤、東邦化学製)2部を加え水和剤とし、こ
れを遠心式粉砕機で20000rpmで25分間粉砕
し、平均粒径を測定した。その結果、A型は5.6μ
m、B型は7.8μm、C型は12μmであり、A型が
最も粉砕性が良かった。
Formulation Test Example 1 Crystals of type A, type B, and type C IPCs produced according to Production Example 1 were tested for crushability, cohesiveness, and caking properties as respective wettable powders. For crushability, IP
5 parts of white carbon and 50 parts of Solpol 50
50 parts (dispersing agent, manufactured by Toho Chemical Co., Ltd.) was added to obtain a wettable powder, which was pulverized with a centrifugal pulverizer at 20,000 rpm for 25 minutes, and the average particle size was measured. As a result, type A was 5.6μ
Types m and B were 7.8 μm, type C was 12 μm, and type A had the best crushability.

【0022】凝集性については上記の粉砕品をポリ袋に
いれて25日間、室温で放置後、試料30gをとり、1
6メッシュ篩で篩別した。その結果、16メッシュ以上
がA型結晶では0.3%と何ら凝集性に問題はなく、B
型では55%、C型では48%であった。
Regarding the cohesiveness, the above ground product was placed in a plastic bag and allowed to stand at room temperature for 25 days.
The mixture was sieved with a 6-mesh sieve. As a result, there was no problem with the cohesion of the A-type crystal of 16% or more in the case of the A-type crystal.
It was 55% for the mold and 48% for the C type.

【0023】固結性については、上記水和剤に製剤した
試料約20gを内径5cmのステンレス製円筒に秤取
し、上面を平らにした後、25g/cm2 の荷重をか
け、54℃で2週間保存した。その後、試料を取り出
し、一辺が1cmの立方体を切出し、これに荷重をかけ
ていき、該立方体が破壊する重量を以て固結性の指標と
した。その結果、A型は10g、B型は100g以上、
C型は100gないしそれ以上であり、B型およびC型
は固結していた。
Regarding the caking property, about 20 g of a sample prepared in the above wettable powder was weighed into a stainless steel cylinder having an inner diameter of 5 cm, the upper surface thereof was flattened, and a load of 25 g / cm 2 was applied. Stored for 2 weeks. Thereafter, the sample was taken out, a cube having a side of 1 cm was cut out, a load was applied thereto, and the weight at which the cube was broken was used as an index of solidification. As a result, type A is 10 g, type B is 100 g or more,
Form C weighed 100 g or more, while forms B and C were consolidated.

【0024】表2にIPCのA型、B型及びC型結晶の
物性と、製剤性の評価結果をまとめて示す。
Table 2 summarizes the physical properties of IPC type A, B type and C type crystals and the evaluation results of the formulation.

【0025】[0025]

【表2】 [Table 2]

【図面の簡単な説明】[Brief description of the drawings]

【図1】IPCのA型結晶、B型結晶、C型結晶および
非晶型のX線回折図を示す図である。
FIG. 1 is a diagram showing X-ray diffraction patterns of A-type crystal, B-type crystal, C-type crystal and amorphous type of IPC.

【図2】IPCのA型結晶、B型結晶、C型結晶および
非晶型の熱処理前後のX線回折図を示す図である。
FIG. 2 is a diagram showing X-ray diffraction diagrams of an A-type crystal, a B-type crystal, a C-type crystal, and an amorphous type of IPC before and after heat treatment.

【図3】製造例1における溶融IPCの冷却速度を示す
図である。
FIG. 3 is a diagram showing a cooling rate of molten IPC in Production Example 1.

【図4】製造例2で用いた装置の概要を示す図である。FIG. 4 is a diagram showing an outline of an apparatus used in Production Example 2.

【図5】製造例2におけるドラム冷却水温度とA型IP
C結晶の生成割合を示す図である。
FIG. 5 shows drum cooling water temperature and A-type IP in Production Example 2.
It is a figure which shows the production ratio of C crystal.

フロントページの続き (72)発明者 平生 義孝 愛媛県新居浜市惣開町5番1号 住友化 学工業株式会社内 (56)参考文献 特開 昭58−74652(JP,A) 特開 昭58−126856(JP,A) 特開 昭59−204165(JP,A) (58)調査した分野(Int.Cl.7,DB名) CA(STN) REGISTRY(STN)Continuation of front page (72) Inventor Yoshitaka Hirao 5-1 Sokai-cho, Niihama-shi, Ehime Sumitomo Chemical Industries, Ltd. (56) References JP-A-58-74652 (JP, A) JP-A-58-126856 (JP, A) JP-A-59-204165 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) CA (STN) REGISTRY (STN)

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 X線回折(CuKα:λ=1.5412
Å)において2θが10.6°及び12.2°に特有の
回折ピークを有するイソプロピル N−(3,4−ジエ
トキシフェニル)カーバメート。
1. X-ray diffraction (CuKα: λ = 1.5412)
Isopropyl N- (3,4-diethoxyphenyl) carbamate having characteristic diffraction peaks at 2θ of 10.6 ° and 12.2 ° in Å).
【請求項2】 X線回折(CuKα:λ=1.5412
Å)において2θが15.3°に特有の回折ピークを有
するイソプロピル N−(3,4−ジエトキシフェニ
ル)カーバメート。
2. X-ray diffraction (CuKα: λ = 1.5412)
Isopropyl N- (3,4-diethoxyphenyl) carbamate having a specific diffraction peak at 2θ of 15.3 ° in Å).
【請求項3】 X線回折(CuKα:λ=1.5412
Å)において2θが16.9°に特有の回折ピークを有
するイソプロピル N−(3,4−ジエトキシフェニ
ル)カーバメート。
3. X-ray diffraction (CuKα: λ = 1.5412)
Isopropyl N- (3,4-diethoxyphenyl) carbamate having a unique diffraction peak at 2θ of 16.9 ° in Å).
【請求項4】溶融状態のイソプロピル N−(3,4−
ジエトキシフェニル)カーバメートを1分間に2℃以下
の速度で冷却し、結晶を析出させることを特徴とする請
求項1記載のイソプロピル N−(3,4−ジエトキシ
フェニル)カーバメートの製造方法。
4. An isopropyl N- (3,4-) in a molten state.
2. The method for producing isopropyl N- (3,4-diethoxyphenyl) carbamate according to claim 1, wherein the diethoxyphenyl) carbamate is cooled at a rate of 2 ° C. or less per minute to precipitate crystals.
【請求項5】 ドラム型固化器またはベルト型固化器を
用いて行う請求項4記載のイソプロピル N−(3,4
−ジエトキシフェニル)カーバメートの製造方法。
5. The isopropyl N- (3,4) according to claim 4, wherein the isopropyl N- (3,4) is carried out using a drum-type solidifier or a belt-type solidifier.
A process for the production of (diethoxyphenyl) carbamate.
【請求項6】 溶融状態のイソプロピル N−(3,4
−ジエトキシフェニル)カーバメートを40℃以上の温
水中に滴下し、結晶を析出させることを特徴とする請求
項1記載のイソプロピル N−(3,4−ジエトキシフ
ェニル)カーバメートの製造方法。
6. An isopropyl N- (3,4) in a molten state.
The method for producing isopropyl N- (3,4-diethoxyphenyl) carbamate according to claim 1, wherein -diethoxyphenyl) carbamate is dropped into warm water at 40 ° C or higher to precipitate crystals.
【請求項7】 滴下造粒器を用いて行う請求項6記載の
イソプロピル N−(3,4−ジエトキシフェニル)カ
ーバメートの製造方法
7. The method for producing isopropyl N- (3,4-diethoxyphenyl) carbamate according to claim 6, wherein the method is carried out using a dropping granulator.
【請求項8】 100〜130℃の溶融状態のイソプロ
ピル N−(3,4−ジエトキシフェニル)カーバメー
トを用いる請求項4または請求項6記載のイソプロピル
N−(3,4−ジエトキシフェニル)カーバメートの
製造方法。
8. The isopropyl N- (3,4-diethoxyphenyl) carbamate according to claim 4, wherein isopropyl N- (3,4-diethoxyphenyl) carbamate in a molten state at 100 to 130 ° C. is used. Manufacturing method.
JP17813892A 1992-07-06 1992-07-06 Carbamate compound and method for producing the same Expired - Fee Related JP3298158B2 (en)

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Application Number Priority Date Filing Date Title
JP17813892A JP3298158B2 (en) 1992-07-06 1992-07-06 Carbamate compound and method for producing the same

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JP3298158B2 true JP3298158B2 (en) 2002-07-02

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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