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WO2004069802A1 - Process for producing 2-amino-3-substituted pyridine - Google Patents

Process for producing 2-amino-3-substituted pyridine Download PDF

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Publication number
WO2004069802A1
WO2004069802A1 PCT/JP2004/000995 JP2004000995W WO2004069802A1 WO 2004069802 A1 WO2004069802 A1 WO 2004069802A1 JP 2004000995 W JP2004000995 W JP 2004000995W WO 2004069802 A1 WO2004069802 A1 WO 2004069802A1
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Prior art keywords
copper
production method
catalyst
acid
metal
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PCT/JP2004/000995
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French (fr)
Japanese (ja)
Inventor
Yukihito Sumino
Shinobu Wakabayashi
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Shionogi & Co., Ltd.
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Priority to JP2005504814A priority Critical patent/JPWO2004069802A1/en
Publication of WO2004069802A1 publication Critical patent/WO2004069802A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D213/00Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
    • C07D213/02Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
    • C07D213/04Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D213/60Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D213/72Nitrogen atoms
    • C07D213/73Unsubstituted amino or imino radicals

Definitions

  • the present invention relates to 2-amimino 3-substituted pyridines (eg, 2,3-diaminopyridine) useful as synthetic intermediates such as cefm antibacterial agents and imidazopyridines, or as pharmaceutical raw materials such as organometallic complex ligands. It relates to a method for producing the salt.
  • 2-amimino 3-substituted pyridines eg, 2,3-diaminopyridine
  • synthetic intermediates such as cefm antibacterial agents and imidazopyridines
  • pharmaceutical raw materials such as organometallic complex ligands.
  • 2,3-diaminopyridine is described as a raw material of the 3-position side chain of a septum antibacterial agent (eg, Patent Document 1).
  • Non-Patent Document 1 As a typical production method of 2,3-diaminopyridine, a method of synthesizing in four steps using 2-aminoviridine as a starting material is described (eg, Non-Patent Document 1). However, this method uses metals such as bromine and iron as reaction reagents, which is not desirable in terms of environment and safety, and the yield is as low as 26%, which is not a satisfactory method as an industrial method. . Further, in a production method using 3-ethoxycarbonylamino-2-nitropyridine as a starting material, nickel metal, which is concerned with carcinogenicity, is used (eg, Non-Patent Document 2).
  • Non-Patent Document 3 As a method for synthesizing an aminoviridine derivative using a copper catalyst, an amination reaction between bromopyridine and ammonia is known (eg, Non-Patent Document 3).
  • the amination reaction with chloro-open pyridine which is more inert than bromopyridine, has not been successful.
  • this reaction for example, in the case of 2-chloro-1-5-nitropyridine having an electron-withdrawing substituent that enhances the reactivity of the chromatol group, an aminoviridine derivative is produced.
  • No amination reaction with an aminochloropyridine having an electron donating substituent which weakens the reactivity of the group is described. Also, there is no description of a method for removing a water-soluble copper catalyst which has a risk of water pollution used as a reaction catalyst.
  • Patent Document 1 International Publication No. 0/3 2 6 06
  • Patent Document 2 Japanese Patent Application Laid-Open No. 05-33 39 2 36,
  • Non-Patent Document 1 Barham (W.E.Barham), Organic Synthesis (Org. Syn), USA, Vol. 44, P 34-39 (1964)
  • Non-Patent Document 2 J. W. Clark—Lewins, et al., J. Cheni. Soc., UK, P442—447 (1957)
  • Non-Patent Document 3 Lang et al., Tett. Lett, USA, Vol. 42, P3251-3254 (2001) Disclosure of the invention
  • R is NHR 1 N (R 1) 2 , OH, 0 R J s NH CO CH 3, SR 1 (wherein, R 1 is alkyl), a manufacturing method of claim 1, wherein the.
  • the production method of the present invention is constituted or selected from the following three steps.
  • the first step is to react the 3-substituted 1-2-halogenobilizine (I) with ammonia in the presence of a catalyst, preferably a copper catalyst, to form 2-
  • a catalyst preferably a copper catalyst
  • the second step is a method of removing copper from the reaction mixture of the first step by treating it with a sulfide compound.
  • the first step is a method of reacting compound (I) with ammonia in the presence of a catalyst to produce 2-amino-1-substituted pyridine (II), preferably 2,3-diaminopyridine.
  • the halogen is preferably c including fluorine, chlorine, bromine and iodine, and particularly preferably chlorine.
  • the catalyst is preferably a catalyst containing a metal such as cobalt, tin, zinc, iron, aluminum, boron, copper, titanium, arsenic, thallium, nickel, chromium, rhodium, iridium, platinum, palladium, etc.
  • a metal-containing catalyst is preferably a metal exhibiting a coordination property to the N atom and R of pyridine of the compound (I).
  • the catalyst is preferably a catalyst containing copper (hereinafter, referred to as a copper catalyst).
  • the copper catalyst includes, for example, copper salts, copper oxides, metallic copper and mixtures thereof, and further includes complex salts composed of copper salts, copper oxides, metallic copper or mixtures thereof and organic bases.
  • Copper salts include cuprous chloride, cuprous bromide, cupric chloride, cupric bromide, anhydrous cupric nitrate, cupric nitrate heptahydrate, anhydrous copper sulfate and copper sulfate pentahydrate Japanese products.
  • copper oxide include cuprous oxide and cupric oxide.
  • copper salts particularly preferably copper halides, such as cuprous chloride (CuCl).
  • CuCl cuprous chloride
  • the amount of the copper catalyst to be used is generally in the range of 0.01 to 5 equivalents, preferably 0.01 to 0.5 equivalents, particularly preferably 0.1 to 0.4 equivalents, relative to compound (I). Is equivalent.
  • This reaction is preferably performed in an aqueous ammonia solution, but may be performed in a polar solvent or an organic base may be added to the reaction solution.
  • Ammonia used in the amination reaction includes ammonium acetate, ammonium picocarbonate, ammonium benzoate, ammonium carbonate, ammonium formate, ammonia oxalate, aqueous ammonia, and the like. And liquid ammonia.
  • the ammonia is preferably ammonia water having a concentration of 1 to 50%, particularly preferably an aqueous ammonia solution having a concentration of 20 to 30%.
  • the amount of ammonia to be used is generally 1 to 100 equivalents, preferably 2 to 50 equivalents, particularly preferably 3 to 30 equivalents, relative to compound (I).
  • polar solvent examples include cyclic amides such as 1-methyl-1-pyrrolidinone, cyclic ureas such as 1,3-dimethyl-12-imidazolidinone, sulfoxides such as dimethyl sulfoxide, and dimethyl sulfone and sulfolane.
  • ethers such as 1,4-dioxane, N, N —Dialkyl anilines such as dimethyl aniline and N, N-Jetyl aniline; heterocyclic compounds such as pyridine and quinoline; methanol, ethanol, propanol, 2-propanol, ethylene glycol, propylene glycol, Alcohols such as glycerin and water, and the like.
  • the solvents can be used alone or as a mixture of two or more. The amount of the solvent is usually about 1 ml to 100 ml with respect to the compound (I) lg.
  • organic base examples include pyridines such as pyridine, methylpyridine, ethylpyridine, dimethylpyridine, methylethylpyridine, getylviridine, pyridines such as trimethylpyridine, dimethylaminopyridine and 2,2-bipyridyl, triethylamine, tripropylamine and the like.
  • pyridines such as trimethylpyridine, dimethylaminopyridine and 2,2-bipyridyl, triethylamine, tripropylamine and the like.
  • trialkylamines such as tributylamine, N, N-dialkylanilines such as N, N-dimethylaniline and N, N-getylaniline, and liquid ammonia.
  • This reaction is carried out under cooling to room temperature, but is preferably carried out under heating.
  • the preferred reaction temperature is usually 30 to 250. More preferably, the temperature is from 80 to 200 ° C, and preferably from 110 to: L60 ° C.
  • the reaction time is usually several hours to several tens of hours.
  • This reaction may be carried out under atmospheric pressure, but is preferably carried out in a closed pressurized apparatus, and the internal pressure is usually 0.1 to 10 MPa, preferably 0.1 to 2 MPa, particularly It is preferably 0;; to 0.3 MPa.
  • R is various substituents as long as it is an electron-donating substituent which exhibits coordination to the above-mentioned catalyst, preferably a metal in the catalyst.
  • the atom bonded to the pyridine ring is a hetero atom that exhibits coordination to the metal in the catalyst.
  • the heteroatom is selected from atoms other than hydrogen or carbon, but is preferably N, 0, S, etc., more preferably N or 0, and particularly preferably N.
  • residue bonded to the hetero atom examples include hydrogen, alkyl, preferably C1 to C6 alkyl (eg, methyl, ethyl, n-propyl, t-butyl, etc.), lower alkylcarbonyl (eg, acetyl, Carbonyl) and the like.
  • alkyl preferably C1 to C6 alkyl (eg, methyl, ethyl, n-propyl, t-butyl, etc.)
  • lower alkylcarbonyl eg, acetyl, Carbonyl
  • R is preferably an optionally substituted amino (eg, amino, NHR 1 N (R 2 (R 1 is alkyl)) (eg, methylamino, ethylamino, dimethylamino, getylamino), lower alkylcarbonylamino (example: NHC OCH 3 )), optionally substituted hydroxy (eg, 0 H, OR 1 (eg, methoxy, ethoxy)) or optionally substituted thiol (eg, thiol, SR 1 (eg, Methylthio)) It is.
  • R is more preferably an optionally substituted amino, particularly preferably NH 2 . Since R is an electron donating group, naturally, for example, halogen, nitro, methyl halide and the like are excluded.
  • the compound (I) as a raw material is a known compound (eg, 3-amino-2-chloropyridin, 3-hydroxy-2-chloropyridine, 3-methoxy-2-chloropyridine) or a known compound containing these. It can be easily synthesized from compounds.
  • the compound (II) can be obtained by treating the reaction solution by a conventional method (concentration, extraction, separation, etc.). To obtain a higher quality compound (II), the second and third steps are preferably performed. (2nd step)
  • the second step is optionally performed when a copper catalyst is used in the reaction of the first step, and is a method of removing copper from the reaction mixture as copper sulfide.
  • the acid may be either an organic acid or an inorganic acid, but is preferably an inorganic acid, particularly preferably sulfuric acid.
  • concentration of sulfuric acid is about 10-80%, preferably 50-70%.
  • the amount of the acid used is, for example, about 1 ml to 10 ml for compound (I) 1 in the case of 64% sulfuric acid.
  • the temperature at which the acid is added is usually 0 to 50 ° C, preferably 0 to 25 ° C.
  • sulfide compounds such as sodium thiosulfate, sodium hydrosulfide, sodium sulfide, ammonium sulfide, potassium sulfide, lithium sulfide and hydrogen sulfide are added to the acidic mixture prepared above, and stirred for several hours to precipitate copper as copper sulfide. After that, the insoluble matter is filtered.
  • sodium thiosulfate sodium hydrosulfide and hydrogen sulfide are particularly preferred, and sodium thiosulfate is particularly preferred.
  • the amount of the sulfide compound used is, for example, about 1 ml to 15 ml for 1 g of the compound (1) in the case of a saturated aqueous solution of sodium thiosulfate.
  • the temperature at which the sulfide compound is added is usually 0 to 40 ° C, preferably 10 to 30 ° C.
  • the stirring time is usually 1 to 20 hours, depending on the state of copper sulfide precipitation.
  • Copper sulfide usually refers to monovalent and divalent copper sulfides, but may include metallic copper and sulfur.
  • the third step is a step of producing a salt of the compound (II) such as 2,3-diaminopyridine and a step of purifying the compound (II) using the salt.
  • a salt of the compound (II) such as 2,3-diaminopyridine
  • a step of purifying the compound (II) using the salt is described as an example.
  • the production of the salt of 2,3-diaminopyridine is preferably performed in the first step, More preferably, a base is added to the filtrate prepared in the second step to prepare a solution having a pH of preferably 8-9.
  • the base may be any of an organic base and an inorganic base, but is preferably an inorganic base, particularly preferably a 30 to 50% sodium hydroxide aqueous solution.
  • the base is used in an appropriate amount. For example, if the base is a 48% aqueous sodium hydroxide solution, add an appropriate amount until the solution has a pH of 8-9.
  • the temperature at which the base is added is usually 0 to 40 ° C.
  • This acid addition salt may be subjected to desalting treatment as described later to convert it to 2,3-diaminopyridine, and then to another salt.
  • the amount of the acid used is preferably 0.6 to 10 equivalents to 1 equivalent of the raw material 3-amino 2-chloropyridine. Particularly preferred is 0.8 to 1.4 equivalents.
  • crystals are precipitated in about 10 minutes to several tens of hours, preferably several hours, at room temperature with stirring. When no precipitation occurs, the crystals may be precipitated by, for example, applying a stimulus such as ultrasonic treatment and stirring under cooling or adding a seed crystal.
  • Salt binding has the advantage of good operability in the manufacturing process because of good filterability and easy separation from solvents (eg, water). Further, in a salt state at normal temperature and normal pressure, it is easy to obtain a stable and high quality product.
  • 2,3-Diaminopyridine can be obtained by treating the isolated and purified acid addition salt, preferably benzoate, with a base.
  • the base may be any of an inorganic base and an organic base, but is preferably an inorganic base.
  • the inorganic base include sodium hydroxide, potassium hydroxide, calcium hydroxide, sodium carbonate, sodium hydrogen carbonate, and lithium carbonate. Particularly preferred is sodium hydroxide.
  • 2,3-Diaminopyridine can be obtained, for example, by suspending a salt of benzoic acid in water or an organic solvent, or in an organic solvent (eg, methanol, ethanol, chloroform, dichloromethan). After dissolving in ethyl acetate and ethyl acetate (preferably ethyl acetate), a base such as sodium hydroxide is added under cooling, and the mixture is stirred for several hours to produce.
  • a salt of benzoic acid in water or an organic solvent, or in an organic solvent (eg, methanol, ethanol, chloroform, dichloromethan).
  • an organic solvent eg, methanol, ethanol, chloroform, dichloromethan
  • a base such as sodium hydroxide
  • the amount of the solvent is usually about 1 ml to 100 ml per 1 g of the salt.
  • the amount of the base is preferably 1 to 10 equivalents to 1 equivalent of the salt.
  • the reaction temperature is generally 0 to 40 ° C, preferably 0 to 30 ° C.
  • the stirring time is usually 1 to several tens hours, preferably 1 to 2 hours.
  • 2,3-Diaminopyridine is obtained by treating a base-treated solution or a concentrated solution thereof with ethers (eg, dimethyl ether, diisopropyl ether, methyl tert-butyl ether), ethyl acetate, toluene, acetonitrile, and acetone.
  • ethers eg, dimethyl ether, diisopropyl ether, methyl tert-butyl ether
  • ethyl acetate ethyl acetate
  • toluene acetonitrile
  • acetone e.g, 2,3-Diaminopyridine
  • Organic or inorganic salts may precipitate, but can be removed by washing with a small amount of cold water.
  • the target crystal can be obtained more efficiently.
  • Compound (II) may be a solvate coordinated with any number of suitable organic solvents or water.
  • the compound ( ⁇ ⁇ ) produced in 43 can be further converted to various salts by standard methods. For example, it can be crystallized as a benzoate by treating with a hydrated solvent containing benzoic acid.
  • Examples of the salts of 2,3-diaminopyridine include salts with various bases and acid addition salts.
  • the aqueous ammonia in the above reaction mixture was distilled off under reduced pressure, and the residue was dissolved in a 64% aqueous sulfuric acid solution (4 ml).
  • a saturated aqueous sodium thiosulfate solution (3 ml) is added to the solution, and the mixture is stirred at room temperature for 2 hours.
  • the present invention relates to 2-amino-3-substituted pyridines such as 2,3-diaminopyridine and the like.
  • An industrially advantageous process for preparing the salts or solvates thereof is provided.
  • pharmaceuticals eg, CFM antibacterial agents
  • their raw materials can be industrially and efficiently produced.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pyridine Compounds (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

A process for producing a compound (II), characterized by reacting a compound (I) with ammonia in the presence of a catalyst. (In the formulae, X is halogeno; and R is an electron-donating substituent having the property of coordinating to the catalyst.)

Description

明細書  Specification
2—アミノー 3—置換ピリジンの製造方法 技術分野  Method for producing 2-amino-3-substituted pyridine
本発明は、 セフエム系抗菌剤やイ ミダゾピリジン等の合成中間体、 または有機 金属錯体のリガン ド等の医薬原料として有用な 2—ァミノー 3—置換ピリ ジン (例 : 2 , 3—ジアミノピリジン) 及びその塩の製造法に関する。 背景技術 ,  The present invention relates to 2-amimino 3-substituted pyridines (eg, 2,3-diaminopyridine) useful as synthetic intermediates such as cefm antibacterial agents and imidazopyridines, or as pharmaceutical raw materials such as organometallic complex ligands. It relates to a method for producing the salt. Background Art,
2—ァミノ一 3—置換ピリジンと して、 例えば 2, 3—ジァミノピリジンは、 セフヱム系抗菌剤の 3位側鎖原料として記載されている (例 : 特許文献 1 ) 。  As a 2-amino-3-substituted pyridine, for example, 2,3-diaminopyridine is described as a raw material of the 3-position side chain of a septum antibacterial agent (eg, Patent Document 1).
2 , 3—ジァミノピリジンの典型的な製法は、 2—アミノビリジンを出発原料 に用いて 4工程で合成する方法が記載されている (例 :非特許文献 1 ) 。 しかし、 該製法では、 反応試薬として臭素や鉄等の金属を使用するので環境や安全面で望 ま しくなく、 収率も 2 6 %と低いため、 工業的製法として満足のいく方法ではな い。 また、 3—エトキシカルポニルアミノー 2—二トロピリジンを出發原料とす る製法では、 発癌性が懸念されるニッケル金属を使用している (例 : 非特許文献 2 ) 。 また 2, 3—ジァミノピリジンは、 水と有機溶媒との双方に可溶であるた め反応後、 抽出を行なうには通常、 大量の有機溶媒が必要である。 また、 再結晶 法において、 有害なベンゼンを使用して精製され、 環境上好ましくない (例 : 非 特許文献 1、 2 ) 。  As a typical production method of 2,3-diaminopyridine, a method of synthesizing in four steps using 2-aminoviridine as a starting material is described (eg, Non-Patent Document 1). However, this method uses metals such as bromine and iron as reaction reagents, which is not desirable in terms of environment and safety, and the yield is as low as 26%, which is not a satisfactory method as an industrial method. . Further, in a production method using 3-ethoxycarbonylamino-2-nitropyridine as a starting material, nickel metal, which is concerned with carcinogenicity, is used (eg, Non-Patent Document 2). Since 2,3-diaminopyridine is soluble in both water and organic solvents, extraction after the reaction usually requires a large amount of organic solvent. In addition, in the recrystallization method, it is purified using harmful benzene, which is environmentally unfavorable (eg, Non-Patent Documents 1 and 2).
2 , 3—ジァミノピリジンを酸付加塩として単離する方法として、 2—ァミノ —5—ブロモ一3—ニトロピリジンをパラジウム還元した後、 2 , 3—ジァミノ ピリジンを 2臭化水素酸塩と して単離精製する方法が知られている (例 : 特許文 献 2 ) 。 しかし、 該精製法では、 反応液を濃縮後のスラ リー液へ有機溶媒を加え て結晶化しており、 精製操作が煩雑で大量生産法としては好ましくない。  As a method of isolating 2,3-diaminopyridine as an acid addition salt, palladium reduction of 2-amino-5-bromo-3-nitropyridine is performed, and then 2,3-diaminopyridine is converted to dihydrobromide. Methods for isolation and purification are known (eg, Patent Document 2). However, in this purification method, the reaction solution is crystallized by adding an organic solvent to the concentrated slurry solution, and the purification operation is complicated, which is not preferable as a mass production method.
銅触媒を用いたアミノビリジン誘導体の合成法としては、 ブロモピリジンとァ ンモニァとのアミノ化反応が知られている (例 : 非特許文献 3 ) 。 しかし、 当該 反応条件では、 ブロモピリジンより不活性なクロ口ピリジンとのァミノ化反応に は成功していない。 該反応においては、 例えばクロ口基の反応性を高める電子吸 引性の置換基を有する 2—クロ口一 5—二トロピリジンの場合には、 アミノビリ ジン誘導体が製造されているが、 ク口口基の反応性を弱める電子供与性の置換基 を有するアミノクロロピリジンとのアミノ化反応は記載されていない。 又、 反応 触媒として用いた水質汚濁の危険性のある水溶性銅触媒の除去方法についても記 載されていない。 As a method for synthesizing an aminoviridine derivative using a copper catalyst, an amination reaction between bromopyridine and ammonia is known (eg, Non-Patent Document 3). However, Under the reaction conditions, the amination reaction with chloro-open pyridine, which is more inert than bromopyridine, has not been successful. In this reaction, for example, in the case of 2-chloro-1-5-nitropyridine having an electron-withdrawing substituent that enhances the reactivity of the chromatol group, an aminoviridine derivative is produced. No amination reaction with an aminochloropyridine having an electron donating substituent which weakens the reactivity of the group is described. Also, there is no description of a method for removing a water-soluble copper catalyst which has a risk of water pollution used as a reaction catalyst.
(特許文献 1 ) 国際公開第 0 0 / 3 2 6 0 6号公報  (Patent Document 1) International Publication No. 0/3 2 6 06
(特許文献 2 ) 特開平 0 5— 3 3 9 2 3 6 ,  (Patent Document 2) Japanese Patent Application Laid-Open No. 05-33 39 2 36,
(非特許文献 1 )バーハム (W.E.Barham)、 オルガニックシンテシス(Org. Syn), 米国、 第 44卷、 P 34—39 (1964)  (Non-Patent Document 1) Barham (W.E.Barham), Organic Synthesis (Org. Syn), USA, Vol. 44, P 34-39 (1964)
(非特許文献 2 ) クラークレゥイス(J. W. Cl ark— Lewins)ら、 ジャーナルォブザケ ミカルソサイァティ(J. Cheni. Soc . ) 英国、 P442— 447( 1957)  (Non-Patent Document 2) J. W. Clark—Lewins, et al., J. Cheni. Soc., UK, P442—447 (1957)
(非特許文献 3 ) ラング(F . Lang)ら、 テトラへドロンレ夕一ズ(Tett. Lett )、 米国、 第 42卷、 P3251— 3254(2001 ) 発明の開示  (Non-Patent Document 3) Lang et al., Tett. Lett, USA, Vol. 42, P3251-3254 (2001) Disclosure of the invention
(発明が解決しょうとする課題)  (Problems to be solved by the invention)
よって、 2 , 3—ジァミノピリジン及びその塩の工業的に有用な新規製法の開 発が要望されていた。 またその他の 2—アミノー 3—置換ピリジンの新規製法の 開発も要望されていた。  Therefore, there has been a demand for the development of a new industrially useful method for producing 2,3-diaminopyridine and salts thereof. There was also a demand for the development of new methods for producing other 2-amino-3-substituted pyridines.
(課題を解決するための手段)  (Means for solving the problem)
本発明者らは鋭意検討した結果、 2—ハロゲノー 3—置換ピリジン、 好ましく は公知物質で入手容易な 3—ァミノー 2—クロ口ピリジン等に触媒 (例 : C u C 1 ) 存在下、 アンモニアを反応させれば、 短工程でしかも緩和な条件で、 2—ァ ミノ一 3—置換ピリジン、 好ましくは 2、 3—ジァミノピリジンが効率良く製造 されることを見出した。 又、 反応混合物から回収が困難であった銅は、 硫化化合 物 (例 : チォ硫酸ナト リウム) で処理することにより容易に除去可能となった。 また、 2、 3—ジァミノピリジンを安息香酸塩として単離することにより、 収率 良く製造できた。 本発明を以下に示す。 As a result of intensive studies, the present inventors have found that ammonia is added to a 2-halogeno 3-substituted pyridine, preferably 3-amine chloro-2-pyridine, which is easily available as a known substance, in the presence of a catalyst (eg, CuCl). It has been found that 2-amino-1-substituted pyridine, preferably 2,3-diaminopyridine, can be efficiently produced in a short step and under mild conditions by the reaction. Copper, which was difficult to recover from the reaction mixture, could be easily removed by treating it with a sulfide compound (eg, sodium thiosulfate). In addition, by isolating 2,3-diaminopyridine as a benzoate, it was possible to produce it in good yield. The present invention is described below.
( 1 ) 式 ( 1 set
(I) (I)
、N八 X  , N eight X
(式中、 Xはハロゲン; Rは、 電子供与性でありかつ触媒に配位性を示す置換基) で示される化合物 (I ) を、 触媒存在下、 アンモニアと反応させることを特徴と する、 式:
Figure imgf000005_0001
(Wherein, X is a halogen; R is a substituent that is electron-donating and has a coordination property to a catalyst), wherein the compound (I) is reacted with ammonia in the presence of a catalyst. formula:
Figure imgf000005_0001
(式中、 Rは前記と同意義) で示される化合物 (II) 、 その塩、 またはそれらの 溶媒和物の製造方法。  (Wherein R is as defined above), a method for producing the compound (II), a salt thereof, or a solvate thereof.
(2 ) Rが、 電子供与性の置換基でありかつピリジン環と結合している R中の原 子が触媒に配位性を示すヘテロ原子である、 上記 1記載の製造方法。  (2) The production method according to the above (1), wherein R is an electron-donating substituent and the atom in R bonded to the pyridine ring is a heteroatom showing coordination to the catalyst.
(3 ) が、 置換されていてもよいァミノ、 置換されていてもよいヒドロキシま たは置換されていてもよいチオールである、 上記 1記載の製造方法。  2. The production method according to the above 1, wherein (3) is an optionally substituted amino, an optionally substituted hydroxy or an optionally substituted thiol.
(4) Rが NHR 1 N (R 1) 2、 OH、 0 R J s NH CO CH3、 S R 1 (式中、 R 1はアルキル) である、 上記 1記載の製造方法。 (4) R is NHR 1 N (R 1) 2 , OH, 0 R J s NH CO CH 3, SR 1 ( wherein, R 1 is alkyl), a manufacturing method of claim 1, wherein the.
( 5 ) Rが NH2である、 上記 1記載の製造方法。 (5) The production method according to the above 1, wherein R is NH 2 .
( 6 ) Xが C 1である、 上記 1記載の製造方法。  (6) The production method according to the above (1), wherein X is C1.
( 7 ) 触媒が金属含有触媒である、 上記 1記載の製造方法。  (7) The production method according to the above (1), wherein the catalyst is a metal-containing catalyst.
( 8 ) 金属含有触媒が銅を含む、 上記 1記載の製造方法。  (8) The production method according to the above (1), wherein the metal-containing catalyst contains copper.
( 9 ) 金属含有触媒が銅塩、 銅酸化物または金属銅である、 上記 1記載の製造方 法。  (9) The production method according to (1) above, wherein the metal-containing catalyst is a copper salt, a copper oxide or copper metal.
( 1 0 ) 金属含有触媒が銅塩である、 上記 1記載の製造方法。 ( 1 1 ) 銅塩がハロゲン化銅である、 上記 1 0記載の製造方法。(10) The production method according to the above 1, wherein the metal-containing catalyst is a copper salt. (11) The production method according to the above item 10, wherein the copper salt is a copper halide.
β Λ  β Λ
( 1 2)同ハロゲン化銅が Cu C 1である、 上記 1 1記載の製造方法。  (12) The production method according to the above (11), wherein the copper halide is CuC1.
( 1 3) Rが NH2 ;金属含有触媒が銅含有触媒である、 上記 1記載の製造方法。(13) The production method according to (1) above, wherein R is NH 2 ; and the metal-containing catalyst is a copper-containing catalyst.
( 1 4) アンモニアをアンモニア水溶液として反応させる、 上記 1記載の製造方 法。 (14) The production method according to the above (1), wherein the ammonia is reacted as an aqueous ammonia solution.
( 1 5) アンモニア水溶液の濃度が 2 0〜 3 0 %である、 上記 1 4記載の製造方 法。  (15) The production method according to the above (14), wherein the concentration of the aqueous ammonia solution is 20 to 30%.
( 1 6) 反応温度が 1 1 0〜 1 6 0 °Cである、 上記 1記載の製造方法。  (16) The production method according to the above (1), wherein the reaction temperature is 110 to 160 ° C.
( 1 7) 反応混合物を、 硫化化合物で処理することにより、 銅を 去する工程を 包含する、 上記 8 ~ 1 3のいずれかに記載の製造方法。  (17) The production method according to any one of the above items 8 to 13, comprising a step of removing copper by treating the reaction mixture with a sulfide compound.
( 1 8) Rが N H 2であり、 反応後、 生成した 2, 3—ジァミノピリ ジンを安息 香酸塩として単離する工程を包含する、 上記 1〜 1 7のいずれかに記載の製造方 法。 (18) The method according to any one of (1) to (17) above, wherein R is NH 2 , and the method comprises a step of isolating the produced 2,3-diaminopyridine as a benzoate after the reaction. .
( 1 9 ) 2 , 3—ジァミノピリジンの安息香酸塩。  (19) Benzoic acid salt of 2,3-diaminopyridine.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
本発明についてさらに詳細に説明する。  The present invention will be described in more detail.
本発明の製法は、 以下の 3工程から構成または選択される。 The production method of the present invention is constituted or selected from the following three steps.
第 1工程 触媒 Step 1 Catalyst
アンモニア ammonia
Figure imgf000006_0001
Figure imgf000006_0001
(I) (ID  (I) (ID
第 2工程 2nd step
1) 酸  1) acid
硫化銅  Copper sulfide
2) 硫化化合物 第 3工程
Figure imgf000007_0001
2) Sulfur compound 3rd step
Figure imgf000007_0001
(Rは前記と同意義、 好ま しくは NH2である) 第 1工程は、 3—置換一 2—ハロゲノビリジン ( I ) とアンモニアとを触媒、 好ましくは銅触媒存在下に反応させて 2—ァミノ一 3—置換ピリジン ( 1 1 ) 、 好ましくは 2 , 3—ジァミノピリジンを製造する方法である。 (R is as defined above, preferably NH 2. ) The first step is to react the 3-substituted 1-2-halogenobilizine (I) with ammonia in the presence of a catalyst, preferably a copper catalyst, to form 2- This is a method for producing an amino-3-substituted pyridine (11), preferably 2,3-diaminopyridine.
第 2工程は、 第 1工程の反応混合物から銅を硫化化合物で処理することにより 除去する方法である。  The second step is a method of removing copper from the reaction mixture of the first step by treating it with a sulfide compound.
第 3工程は、 銅を除いた反応液から 2—アミノー 3—置換ピリジン ( I I ) 、 好ましくは 2, 3—ジアミノピリジンを難水溶性塩として単離する方法及び単離 した塩を塩基処理して高品質の 2—アミノー 3—置換ピリジン ( I I ) 、 好ま し くは 2 , 3—ジァミノピリジンを製造する方法である。 反応条件の説明  In the third step, a method of isolating 2-amino-3-substituted pyridine (II), preferably 2,3-diaminopyridine as a poorly water-soluble salt from the reaction solution from which copper has been removed, and treating the isolated salt with a base. High-quality 2-amino-3-substituted pyridines (II), preferably 2,3-diaminopyridines. Description of reaction conditions
(第 1工程)  (First step)
第 1工程は、 触媒存在下、 化合物 ( I ) とアンモニアとを反応させて 2—アミ ノ一 3—置換ピリジン ( I I ) 、 好ましくは 2, 3—ジァミノピリジンを製造す る方法である。  The first step is a method of reacting compound (I) with ammonia in the presence of a catalyst to produce 2-amino-1-substituted pyridine (II), preferably 2,3-diaminopyridine.
本明細書中において、 ハロゲンは、 フッ素、 塩素、 臭素及びヨウ素を包含する c 特に塩素が好ましい。 In the present specification, the halogen is preferably c including fluorine, chlorine, bromine and iodine, and particularly preferably chlorine.
触媒は、 好ましくはコバルト、 錫、 亜鉛、 鉄、 アルミニウム、 ホウ素、 銅、 チ 夕ン、 砒素、 タリウム、 ニッケル、 クロム、 ロジウム、 イ リジウム、 白金、 パラ ジゥム等の金属を含有する触媒 (以下、 金属含有触媒という) が例示される。 該 金属は好ましくは化合物 ( I ) のピリジンの N原子および Rに配位性を示す金属 である。 該触媒は、 好ましくは銅を含む触媒 (以下、 銅触媒という) である。 銅触媒としては、 例えば銅塩、 銅酸化物、 金属銅及びそれらの混合物があげら れ、 更に銅塩、 銅酸化物、 金属銅又はそれらの混合物及び有機塩基からなる錯塩 があげられる。 銅塩としては、 塩化第一銅、 臭化第一銅、 塩化第二銅、 臭化第二 銅、 無水硝酸第二銅、 硝酸第二銅七水和物、 無水硫酸銅及び硫酸銅五水和物等が あげられる。 酸化銅としては、 酸化第一銅、 酸化第二銅等が挙げられる。 好ま し くは銅塩、 特に好ましくはハロゲン化銅、 例えば塩化第一銅 (C u C 1 ) である。 これらの銅触媒は単独または 2種類以上を混合して使用することができる。 銅 触媒の使用量は、 化合物 ( I ) に対して通常 0 . 0 0 1〜 5当量の範囲であり、 好ましくは 0 . 0 1 ~ 0 . 5当量、 特に好ましくは 0 . 1〜 0 . 4当量である。 The catalyst is preferably a catalyst containing a metal such as cobalt, tin, zinc, iron, aluminum, boron, copper, titanium, arsenic, thallium, nickel, chromium, rhodium, iridium, platinum, palladium, etc. A metal-containing catalyst). The metal is preferably a metal exhibiting a coordination property to the N atom and R of pyridine of the compound (I). The catalyst is preferably a catalyst containing copper (hereinafter, referred to as a copper catalyst). The copper catalyst includes, for example, copper salts, copper oxides, metallic copper and mixtures thereof, and further includes complex salts composed of copper salts, copper oxides, metallic copper or mixtures thereof and organic bases. Copper salts include cuprous chloride, cuprous bromide, cupric chloride, cupric bromide, anhydrous cupric nitrate, cupric nitrate heptahydrate, anhydrous copper sulfate and copper sulfate pentahydrate Japanese products. Examples of copper oxide include cuprous oxide and cupric oxide. Preference is given to copper salts, particularly preferably copper halides, such as cuprous chloride (CuCl). These copper catalysts can be used alone or in combination of two or more. The amount of the copper catalyst to be used is generally in the range of 0.01 to 5 equivalents, preferably 0.01 to 0.5 equivalents, particularly preferably 0.1 to 0.4 equivalents, relative to compound (I). Is equivalent.
本反応は、 好ましくはアンモニア水溶液中で行われるが、 極性溶媒中で行われ ても良いし、 有機塩基を反応液中に加えても良い。  This reaction is preferably performed in an aqueous ammonia solution, but may be performed in a polar solvent or an organic base may be added to the reaction solution.
アミノ化反応に使用するアンモニアとしては、 アンモニゥムアセテート、 アン モニゥムピカルポネート、 アンモニゥムベンゾエート、 アンモニゥムカルボネー ト、 アンモニゥムホルメート、 アンモニゥムオギザレート、 アンモニア水溶液及 び液体アンモニア等である。 アンモニアとして好ましくは、 1 ~ 5 0 %濃度のァ ンモニァ水、 特に好ましくは 2 0 ~ 3 0 %濃度のアンモニア水溶液である。  Ammonia used in the amination reaction includes ammonium acetate, ammonium picocarbonate, ammonium benzoate, ammonium carbonate, ammonium formate, ammonia oxalate, aqueous ammonia, and the like. And liquid ammonia. The ammonia is preferably ammonia water having a concentration of 1 to 50%, particularly preferably an aqueous ammonia solution having a concentration of 20 to 30%.
アンモニアの使用量は、 化合物 ( I ) に対して通常、 1〜 1 0 0当量であり、 好ましくは 2 ~ 5 0当量、 特に好ましくは 3〜3 0当量である。  The amount of ammonia to be used is generally 1 to 100 equivalents, preferably 2 to 50 equivalents, particularly preferably 3 to 30 equivalents, relative to compound (I).
極性溶媒としては、 1一メチル一2—ピロ リジノン等の環状アミ ド類、 1 , 3 —ジメチル一 2—イ ミダゾリジノン等の環状ウレァ類、 ジメチルスルホキシド等 のスルホキシド類、 ジメチルスルホン及ぴスルホラン等のスルホン類、 ジェチレ ングリコールジメチルエーテル、 ジエチレングリコールジェチルエーテル、 ト リ ェチレングリコールジメチルエーテル及びポリェチレングリコールジメチルエー テル等のエチレングリコールジアルキルエーテル類、 1, 4一ジォキサン等のェ —テル類、 N , N—ジメチルァニリ ン及び N , N—ジェチルァニリン等のジアル キルァニリ ン類、 ピリジン及びキノ リン等のへテロ環化合物類、 メタノール、 ェ 夕ノール、 プロパノール、 2—プロパノール、 エチレングリコール、 プロピレン グリコール、 グリセリン等のアルコール類及び水等があげられる。 これらの極性 溶媒は単独、 も しくは 2種類以上を混合して使用することができる。 溶媒量は、 化合物 (I) l gに対して通常、 1 m 1 ~ 1 0 0 m 1程度である。 Examples of the polar solvent include cyclic amides such as 1-methyl-1-pyrrolidinone, cyclic ureas such as 1,3-dimethyl-12-imidazolidinone, sulfoxides such as dimethyl sulfoxide, and dimethyl sulfone and sulfolane. Sulfones, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, ethylene glycol dialkyl ethers such as triethylene glycol dimethyl ether and polyethylene glycol dimethyl ether, ethers such as 1,4-dioxane, N, N —Dialkyl anilines such as dimethyl aniline and N, N-Jetyl aniline; heterocyclic compounds such as pyridine and quinoline; methanol, ethanol, propanol, 2-propanol, ethylene glycol, propylene glycol, Alcohols such as glycerin and water, and the like. These polarities The solvents can be used alone or as a mixture of two or more. The amount of the solvent is usually about 1 ml to 100 ml with respect to the compound (I) lg.
有機塩基としては、 ピリジン、 メチルピリジン、 ェチルピリジン、 ジメチルビ リジン、 メチルェチルピリジン、 ジェチルビリジン、 ト リメチルピリジン、 ジメ チルアミノピリジン及び 2, 2—ビピリジル等のピリジン類、 ト リェチルアミン、 ト リプロピルアミン及びト リブチルァミン等のト リアルキルアミン類、 N, N— ジメチルァニリン及び N, N—ジェチルァニリン等の N, N—ジアルキルァニリ ン類及び液体アンモニア等があげられる。  Examples of the organic base include pyridines such as pyridine, methylpyridine, ethylpyridine, dimethylpyridine, methylethylpyridine, getylviridine, pyridines such as trimethylpyridine, dimethylaminopyridine and 2,2-bipyridyl, triethylamine, tripropylamine and the like. Examples include trialkylamines such as tributylamine, N, N-dialkylanilines such as N, N-dimethylaniline and N, N-getylaniline, and liquid ammonia.
本反応は冷却下〜室温でも行われるが、 好ましくは、 加熱下で行なわれる。 好 ましい反応温度は、 通常 3 0 ~ 25 0。 より好ましくは 8 0〜 2 0 0 °C、 ^に 好ま しくは 1 1 0〜: L 6 0°Cである。  This reaction is carried out under cooling to room temperature, but is preferably carried out under heating. The preferred reaction temperature is usually 30 to 250. More preferably, the temperature is from 80 to 200 ° C, and preferably from 110 to: L60 ° C.
反応時間は、 通常数時間から数十時間である。  The reaction time is usually several hours to several tens of hours.
本反応は大気圧下で行われても良いが、 好ましくは密閉加圧装置内で行なわれ、 その内圧は通常 0. 1 ~ 1 0 MP a、 好ましぐは 0. l ~ 2MP a、 特に好ま し くは 0. ;!〜 0. 3 MP aである。  This reaction may be carried out under atmospheric pressure, but is preferably carried out in a closed pressurized apparatus, and the internal pressure is usually 0.1 to 10 MPa, preferably 0.1 to 2 MPa, particularly It is preferably 0;; to 0.3 MPa.
Rは、 電子供与性であり、 かつ上記触媒、 好ましくは触媒中の金属に配位性を 示す置換基であれば種々の置換基が例示される。 Rの好ましい態様においては、 ピリジン環と結合している原子が触媒中の金属に配位性を示すヘテロ原子である。 該ヘテロ原子は、 水素または炭素以外の原子から選択されるが、 好ましくは N、 0、 Sなどであり、 さらに好ましくは Nまたは 0であり、 特に好ましくは Nであ る。 該ヘテロ原子に結合する残基としては、 水素、 アルキル、 好ましくは C l〜 C 6アルキル (例 : メチル、 ェチル、 n—プロピル、 t一ブチル等) 、 低級アル キルカルボニル (例 : ァセチル、 ェチルカルボニル) などが例示される。  R is various substituents as long as it is an electron-donating substituent which exhibits coordination to the above-mentioned catalyst, preferably a metal in the catalyst. In a preferred embodiment of R, the atom bonded to the pyridine ring is a hetero atom that exhibits coordination to the metal in the catalyst. The heteroatom is selected from atoms other than hydrogen or carbon, but is preferably N, 0, S, etc., more preferably N or 0, and particularly preferably N. Examples of the residue bonded to the hetero atom include hydrogen, alkyl, preferably C1 to C6 alkyl (eg, methyl, ethyl, n-propyl, t-butyl, etc.), lower alkylcarbonyl (eg, acetyl, Carbonyl) and the like.
Rは好ましくは、 置換されていてもよいアミノ (例 :ァミノ、 NHR 1 N (R 2 (R1はアルキル) ) (例 : メチルァミノ、 ェチルァミノ、 ジメチルァミノ、 ジェチルァミノ) 、 低級アルキルカルボニルァミノ (例 : NHC O C H3 ) ) 、 置換されていてもよぃヒ ドロキシ (例: 0 H、 OR 1 (例 :メ トキシ、 ェトキシ) ) または置換されていてもよいチオール (例:チオール、 S R 1 (例:メチルチオ) ) である。 Rはより好ましくは、 置換されていてもよいァミノであり、 特に好まし くは N H 2である。 なお Rは電子供与性基であるので、 当然ながら例えばハロゲ ン、 ニトロ、 ハロゲン化メチル等は除外される。 R is preferably an optionally substituted amino (eg, amino, NHR 1 N (R 2 (R 1 is alkyl)) (eg, methylamino, ethylamino, dimethylamino, getylamino), lower alkylcarbonylamino (example: NHC OCH 3 )), optionally substituted hydroxy (eg, 0 H, OR 1 (eg, methoxy, ethoxy)) or optionally substituted thiol (eg, thiol, SR 1 (eg, Methylthio)) It is. R is more preferably an optionally substituted amino, particularly preferably NH 2 . Since R is an electron donating group, naturally, for example, halogen, nitro, methyl halide and the like are excluded.
原料である化合物 ( I ) は、 公知化合物 (例 : 3—ァミノー 2—クロロピリジ ン、 3—ヒド口キシー 2—クロロピリジン、 3—メ トキシー 2—クロロピリジン) であるか、 またはこれらを含む公知化合物より容易に合成可能である。  The compound (I) as a raw material is a known compound (eg, 3-amino-2-chloropyridin, 3-hydroxy-2-chloropyridine, 3-methoxy-2-chloropyridine) or a known compound containing these. It can be easily synthesized from compounds.
なお、 ハロゲン原子の隣接部位等にアミノ等の電子供与性基が存在する場合、 一般的には、 ニトロ等の電子吸引性基が存在する場合に比べて、 ハロゲンか.らァ ミノ化への反応性は非常に低下する。 しかし、 本発明では、 触媒、 好ましくは金 属含有触媒を使用することにより、 緩和な反応条件で比較的収率よく反応が進行 することが分かった。 この反応機構の詳細は不明であるが、 1仮説としては、 以 下に例示されるように、 触媒中の金属 (例 :銅) などがピリジン環の N原子およ び 3位に結合しているへテロ原子 (例 : N ) に配位することにより、 2位ハロゲ ン (例 : C 1 ) の反応性が向上しているものと考えられる。  In addition, when an electron donating group such as amino is present at a site adjacent to a halogen atom, etc., generally, compared to the case where an electron withdrawing group such as nitro exists, the conversion from halogen to amination can be performed. Reactivity is greatly reduced. However, in the present invention, it has been found that the use of a catalyst, preferably a metal-containing catalyst, allows the reaction to proceed at a relatively high yield under mild reaction conditions. Although the details of this reaction mechanism are unknown, one hypothesis is that, as illustrated below, a metal (eg, copper) in the catalyst is bonded to the N atom and the 3-position of the pyridine ring. It is thought that the coordination to a heteroatom (eg, N) improves the reactivity of the 2-position halogen (eg, C 1).
Figure imgf000010_0001
よって、 ピリジン環の 3位置換基がアミノ以外の電子供与性基であつたとして も、 触媒が上記のように配位性を示すことにより、 本反応は同様に進行するもの と推測される。 なお、 本発明者らの実験によれば、 ο~クロロア二リン等では、 当 該ァミノ化反応が十分に進行しなかった。 このことは、 上記反応機構の可能性を 示唆するものである。
Figure imgf000010_0001
Therefore, even if the 3-position substituent on the pyridine ring is an electron-donating group other than amino, it is presumed that the reaction proceeds similarly when the catalyst exhibits coordination as described above. According to the experiments of the present inventors, the amination reaction did not sufficiently proceed with o-chloroaniline and the like. This suggests the possibility of the above reaction mechanism.
第 1工程後、 反応液を常法 (濃縮、 抽出、 分離等) により処理することにより 化合物 ( I I ) が得られる。 より高品質の化合物 ( I I ) を得るには、 好ましく は、 第 2、 3工程が行われる。 (第 2工程) After the first step, the compound (II) can be obtained by treating the reaction solution by a conventional method (concentration, extraction, separation, etc.). To obtain a higher quality compound (II), the second and third steps are preferably performed. (2nd step)
第 2工程は、 第 1工程の反応で銅触媒を使用した場合に所望により行われ、 反 応混合物から銅を硫化銅として除去する方法である。  The second step is optionally performed when a copper catalyst is used in the reaction of the first step, and is a method of removing copper from the reaction mixture as copper sulfide.
①本工程はまず、 反応混合物が酸性になるまで酸を加えるか、 反応混合物からァ ンモニァを留去した後、 残渣に酸を加えて酸性混合物とするか何れの方法でも良 い o  (1) In this step, either acid is added until the reaction mixture becomes acidic, or ammonia is distilled off from the reaction mixture, and then acid is added to the residue to form an acidic mixture.
酸としては、 有機酸、 無機酸何れの酸でもよいが、 好ましくは無機酸であり、 特に好ましくは硫酸である。 硫酸の濃度は約 1 0〜8 0 %であり、 好ましくは 5 0〜7 0 %である。 酸の使用量は、 例えば 64%硫酸ならば化合物 ( I ) 1 に 対して約 l m l〜 1 0 mlである。  The acid may be either an organic acid or an inorganic acid, but is preferably an inorganic acid, particularly preferably sulfuric acid. The concentration of sulfuric acid is about 10-80%, preferably 50-70%. The amount of the acid used is, for example, about 1 ml to 10 ml for compound (I) 1 in the case of 64% sulfuric acid.
酸を加える時の温度は通常 0〜5 0°C、 好ましくは 0〜2 5°Cである。  The temperature at which the acid is added is usually 0 to 50 ° C, preferably 0 to 25 ° C.
②次いで上記で調製した酸性混合物にチォ硫酸ナトリウム、 水硫化ナトリウム、 硫化ナトリウム、 硫化アンモニゥム、 硫化カリウム、 硫化リチウム及び硫化水素 等の硫化化合物を加え、 数時間攪拌し、 銅を硫化銅として析出させた後、 不溶物 を濾過する。  ② Then, sulfide compounds such as sodium thiosulfate, sodium hydrosulfide, sodium sulfide, ammonium sulfide, potassium sulfide, lithium sulfide and hydrogen sulfide are added to the acidic mixture prepared above, and stirred for several hours to precipitate copper as copper sulfide. After that, the insoluble matter is filtered.
硫化化合物として、 好ましくはチォ硫酸ナトリウム、 水硫化ナトリゥム及び硫 化水素、 特に好ましくはチォ硫酸ナトリウムである。 硫化化合物の使用量は、 例 えば飽和チォ硫酸ナトリゥム水溶液ならば化合物 ( 1 ) 1 gに対して約 1 m 1〜 1 5 m 1である。  As the sulfurized compound, sodium thiosulfate, sodium hydrosulfide and hydrogen sulfide are particularly preferred, and sodium thiosulfate is particularly preferred. The amount of the sulfide compound used is, for example, about 1 ml to 15 ml for 1 g of the compound (1) in the case of a saturated aqueous solution of sodium thiosulfate.
硫化化合物を加える時の温度は通常 0〜 40 °C、 好ましくは 1 0 ~ 3 0 °Cであ る。 攪拌時間は、 硫化銅の析出状態にもよるが、 通常 1 ~2 0時間である。 硫化 銅とは、 通常一価及び二価銅の硫化物を示すが、 金属銅及び硫黄を包含する場合 もある。  The temperature at which the sulfide compound is added is usually 0 to 40 ° C, preferably 10 to 30 ° C. The stirring time is usually 1 to 20 hours, depending on the state of copper sulfide precipitation. Copper sulfide usually refers to monovalent and divalent copper sulfides, but may include metallic copper and sulfur.
(第 3工程)  (3rd step)
第 3工程は、 2, 3—ジァミノピリジン等の化合物 ( I I ) の塩の製造、 およ びそれを利用した化合物 (I I ) の精製工程である。 以下、 2 , 3—ジアミノビ リジンを例に説明する。  The third step is a step of producing a salt of the compound (II) such as 2,3-diaminopyridine and a step of purifying the compound (II) using the salt. Hereinafter, 2,3-diaminopyridine is described as an example.
① 2, 3—ジァミノピリジンの塩の製造は、 まず好ましくは第 1工程の反応液、 より好ましくは第 2工程で調製した濾液に塩基を加えて、 好ましくは p H 8〜9 の溶液を調製する。 (1) The production of the salt of 2,3-diaminopyridine is preferably performed in the first step, More preferably, a base is added to the filtrate prepared in the second step to prepare a solution having a pH of preferably 8-9.
塩基としては、 有機塩基、 無機塩基何れでもよいが、 好ましくは無機塩基であ り、 特に好ましくは 3 0 ~ 5 0 %濃度の水酸化ナトリゥム水溶液である。  The base may be any of an organic base and an inorganic base, but is preferably an inorganic base, particularly preferably a 30 to 50% sodium hydroxide aqueous solution.
塩基の使用量は適量である。例えば塩基が 4 8 %水酸化ナトリゥム水溶液なら ば、 溶液が p H 8 ~ 9になるまで適量加える。  The base is used in an appropriate amount. For example, if the base is a 48% aqueous sodium hydroxide solution, add an appropriate amount until the solution has a pH of 8-9.
塩基を加える時の温度は通常 0 ~ 4 0 °Cである。  The temperature at which the base is added is usually 0 to 40 ° C.
②上記①で調製した溶液に 2 , 3—ジァミノピリジンと塩を形成し得る酸、 好ま しくは有機酸 (例 :安息香酸) を加え、 室温下数時間攪拌した後、 析出した 2, 3—ジァミノピリジンの酸付加塩を得る。  (2) An acid capable of forming a salt with 2,3-diaminopyridine, preferably an organic acid (eg, benzoic acid) is added to the solution prepared in (1) above, and the mixture is stirred at room temperature for several hours, and then precipitated 2,3-diaminopyridine To give an acid addition salt of
この酸付加塩は、 後記の通り脱塩処理して、 2, 3—ジァミノピリジンに変換 した後、 さらに別の塩に変換しても良い。  This acid addition salt may be subjected to desalting treatment as described later to convert it to 2,3-diaminopyridine, and then to another salt.
酸の使用量は、原料である 3—ァミノー 2—クロロピリジン 1当量に対して好 ましくは 0 . 6 ~ 1 0当量である。 特に好ましくは 0 . 8 ~ 1 . 4当量である。 上記塩の好ましい製造方法においては、 室温攪拌下、 約 1 0分〜数十時間、 好ま しくは数時間で結晶が析出する。 析出しない場合には、 例えば冷却下、 超音波処 理ゃ攪拌等の刺激を与えるか種結晶を加える等により結晶を析出させてもよい。 塩の結 は濾過性が良く溶媒 (例えば、 水) との分離が容易であるため製造過程 において操作性が良いという利点を有する。 更に、 常温常圧において塩の状態で は、 安定で高品質のものを得やすい。  The amount of the acid used is preferably 0.6 to 10 equivalents to 1 equivalent of the raw material 3-amino 2-chloropyridine. Particularly preferred is 0.8 to 1.4 equivalents. In a preferred method for producing the above salt, crystals are precipitated in about 10 minutes to several tens of hours, preferably several hours, at room temperature with stirring. When no precipitation occurs, the crystals may be precipitated by, for example, applying a stimulus such as ultrasonic treatment and stirring under cooling or adding a seed crystal. Salt binding has the advantage of good operability in the manufacturing process because of good filterability and easy separation from solvents (eg, water). Further, in a salt state at normal temperature and normal pressure, it is easy to obtain a stable and high quality product.
③ 2, 3—ジァミノピリジンは、 前記単離精製された酸付加塩、 好ましくは安息 香酸塩を塩基処理することにより得られる。  (3) 2,3-Diaminopyridine can be obtained by treating the isolated and purified acid addition salt, preferably benzoate, with a base.
塩基としては、 無機塩基及び有機塩基、 何れでも構わないが、 好ましくは無機 塩基である。 無機塩基としては、 水酸化ナトリウム、 水酸化カリウム、 水酸化力 ルシゥム、 炭酸ナトリウム、 炭酸水素ナトリゥム及び炭酸力リウム等である。 特 に好ましくは水酸化ナトリウムである。  The base may be any of an inorganic base and an organic base, but is preferably an inorganic base. Examples of the inorganic base include sodium hydroxide, potassium hydroxide, calcium hydroxide, sodium carbonate, sodium hydrogen carbonate, and lithium carbonate. Particularly preferred is sodium hydroxide.
2 , 3—ジアミノピリジンは、 例えば安息香酸の塩を水もしくは有機溶媒に懸 濁、 または有機溶媒 (例; メタノール、 エタノール、 クロ口ホルム、 ジクロロメ 夕ン及ぴ酢酸ェチル、 好ましくは酢酸ェチル) に溶解した後、 冷却下で水酸化ナ ト リ ウム等の塩基を加え、 数時間攪拌し製造される。 2,3-Diaminopyridine can be obtained, for example, by suspending a salt of benzoic acid in water or an organic solvent, or in an organic solvent (eg, methanol, ethanol, chloroform, dichloromethan). After dissolving in ethyl acetate and ethyl acetate (preferably ethyl acetate), a base such as sodium hydroxide is added under cooling, and the mixture is stirred for several hours to produce.
溶媒の量は、 塩 1 gに対して通常、 1 m l ~ 1 0 0 m l程度である。  The amount of the solvent is usually about 1 ml to 100 ml per 1 g of the salt.
塩基の量は、 塩 1当量に対して好ましくは 1〜 1 0当量である。  The amount of the base is preferably 1 to 10 equivalents to 1 equivalent of the salt.
反応温度は、 通常 0 ~ 4 0 °C、 好ましくは 0 ~ 3 0 °Cである。  The reaction temperature is generally 0 to 40 ° C, preferably 0 to 30 ° C.
攪拌時間は、 通常 1〜数十時間、 好ましくは 1〜 2時間である。  The stirring time is usually 1 to several tens hours, preferably 1 to 2 hours.
2 , 3—ジァミノピリジンは、 塩基処理溶液又はその濃縮溶液を例えばェ一テ ル類 (例 ; ジェチルエーテル、 ジイソプロピルエーテル、 メチル t一ブチルエー テル) 、 酢酸ェチル、 トルエン、 ァセ トニト リル、 アセ トン又はメチルイソブチ ルケトン等で希釈することにより、 いずれの場合も好ましくは結晶として単離す ることができる。  2,3-Diaminopyridine is obtained by treating a base-treated solution or a concentrated solution thereof with ethers (eg, dimethyl ether, diisopropyl ether, methyl tert-butyl ether), ethyl acetate, toluene, acetonitrile, and acetone. Alternatively, by diluting with methyl isobutyl ketone or the like, in any case, it can be preferably isolated as crystals.
有機塩又は無機塩が析出する場合もあるが、 小量の冷水で洗浄して除去できる。 再結晶の再には別途調製した種晶を投入すると更に効率良く 目的結晶が得ら れる。  Organic or inorganic salts may precipitate, but can be removed by washing with a small amount of cold water. When the seed crystal prepared separately is added to the recrystallization, the target crystal can be obtained more efficiently.
化合物 ( I I ) は、 任意の数の適当な有機溶媒または水と配位した溶媒和物で あっても良い。  Compound (II) may be a solvate coordinated with any number of suitable organic solvents or water.
④③で製造した化合物 ( Γ Ι ) は、 さらに定法により各種塩に変換することがで きる。 例えば安息香酸を含む含水溶媒で処理して安息香酸塩として結晶化するこ とができる。 The compound (で Ι) produced in ④③ can be further converted to various salts by standard methods. For example, it can be crystallized as a benzoate by treating with a hydrated solvent containing benzoic acid.
2 , 3—ジァミノピリジンの塩としては、 各種塩基との塩ならびに酸付加塩を あげることができる。 好ましくは、 酸付加塩であり、 例えば塩酸、 硫酸、 硝酸、 リン酸、 フッ化水素酸、 臭化水素酸、 過塩素酸及び炭酸等の無機酸の塩、 ギ酸、 酢酸、プロピオン酸、 ト リクロ口酢酸、 ト リフルォ口酢酸、 酒石酸、 乳酸、 ヒ ドロ キシ酢酸、 クェン酸、 フマール酸、 マレイン酸、 コハク酸、 シユウ酸、 マンデル 酸、 酪酸、 リンゴ酸、 安息香酸、 メタンスルホン酸、 ベンゼンスルホン酸及び p 一トルエンスルホン酸等の有機酸の塩、 オル二チン、 ァスパラギン酸及びグルタ ミン酸等の酸性アミノ酸の塩等を挙げることができる。 以下に実施例を記載し、 本発明をさらに詳細に説明するが、 これらは本発明の 限定を意図するものではない。 実施例 1 Examples of the salts of 2,3-diaminopyridine include salts with various bases and acid addition salts. Preferred are acid addition salts, for example, salts of inorganic acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, hydrofluoric acid, hydrobromic acid, perchloric acid and carbonic acid, formic acid, acetic acid, propionic acid, and trichloroacetic acid. Mouth acetic acid, trifluoro acetic acid, tartaric acid, lactic acid, hydroxyacetic acid, cunic acid, fumaric acid, maleic acid, succinic acid, oxalic acid, mandelic acid, butyric acid, malic acid, benzoic acid, methanesulfonic acid, benzenesulfonic acid And salts of organic acids such as p-toluenesulfonic acid, and salts of acidic amino acids such as ordinine, aspartic acid and glutamic acid. Hereinafter, the present invention will be described in more detail with reference to Examples, but these are not intended to limit the present invention. Example 1
2 , 3—ジァミノピリジン安息香酸塩の合成  Synthesis of 2,3-diaminopyridine benzoate
1 ) 3ーァミノー 2—クロ口ピリ ジン ( I ) から 2, 3ージアミ ノ ビ リ ジン ( I I ) の合成  1) Synthesis of 2,3-diaminobilizine (II) from 3-aminopurine 2-pyridine (I)
耐圧反応チューブ (密閉加圧装置) に 3—ァミノ一 2—クロ口ピリジン (I ) 512mg(4mmol)、 25%ア ンモニア水溶液(5ml)を入れ、 塩ィ匕銅 ( CuCl ) 120mg(1.2nmiol)を加える。 油浴温度 1 2 0 °Cにて 8時間加熱攪拌後、 室温に冷 却、 ー晚放置する。  In a pressure-resistant reaction tube (closed pressurized device), put 3-amino-2-cyclomouth pyridine (I) 512 mg (4 mmol) and a 25% aqueous ammonia solution (5 ml), and add 120 mg (1.2 nmol) of salted copper (CuCl) Add. After heating and stirring at an oil bath temperature of 120 ° C for 8 hours, cool to room temperature, and leave it at room temperature.
2 ) 銅の除去操作  2) Copper removal operation
上記反応混合物中のアンモニア水を減圧下留去し、 残渣は 6 4%硫酸水溶液 (4ml)に溶解する。 その溶液に飽和チォ硫酸ナト リウム水溶液(3ml)を加え、 室温 下 2時間攪拌する。 硫化銅、 硫黄を含む茶褐色固体が析出するので、 これを濾去 すると赤褐色透明溶液が得られる。  The aqueous ammonia in the above reaction mixture was distilled off under reduced pressure, and the residue was dissolved in a 64% aqueous sulfuric acid solution (4 ml). A saturated aqueous sodium thiosulfate solution (3 ml) is added to the solution, and the mixture is stirred at room temperature for 2 hours. A brown solid containing copper sulfide and sulfur precipitates, and this is filtered off to obtain a reddish brown transparent solution.
3 ) 2, 3—ジァミノピリジン安息香酸塩  3) 2,3-diaminopyridine benzoate
上記赤褐色透明溶液に 48 %水酸化ナト リゥム水溶液を加え、 pH8〜 9にす る。 この溶液に、 メタノール (0.9ml)に溶解した安息香酸(488mg,4mmol)を加え、 室温下 2時間攪拌すると黒茶色の固体が析出する。濾取した固体を冷水で洗浄し、 乾燥後、 2, 3—ジァミノピリジン安息香酸塩を 576mg (収率 64%) 得る。 . iHDNMR (3 0 0MH z , C D 30 D , p p m) δ: 6. 58 (d d, J= 6 , 7. 5 H z , 1 H) , 6. 9 7 (d d, J= 1. 2, 7. 5 H z , 2 H) , 7. 1 7 ( d d , J= 1. 2 , 6 H z , 2 H) , 7. 2 8— 7. 40 (m, 3 H) , 7. 8 7— 7. 9 0 (m, 2 H) 産業上の利用可能性 Add a 48% aqueous sodium hydroxide solution to the above reddish brown transparent solution to adjust the pH to 8-9. To this solution, benzoic acid (488 mg, 4 mmol) dissolved in methanol (0.9 ml) is added, and the mixture is stirred at room temperature for 2 hours to precipitate a black-brown solid. The solid collected by filtration is washed with cold water and dried to give 576 mg (64% yield) of 2,3-diaminopyridine benzoate. . IHDNMR (3 0 0MH z, CD 3 0 D, ppm) δ: 6. 58 (dd, J = 6, 7. 5 H z, 1 H), 6. 9 7 (dd, J = 1. 2, 7.5 Hz, 2H), 7.17 (dd, J = 1.2, 6Hz, 2H), 7.28-- 7.40 (m, 3H), 7.87 — 7.90 (m, 2 H) Industrial applicability
本発明は、 2 , 3—ジァミノピリジン等の 2—ァミノ一 3—置換ピリジン及び その塩またはそれらの溶媒和物の工業的に有利な製法を提供する。 本製法を利用 することにより、 医薬 (例 :セフエム系抗菌剤) またはその原料を工業的に効率 よく生産することができる。 The present invention relates to 2-amino-3-substituted pyridines such as 2,3-diaminopyridine and the like. An industrially advantageous process for preparing the salts or solvates thereof is provided. By using this production method, pharmaceuticals (eg, CFM antibacterial agents) or their raw materials can be industrially and efficiently produced.

Claims

請求の範囲 式:
Figure imgf000016_0001
Claim formula:
Figure imgf000016_0001
(式中、 Xはハロゲン; Rは、 電子供与性でありかつ触媒に配位性を示す置換基) で示される化合物 ( I ) を、 触媒存在下、 アンモニアと反応させることを特徴と する、 式:
Figure imgf000016_0002
(Wherein, X is a halogen; R is a substituent that is electron-donating and has a coordination property to the catalyst), wherein the compound (I) is reacted with ammonia in the presence of a catalyst. formula:
Figure imgf000016_0002
(式中、 Rは前記と同意義) で示される化合物 (II) 、 その塩、 またはそれらの 溶媒和物の製造方法。  (Wherein R is as defined above), a method for producing the compound (II), a salt thereof, or a solvate thereof.
2 . Rが、 電子供与性の置換基でありかつピリジン環と結合している R中の原子 が触媒に配位性を示すヘテロ原子である、 請求項 1記載の製造方法。  2. The production method according to claim 1, wherein R is an electron-donating substituent and the atom in R bonded to the pyridine ring is a heteroatom that exhibits coordination to the catalyst.
3 . Rが、 置換されていてもよいァミノ、 置換されていてもよいヒドロキシまた は置換されていてもよいチオールである、 請求項 1記載の製造方法。  3. The production method according to claim 1, wherein R is an optionally substituted amino, an optionally substituted hydroxy, or an optionally substituted thiol.
4. Rが NHR 1 N (R 1) 2、 O H、 O R NH C O C H3、 S R 1 (式中、4. R is NHR 1 N (R 1 ) 2 , OH, OR NH COCH 3 , SR 1 (where
R 1はアルキル) である、 請求項 1記載の製造方法。 The production method according to claim 1, wherein R 1 is alkyl).
5 . Rが NH2である、 請求項 1記載の製造方法。 5. R is NH 2, A process according to claim 1, wherein.
6. Xが C 1である、 請求項 1記載の製造方法。  6. The method according to claim 1, wherein X is C1.
7. 触媒が金属含有触媒である、 請求項 1記載の製造方法。  7. The production method according to claim 1, wherein the catalyst is a metal-containing catalyst.
8. 金属含有触媒が銅を含む、 請求項 1記載の製造方法。 8. The production method according to claim 1, wherein the metal-containing catalyst contains copper.
9. 金属含有触媒が銅塩、 銅酸化物または金属銅である、 請求項 1記載の製造方 法。  9. The method according to claim 1, wherein the metal-containing catalyst is a copper salt, a copper oxide, or copper metal.
1 0 . 金属含有触媒が銅塩である、 請求項 1記載の製造方法。  10. The production method according to claim 1, wherein the metal-containing catalyst is a copper salt.
1 1. 銅塩がハロゲン化銅である、 請求項 1 0記載の製造方法。 11. The production method according to claim 10, wherein the copper salt is a copper halide.
2. ハロゲン化銅が Cu C 1である、 請求項 1 1記載の製造方法。 2. The method according to claim 11, wherein the copper halide is CuC1.
3. Rが NH 2 ;金属含有触媒が銅含有触媒である、 請求項 1記載の製造方法。3. The production method according to claim 1, wherein R is NH 2 ; and the metal-containing catalyst is a copper-containing catalyst.
4. アンモニアをアンモニア水溶液として反応させる、 請求項 1記載の製造方 法 < 4. The method according to claim 1, wherein the ammonia is reacted as an aqueous ammonia solution.
5. アンモニア水溶液の濃度が 2 0〜 3 0 %である、 請求項 1 4記載の製造方  5. The method according to claim 14, wherein the concentration of the aqueous ammonia solution is 20 to 30%.
1 6. 反応温度が 1 1 0~ 1 6 0°Cである、 請求項 1記載の製造方法。 1 6. The production method according to claim 1, wherein the reaction temperature is 110 to 160 ° C.
1 7. 反応混合物を、 硫化化合物で処理することにより、 銅を除去する工程を包 含する、 請求項 8〜 1 3のいずれかに記載の製造方法。  17. The method according to any one of claims 8 to 13, further comprising a step of removing copper by treating the reaction mixture with a sulfide compound.
1 8. Rが NH2であり、 反応後、 生成した 2 , 3—ジアミノピリジンを安息香 酸塩として単離する工程を包含する、 請求項 1 ~ 1 7のいずれかに記載の製造方 法。 18. The production method according to any one of claims 1 to 17, wherein R is NH 2 , and the method comprises a step of isolating the generated 2,3-diaminopyridine as a benzoate after the reaction.
1 9. 2 , 3—ジァミノピリジンの安息香酸塩。  19.2 The benzoate of 2,3-diaminopyridine.
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DE102009022830A1 (en) 2008-10-24 2010-04-29 Jubilant Organosys Ltd. Preparing 2,3-diaminopyridine compounds, useful e.g. as intermediates to produce pharmaceutical compounds, comprises aminating 3-amino-2-halopyridine compounds with aqueous ammonia in the presence of catalyst, heating and extracting
DE102009022830B4 (en) * 2008-10-24 2013-07-04 Jubilant Organosys Ltd. Improved process for producing diaminopyridines

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