JP2005336073A - Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine - Google Patents

Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine Download PDF

Info

Publication number
JP2005336073A
JP2005336073A JP2004154684A JP2004154684A JP2005336073A JP 2005336073 A JP2005336073 A JP 2005336073A JP 2004154684 A JP2004154684 A JP 2004154684A JP 2004154684 A JP2004154684 A JP 2004154684A JP 2005336073 A JP2005336073 A JP 2005336073A
Authority
JP
Japan
Prior art keywords
methylthiopyrimidine
ethoxycarbonyl
reaction
chloro
purity
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
JP2004154684A
Other languages
Japanese (ja)
Inventor
Nobumasa Makihara
伸征 牧原
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.)
Air Water Inc
Original Assignee
Air Water Chemical Inc
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 Air Water Chemical Inc filed Critical Air Water Chemical Inc
Priority to JP2004154684A priority Critical patent/JP2005336073A/en
Publication of JP2005336073A publication Critical patent/JP2005336073A/en
Pending legal-status Critical Current

Links

Landscapes

  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for efficiently producing a high-purity 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine useful as an intermediate for pharmaceuticals. <P>SOLUTION: The method comprises chlorinating 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine with phosphorus oxychloride at 10-90°C, quenching the resultant reaction mixture with ice water to deposit the objective 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine in the form of a solid followed by isolating it. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、医薬品の中間体として有用な4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンを工業的に有利に取得する方法に関する。   The present invention relates to a method for industrially advantageously obtaining 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine which is useful as an intermediate of a pharmaceutical product.

5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジンを塩化チオニル又はオキシ塩化リンによりクロル化して4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンを製造する方法はすでに知られている。塩化チオニルを使用する方法においては、還流条件下、すなわち79℃近辺における反応例が示されている(非特許文献1)。この報告において単離された生成物は、その融点が低く、純度が悪いものと想定され、そのためエタノール水から再結晶により精製しているが、この再結晶溶媒は、生成物の溶媒分解を起こすのであまり好ましいものではない。また本発明者が若干純度の低い原料を用いて追試したところでは、反応の進行が極めて遅く、収率よく目的物を得ることはできなかった。   A method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine by chlorinating 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine with thionyl chloride or phosphorus oxychloride is already known. In the method using thionyl chloride, a reaction example under reflux conditions, that is, around 79 ° C. is shown (Non-patent Document 1). The product isolated in this report is assumed to have a low melting point and poor purity and is therefore purified by recrystallization from ethanol water, but this recrystallization solvent causes solvolysis of the product. So it is not very preferable. In addition, when the present inventor made additional trials using raw materials of slightly low purity, the progress of the reaction was extremely slow, and the target product could not be obtained in good yield.

一方、オキシ塩化リンを使用する方法においても、還流条件下の反応(105℃近辺)が行なわれており、反応終了後は、過剰のオキシ塩化リンを減圧下に留去したのち、氷とエーテルを加え、エーテル層から目的物を単離する方法が採用されている(非特許文献2)。この場合、反応混合物に水を加えてクエンチすると、反応生成物は油状となるため、エーテルのような有機溶媒による抽出が必須であった。この方法は後処理工程が煩雑であり、また本発明者が追試したところでは、目的物の収率がそれほど高くなく、目的物の純度も高くないため、再結晶操作が必須であった。   On the other hand, in the method using phosphorus oxychloride, a reaction under reflux conditions (around 105 ° C.) is performed. After the reaction is completed, excess phosphorus oxychloride is distilled off under reduced pressure, and then ice and ether are used. And the method of isolating the target product from the ether layer is employed (Non-patent Document 2). In this case, when the reaction mixture was quenched by adding water, the reaction product became an oil, and extraction with an organic solvent such as ether was essential. In this method, the post-treatment process is complicated, and the inventor further made a recrystallization operation because the yield of the target product was not so high and the purity of the target product was not high.

ジャーナル オブ アメリカン ケミカル ソサイアティ(J. Am. Chem. Soc.)65巻、350〜354頁(1943年)J. Am. Chem. Soc. 65, 350-354 (1943) Journal of American Chemical Society キャンサー リサーチ(Cancer Research) 19巻、729〜730頁(1959年)Cancer Research Vol. 19, 729-730 (1959)

上記のごとく従来提案されている4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンの製造方法においては、反応収率が必ずしも高くなく、その上反応終了後の後処理工程が多いという欠点があった。そこで本発明者は、5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジンから反応収率が高く、かつ簡単な操作で純度の高い4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンを得るべく検討を行なった。その結果、オキシ塩化リンをクロル化剤兼溶媒として用い、一定の温度範囲で反応を行なった後、氷水でクエンチするという簡略化された方法を見出すに至った。   As described above, the conventionally proposed method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine has the disadvantage that the reaction yield is not necessarily high and that there are many post-treatment steps after completion of the reaction. It was. Therefore, the present inventor should obtain 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine having a high reaction yield and high purity by simple operation from 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine. A study was conducted. As a result, they have come to find a simplified method in which phosphorous oxychloride is used as a chlorinating agent and solvent and the reaction is carried out in a certain temperature range and then quenched with ice water.

すなわち本発明は、5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジンをオキシ塩化リン中でクロル化して得られる反応混合物を、氷水でクエンチした後、固体として単離することを特徴とする4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンの製造方法に関する。   That is, the present invention is characterized in that a reaction mixture obtained by chlorinating 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine in phosphorus oxychloride is isolated as a solid after being quenched with ice water. The present invention relates to a method for producing -chloro-5-ethoxycarbonyl-2-methylthiopyrimidine.

本発明によれば、簡単な操作で、高収率で高純度の4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンを取得することができる。また比較的純度の低い原料を用いてもかなり高い収率で4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンを製造することができる。   According to the present invention, 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine having a high yield and high purity can be obtained by a simple operation. Further, 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine can be produced with a considerably high yield even when a raw material having a relatively low purity is used.

本発明の原料として使用される5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジンは、いかなる方法によって合成されたものでもよい。例えば、2−メチル−2−イソチオ尿素とエトキシメチレンマロン酸ジエチルの反応によって得ることができる。原料としては純度が99%を超えるような高純度品を用いることが望ましいが、例えば純度が90〜99%程度のものであれば、反応収率も高く、また比較的高純度の生成物が容易に得られるので原料として充分使用することができる。またさらに純度の低い原料、例えば純度が80〜90%程度のものを使用してもかなりの収率で目的物を得ることができるが、その純度は高くないのでこの場合は目的物の再結晶操作が必要となる。   The 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine used as the raw material of the present invention may be synthesized by any method. For example, it can be obtained by the reaction of 2-methyl-2-isothiourea and diethyl ethoxymethylenemalonate. As a raw material, it is desirable to use a high-purity product having a purity exceeding 99%. For example, if the purity is about 90 to 99%, the reaction yield is high, and a relatively high-purity product is obtained. Since it can be easily obtained, it can be sufficiently used as a raw material. Further, even if a raw material having a lower purity, for example, a material having a purity of about 80 to 90% is used, the target product can be obtained in a considerable yield. Operation is required.

本発明において、5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジンのクロル化は、オキシ塩化リン(三塩化ホスホリル)を溶媒兼塩素化剤として使用して行なわれる。反応を円滑に進行させるためには、5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジン1モルに対し、オキシ塩化リンを3〜10モル、とくに5〜7モルの割合で使用するのが好ましい。   In the present invention, chlorination of 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine is carried out using phosphorus oxychloride (phosphoryl trichloride) as a solvent and chlorinating agent. In order to make the reaction proceed smoothly, it is preferable to use 3 to 10 moles, particularly 5 to 7 moles of phosphorus oxychloride with respect to 1 mole of 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine. .

反応は、10〜90℃、とくに20〜80℃の条件で行なうことが好ましい。すなわち反応温度が前記範囲を超えると、反応収率が低下し、また反応生成物が油状になるので本発明のような方法で目的物を単離することはできない。反応時間は、他の反応条件、例えば反応温度によっても異なるが、例えば2〜10時間程度である。   The reaction is preferably carried out under conditions of 10 to 90 ° C, particularly 20 to 80 ° C. That is, when the reaction temperature exceeds the above range, the reaction yield decreases and the reaction product becomes oily, so that the target product cannot be isolated by the method of the present invention. The reaction time varies depending on other reaction conditions, for example, the reaction temperature, but is, for example, about 2 to 10 hours.

反応終了後は、要すれば反応混合物を10℃以下に冷却し、これを氷水中に添加して、過剰のオキシ塩化リンを分解すると共に、反応混合物をクエンチする。必要に応じ、氷水によるクエンチに先立って、反応混合物中のオキシ塩化リンの一部を減圧下に除去しておいてもよい。氷水の添加量は、例えば反応混合物の2〜7重量倍程度とするのがよい。これによって目的物である4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンは水に懸濁した状態で得られるので、これを濾別することによりウェットケーキとして単離することができる。このようにして得られるウェットケーキは、そのままあるいは必要に応じ水洗した後、乾燥することによって目的物を得ることができる。一般にはこのようにして得られる4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンは、純度も高く、そのまま医薬品の中間原料として使用可能であるが、より一層純度を高めたい場合には、再結晶や分子蒸留などを施すことができる。   After completion of the reaction, if necessary, the reaction mixture is cooled to 10 ° C. or lower and added to ice water to decompose excess phosphorus oxychloride and quench the reaction mixture. If necessary, a part of the phosphorus oxychloride in the reaction mixture may be removed under reduced pressure prior to quenching with ice water. The amount of ice water added is preferably about 2 to 7 times the weight of the reaction mixture. As a result, 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine, which is the target product, is obtained in a state of being suspended in water, and can be isolated as a wet cake by filtration. The wet cake obtained in this manner can be used as it is or after being washed with water if necessary and then dried to obtain the desired product. In general, 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine thus obtained has high purity and can be used as an intermediate raw material for pharmaceuticals as it is. Crystals and molecular distillation can be applied.

以下、実施例により本発明をさらに詳細に説明する。   Hereinafter, the present invention will be described in more detail with reference to examples.

[実施例1]
反応容器に、2−メチル−2−イソチオ尿素とエトキシメチレンマロン酸ジエチルの反応によって得た純度94.8%の5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジン4.3g(0.019モル)及びオキシ塩化リン18.4g(0.12モル)を加え、30℃で5時間攪拌した。反応液を氷水150gに加え、析出した固体を濾過した。固体を水150gで洗浄し、減圧下で乾燥して、白色固体の4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジン3.8g(液体クロマトグラフィによる純度(面積百分率)98.1%、0.016モル、DSCによる融点63.2℃、単離収率84.2モル%)を得た。
[Example 1]
In a reaction vessel, 4.3 g (0.019 mol) of 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine having a purity of 94.8% obtained by the reaction of 2-methyl-2-isothiourea and diethyl ethoxymethylenemalonate was obtained. And 18.4 g (0.12 mol) of phosphorus oxychloride were added and stirred at 30 ° C. for 5 hours. The reaction solution was added to 150 g of ice water, and the precipitated solid was filtered. The solid was washed with 150 g of water and dried under reduced pressure to give 3.8 g of 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine as a white solid (purity by liquid chromatography (area percentage) 98.1%, 0.0. 016 mol, melting point 63.2 ° C. by DSC, isolated yield 84.2 mol%).

[実施例2]
反応容器に、同様な反応により得た純度86.6%の5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジン15.0g(0.061モル)及びオキシ塩化リン53.7g(0.35モル)を加え、80℃で4時間攪拌した。反応液を氷水150gに加え、析出した固体を濾過した。固体を水150gで洗浄し、減圧下で乾燥して、白色固体の4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジン10.4g(液体クロマトグラフィによる純度(面積百分率)98.3%、0.044モル、単離収率72.1モル%)を得た。
[Example 2]
In a reaction vessel, 15.0 g (0.061 mol) of 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine having a purity of 86.6% obtained by the same reaction and 53.7 g (0.35 mol) of phosphorus oxychloride were obtained. ) And stirred at 80 ° C. for 4 hours. The reaction solution was added to 150 g of ice water, and the precipitated solid was filtered. The solid was washed with 150 g of water, dried under reduced pressure, and 10.4 g of 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine as a white solid (purity (area percentage) by liquid chromatography 98.3%, 0.0. 044 mol, isolated yield 72.1 mol%).

[実施例3]
反応容器に、同様な反応により得た純度85.7%の5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジン15.0g(0.060モル)及びオキシ塩化リン53.7g(0.35モル)を加え、15℃で8時間攪拌した。反応液を氷水150gに加え、析出した固体を濾過した。固体を水150gで洗浄し、減圧下で乾燥して、白色固体の4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジン10.0g(液体クロマトグラフィによる純度(面積百分率)94.7%、0.041モル、単離収率68.3モル%)を得た。
[Example 3]
In a reaction vessel, 15.0 g (0.060 mol) of 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine having a purity of 85.7% obtained by the same reaction and 53.7 g (0.35 mol) of phosphorus oxychloride were obtained. ) And stirred at 15 ° C. for 8 hours. The reaction solution was added to 150 g of ice water, and the precipitated solid was filtered. The solid was washed with 150 g of water, dried under reduced pressure, and 10.0 g of white solid 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine (purity (area percentage) by liquid chromatography 94.7%, 0. 041 mol, isolated yield 68.3 mol%).

[比較例1]
反応容器に、同様な反応により得た純度99.7%の5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジン15.0g(0.070モル)及びオキシ塩化リン53.7g(0.35モル)を加え、還流条件下(105℃)で1時間攪拌した。反応液を0℃に冷やした水150gに加え、得られた油状物をエーテル75gに抽出した。エーテル層を分液後、飽和重曹水150g及び飽和食塩水150gで洗浄し、無水硫酸ナトリウムで乾燥した。エーテルを減圧下で除去して、白色固体の白色固体の4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジン7.45g(液体クロマトグラフィによる純度(面積百分率)92.4%、0.030モル、DSCによる融点62.9℃、単離収率42.8モル%)を得た。
[Comparative Example 1]
In a reaction vessel, 15.0 g (0.070 mol) of 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine having a purity of 99.7% obtained by the same reaction and 53.7 g (0.35 mol) of phosphorus oxychloride were obtained. ) And stirred under reflux conditions (105 ° C.) for 1 hour. The reaction mixture was added to 150 g of water cooled to 0 ° C., and the resulting oil was extracted into 75 g of ether. The ether layer was separated, washed with 150 g of saturated aqueous sodium bicarbonate and 150 g of saturated brine, and dried over anhydrous sodium sulfate. The ether was removed under reduced pressure to give 7.45 g of white solid 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine (purity by liquid chromatography (area percentage) 92.4%, 0.030 mol, DSC melting point 62.9 ° C., isolated yield 42.8 mol%).

Claims (2)

5−エトキシカルボニル−4−ヒドロキシ−2−メチルチオピリミジンをオキシ塩化リン中でクロル化して得られる反応混合物を、氷水でクエンチした後、固体として単離することを特徴とする4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンの製造方法。   A reaction mixture obtained by chlorinating 5-ethoxycarbonyl-4-hydroxy-2-methylthiopyrimidine in phosphorus oxychloride is quenched with ice water and then isolated as a solid. A method for producing ethoxycarbonyl-2-methylthiopyrimidine. クロル化反応を、10〜90℃の温度範囲で行なう請求項1記載の4−クロロ−5−エトキシカルボニル−2−メチルチオピリミジンの製造方法。   The method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine according to claim 1, wherein the chlorination reaction is carried out in a temperature range of 10 to 90 ° C.
JP2004154684A 2004-05-25 2004-05-25 Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine Pending JP2005336073A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004154684A JP2005336073A (en) 2004-05-25 2004-05-25 Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004154684A JP2005336073A (en) 2004-05-25 2004-05-25 Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine

Publications (1)

Publication Number Publication Date
JP2005336073A true JP2005336073A (en) 2005-12-08

Family

ID=35490034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004154684A Pending JP2005336073A (en) 2004-05-25 2004-05-25 Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine

Country Status (1)

Country Link
JP (1) JP2005336073A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439964A (en) * 2015-12-09 2016-03-30 河北大学 Preparation method of Avanafil intermediate

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004137270A (en) * 2002-09-26 2004-05-13 Nippon Nohyaku Co Ltd New herbicide, method for using the same, new substituted thienopyrimidine derivative, intermediate for the same and method for producing the same

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004137270A (en) * 2002-09-26 2004-05-13 Nippon Nohyaku Co Ltd New herbicide, method for using the same, new substituted thienopyrimidine derivative, intermediate for the same and method for producing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439964A (en) * 2015-12-09 2016-03-30 河北大学 Preparation method of Avanafil intermediate

Similar Documents

Publication Publication Date Title
JP2021504418A (en) Method for producing 2- (5-methoxyisochroman-1-yl) -4,5-dihydro-1H-imidazole and its hydrogen sulfate
WO2008078482A1 (en) Process for producing intermediate of asenapine synthesis
JP6340471B2 (en) Apixaban production method
CN103298783A (en) 2-(alkoxy or aryloxy carbonyl)-4-methyl-6-(2,6,6-trimethylcyclohex-1-enyl)hex-2-enoic acid compounds, its preparation and use
JP2012193125A (en) Method for producing 2,3-dichloropyridine
KR20230117260A (en) Process for the preparation of 1-(3,5-dichlorophenyl)-2,2,2-trifluoroethanone and derivatives thereof
JP2005336073A (en) Method for producing 4-chloro-5-ethoxycarbonyl-2-methylthiopyrimidine
JP4879907B2 (en) Process for producing phenyl 2-pyrimidinyl ketones and novel intermediates thereof
JP2017530997A (en) Process for preparing halo-substituted trifluoroacetophenones
WO2015012271A1 (en) Method for producing heterocyclic compound
JP5628015B2 (en) Method for producing high purity 4-tert-butylbenzenesulfonyl chloride
CN104030938A (en) Method for preparing propacetamol hydrochloride
JP6477187B2 (en) Process for producing 2-amino-6-methylnicotinic acid ester
KR101004133B1 (en) Process for production of an acetylenic compound
JP2010053073A (en) Method for producing halogenated isoquinolines
KR100654923B1 (en) Process for continuously preparing high purity chiral amide compound
JP4596804B2 (en) Method for producing cilazapril
JP6755775B2 (en) 4-Fluoroisoquinoline manufacturing method
KR101483977B1 (en) Process of preparing α-keto (cyanomethylene)triphenylphosphoranes using sulfonyl compounds
JP2005097158A (en) Method for producing fluorine-containing organic compound
JP6042153B2 (en) Olanzapine production method
JP4475901B2 (en) Method for producing 3-acetylthiophenes
JP2006076970A (en) Method for production of 4-chloro-2-(methylthio)pyrimidines
TWI460163B (en) A novel process for the preparation of roflumilast
JP2016065024A (en) Optical resolution method for carboxylic acid

Legal Events

Date Code Title Description
A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20060529

A621 Written request for application examination

Effective date: 20070507

Free format text: JAPANESE INTERMEDIATE CODE: A621

A131 Notification of reasons for refusal

Effective date: 20100817

Free format text: JAPANESE INTERMEDIATE CODE: A131

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20110104