JPS6119626B2 - - Google Patents
Info
- Publication number
- JPS6119626B2 JPS6119626B2 JP21552883A JP21552883A JPS6119626B2 JP S6119626 B2 JPS6119626 B2 JP S6119626B2 JP 21552883 A JP21552883 A JP 21552883A JP 21552883 A JP21552883 A JP 21552883A JP S6119626 B2 JPS6119626 B2 JP S6119626B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- methylpyrimidine
- parts
- amino
- pressure
- 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
Links
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 48
- 238000006243 chemical reaction Methods 0.000 claims description 26
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 claims description 18
- -1 formimidate Chemical compound 0.000 claims description 7
- JIHQDMXYYFUGFV-UHFFFAOYSA-N 1,3,5-triazine Chemical compound C1=NC=NC=N1 JIHQDMXYYFUGFV-UHFFFAOYSA-N 0.000 claims description 5
- PNKUSGQVOMIXLU-UHFFFAOYSA-N Formamidine Chemical compound NC=N PNKUSGQVOMIXLU-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 3
- FZZMTSNZRBFGGU-UHFFFAOYSA-N 2-chloro-7-fluoroquinazolin-4-amine Chemical compound FC1=CC=C2C(N)=NC(Cl)=NC2=C1 FZZMTSNZRBFGGU-UHFFFAOYSA-N 0.000 claims 1
- LNJMHEJAYSYZKK-UHFFFAOYSA-N 2-methylpyrimidine Chemical compound CC1=NC=CC=N1 LNJMHEJAYSYZKK-UHFFFAOYSA-N 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 30
- GKVDLTTVBNOGNJ-UHFFFAOYSA-N 2-methylpyrimidin-4-amine Chemical compound CC1=NC=CC(N)=N1 GKVDLTTVBNOGNJ-UHFFFAOYSA-N 0.000 description 15
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 14
- 239000002994 raw material Substances 0.000 description 10
- 229910021529 ammonia Inorganic materials 0.000 description 7
- 239000002775 capsule Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000012458 free base Substances 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- DPJRMOMPQZCRJU-UHFFFAOYSA-M thiamine hydrochloride Chemical compound Cl.[Cl-].CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N DPJRMOMPQZCRJU-UHFFFAOYSA-M 0.000 description 3
- 239000011691 vitamin B1 Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- QDRKDTQENPPHOJ-UHFFFAOYSA-N sodium ethoxide Chemical compound [Na+].CC[O-] QDRKDTQENPPHOJ-UHFFFAOYSA-N 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- 150000000182 1,3,5-triazines Chemical class 0.000 description 1
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- HMUNWXXNJPVALC-UHFFFAOYSA-N 1-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C(CN1CC2=C(CC1)NN=N2)=O HMUNWXXNJPVALC-UHFFFAOYSA-N 0.000 description 1
- VTSWSQGDJQFXHB-UHFFFAOYSA-N 2,4,6-trichloro-5-methylpyrimidine Chemical compound CC1=C(Cl)N=C(Cl)N=C1Cl VTSWSQGDJQFXHB-UHFFFAOYSA-N 0.000 description 1
- FEYDZHNIIMENOB-UHFFFAOYSA-N 2,6-dibromopyridine Chemical compound BrC1=CC=CC(Br)=N1 FEYDZHNIIMENOB-UHFFFAOYSA-N 0.000 description 1
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 1
- SXAMGRAIZSSWIH-UHFFFAOYSA-N 2-[3-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,2,4-oxadiazol-5-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NOC(=N1)CC(=O)N1CC2=C(CC1)NN=N2 SXAMGRAIZSSWIH-UHFFFAOYSA-N 0.000 description 1
- YJLUBHOZZTYQIP-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)NN=N2 YJLUBHOZZTYQIP-UHFFFAOYSA-N 0.000 description 1
- ZFFBIQMNKOJDJE-UHFFFAOYSA-N 2-bromo-1,2-diphenylethanone Chemical compound C=1C=CC=CC=1C(Br)C(=O)C1=CC=CC=C1 ZFFBIQMNKOJDJE-UHFFFAOYSA-N 0.000 description 1
- MLIREBYILWEBDM-UHFFFAOYSA-M 2-cyanoacetate Chemical compound [O-]C(=O)CC#N MLIREBYILWEBDM-UHFFFAOYSA-M 0.000 description 1
- OAKURXIZZOAYBC-UHFFFAOYSA-N 3-oxopropanoic acid Chemical compound OC(=O)CC=O OAKURXIZZOAYBC-UHFFFAOYSA-N 0.000 description 1
- YBPNIILOUYAGIF-UHFFFAOYSA-N 4-amino-2-methylpyrimidine-5-carbonitrile Chemical compound CC1=NC=C(C#N)C(N)=N1 YBPNIILOUYAGIF-UHFFFAOYSA-N 0.000 description 1
- CONKBQPVFMXDOV-QHCPKHFHSA-N 6-[(5S)-5-[[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]methyl]-2-oxo-1,3-oxazolidin-3-yl]-3H-1,3-benzoxazol-2-one Chemical group C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C[C@H]1CN(C(O1)=O)C1=CC2=C(NC(O2)=O)C=C1 CONKBQPVFMXDOV-QHCPKHFHSA-N 0.000 description 1
- OQLZINXFSUDMHM-UHFFFAOYSA-N Acetamidine Chemical compound CC(N)=N OQLZINXFSUDMHM-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- BDAGIHXWWSANSR-UHFFFAOYSA-M Formate Chemical compound [O-]C=O BDAGIHXWWSANSR-UHFFFAOYSA-M 0.000 description 1
- LDKDGDIWEUUXSH-UHFFFAOYSA-N Thymophthalein Chemical compound C1=C(O)C(C(C)C)=CC(C2(C3=CC=CC=C3C(=O)O2)C=2C(=CC(O)=C(C(C)C)C=2)C)=C1C LDKDGDIWEUUXSH-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- NMVVJCLUYUWBSZ-UHFFFAOYSA-N aminomethylideneazanium;chloride Chemical compound Cl.NC=N NMVVJCLUYUWBSZ-UHFFFAOYSA-N 0.000 description 1
- 230000031709 bromination Effects 0.000 description 1
- 238000005893 bromination reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- JPUTTYRVDANTBN-UHFFFAOYSA-N ethyl methanimidate;hydrochloride Chemical compound Cl.CCOC=N JPUTTYRVDANTBN-UHFFFAOYSA-N 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
本発明はビタミンB1その他の医薬の原料とな
る4−アミノ−2−メチルピリミジンを安価な原
料を用い、1反応工程により収率よく製造する方
法に関するものである。
4−アミノ−2−メチルピリミジンの製造方法
でこれまでに知られているものとしては、シアノ
酢酸エステルから導いた2−エトキシカルボニミ
ドイル酢酸エステル又はギ酸エステルと酢酸エス
テルから導いた2−ホルミル酢酸エステルのいず
れかをアセトニトリルから導いたアセトアミジン
と反応させて4−アミノ−6−ヒドロキシ−2−
メチルピリミジンとなし、臭素化、還元を経て目
的の4−アミノ−2−メチルピリミジンに至るも
のや、2,6−ジブロモピリジンを液体アンチニ
ア中カリウムアミドと処理するものなどがある
が、前者では反応工程が繁雑なうえに通算収率が
非常に低くなる欠点があり、また後者では原料が
高価なうえに収率が低い欠点を有している。
本発明者らは上記のような欠点のない4−アミ
ノ−2−メチルピリミジンの製造方法を見出すた
め鋭意研究を重ねた結果、1000Kg/cm2以上の高圧
の下では、安価な基礎化学品であるアセトニトリ
ルと同じく安価に得られるホルムアミド、ホルム
イミダート、ホルムアミジン及び1,3,5−ト
リアジンの中から選ばれる少なくとも1種とから
わずか1反応工程によつて、良好な収率で目的の
4−アミノ−2−メチルピリミジンを取得できる
ことを見出し、この知見に基いて本発明をなすに
至つた。
本発明はホルムアミド、ホルムイミダート、ホ
ルムアミジン及び1,3,5−トリアジンの中か
ら選ばれる化合物の1種、あるいはそれらのうち
の複数のものの混合物とアセトニトリルとを反応
させることを特徴とする4−アミノ−2−メチル
ピリミジンの製造方法であつて、これらの反応は
1000Kg/cm2以上の圧力の下で加熱してはじめて進
行する。すなわち、常圧においてはいずれの反応
も全く進行せず、1000Kg/cm2に加圧するとわずか
に進行が認められる。経済的な反応速度は2000
Kg/cm2以上に加圧することによつて達成される。
圧力の上限は特に存在しない。圧力が高いほど反
応速度は増大するが、2000Kg/cm2〜12000Kg/cm2
の圧力範囲が技術的にもまた経済的にも適当であ
る。高圧力の発生手段としては、原料混合物、あ
るいは原料混合物を内容積が外圧に応じて変化し
得るようなカプセルに封入したものを耐圧反応容
器に充てんした後にガス又は液状の高圧媒体を導
入して直接又は可動隔壁を介して加圧する方法、
原料混合液を高圧ポンプによつて圧入する方法、
原料液を低い温度で耐圧反応容器に密封したのち
に加熱して液の熱膨脹によつて高圧を発生させる
など種々の方法がある。反応温度については50℃
以下では極端に反応が遅く、200℃以上では目的
の4−アミノ−2−メチルピリミジンの変質が起
るので80〜200℃の温度範囲が適当である。反応
時間については圧力、温度、触媒量等に左右され
るが通常5〜100時間で十分である。これらの反
応は低級アルコール、特にメタノールによつて促
進され、またアンモニアを添加すると4−アミノ
−2−メチルピリミジンの収率が向上する。した
がつて通常数モル%から等モルのメタノール又は
アンモニアあるいは両者を触媒として同時に添加
する。またメタノールは反応溶媒の目的を兼ねて
多量に使用することもある。本反応においては反
応に不活性な溶媒の使用は自由である。
本反応においてホルムアミドは式(1)に従つて
反応するものと推定されるので、ホルムアミド1
モルに対し3モル前後のアセトニトリルを使用す
ればよいが厳密な最適モル数は反応条件毎に実験
的に決定される。本反応に使用されるホルムイミ
ダートは一般式HC(NH)ORで表されるもので
あつて、Rは通常低級アルキル基のものが知られ
ており、その種類は問わない。通常塩の形で供給
されるので使用に先立ちアルカリで中和して遊離
塩基とするかあるいは他の原料や溶媒と混合した
後に計算量のアルカリを加えて反応混合物中に遊
離塩基を発生させる。式(2)により反応するものと
推定されるので、ホルムイミダートに対し通常2
倍モル前後のアセトニトリルが使用される。ホル
ムアミジンは通常塩の形で供給されるので前述の
ホルムイミダートの場合と同様に中和して遊離塩
基にして使用する。式(3)
で反応が進むと推定される。ホルムアミジンとア
セトニトリルのモル比は1:2を中心として前後
に多少変動する程度が普通である。1,3,5−
トリアジンは通常シアン化アルカリ又はホルムイ
ミダートを原料として製造される。反応は(4)式で
進むものと推定される。
したがつて1,3,5−トリアジンに対し約6
倍モルのアセトニトリルを使用する。
本発明の結果、4−アミノ−2−メチルピリミ
ジンがわずか1反応工程により従来よりも遥かに
安価に供給されることになるので、このものを原
料とする新な各種の合成ルートを開発することが
可能である。例えばこのものは容易に4−アミノ
−5−ハロゲノ−2−メチルピリミジンを経て、
ビタミンB1を製造する際の中間体である4−ア
ミノ−5−シアノ−2−メチルピリミジンに導く
ことができる。このことはビタミンB1の生産費
の低減に資するものと考えられる。
つぎに実施例によつて本発明をさらに詳細に説
明する。各実施例中に示す部は重量部を表す。収
率を示す%は既に本発明で述べた推定反応式(1)〜
(4)に基く理論収率であつて、各式の第一項に示さ
れた原料化合物当りのものである。なお各実施例
で示す収率は必ずしも最適反応条件による最高収
率を意味するものではない。
実施例 1
ホルムアミド1部、アセトニトリル2.73部、メ
タノール1.42部、アンモニア0.038部(モル比
1:3:2:0.1)をフツ素系プラスチツク(ア
フロン)製カプセルに溶封したものを耐圧反応容
器に充てんし、その容器にエチレングリコール・
水等量からなる圧媒体を所定の圧力に達するまで
圧入し、つぎに容器を外熱して内温を140℃に昇
温し、以後同温度に20時間保持した。この間に圧
媒体の一部の抜き出し及び圧入により容器内の圧
力を所定の一定圧力に保つた。20時間が経過した
ところで容器を冷却し、ついで圧力を除いてから
カプセルを取り出して開封し、内容物を高速液体
クロマトグラフイー及びガスクロマトグラフイー
によつて分析した。各所定の反応圧力における目
的の4−アミノ−2−メチルピリミジンの収率は
次表に示す通りであつた。
The present invention relates to a method for producing 4-amino-2-methylpyrimidine, which is a raw material for vitamin B1 and other pharmaceuticals, in a high yield in one reaction step using inexpensive raw materials. So far known methods for producing 4-amino-2-methylpyrimidine include 2-ethoxycarbonimidoyl acetate derived from cyanoacetate or 2-formylacetic acid derived from formate and acetate. Either of the esters is reacted with acetamidine derived from acetonitrile to form 4-amino-6-hydroxy-2-
There are methods that lead to the desired 4-amino-2-methylpyrimidine through methylpyrimidine, bromination, and reduction, and methods that treat 2,6-dibromopyridine with potassium amide in liquid antinia, but in the former, the reaction is The disadvantage is that the process is complicated and the total yield is very low, and the latter has the disadvantage that the raw materials are expensive and the yield is low. The inventors of the present invention have conducted extensive research to find a method for producing 4-amino- 2 -methylpyrimidine that does not have the drawbacks mentioned above. The desired product 4 can be obtained in good yield through just one reaction step from a certain acetonitrile and at least one member selected from formamide, formimidate, formamidine, and 1,3,5-triazine, which are also obtained at low cost. -Amino-2-methylpyrimidine could be obtained, and based on this knowledge, the present invention was accomplished. The present invention is characterized in that one compound selected from formamide, formimidate, formamidine, and 1,3,5-triazine, or a mixture of a plurality of them, is reacted with acetonitrile. -A method for producing amino-2-methylpyrimidine, the reactions comprising:
It only progresses when heated under a pressure of 1000Kg/cm2 or more . That is, none of the reactions proceed at all under normal pressure, but slight progress is observed when the pressure is increased to 1000 Kg/cm 2 . Economic reaction rate is 2000
This is achieved by applying pressure to Kg/cm 2 or more.
There is no particular upper limit to the pressure. The higher the pressure, the higher the reaction rate, but between 2000Kg/cm 2 and 12000Kg/cm 2
A pressure range of 100 to 100% is technically and economically suitable. High pressure can be generated by filling a pressure-resistant reaction vessel with a raw material mixture or a capsule containing the raw material mixture whose internal volume can change depending on external pressure, and then introducing a gas or liquid high-pressure medium. A method of pressurizing directly or through a movable bulkhead,
A method of pressurizing the raw material mixture using a high-pressure pump,
There are various methods, such as sealing the raw material liquid in a pressure-resistant reaction vessel at a low temperature and then heating it to generate high pressure due to thermal expansion of the liquid. 50℃ for reaction temperature
Below 200°C, the reaction is extremely slow, and above 200°C the target 4-amino-2-methylpyrimidine undergoes deterioration, so a temperature range of 80 to 200°C is appropriate. The reaction time depends on the pressure, temperature, amount of catalyst, etc., but usually 5 to 100 hours is sufficient. These reactions are promoted by lower alcohols, especially methanol, and the addition of ammonia improves the yield of 4-amino-2-methylpyrimidine. Therefore, methanol or ammonia or both are usually added at the same time as a catalyst in an amount ranging from several mol % to an equimolar amount. Methanol may also be used in large amounts to serve as a reaction solvent. In this reaction, any solvent inert to the reaction may be used freely. In this reaction, formamide is Since it is presumed to react, formamide 1
Approximately 3 moles of acetonitrile may be used, but the exact optimum number of moles is determined experimentally for each reaction condition. The formimidate used in this reaction is represented by the general formula HC(NH)OR, and R is generally known to be a lower alkyl group, and its type is not limited. It is usually supplied in the form of a salt and is either neutralized to the free base with an alkali prior to use or mixed with other raw materials and solvents and then added with a calculated amount of alkali to generate the free base in the reaction mixture. What reacts according to formula (2) Since it is estimated that the
Around twice the molar amount of acetonitrile is used. Since formamidine is normally supplied in the form of a salt, it is used as a free base by neutralization as in the case of formimidate described above. Formula (3) It is estimated that the reaction proceeds at The molar ratio of formamidine and acetonitrile is usually around 1:2 and varies to some extent. 1,3,5-
Triazines are usually produced from alkali cyanide or formimidate. The reaction is estimated to proceed according to equation (4). Therefore, about 6 for 1,3,5-triazine
Use twice the molar amount of acetonitrile. As a result of the present invention, 4-amino-2-methylpyrimidine can be supplied at a much lower cost than before through just one reaction step, so it is important to develop various new synthetic routes using this product as a raw material. is possible. For example, this one can easily be converted into 4-amino-5-halogeno-2-methylpyrimidine,
It can lead to 4-amino-5-cyano-2-methylpyrimidine, which is an intermediate in producing vitamin B1 . This is considered to contribute to reducing the production cost of vitamin B1 . Next, the present invention will be explained in more detail with reference to Examples. Parts shown in each example represent parts by weight. The percentage indicating the yield is based on the estimated reaction formula (1) ~ already described in the present invention.
This is the theoretical yield based on (4), and is per raw material compound shown in the first term of each formula. Note that the yield shown in each example does not necessarily mean the highest yield under optimal reaction conditions. Example 1 1 part of formamide, 2.73 parts of acetonitrile, 1.42 parts of methanol, and 0.038 parts of ammonia (molar ratio 1:3:2:0.1) were melt-sealed in a capsule made of fluorine-based plastic (Aflon), which was then filled into a pressure-resistant reaction vessel. Then add ethylene glycol to the container.
A pressure medium consisting of an equal amount of water was injected until a predetermined pressure was reached, and then the container was externally heated to raise the internal temperature to 140°C, and the temperature was then maintained at the same temperature for 20 hours. During this time, the pressure inside the container was maintained at a predetermined constant pressure by partially withdrawing and press-fitting the pressure medium. After 20 hours had elapsed, the container was cooled, the pressure was removed, the capsule was removed and opened, and the contents were analyzed by high performance liquid chromatography and gas chromatography. The yield of the target 4-amino-2-methylpyrimidine at each predetermined reaction pressure was as shown in the following table.
【表】
実施例 2
ホルムアミド1部、アセトニトリル2.73部、メ
タノール0.71部、アンモニア0.019部(モル比
1:3:1:0.05)及びテトラヒドロフラン3.2
部の混合物を実施例1と同様の操作により12000
Kg/cm2において100℃で63時間反応させた結果4
−アミノ−2−メチルピリミジンの収率は50.5%
であつた。
実施例 3
ホルムアミド1部、アセトニトリル2.73部、メ
タノール0.36部、アンモニア0.0095部(モル比
1:3:0.5:0.025)をポリエチレン製カプセル
に封入し、実施例1と同様にして80℃、12800〜
11600Kg/cm2に40時間保つたところ4−アミノ−
2−メチルピリミジンが34.3%の収率で生成し
た。
実施例 4
ホルムアミド1部、アセトニトリル1.37部、メ
タノール0.53部及びアンモニア0.014部(モル比
1:1.5:0.75:0.038)の混合物を実施例1と同
様にして100℃、13000〜10400Kg/cm2に1週間保
つたところ4−アミノ−2−メチルピリミジンの
収率は28.9%であつた。ただしこの収率をアセト
ニトリル当りに換算すると57.6%である。反応生
成物より固形物をロ別し、それを1,4−ジオキ
サンで抽出すると0.57部の粗製品が得られた。そ
れをメタノールで再結晶を繰返した結果白色の4
−アミノ−2−メチルピリミジンの純品0.45部が
得られた。融点は207.8℃を示した。これまでに
知られた値は203〜206℃の範囲である。
C5H7N3としての元素分析値
C% H% N%
理論値 55.03 6.47 38.50
実験値 54.68 6.49 38.27
実施例 5
エチルホルムイミダート塩酸塩1部、アセトニ
トリル0.75部及びメタノール0.073部(モル比
1:2:0.25)をポリエチレン製カプセルに量り
取り、スラリー状にかきまぜながら2.9モル/
のナトリウムエチラートエタノール溶液をチモー
ルフタレインを指示薬として中和するまで滴下
し、カプセルを溶封する。これを実施例1と同様
の操作により、実施例2と同一条件で反応させた
結果4−アミノ−2−メチルピリミジンの収率は
44.5%であつた。
実施例 6
ホルムアミジン塩酸塩1部、アセトニトリル
1.02部(モル比1:2)の混合スラリーをナトリ
ウムエチラートで中和したものを実施例5と同様
に処理したところ4−アミノ−2−メチルピリミ
ジンが37.7%の収率で生成した。
実施例 7
1,3,5−トリアジン1部、アセトニトリル
3.04部、メタノール1.18部、アンモニア0.032部
(モル比1:6:3:0.5)にテトラヒドロフラン
5.34部を加え、ポリエチレン製カプセルに封入
し、実施例2と同様の条件で反応させた結果4−
アミノ−2−メチルピリミジンの収率は20.9%で
あつた。[Table] Example 2 1 part of formamide, 2.73 parts of acetonitrile, 0.71 parts of methanol, 0.019 parts of ammonia (molar ratio 1:3:1:0.05), and 3.2 parts of tetrahydrofuran
12,000 parts of the mixture was treated in the same manner as in Example 1.
Results of reaction at 100℃ for 63 hours at Kg/cm 2 4
-Yield of amino-2-methylpyrimidine is 50.5%
It was hot. Example 3 1 part of formamide, 2.73 parts of acetonitrile, 0.36 parts of methanol, and 0.0095 parts of ammonia (molar ratio 1:3:0.5:0.025) were encapsulated in a polyethylene capsule, and heated in the same manner as in Example 1 at 80°C and 12800~
When kept at 11600Kg/ cm2 for 40 hours, 4-amino-
2-methylpyrimidine was produced in a yield of 34.3%. Example 4 A mixture of 1 part of formamide, 1.37 parts of acetonitrile, 0.53 parts of methanol and 0.014 parts of ammonia (molar ratio 1:1.5:0.75:0.038) was prepared in the same manner as in Example 1 at 100°C and 13000 to 10400 Kg/ cm2 . When kept for a week, the yield of 4-amino-2-methylpyrimidine was 28.9%. However, this yield is 57.6% when converted to acetonitrile. Solid matter was filtered out from the reaction product and extracted with 1,4-dioxane to obtain 0.57 parts of a crude product. After repeated recrystallization with methanol, a white 4
0.45 part of pure -amino-2-methylpyrimidine was obtained. The melting point was 207.8°C. Values known so far range from 203 to 206°C. Elemental analysis value as C 5 H 7 N 3 C% H% N% Theoretical value 55.03 6.47 38.50 Experimental value 54.68 6.49 38.27 Example 5 1 part of ethylformimidate hydrochloride, 0.75 part of acetonitrile and 0.073 part of methanol (molar ratio 1 :2:0.25) into a polyethylene capsule, and while stirring to form a slurry, add 2.9 mol/
A solution of sodium ethylate in ethanol is added dropwise until it is neutralized using thymolphthalein as an indicator, and the capsule is melt-sealed. This was reacted in the same manner as in Example 1 and under the same conditions as in Example 2. As a result, the yield of 4-amino-2-methylpyrimidine was
It was 44.5%. Example 6 1 part formamidine hydrochloride, acetonitrile
When 1.02 parts (molar ratio 1:2) of the mixed slurry was neutralized with sodium ethylate and treated in the same manner as in Example 5, 4-amino-2-methylpyrimidine was produced in a yield of 37.7%. Example 7 1 part 1,3,5-triazine, acetonitrile
3.04 parts, methanol 1.18 parts, ammonia 0.032 parts (molar ratio 1:6:3:0.5) and tetrahydrofuran.
5.34 parts was added, sealed in a polyethylene capsule, and reacted under the same conditions as in Example 2. Result 4-
The yield of amino-2-methylpyrimidine was 20.9%.
Claims (1)
ミジン及び1,3,5−トリアジンの中から選ば
れる化合物の少なくとも1種と、アセトニトリル
とを反応圧力1000Kg/cm2以上で反応させることを
特徴とする4−アミン−2−メチルピリミジンの
製造方法。1. A 4-amine characterized by reacting at least one compound selected from formamide, formimidate, formamidine, and 1,3,5-triazine with acetonitrile at a reaction pressure of 1000 Kg/cm 2 or more. -A method for producing 2-methylpyrimidine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21552883A JPS60109571A (en) | 1983-11-16 | 1983-11-16 | Production of 4-amino-2-methylpyrimidine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21552883A JPS60109571A (en) | 1983-11-16 | 1983-11-16 | Production of 4-amino-2-methylpyrimidine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60109571A JPS60109571A (en) | 1985-06-15 |
| JPS6119626B2 true JPS6119626B2 (en) | 1986-05-17 |
Family
ID=16673914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21552883A Granted JPS60109571A (en) | 1983-11-16 | 1983-11-16 | Production of 4-amino-2-methylpyrimidine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60109571A (en) |
-
1983
- 1983-11-16 JP JP21552883A patent/JPS60109571A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60109571A (en) | 1985-06-15 |
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