JPH02292283A - Production of 5-(4-pyridyl)oxazole - Google Patents
Production of 5-(4-pyridyl)oxazoleInfo
- Publication number
- JPH02292283A JPH02292283A JP11315089A JP11315089A JPH02292283A JP H02292283 A JPH02292283 A JP H02292283A JP 11315089 A JP11315089 A JP 11315089A JP 11315089 A JP11315089 A JP 11315089A JP H02292283 A JPH02292283 A JP H02292283A
- Authority
- JP
- Japan
- Prior art keywords
- pyridyl
- oxazole
- reaction
- water
- carboxylic acid
- 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.)
- Granted
Links
- AFQAOCIKCVFASO-UHFFFAOYSA-N 5-pyridin-4-yl-1,3-oxazole Chemical compound O1C=NC=C1C1=CC=NC=C1 AFQAOCIKCVFASO-UHFFFAOYSA-N 0.000 title claims description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- 150000001408 amides Chemical class 0.000 claims abstract description 17
- RSIXBZMVZGQXAH-UHFFFAOYSA-N 5-pyridin-4-yl-1,3-oxazole-4-carboxylic acid Chemical compound N1=COC(C=2C=CN=CC=2)=C1C(=O)O RSIXBZMVZGQXAH-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 230000000911 decarboxylating effect Effects 0.000 claims description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 abstract description 23
- 238000006114 decarboxylation reaction Methods 0.000 abstract description 8
- 150000001875 compounds Chemical class 0.000 abstract description 6
- JBCFJMYPJJWIRG-UHFFFAOYSA-N 1,3-oxazole-4-carboxylic acid Chemical compound OC(=O)C1=COC=N1 JBCFJMYPJJWIRG-UHFFFAOYSA-N 0.000 abstract description 3
- 238000001953 recrystallisation Methods 0.000 abstract description 2
- 238000004821 distillation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 14
- 239000000047 product Substances 0.000 description 11
- 239000002904 solvent Substances 0.000 description 11
- 239000012141 concentrate Substances 0.000 description 10
- 238000009835 boiling Methods 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 4
- 150000007530 organic bases Chemical class 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 150000007529 inorganic bases Chemical class 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 2
- RVQZKNOMKUSGCI-UHFFFAOYSA-N pyridine-4-carbonyl chloride Chemical compound ClC(=O)C1=CC=NC=C1 RVQZKNOMKUSGCI-UHFFFAOYSA-N 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000013076 target substance Substances 0.000 description 2
- UEIZUEWXLJOVLD-UHFFFAOYSA-N 3-(1-methylpyrrolidin-3-yl)pyridine Chemical compound C1N(C)CCC1C1=CC=CN=C1 UEIZUEWXLJOVLD-UHFFFAOYSA-N 0.000 description 1
- 125000000339 4-pyridyl group Chemical group N1=C([H])C([H])=C([*])C([H])=C1[H] 0.000 description 1
- 239000005973 Carvone Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- SUAKHGWARZSWIH-UHFFFAOYSA-N N,N‐diethylformamide Chemical compound CCN(CC)C=O SUAKHGWARZSWIH-UHFFFAOYSA-N 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- ZCQWOFVYLHDMMC-UHFFFAOYSA-N Oxazole Chemical compound C1=COC=N1 ZCQWOFVYLHDMMC-UHFFFAOYSA-N 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 244000309464 bull Species 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000001055 chewing effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- WBJINCZRORDGAQ-UHFFFAOYSA-N formic acid ethyl ester Natural products CCOC=O WBJINCZRORDGAQ-UHFFFAOYSA-N 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000010813 internal standard method Methods 0.000 description 1
- -1 isocyanoacetic acid ester Chemical class 0.000 description 1
- TWBYWOBDOCUKOW-UHFFFAOYSA-N isonicotinic acid Chemical class OC(=O)C1=CC=NC=C1 TWBYWOBDOCUKOW-UHFFFAOYSA-N 0.000 description 1
- REPVNSJSTLRQEQ-UHFFFAOYSA-N n,n-dimethylacetamide;n,n-dimethylformamide Chemical compound CN(C)C=O.CN(C)C(C)=O REPVNSJSTLRQEQ-UHFFFAOYSA-N 0.000 description 1
- BGUWFUQJCDRPTL-UHFFFAOYSA-N pyridine-4-carbaldehyde Chemical compound O=CC1=CC=NC=C1 BGUWFUQJCDRPTL-UHFFFAOYSA-N 0.000 description 1
- 125000004076 pyridyl group Chemical group 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000009958 sewing Methods 0.000 description 1
- CFOAUYCPAUGDFF-UHFFFAOYSA-N tosmic Chemical compound CC1=CC=C(S(=O)(=O)C[N+]#[C-])C=C1 CFOAUYCPAUGDFF-UHFFFAOYSA-N 0.000 description 1
- GKASDNZWUGIAMG-UHFFFAOYSA-N triethyl orthoformate Chemical compound CCOC(OCC)OCC GKASDNZWUGIAMG-UHFFFAOYSA-N 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業ヒの利用分野]
本発明は.5−(4−ピリジル)才キサゾール−4−カ
ルボン酸から、その脱炭酸反応物である5−(4−ピリ
ジル)オキサゾールを工業的に有利に製造する方法に関
するものである.[従来の技術]
5−(4−ピリジル)オキサゾールは、セファロスボリ
ン化合物を得るための中間体として屯要である。(たと
えば特開昭s 1 − 7 2 a o ty公報参照
)
5−(4−ピリジル)オギサゾールを製ωする従来技術
としては、4−ビリジンアルデヒドとトシルメチルイソ
シアニドを縮合させる方法(Chew. Pharm.
Bull., 27, 793 (+979)参照)
,4−7セチルピリジンより7ミノイソニコチメイルメ
タンを製造し,ついでオルトギ酸エチルで閉環する方法
(J. Org. Che+s., 22B+ (19
80)参照)が知られている。[Detailed Description of the Invention] [Field of Industrial Application] The present invention... The present invention relates to an industrially advantageous method for producing 5-(4-pyridyl)oxazole, which is a decarboxylation product thereof, from 5-(4-pyridyl)oxazole-4-carboxylic acid. [Prior Art] 5-(4-pyridyl)oxazole is often needed as an intermediate for obtaining cephalosborin compounds. (For example, see Japanese Patent Application Laid-Open No. 1-72-2003.) As a conventional technique for producing 5-(4-pyridyl)ogisazole, there is a method of condensing 4-pyridine aldehyde and tosylmethyl isocyanide (Chew. Pharm.
Bull. , 27, 793 (+979))
, 4-7 A method of producing 7-minoisonicothimeylmethane from cetylpyridine and then ring-closing it with ethyl orthoformate (J. Org. Che+s., 22B+ (19
80)) is known.
しかしながらこれらの方法は、前者にあっては使用する
原料化合物が高価であるという問題点があり,後者にあ
っては反応工程が艮〈なるという問題点があり、いずれ
も工業的見地からは有利とはrTい難いものであった.
そこで−ヒ記の方法とは異なる製造ルートとして、本出
願人のうちの一人は、特開昭63−150280号公報
において、イソシアノ酢酸エステルとインニコチン酎活
性体(イソニコチン酸クロライド等)との反応物を加水
分解して得られる5−(4−ピリジル)才キサゾール−
4−カルボン酸を原料として用い、これをジメチルホル
ムアミド等の溶媒中で触媒の存在下に脱炭酸反応させて
目的物である5−(4−ピリジル)オキサゾールを製造
する方法を提案している。なお、この脱炭酸反応におけ
る触媒としては、金属粉末(たとえば銅粉末)および有
機塩基(たとえばピリジン)からなる触媒を使用してい
る。However, these methods have the problem that the raw material compounds used in the former are expensive, and the latter have the problem that the reaction process is complicated, and both methods are not advantageous from an industrial standpoint. It was very difficult. Therefore, as a production route different from the method described in (A), one of the present applicants proposed in Japanese Patent Application Laid-open No. 150280/1983 a method of combining isocyanoacetic ester and innicotine liquor active substance (isonicotinic acid chloride, etc.). 5-(4-pyridyl)xazole obtained by hydrolyzing the reactant
They have proposed a method for producing the target product, 5-(4-pyridyl)oxazole, by using 4-carboxylic acid as a raw material and subjecting it to a decarboxylation reaction in a solvent such as dimethylformamide in the presence of a catalyst. Note that, as a catalyst in this decarboxylation reaction, a catalyst consisting of a metal powder (for example, copper powder) and an organic base (for example, pyridine) is used.
[発明が解決しようとする課題]
1一述の特開昭63−150280号公報に記載の方法
は、安価で入手容易な原料を利用できる点でその丁業的
価値が極めて高いものである。[Problems to be Solved by the Invention] 1. The method described in Japanese Unexamined Patent Publication No. 150280/1983 has extremely high industrial value in that it can utilize inexpensive and easily available raw materials.
しかしながら、この方法は次に述べるような問題・jス
、すなわち、脱炭酸反応終了後は反応混合物から不溶物
および溶媒を留去すると共に、残渣から11的物を分離
することが必要となるところ、残清中の目的物の純度が
低い上、残渣中に混入する金1泥の分離を行わなければ
ならず(高価な金属であればその回収も必要)、また留
去した溶媒を再使用するには溶媒中に混入する有機塩基
を除去しなければならない場合があり、精製工程が複雑
となること、目的物の収率が70%前後と必ずしも高く
はないことなどのことから、工業的規模で実施するため
にはさらに改良を図ることが望まれる。However, this method has the following problems: After the decarboxylation reaction is complete, it is necessary to distill off the insoluble matter and solvent from the reaction mixture and to separate the 11 substances from the residue. , the purity of the target substance in the residue is low, the gold mixed in the residue must be separated (if it is an expensive metal, it must also be recovered), and the distilled solvent must be reused. In order to do this, it may be necessary to remove the organic base mixed in the solvent, which complicates the purification process, and the yield of the target product is not necessarily high at around 70%. Further improvements are desired in order to implement it on a large scale.
本発明は、−L記脱炭酸反応において、特別の触媒の使
用を要せず、しかも収率を顕著に向七させる方法を提供
することを目的とするものである。An object of the present invention is to provide a method that does not require the use of a special catalyst in the -L decarboxylation reaction and can significantly improve the yield.
[課題を解決するための手没]
本発明の5−(4−ピリジル)オキサゾールの製造法は
、5−(4−ピリジル)才キサゾールー4−カルボン酸
を加熱して脱炭酸することにより5−(4−ピリジル)
オキサゾールを製造するにあたり、水を含イイする非プ
ロトン性アミドの存在−ドで反応を行うことを特徴とす
るものである。[Efforts to Solve the Problems] The method for producing 5-(4-pyridyl)oxazole of the present invention is to produce 5-(4-pyridyl)oxazole by heating and decarboxylating 5-(4-pyridyl)oxazole-4-carboxylic acid. (4-pyridyl)
In producing oxazole, the reaction is carried out in the presence of an aprotic amide containing water.
以ド本発明を詳細に説明する。The present invention will now be described in detail.
出発物質である5−(4−ピリジル)オキサソール−4
−カルボン酸は、先に引用した特開昭63−15028
0号公報に記載されているように.イソシアノ酢酸エス
テルとイソニコチンlli性体(殊にイソニコチン酸ク
ロライド)との反応物を加水分解することにより得られ
る。Starting material 5-(4-pyridyl)oxazole-4
- Carboxylic acid is the JP-A No. 63-15028 cited above.
As stated in Publication No. 0. It is obtained by hydrolyzing a reaction product of isocyanoacetic ester and isonicotine lli compound (especially isonicotinic acid chloride).
イソシアノ酢酸エステルとイソニコチン酸活性体との反
応は、有機または無機塩基の存在下、適当な溶々V中で
、O〜50℃程度の温度条件下に行われる。加水分解反
応は、無機塩基の存在下、水または含水アルコール中で
、室温ないし50℃程度の温度条件下に行われる.
本発明においては、このようにして得られた5−(4−
ピリジル)オキサゾール−4−カルボン酸を加熱して脱
炭酸するにあたり、水を含有する非プロトン性アミドの
存在下で反応を行う。The reaction between the isocyanoacetic acid ester and the activated isonicotinic acid is carried out in the presence of an organic or inorganic base in a suitable solvent at a temperature of about 0 to 50°C. The hydrolysis reaction is carried out in water or hydroalcohol in the presence of an inorganic base at a temperature from room temperature to about 50°C. In the present invention, the 5-(4-
When decarboxylating pyridyl)oxazole-4-carboxylic acid by heating, the reaction is carried out in the presence of an aprotic amide containing water.
ここで非プロトン性アミドとしては、N,N−ジメチル
ホルムアミド(沸.九t 5 3℃)、N,Nジメチル
アセトアミド(沸点166゜C).N,N−ジエチルホ
ルムアミド′(沸へ177〜178℃).N.N,N’
.N’−テトラメチル尿素(沸点177〜178℃)
、N−メチルピロリドン(沸点202℃)、N−ホルミ
ルビペリジンなどがあげられる。これらの中では、沸点
、収率コストなどを総合考虜すると、N.N−ジメチル
ホルムアミドが最もT業性に富む。なおもし必要であれ
ば、本発明の趣旨を損なわない範囲で、他の溶媒を併用
しても差支えない.
非プロトン性アミドの含水率(含水アミド中の水の割合
)は、0.1〜50千驕%、殊に0.5〜30重量%と
するのが有利であり、このような含水率範囲において最
も好ましい結果がjIIられる.
含水非プロトン性アミド使用縫は、5−(4−ピリジル
)オギサゾール−4−カルボン酸1 −W ?A部に対
して5〜20重品一部程度、殊に10屯早部1i?j後
とするのが適当であるが、必ずしもこの範囲に限られな
い。Examples of aprotic amides include N,N-dimethylformamide (boiling point: 9t 5 3°C), N,N dimethylacetamide (boiling point: 166°C). N,N-diethylformamide' (boiling 177-178°C). N. N,N'
.. N'-tetramethylurea (boiling point 177-178°C)
, N-methylpyrrolidone (boiling point 202°C), N-formylbiperidine, and the like. Among these, when considering boiling point, yield cost, etc., N. N-dimethylformamide has the highest T-performance. If necessary, other solvents may be used in combination without departing from the spirit of the present invention. The water content of the aprotic amide (proportion of water in the water-containing amide) is advantageously between 0.1 and 50,000%, particularly between 0.5 and 30% by weight; The most favorable result is shown in jII. The sewing using hydrous aprotic amide is 5-(4-pyridyl)oxazole-4-carboxylic acid 1-W? About 5 to 20 heavy items for part A, especially 10 ton early part 1i? It is appropriate to set it after j, but it is not necessarily limited to this range.
前記の出発物質および上記アミドの仕込み方法は任意で
あり、両者を一括仕込みする方法、いずれかまたは双方
を分割仕込みする方法、いずれかまたは双方をdhl仕
込みする方法などがいずれも採用される。The method of charging the above-mentioned starting material and the above-mentioned amide is arbitrary, and a method of charging both at once, a method of charging either or both in portions, a method of charging either or both by DHL, etc. can be adopted.
反応温度はlOO〜210″C程度が適当であり、通常
は還F− ”Fに反応を行う。反応時間は0.5〜10
時間程度とすることが多い。The reaction temperature is suitably about 100 to 210"C, and the reaction is usually carried out to reflux F-"F. Reaction time is 0.5-10
It is often about an hour.
反応終了後は、減圧蒸留等の手段により上記アミドを除
去する。濃縮物は若干の不純物を含む5−(4−ピリジ
ル)オキサゾールであるので、再結晶、洗浄、その他の
手段により精製して、目的物を1リる。After the reaction is completed, the amide is removed by means such as vacuum distillation. Since the concentrate is 5-(4-pyridyl)oxazole containing some impurities, it is purified by recrystallization, washing, and other means to obtain the desired product.
[作 用]
未発明の反応は下記の式で表わされる。水を含イ1する
非プロトン性アミドは、脱炭酸反応を促進する触媒とし
ての役割と共に、溶媒としての役割をl.!4たすもの
と考えられる.
[実施例]
次に実施例をあげて本発明をさらに説明する。[Function] The uninvented reaction is expressed by the following formula. The aprotic amide containing water plays the role of a catalyst that promotes the decarboxylation reaction, as well as the role of a solvent. ! It is considered to be 4 plus. [Example] Next, the present invention will be further explained with reference to Examples.
実施例1
還流装1在を備えたフラスコに、5−(4−ピリジル)
オキサゾール−4−カルボン酸e.oog、N,N−ジ
メチルホルムアミド5eJgおよび水1.15g (含
水率約2重場゛%)を仕込み、加熱して口流下に5時間
説炭酸反応させた。Example 1 5-(4-pyridyl) was added to a flask equipped with a reflux device.
Oxazole-4-carboxylic acid e. 5 eJg of N,N-dimethylformamide and 1.15 g of water (moisture content: about 2%) were charged and heated to carry out a carbonic acid reaction under a stream of water for 5 hours.
反応終了後、減圧下に溶媒を留去し,濃縮物4.66g
を得た。After the reaction was completed, the solvent was distilled off under reduced pressure to obtain 4.66 g of concentrate.
I got it.
ガスクロマトグラフィーによる分析(内部標準法による
定量分析)の結果、このe縮物ほ93.8iT.:♀〜
%の5−(4−ピリジル)オギサゾールを含んでいるこ
とが判明した。収率は94.6%であった.
実施例2
氷の添加賃を0.57g (含水率約1重{一%)とし
たほかは実施例lを繰り返した。濃縮物中の11的物の
含IJは9 0 . 8 屯κ%,収率は91.2%で
あった。As a result of analysis by gas chromatography (quantitative analysis by internal standard method), this e-condensate was 93.8 iT. :♀〜
% of 5-(4-pyridyl)oxazole. The yield was 94.6%. Example 2 Example 1 was repeated except that the amount of ice added was 0.57 g (water content approximately 1%). The IJ of 11 compounds in the concentrate is 90. The yield was 91.2%.
実施例3
水の添加}値を2.30g (含水率約4屯量%)とし
たほかは実施例1を繰り返した。濃縮物中の目的物の含
tl{は90.2重着%,収率は86.3%であった。Example 3 Example 1 was repeated except that the water addition value was changed to 2.30 g (water content approximately 4 tonne %). The content of the target product in the concentrate was 90.2%, and the yield was 86.3%.
゛実施例4
N,N−ジメチルホルムアミド58.8gに代えてNN
−ジメチルアセトアミド5ta.8gを用い、かつ水の
仕込み量を1.15g (含水率約2重45%)とした
ほかは,実施例lを繰り返した.
濃縮物中の目的物の含量は77.9重量%、収率は80
.1%であった。Example 4 NN in place of 58.8 g of N,N-dimethylformamide
-dimethylacetamide 5ta. Example 1 was repeated, except that 8 g was used and the amount of water added was 1.15 g (moisture content about 2 times 45%). The content of the target product in the concentrate was 77.9% by weight, and the yield was 80%.
.. It was 1%.
実施例5
N,N−ジメチルホルムアミド58.8gに代えてN−
ホルミルビペリジン81.1gを用い、かつ水の仕込み
量を1.22g (含水率約2重埴%)としたほかは,
実施例1をhり返した.
反応液中の目的物の含量ほf3.09%量%、収率は8
7.5%であった.
実施例6
N,N−ジメチルホルムアミド47.3gと水189g
(含水一F約3.8重早%)とからなる5流状態の混合
液に、5−(4−ピリジル)才キサゾール4−カルボン
酎2.Ogを1時間ごとに5回、計10.0g加え,そ
の後さらに亮流下に4時間反I5させた。Example 5 N- in place of 58.8 g of N,N-dimethylformamide
Except that 81.1 g of formylbiperidine was used and the amount of water was 1.22 g (water content approximately 20%),
Example 1 was repeated several times. The content of the target substance in the reaction solution was approximately f3.09% by weight, and the yield was 8.
It was 7.5%. Example 6 47.3 g of N,N-dimethylformamide and 189 g of water
(Water content: approximately 3.8% by weight) and 2.5-(4-pyridyl)xazole 4-carboxylic liquor. A total of 10.0 g of Og was added 5 times every 1 hour, and then the mixture was further heated under a light flow for 4 hours.
反応終了後、減圧下に溶媒を留去し、濃1h物8.02
gを得た.
カスクロマトグラフィーによる分析の結果、この濃縮物
は94.1重賃%の5−(4−ピリジル)オキサゾール
を含んでいることが判明した。収−トは98.2%であ
った。After the reaction was completed, the solvent was distilled off under reduced pressure to obtain a concentrated 1h product of 8.02
I got g. Analysis by gas chromatography showed that this concentrate contained 94.1% by weight of 5-(4-pyridyl)oxazole. The yield was 98.2%.
実施例7
水の添加賃を5.75g (含水率約9.2重jJ−%
)としたほかは実施例1を繰り返した。濃縮物中の11
的物の含11は90.7重量%、収率は83.8%であ
った.
比較例1
水の添加を省略したほかは実施例1を繰り返した.(た
だし、N,N−ジメチルホルムアミド中の水分は0.0
1東;,}%である。)反応終了後,減圧下に溶媒を留
去し、濃縮物4.43gを得た。Example 7 Addition of 5.75 g of water (moisture content approximately 9.2%
), Example 1 was repeated. 11 in concentrate
The target content 11 was 90.7% by weight, and the yield was 83.8%. Comparative Example 1 Example 1 was repeated except that the addition of water was omitted. (However, the water content in N,N-dimethylformamide is 0.0
1 East;,}%. ) After the reaction was completed, the solvent was distilled off under reduced pressure to obtain 4.43 g of a concentrate.
濃縮物中の目的物の含場は53,0重κ%、収率は50
.8%であった。The concentration of the target product in the concentrate is 53.0% by weight, and the yield is 50%.
.. It was 8%.
比較例2
5−(4−ピリジル)オギサゾール−4−カルボン酊e
.oogに、N−ジメチルホルムアミド56.4g.銅
粉0.28 g、ビリジン1.98gを加え、加熱して
侵渣下に5時間脱炭酸反応させた。Comparative Example 2 5-(4-pyridyl)oxazole-4-carvone
.. oog, 56.4 g of N-dimethylformamide. 0.28 g of copper powder and 1.98 g of pyridine were added, and the mixture was heated to carry out a decarboxylation reaction under erosion for 5 hours.
咬応終7′後、氷冷してから不溶物をろ過により分離し
,ついで減圧下に溶媒を留去して、e縮物5.25 1
jを得た。After 7' of chewing, the insoluble matter was separated by filtration after cooling on ice, and then the solvent was distilled off under reduced pressure to obtain a condensate of 5.25 1
I got j.
濃縮物中の目的物の含t・はB2.2改♀%、収率は7
0.8%であった。The content of the target product in the concentrate is B2.2%, and the yield is 7.
It was 0.8%.
〈結果のまとめ〉
以ヒ,実施例1〜7,比較例1〜2の結果をまとめると
次のようになる.
旦町1匹n±
実施例1 94.8 %
実施例2 91.2 g
実施例3 8G.3 2
実施例4 80.1 %
実施例5 87.5 2
実施例6 98.2 2
実施例7 83.8 2
比較例1 50.8 2
比較例2 70.8 2
〔発明の効果]
k Q l旧においては 含氷非プロトン性アミドの存
在下で反応を行うだけで,目的物である5一(4−ピリ
ジル)オキサゾールを好収率で得ることができる.
金屈粉末や有機塩基等の触媒の使用は不要となるL,反
応物からの含水非プロトン性アミドの除去は容易であり
,また反応物中の目的物の純度も極めて高いので,反応
終了後の反応物からの[]的物のtp.!、精製工程は
従来法に比し格段にシンプルなものとになる。<Summary of Results> The results of Examples 1 to 7 and Comparative Examples 1 to 2 are summarized as follows. Danmachi 1 animal n ± Example 1 94.8% Example 2 91.2 g Example 3 8G. 3 2 Example 4 80.1% Example 5 87.5 2 Example 6 98.2 2 Example 7 83.8 2 Comparative example 1 50.8 2 Comparative example 2 70.8 2 [Effect of the invention] k In the old QI method, the desired product, 5-(4-pyridyl)oxazole, can be obtained in good yield simply by carrying out the reaction in the presence of an ice-containing aprotic amide. It is not necessary to use catalysts such as Kinku powder or organic bases, and the water-containing aprotic amide can be easily removed from the reactants, and the purity of the target product in the reactants is extremely high, so it can be easily removed after the reaction is completed. tp of [] target from the reactant. ! The purification process is much simpler than conventional methods.
よって未発明により、5−(4−ピリジル)オキサソー
ルをT業的に有利に製造することができる。Therefore, without the invention, 5-(4-pyridyl)oxazole can be produced advantageously in terms of T industry.
4ν訂出顧人 4′?詐出願人 代 理 人 目木合成化学T業株式会社 第一製薬株式会社4v revised consultant 4′? fraudulent applicant representative person Megi Synthetic Chemical T-gyo Co., Ltd. Daiichi Pharmaceutical Co., Ltd.
Claims (2)
ン酸を加熱して脱炭酸することにより5−(4−ピリジ
ル)オキサゾールを製造するにあたり、水を含有する非
プロトン性アミドの存在下で反応を行うことを特徴とす
る5−(4−ピリジル)オキサゾールの製造法。(1) In producing 5-(4-pyridyl)oxazole by heating and decarboxylating 5-(4-pyridyl)oxazole-4-carboxylic acid, in the presence of an aprotic amide containing water. A method for producing 5-(4-pyridyl)oxazole, which comprises carrying out a reaction.
の存在下で反応を行うことを特徴とする請求項1記載の
製造法。(2) The production method according to claim 1, characterized in that the reaction is carried out in the presence of an aprotic amide having a water content of 0.1 to 50% by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11315089A JP2769354B2 (en) | 1989-05-03 | 1989-05-03 | Method for producing 5- (4-pyridyl) oxazole |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11315089A JP2769354B2 (en) | 1989-05-03 | 1989-05-03 | Method for producing 5- (4-pyridyl) oxazole |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02292283A true JPH02292283A (en) | 1990-12-03 |
JP2769354B2 JP2769354B2 (en) | 1998-06-25 |
Family
ID=14604837
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11315089A Expired - Fee Related JP2769354B2 (en) | 1989-05-03 | 1989-05-03 | Method for producing 5- (4-pyridyl) oxazole |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2769354B2 (en) |
-
1989
- 1989-05-03 JP JP11315089A patent/JP2769354B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2769354B2 (en) | 1998-06-25 |
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