JPH0791270B2 - Method for producing 2,3,5-trichloropyridine - Google Patents
Method for producing 2,3,5-trichloropyridineInfo
- Publication number
- JPH0791270B2 JPH0791270B2 JP62108564A JP10856487A JPH0791270B2 JP H0791270 B2 JPH0791270 B2 JP H0791270B2 JP 62108564 A JP62108564 A JP 62108564A JP 10856487 A JP10856487 A JP 10856487A JP H0791270 B2 JPH0791270 B2 JP H0791270B2
- Authority
- JP
- Japan
- Prior art keywords
- trichloropyridine
- tetrachloropyridine
- reaction
- producing
- catalyst
- 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 - Lifetime
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Pyridine Compounds (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、農・医薬中間体として、有用な2,3,5−トリ
クロロピリジンを製造する方法に関する。TECHNICAL FIELD The present invention relates to a method for producing 2,3,5-trichloropyridine, which is useful as an agricultural / pharmaceutical intermediate.
(従来技術) 2,3,5−トリクロロピリジンの製造法はいくつか知られ
ている。しかし、収率が良く、プロセスも効率が良いと
いう例は少なく、実際に工業化が困難と考えられる例が
多い。比較的、効率の良い例としては、2−ピリドン又
は2−アミノピリジンの3位、5位を塩素化した後、2
位の水酸基(カルボニル基)、アミノ基を塩素化する方
法がある。(英国特許1,215,387、特開昭53−68783、特
開昭54−59283、米国特許4287347)又、2,3,5,6−テト
ラクロロピリジンのα位を還元する方法もある。還元剤
としては、亜鉛(J.Hetero−cycl Chem17.493.米国特許
4259495、4258194、4111938)、電解法(Eur.Pat.1806
9)、水素化リチウムアルミニウム(J.C.S.D(20)121
1)などが用いられている。(Prior Art) Several methods for producing 2,3,5-trichloropyridine are known. However, there are few cases where the yield is good and the process is efficient, and there are many cases where industrialization is actually considered difficult. As a relatively efficient example, 2-pyridone or 2-aminopyridine is chlorinated at the 3-position and 5-position, and then 2
There is a method of chlorinating the hydroxyl group (carbonyl group) at the position and the amino group. (British Patent 1,215,387, JP-A-53-68783, JP-A-54-59283, US Pat. No. 4,287,347) Also, there is a method of reducing the α-position of 2,3,5,6-tetrachloropyridine. As a reducing agent, zinc (J. Hetero-cycl Chem 17 .493. US Patent
4259495, 4258194, 4111938), electrolytic method (Eur.Pat.1806
9), lithium aluminum hydride (JCSD (20) 121
1) etc. are used.
(発明が解決しようとする問題点) 前記の2−ピリドン、2−アミノピリジンの塩素化法
は、原料が高価であり、かつ反応工程が長いためコスト
面で不利である。2,3,5,6−テトラクロロピリジンは比
較的安価に入手可能であるが、これまで知られている還
元法は、大量の溶媒を用いる必要があり、いわゆる空時
収率が悪い。又、還元剤として亜鉛を用いる場合、当量
必要であり、多量に生成する亜鉛塩の毒性のため、排水
により河川が汚染されるため、工業的に実施する場合は
亜鉛を回収することが必要となる。(Problems to be Solved by the Invention) The above-mentioned chlorination method for 2-pyridone and 2-aminopyridine is disadvantageous in cost because the raw materials are expensive and the reaction process is long. Although 2,3,5,6-tetrachloropyridine is relatively inexpensively available, the reduction methods known so far require the use of a large amount of solvent and the so-called space-time yield is poor. Also, when using zinc as a reducing agent, an equivalent amount is required, and because the toxicity of zinc salts produced in large amounts pollutes rivers by wastewater, it is necessary to recover zinc when industrially implemented. Become.
(問題を解決するための手段) 発明者らは2,3,5,6−テトラクロロピリジンを用いて、
効率が良く、かつ排水等の公害問題の生ずることのな
い、2,3,5−トリクロロピリジンの製造法を鋭意検討し
た結果、本発明に至った。即ち、2,3,5,6−テトラクロ
ロピリジンをパラジウム、白金などの白金属、又はラネ
ーニッケルなどの触媒存在下、水素と接触させることを
特徴とする方法である。2,3,5,6−テトラクロロピリジ
ンの水素接触還元法については従来例がなく、本発明が
初めての例である。(Means for Solving the Problem) The inventors have used 2,3,5,6-tetrachloropyridine to
The present invention has been achieved as a result of extensive studies on a method for producing 2,3,5-trichloropyridine that is highly efficient and does not cause pollution problems such as drainage. That is, the method is characterized in that 2,3,5,6-tetrachloropyridine is contacted with hydrogen in the presence of a white metal such as palladium or platinum, or a catalyst such as Raney nickel. There is no conventional example for the hydrogen catalytic reduction method of 2,3,5,6-tetrachloropyridine, and the present invention is the first example.
触媒としては、先に述べたように、パラジウム、白金、
ルテニウム、ロジウムなどの白金属、又はラネーニッケ
ル、ラネー銅等のラネー系触媒が用いられる。As the catalyst, as mentioned above, palladium, platinum,
A white metal such as ruthenium or rhodium, or a Raney catalyst such as Raney nickel or Raney copper is used.
溶媒としては、ヘキサン、ヘプタンのような炭化水素
類、メタノール、エタノール、イソプロピルアルコール
のようなアルコール類、ギ酸、酢酸のような有機酸、酢
酸エチルのようなエステルなどを使用できる。その量は
2,3,5,6−テトラクロロピリジンを溶解させるに足る量
で良く、通常、2,3,5,6−テトラクロロピリジンに対し
て、0.5〜3重量倍用いられる。なお、酢酸ナトリウ
ム、トリエチルアミン、炭酸ナトリウムなどの塩基の添
加によって反応はさらに促進される。反応温度は、実質
的に反応が進行する最低温度以上、及び、ある程度の選
択性を保ちかつ工業的に容易に実施できる温度範囲とし
て、通常0℃〜150℃の間で行なわれる。圧力は常圧、
加圧どちらにおいても実施できる。長時間の反応では、
目的物の2,3,5−トリクロロピリジンがさらに還元され
る恐れがあるため、進行度をGCクロマトグラフィー等で
チェックし、最も経済的な組成で反応を停止するべきで
ある。通常、2,6−ジクロロピリジン、2,3,6−トリクロ
ロピリジン等が若干副生するが、これらは蒸留により目
的物である2,3,5−トリクロロピリジンと分離でき、さ
らに塩素を作用させることにより、出発物である2,3,5,
6−テトラクロロピリジンとして回収可能である。As the solvent, hydrocarbons such as hexane and heptane, alcohols such as methanol, ethanol and isopropyl alcohol, organic acids such as formic acid and acetic acid, and esters such as ethyl acetate can be used. The amount is
The amount is sufficient to dissolve 2,3,5,6-tetrachloropyridine, and it is usually used in an amount of 0.5 to 3 times by weight that of 2,3,5,6-tetrachloropyridine. The reaction is further promoted by the addition of a base such as sodium acetate, triethylamine or sodium carbonate. The reaction temperature is generally at least the minimum temperature at which the reaction proceeds, and is a temperature range that maintains a certain degree of selectivity and can be easily carried out industrially, and is usually 0 ° C. to 150 ° C. Pressure is normal pressure,
It can be carried out under either pressure. In a long reaction,
Since the target 2,3,5-trichloropyridine may be further reduced, the progress should be checked by GC chromatography or the like to stop the reaction at the most economical composition. Usually, 2,6-dichloropyridine, 2,3,6-trichloropyridine, etc. are by-produced slightly, but these can be separated from the target 2,3,5-trichloropyridine by distillation, and chlorine is further applied. Therefore, the starting material is 2,3,5,
It can be recovered as 6-tetrachloropyridine.
反応後の後処理法としては、触媒をロ過、又はデカンテ
ーションで除去(これは再使用できる)した後、溶媒を
留去し、水洗浄により塩基物を分り除去した後、分留又
は再結晶により精製する方法が効率的である。As a post-treatment method after the reaction, the catalyst is removed by filtration or decantation (which can be reused), the solvent is distilled off, and the basic substance is removed by washing with water, followed by fractional distillation or re-dosing. The method of purifying by crystals is efficient.
(発明の効果) 本発明の方法によれば、安価な原料である2,3,5,6−テ
トラクロロピリジンを用いて反応、後処理が簡便であ
り、副生物を原料として回収することができる効率的な
プロセスにより2,3,5−トリクロロピリジンをつくるこ
とができる。又、亜鉛使用の場合のような排水等の公害
問題もない。(Effects of the Invention) According to the method of the present invention, the reaction using the inexpensive raw material 2,3,5,6-tetrachloropyridine, the post-treatment is simple, and the by-product can be recovered as the raw material. 2,3,5-trichloropyridine can be made by an efficient process that can be done. In addition, there is no problem of pollution such as drainage as in the case of using zinc.
(実施例) 次に本発明を実施例に基ずきさらに詳細に説明する。反
応は300ml SUS製のオートクレーブを用い、2,3,5,6−テ
トラクロロピリジン(純度96.8%、その他不純物とし
て、2,3,6−トリクロロピリジン1.5%、ペンタクロロピ
リジン1.7%を含む)を26.2g(1.2モル)、溶媒をテト
ラクロロピリジンに対して3重量倍、触媒として湿5%
Pd/C(含水率50%)1.3g仕込んだ。又各種塩基の添加量
は、テトラクロロピリジンに対して等モルを用いた。水
素圧は室温で、初圧15kg/cm2とし、50℃まで昇温しその
温度で圧力が0になるか又は圧力降下が止まるまで反応
させた。結果を次表にまとめる。EXAMPLES Next, the present invention will be described in more detail based on examples. The reaction was carried out using a 300 ml SUS autoclave, containing 2,3,5,6-tetrachloropyridine (purity 96.8%, other impurities including 2,3,6-trichloropyridine 1.5%, pentachloropyridine 1.7%). 26.2g (1.2mol), solvent is 3 times the weight of tetrachloropyridine, 5% wet as catalyst
1.3 g of Pd / C (water content 50%) was charged. The addition amount of each base was equimolar to tetrachloropyridine. The hydrogen pressure was room temperature, the initial pressure was 15 kg / cm 2 , the temperature was raised to 50 ° C., and the reaction was continued until the pressure became 0 or the pressure drop stopped. The results are summarized in the table below.
Claims (1)
存在下、水素と反応せしめることを特徴とする、2,3,5
−トリクロロピリジンの製造法1. A method comprising reacting 2,3,5,6-tetrachloropyridine with hydrogen in the presence of a catalyst.
-Method for producing trichloropyridine
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62108564A JPH0791270B2 (en) | 1987-05-01 | 1987-05-01 | Method for producing 2,3,5-trichloropyridine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62108564A JPH0791270B2 (en) | 1987-05-01 | 1987-05-01 | Method for producing 2,3,5-trichloropyridine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63275565A JPS63275565A (en) | 1988-11-14 |
JPH0791270B2 true JPH0791270B2 (en) | 1995-10-04 |
Family
ID=14488023
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62108564A Expired - Lifetime JPH0791270B2 (en) | 1987-05-01 | 1987-05-01 | Method for producing 2,3,5-trichloropyridine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0791270B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6051714A (en) * | 1998-03-12 | 2000-04-18 | Reilly Industries, Inc. | Processes for dechlorinating pyridines |
CN103664755B (en) * | 2013-12-31 | 2016-07-13 | 沈阳化工研究院有限公司 | A kind of preparation method of dichloromethyl substituted pyridines |
CN108341767A (en) * | 2017-01-24 | 2018-07-31 | 盐城恒盛化工有限公司 | A method of preparing 2,3,5- trichloropyridines |
CN106866647A (en) * | 2017-03-31 | 2017-06-20 | 九江善水科技股份有限公司 | The synthetic method of Yi Zhong Evil grass ethers and its trichloropyridine of intermediate 2,3,5 |
CN110551062A (en) * | 2019-09-16 | 2019-12-10 | 西安凯立新材料股份有限公司 | Method for preparing 2,3, 5-trichloropyridine by adopting 2,3,5, 6-tetrachloropyridine |
-
1987
- 1987-05-01 JP JP62108564A patent/JPH0791270B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS63275565A (en) | 1988-11-14 |
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