JPH01193246A - Production of 2,3-dichloropyridine - Google Patents
Production of 2,3-dichloropyridineInfo
- Publication number
- JPH01193246A JPH01193246A JP63016284A JP1628488A JPH01193246A JP H01193246 A JPH01193246 A JP H01193246A JP 63016284 A JP63016284 A JP 63016284A JP 1628488 A JP1628488 A JP 1628488A JP H01193246 A JPH01193246 A JP H01193246A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- raney
- trichloropyridine
- dichloropyridine
- hydrogen
- 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
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
- Pyridine Compounds (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
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−ジクロロ
ピリジンを製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing 2,3-dichloropyridine, which is useful as an agricultural and pharmaceutical intermediate.
2.3−ジクロロピリジン(以下2.3−DCP)の製
造法としては、ピリジンもしくはピリジン塩酸塩の液相
塩素化により製造する方法(特開昭61−249965
号)やピリジンの気相塩素化により製造する方法(特開
昭58−206564号)などがある。また、ピリジン
の塩化パラジウム錯体の塩素化により製造する方法(S
ynthesis、 5,378(1980) )があ
る。2.3-dichloropyridine (hereinafter referred to as 2.3-DCP) can be produced by liquid phase chlorination of pyridine or pyridine hydrochloride (Japanese Unexamined Patent Publication No. 61-249965).
(No.) and a method of producing by gas phase chlorination of pyridine (Japanese Patent Application Laid-open No. 206564/1983). In addition, a method for producing by chlorination of palladium chloride complex of pyridine (S
Synthesis, 5, 378 (1980)).
しかしながら、上記方法において塩化パラジウムを用い
る方法では、収率は良いが、高価な塩化パラジウムを基
質に対して当量用いるため、実用上問題がある。また他
の方法では、目的物である2、、3−DCPはピリジン
多塩素化物との混合物として得られ、さらに反応収率も
10〜15%と非常に低いという欠点があった。このた
めに、更に目的物の精製に蒸留等の操作を用いざるを得
す、煩雑になると共に収率の一層の低下は避けえなかっ
た。However, the method using palladium chloride in the above method has a good yield, but has a practical problem because an equivalent amount of expensive palladium chloride is used relative to the substrate. In other methods, the target product 2,,3-DCP is obtained as a mixture with polychlorinated pyridine, and the reaction yield is also very low at 10 to 15%. For this reason, operations such as distillation have to be used for further purification of the target product, which becomes complicated and further decreases in yield are unavoidable.
本発明者は、2,3.6−)ジクロロピリジン(以下T
RCPという)を用いる収率の良い2.3−DCPの製
造法を鋭意検討した結果、触媒の存在下、水素と反応さ
せると選択的に2.3−ジクロロピリジンが得られるこ
とを見出し、本発明に至った。The present inventor has discovered that 2,3,6-)dichloropyridine (hereinafter T
As a result of intensive investigation into a method for producing 2.3-DCP with good yield using RCP, we discovered that 2,3-dichloropyridine can be selectively obtained by reacting with hydrogen in the presence of a catalyst. This led to the invention.
即ち、本発明はTRCPを触媒の存在下、水素と反応さ
せることを特徴とする2、3−DCPの製造法を提供す
るものである。That is, the present invention provides a method for producing 2,3-DCP, which is characterized by reacting TRCP with hydrogen in the presence of a catalyst.
TRCPは、例えばピリジンの光塩素化で2゜6−トリ
クロルピリジンとした後、更に塩化第二鉄触媒存在下で
塩素化することにより容易に得ることができる。TRCP can be easily obtained, for example, by photochlorinating pyridine to form 2°6-trichloropyridine and then further chlorinating it in the presence of a ferric chloride catalyst.
上記触媒としては、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挙げられる。Examples of the catalyst include platinum metals such as palladium, platinum, ruthenium, and rhodium, and Raney catalysts such as Raney nickel and Raney copper.
これらの触媒は炭素、シリカ等の担体に担持されたもの
でもよい。These catalysts may be supported on a carrier such as carbon or silica.
又、この様な本発明の触媒の含水率が高いと、更に水添
が進みモノクロロピリジンあるいはピリジンにまで変化
する傾向が高くなる。従って触媒中の水分は19wt%
以下、更には2〜3wt%以下である事が好ましい。Furthermore, if the water content of the catalyst of the present invention is high, there is a high tendency for hydrogenation to proceed further and change to monochloropyridine or pyridine. Therefore, the water content in the catalyst is 19wt%
The content is preferably 2 to 3 wt% or less.
触媒の量は金属基準でTRCPに対し、0.01〜20
重量%、好ましくは0.1〜1重量%が適当である。The amount of catalyst is 0.01 to 20% of TRCP on a metal basis.
% by weight, preferably from 0.1 to 1% by weight, is suitable.
本発明の方法を行うのに溶媒の使用は必ずし−も必要で
はないが、ヘキサン、ヘプタンのような炭化水素類、メ
タノール、エタノーノペ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してもよい。その量は水
素化分解するピリジン塩素化物を溶解させるに足りる量
で良く、通常水素化分解するピリジン塩素化物に対して
0.5〜4重量倍用いられる。Although the use of solvents is not necessary in carrying out the process of the invention, hydrocarbons such as hexane, heptane, alcohols such as methanol, ethanol, nopeisopropyl alcohol, formic acid, acetic acid, etc. Organic acids, esters such as ethyl acetate, etc. may also be used. The amount thereof may be sufficient to dissolve the pyridine chloride to be hydrogenolyzed, and is usually used in an amount of 0.5 to 4 times the weight of the pyridine chloride to be hydrogenolyzed.
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促進される。Note that the reaction is accelerated by the addition of a base such as sodium acetate, triethylamine, or sodium carbonate.
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
る温度範囲で適時選択される。通常は0〜200℃、好
ましくは30〜150℃の間で行われる。The reaction temperature is appropriately selected within a temperature range that is higher than the minimum temperature at which the reaction substantially proceeds, and that maintains a certain degree of selectivity and can be easily carried out industrially. It is usually carried out at a temperature of 0 to 200°C, preferably 30 to 150°C.
圧力は、常圧、加圧どちらにおいても実施できる。The pressure can be either normal pressure or increased pressure.
反応させる水素の量、又反応時間は反応器の形状、容積
、構造、水素の吹き込み方法等に応じて適当に選択すれ
ばよい。The amount of hydrogen to be reacted and the reaction time may be appropriately selected depending on the shape, volume, structure, hydrogen blowing method, etc. of the reactor.
反応後の後処理法としては、触媒を濾過、又はデカンテ
ーションで除去(これは再使用する)した後、溶媒を留
去し、水洗浄により塩基物を分離除去した後、分留によ
り精製する方法が効率的である。After the reaction, the post-treatment method is to remove the catalyst by filtration or decantation (this will be reused), distill off the solvent, separate and remove the base by washing with water, and then purify by fractional distillation. The method is efficient.
本発明の方法によれば、簡便なプロセスにより反応、後
処理が実施でき、また極めて高い選択率で目的とする2
、3−ジクロロピリジンを製造することができる。According to the method of the present invention, the reaction and post-treatment can be carried out through a simple process, and the desired 2
, 3-dichloropyridine can be produced.
以下に実施例により本発明を説明するが、本発明はこれ
らの実施例に限定されるものではない。The present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples.
実施例1
還流管、水素ガス吹き込み管、温度計及び撹拌器を備え
た500m1の四つロフラスコに2.3.6−ドリクロ
ロビリジン86.7g (0,48モル)、酢酸ナトリ
ウム39.4g (0,48モル)、炭素上パラジウム
5重量%の触媒(水分1%以下)2.0g。Example 1 86.7 g (0.48 mol) of 2.3.6-dolichloropyridine and 39.4 g of sodium acetate ( 0.48 mol), 2.0 g of a catalyst containing 5% by weight of palladium on carbon (less than 1% moisture).
及び酢酸300.0 gを仕込み、50℃に加温した。and 300.0 g of acetic acid were charged and heated to 50°C.
50℃を維持しながらガス吹き込み管より水素ガスをl
l/Hの速度で14時間連続的に吹き込み水素化分解を
行った。反応後の組成は、2.3−ジクロロピリジン3
3%、原料である2、3.6−)ジクロロピリジン62
%、その他5%であった。Inject 1 liter of hydrogen gas from the gas blowing pipe while maintaining the temperature at 50°C.
Hydrogenolysis was carried out by blowing continuously for 14 hours at a rate of 1/H. The composition after the reaction is 2,3-dichloropyridine 3
3%, raw material 2,3.6-)dichloropyridine 62
%, and others 5%.
Claims (1)
と反応させることを特徴とする2,3−ジクロロピリジ
ンの製造法。A method for producing 2,3-dichloropyridine, which comprises reacting 2,3,6-trichloropyridine with hydrogen in the presence of a catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63016284A JP2523753B2 (en) | 1988-01-27 | 1988-01-27 | Method for producing 2,3-dichloropyridine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63016284A JP2523753B2 (en) | 1988-01-27 | 1988-01-27 | Method for producing 2,3-dichloropyridine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01193246A true JPH01193246A (en) | 1989-08-03 |
| JP2523753B2 JP2523753B2 (en) | 1996-08-14 |
Family
ID=11912253
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63016284A Expired - Fee Related JP2523753B2 (en) | 1988-01-27 | 1988-01-27 | Method for producing 2,3-dichloropyridine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2523753B2 (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102153507A (en) * | 2011-03-13 | 2011-08-17 | 联化科技股份有限公司 | Preparation method of 2,3-dichloropyridine |
| CN103145609A (en) * | 2013-03-05 | 2013-06-12 | 衢州恒顺化工有限公司 | Preparation method of 2,3-dichloropyridine |
| CN103232388A (en) * | 2013-05-07 | 2013-08-07 | 山东天信化工有限公司 | Method for separating 2, 3-dichloropyridine from 2, 3, 6-trichloropyridine |
| CN107597107A (en) * | 2017-08-30 | 2018-01-19 | 重庆中邦科技有限公司 | A kind of 2,3 dichloropyridine production catalyst and preparation method thereof |
| CN109225293A (en) * | 2018-10-15 | 2019-01-18 | 安徽绩溪县徽煌化工有限公司 | A kind of processing method improving 2,3- dichloropyridine output capacity catalyst |
| CN109453786A (en) * | 2018-12-03 | 2019-03-12 | 西安凯立新材料股份有限公司 | A kind of catalyst and its preparation method and application being used to prepare 2,3- dichloropyridine |
| CN112479990A (en) * | 2020-12-17 | 2021-03-12 | 重庆华歌生物化学有限公司 | High-efficiency synthesis method of 2, 3-dichloropyridine |
| CN114192140A (en) * | 2021-12-30 | 2022-03-18 | 西安凯立新材料股份有限公司 | Catalyst for synthesizing 2, 3-dichloropyridine and preparation method thereof |
| CN117358270A (en) * | 2023-10-11 | 2024-01-09 | 利尔化学股份有限公司 | A kind of catalyst for synthesizing 2,3-dichloropyridine and its preparation method and application |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105642280B (en) * | 2016-03-17 | 2018-07-31 | 西安凯立新材料股份有限公司 | Continuous production 2,3- dichloropyridine catalyst and its preparation method and application |
-
1988
- 1988-01-27 JP JP63016284A patent/JP2523753B2/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102153507A (en) * | 2011-03-13 | 2011-08-17 | 联化科技股份有限公司 | Preparation method of 2,3-dichloropyridine |
| WO2012122746A1 (en) * | 2011-03-13 | 2012-09-20 | 联化科技股份有限公司 | Method for preparing 2,3-dichloropyridine |
| CN103145609A (en) * | 2013-03-05 | 2013-06-12 | 衢州恒顺化工有限公司 | Preparation method of 2,3-dichloropyridine |
| CN103232388A (en) * | 2013-05-07 | 2013-08-07 | 山东天信化工有限公司 | Method for separating 2, 3-dichloropyridine from 2, 3, 6-trichloropyridine |
| CN107597107A (en) * | 2017-08-30 | 2018-01-19 | 重庆中邦科技有限公司 | A kind of 2,3 dichloropyridine production catalyst and preparation method thereof |
| CN109225293A (en) * | 2018-10-15 | 2019-01-18 | 安徽绩溪县徽煌化工有限公司 | A kind of processing method improving 2,3- dichloropyridine output capacity catalyst |
| CN109453786A (en) * | 2018-12-03 | 2019-03-12 | 西安凯立新材料股份有限公司 | A kind of catalyst and its preparation method and application being used to prepare 2,3- dichloropyridine |
| CN112479990A (en) * | 2020-12-17 | 2021-03-12 | 重庆华歌生物化学有限公司 | High-efficiency synthesis method of 2, 3-dichloropyridine |
| CN114192140A (en) * | 2021-12-30 | 2022-03-18 | 西安凯立新材料股份有限公司 | Catalyst for synthesizing 2, 3-dichloropyridine and preparation method thereof |
| CN117358270A (en) * | 2023-10-11 | 2024-01-09 | 利尔化学股份有限公司 | A kind of catalyst for synthesizing 2,3-dichloropyridine and its preparation method and application |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2523753B2 (en) | 1996-08-14 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |