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JPH0674255B2 - Process for producing compound containing pyrazine nucleus - Google Patents
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JPH0674255B2 - Process for producing compound containing pyrazine nucleus - Google Patents

Process for producing compound containing pyrazine nucleus

Info

Publication number
JPH0674255B2
JPH0674255B2 JP61138441A JP13844186A JPH0674255B2 JP H0674255 B2 JPH0674255 B2 JP H0674255B2 JP 61138441 A JP61138441 A JP 61138441A JP 13844186 A JP13844186 A JP 13844186A JP H0674255 B2 JPH0674255 B2 JP H0674255B2
Authority
JP
Japan
Prior art keywords
general formula
zinc
present
catalyst
main component
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
Application number
JP61138441A
Other languages
Japanese (ja)
Other versions
JPS62294668A (en
Inventor
敬和 丹羽
孝幸 小路
伸幸 阿部
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.)
Koei Chemical Co Ltd
Original Assignee
Koei Chemical Co Ltd
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 Koei Chemical Co Ltd filed Critical Koei Chemical Co Ltd
Priority to JP61138441A priority Critical patent/JPH0674255B2/en
Publication of JPS62294668A publication Critical patent/JPS62294668A/en
Publication of JPH0674255B2 publication Critical patent/JPH0674255B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明はピラジン核を含有する化合物の製造方法に関し
さらに詳しくはジアミン類を銅および/または亜鉛を主
要成分とする触媒の存在下、気相反応させてピラジン核
を含有する化合物の製造方法である。
TECHNICAL FIELD The present invention relates to a process for producing a compound containing a pyrazine nucleus, more specifically, a diamine is reacted in a gas phase in the presence of a catalyst containing copper and / or zinc as a main component. And a method for producing a compound containing a pyrazine nucleus.

ピラジン類は香料、医薬、農薬の中間体として有用であ
る。
Pyrazines are useful as intermediates for fragrances, medicines and agricultural chemicals.

従来技術と本発明が解決しようとする問題点 従来ピラジン類の製造方法としては (1)ピペラジンの脱水素による方法(特開昭60−1694
68号公報)、(2)エチレングリコールのごときジオー
ル類とエチレンジアミンのごときジアミン類を原料とし
て脱水、脱水素反応する方法(特公昭55−50024号公
報)、(3)アルカノールアミンを環化脱水素する方法
(特開昭60−258168号公報)などが知られているが目的
物によってはこれらは有効な方法であるが、原料の入手
難あるいは目的物の種類によって使いわけしなければな
らない。
Problems to be Solved by the Prior Art and the Present Invention Conventional methods for producing pyrazines include (1) a method by dehydrogenation of piperazine (Japanese Patent Laid-Open No. 60-1694
No. 68), (2) dehydration and dehydrogenation reaction using diols such as ethylene glycol and diamines such as ethylenediamine as raw materials (Japanese Patent Publication No. 5550024), and (3) cyclodehydrogenation of alkanolamines. There are known methods (Japanese Patent Laid-Open No. 60-258168) and the like, which are effective methods depending on the intended product, but they must be used properly depending on the difficulty of obtaining the raw materials or the type of the intended product.

又、主生成物以外の副生成物が出来る場合があり、副生
成物は通常位置異性体の場合が多く、ピラジン類の位置
異性体は分離が困難でありそれぞれの方法に一長一短が
あった。
Further, there are cases where by-products other than the main product are produced, and by-products are usually regioisomers in many cases, and regioisomers of pyrazines are difficult to separate, and each method has advantages and disadvantages.

問題点を解決するための手段 本発明者らは、これらの点について鋭意検討した結果、
ジアミン類を銅および/または亜鉛を主要成分とする触
媒存在下、気相反応させることによりピラジン核を有す
る化合物が生成することを見出し本発明を完成させた。
特に本出願方法は一般式 で示されるフェナジンのごとき縮合環をもつピラジン誘
導体の合成法として好ましい。
Means for Solving Problems As a result of diligent study on these points,
The present invention has been completed by finding that a compound having a pyrazine nucleus is produced by reacting a diamine in the gas phase in the presence of a catalyst containing copper and / or zinc as a main component.
In particular, this application method Is preferred as a method for synthesizing a pyrazine derivative having a condensed ring such as phenazine.

本発明は一般式 (式中R1,R2は水素又は炭素数1乃至6の炭化水素基を
示す) もしくは一般式 (式中R3は炭素数3乃至4の炭化水素残基、(H)はC
−C間が一重結合のときは水素が存在し2重結合ときは
水素がないことを示す) であらわされるジアミン類を銅および/または亜鉛を主
要成分とする触媒の存在下気相接触反応せしめることを
特徴とする一般式 (式中R1,R2は前記と同じ) もしくは一般式 (式中R3は前記と同じ) で示されるピラジン核を含有する化合物の製造法に関す
るものである。
The present invention has the general formula (Wherein R 1 and R 2 represent hydrogen or a hydrocarbon group having 1 to 6 carbon atoms) or the general formula (In the formula, R 3 is a hydrocarbon residue having 3 to 4 carbon atoms, (H) is C
When C is a single bond, hydrogen is present, and when a double bond is present, hydrogen is absent.) A diamine represented by is reacted in the gas phase in the presence of a catalyst containing copper and / or zinc as a main component. General formula characterized by (Wherein R 1 and R 2 are the same as above) or the general formula (Wherein R 3 is the same as the above), and to a method for producing a compound containing a pyrazine nucleus.

本発明に於ける銅および/または亜鉛を主要成分とする
触媒としては銅化合物又は亜鉛化合物を含む触媒であれ
ばよいが、酸化物が好ましい。
The catalyst containing copper and / or zinc as a main component in the present invention may be a catalyst containing a copper compound or a zinc compound, but an oxide is preferable.

又他の金属化合物を含有していてもよく例えばクロム、
バリウム、カルシウム、マンガン、スズ、ビスマス、ト
リウム、チタン、アルミニウム、シリカ、などの1種も
しくは2種以上の金属化合物があげられるが、これら以
外の金属化合物を用いることも出来る。該触媒の特に好
ましい具体例としては酸化銅、銅−クロム、酸化銅−酸
化亜鉛などがあげられる。
It may also contain other metal compounds such as chromium,
Examples thereof include one or more metal compounds such as barium, calcium, manganese, tin, bismuth, thorium, titanium, aluminum and silica, but metal compounds other than these can also be used. Particularly preferred specific examples of the catalyst include copper oxide, copper-chromium, copper oxide-zinc oxide and the like.

又該触媒は担体としてシリカ、ゼオライト、シリカアル
ミナ、けいそう土、シリコンカーバイトなどを用いるこ
とも可能である。本発明中一般式(I)に示されるジア
ミン類としては、エチレンジアミン、2,3−ジアミノブ
タンなどがあげられる。
The catalyst may use silica, zeolite, silica-alumina, diatomaceous earth, silicon carbide or the like as a carrier. Examples of the diamines represented by the general formula (I) in the present invention include ethylenediamine and 2,3-diaminobutane.

一般式(II)で示されるジアミンとしては、o−フェニ
レンジアミン、1,2−ジアミノシクロペンタンなどがあ
げられる。
Examples of the diamine represented by the general formula (II) include o-phenylenediamine and 1,2-diaminocyclopentane.

本発明に於ける反応温度は200℃乃至500℃であり好しく
は250乃至400℃である。
The reaction temperature in the present invention is 200 to 500 ° C, preferably 250 to 400 ° C.

本発明に於て、一般式(I),(II)で示されるジアミ
ン類を反応させる際、希釈剤として水,ベンゼン,ピリ
ジン,窒素,水素,アンモニアなど反応に関与しない化
合物を使用することが出来る。
In the present invention, when the diamines represented by the general formulas (I) and (II) are reacted, it is preferable to use compounds such as water, benzene, pyridine, nitrogen, hydrogen, and ammonia that do not participate in the reaction as diluents. I can.

本発明を実施するには、通常触媒を充填し且つ所定の反
応温度に保持した固定床又は流動床反応器に原料ガスを
導入して触媒と接触させればよい。触媒との接触時間も
広範囲に変化させることが出来、空間速度は50乃至2000
0Hr-1、好ましくは100乃至5000Hr-1である。
In order to carry out the present invention, a raw material gas may be introduced into a fixed bed or fluidized bed reactor which is usually filled with a catalyst and kept at a predetermined reaction temperature and brought into contact with the catalyst. The contact time with the catalyst can be changed over a wide range, and the space velocity is 50 to 2000.
It is 0 Hr -1 , preferably 100 to 5000 Hr -1 .

本発明で得られた反応物は、常法に従って例えば蒸留等
によって分離精製が可能である。
The reaction product obtained in the present invention can be separated and purified by a conventional method such as distillation.

実施例1 硝酸亜鉛182gを含む水溶液と25%アンモニア水100gとを
混合しヒドロゲルを得た。
Example 1 An aqueous solution containing 182 g of zinc nitrate and 100 g of 25% aqueous ammonia were mixed to obtain a hydrogel.

得られた沈殿物を過,水洗後、110℃で乾燥し400℃で
3時間焼成して酸化亜鉛触媒を得た。得られた触媒を内
径12mmのパイレックス製反応管に6g充填し400℃に保持
した。
The obtained precipitate was washed with water, dried at 110 ° C., and calcined at 400 ° C. for 3 hours to obtain a zinc oxide catalyst. 6 g of a Pyrex reaction tube having an inner diameter of 12 mm was filled with the obtained catalyst and kept at 400 ° C.

この反応器にエチレンジアミン4.8gHr,H2O1g/Hrをガス
状で2時間反応させたところピラジンを収率48%で得
た。
When ethylenediamine 4.8 g Hr and H 2 O 1 g / Hr were reacted in a gaseous state for 2 hours in this reactor, pyrazine was obtained in a yield of 48%.

実施例2 硝酸銅46g,硝酸亜鉛128gを含む水溶液に約25%アンモニ
ア水84gを加え、pH7としヒドロゲルを得た。得られた沈
殿物を過、水洗後80℃で乾燥し、500℃で5時間焼成
して、酸化銅−酸化亜鉛触媒(重量比30:70)を得た。
Example 2 To an aqueous solution containing 46 g of copper nitrate and 128 g of zinc nitrate, 84 g of about 25% ammonia water was added to adjust the pH to 7 to obtain a hydrogel. The obtained precipitate was washed with water, dried at 80 ° C., and calcined at 500 ° C. for 5 hours to obtain a copper oxide-zinc oxide catalyst (weight ratio 30:70).

この触媒6gを実施例1と同じ反応器に充填し400℃に保
持したところo−フェニレンジアミン4.6g/Hr,アンモニ
ア1.5/Hr,ベンゼン5g/Hrの混合物をガス状で通したと
ころ、フェナジンを収率51%で得た。
When 6 g of this catalyst was charged in the same reactor as in Example 1 and kept at 400 ° C., a mixture of 4.6 g / Hr of o-phenylenediamine, 1.5 / Hr of ammonia, and 5 g / Hr of benzene was passed in a gaseous state, and phenazine was found Obtained with a yield of 51%.

実施例3〜5 実施例1と同一方法で下記に示す触媒を用いて1,2−ジ
アミノプロパン0.07モル/Hr,H2O0.04モル/Hrで流したと
ころ表−1の結果を得た。
Examples 3 to 5 In the same manner as in Example 1, using the catalyst shown below and flowing 1,2-diaminopropane 0.07 mol / Hr, H 2 O 0.04 mol / Hr, the results shown in Table 1 were obtained. .

実施例6 2,3−ジアミノブタン3g/Hr,H2O3.0g/Hrを原料とする以
外は、実施例1に従って反応したところ、2,3,5,6−テ
トラメチルピラジンを収率45%で得た。
Example 6 The reaction was carried out according to Example 1 except that 3 g / Hr of 2,3-diaminobutane and 3.0 g / Hr of H 2 O were used as starting materials, and yielded 2,3,5,6-tetramethylpyrazine in a yield of 45. Earned in%.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C07D 241/46 8615−4C ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C07D 241/46 8615-4C

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】一般式 (式中、R1,R2は水素又は炭素数1乃至6の炭化水素基
を示す) もしくは一般式 (式中R3は炭素数3乃至4の炭化水素残基、(H)はC
−C間が単結合のときは水素が存在し2重結合のときは
水素がないことを示す) であらわされるジアミン類を銅および/または亜鉛を主
要成分とする触媒の存在下気相接触反応せしめることを
特徴とする一般式 (式中R1,R2は前記と同じ) もしくは一般式 (式中R3は前記と同じ) でされるピラジン核を含有する化合物の製造法
1. A general formula (Wherein R 1 and R 2 represent hydrogen or a hydrocarbon group having 1 to 6 carbon atoms) or the general formula (In the formula, R 3 is a hydrocarbon residue having 3 to 4 carbon atoms, (H) is C
When C is a single bond, hydrogen is present, and when it is a double bond, hydrogen is absent.) A diamine represented by the formula) is present in the presence of a catalyst containing copper and / or zinc as a main component in the presence of a gas phase catalytic reaction. General formula characterized by (Wherein R 1 and R 2 are the same as above) or the general formula (Wherein R 3 is the same as above) and a method for producing a compound containing a pyrazine nucleus
【請求項2】一般式(I)で示される化合物がエチレン
ジアミン、1,2−ジアミノプロパン、ジアミノブタンで
ある特許請求の範囲第1項記載の方法
2. The method according to claim 1, wherein the compound represented by the general formula (I) is ethylenediamine, 1,2-diaminopropane or diaminobutane.
【請求項3】一般式(II)で示される化合物がo−フェ
ニレンジアミンである特許請求の範囲の第1項記載の方
3. The method according to claim 1, wherein the compound represented by the general formula (II) is o-phenylenediamine.
【請求項4】銅および/または亜鉛を主要成分とする触
媒が酸化銅および/または酸化亜鉛を主要成分とする触
媒である特許請求の範囲第1項記載の方法
4. The method according to claim 1, wherein the catalyst containing copper and / or zinc as a main component is a catalyst containing copper oxide and / or zinc oxide as a main component.
JP61138441A 1986-06-13 1986-06-13 Process for producing compound containing pyrazine nucleus Expired - Lifetime JPH0674255B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61138441A JPH0674255B2 (en) 1986-06-13 1986-06-13 Process for producing compound containing pyrazine nucleus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61138441A JPH0674255B2 (en) 1986-06-13 1986-06-13 Process for producing compound containing pyrazine nucleus

Publications (2)

Publication Number Publication Date
JPS62294668A JPS62294668A (en) 1987-12-22
JPH0674255B2 true JPH0674255B2 (en) 1994-09-21

Family

ID=15222065

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61138441A Expired - Lifetime JPH0674255B2 (en) 1986-06-13 1986-06-13 Process for producing compound containing pyrazine nucleus

Country Status (1)

Country Link
JP (1) JPH0674255B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113816912B (en) * 2021-08-30 2023-02-28 上海日异生物科技有限公司 Preparation method of phenazine

Also Published As

Publication number Publication date
JPS62294668A (en) 1987-12-22

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