JPH0910596A - Catalyst for oxidative dehydrogenation reaction and preparation of alpha,beta-unsaturated carbonyl compound - Google Patents
Catalyst for oxidative dehydrogenation reaction and preparation of alpha,beta-unsaturated carbonyl compoundInfo
- Publication number
- JPH0910596A JPH0910596A JP7187897A JP18789795A JPH0910596A JP H0910596 A JPH0910596 A JP H0910596A JP 7187897 A JP7187897 A JP 7187897A JP 18789795 A JP18789795 A JP 18789795A JP H0910596 A JPH0910596 A JP H0910596A
- Authority
- JP
- Japan
- Prior art keywords
- compound
- catalyst
- acetic acid
- unsaturated carbonyl
- general formula
- Prior art date
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Classifications
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- 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
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- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、アリルアルコール類を
酸化脱水素反応してα,β−不飽和カルボニル化合物類
を製造するための触媒および当該触媒の存在下にアリル
アルコール類を酸素雰囲気下で酸化脱水素反応してα,
β−不飽和カルボニル化合物類を製造する方法に関す
る。TECHNICAL FIELD The present invention relates to a catalyst for producing α, β-unsaturated carbonyl compounds by oxidative dehydrogenation of allyl alcohols, and allyl alcohols in an oxygen atmosphere in the presence of the catalyst. Oxidative dehydrogenation reaction at α,
It relates to a method for producing β-unsaturated carbonyl compounds.
【0002】[0002]
【従来の技術】α,β−不飽和カルボニル化合物類は香
料、医薬品など種々の工業薬品やその合成中間体などに
利用される有用な物質である。2. Description of the Related Art α, β-Unsaturated carbonyl compounds are useful substances used for various industrial chemicals such as fragrances and pharmaceuticals and their synthetic intermediates.
【0003】従来より、かかるα,β−不飽和カルボニ
ル化合物類の製造法としては、たとえば、アリルアルコ
ール類を活性二酸化マンガンや六価のクロム酸等の酸化
剤により酸化する方法が古くから知られている。しか
し、これらの酸化反応は量論反応であること、また酸化
剤として毒性のある重金属を用いるためその取り扱い性
に問題がある。Conventionally, as a method for producing such α, β-unsaturated carbonyl compounds, for example, a method of oxidizing allyl alcohols with an oxidizing agent such as active manganese dioxide or hexavalent chromic acid has long been known. ing. However, since these oxidation reactions are stoichiometric reactions and a toxic heavy metal is used as an oxidizing agent, there is a problem in handleability.
【0004】また、アルコール類より水素を引き抜いて
カルボニル化合物類を製造する酸化脱水素反応を、アリ
ルアルコール類に応用して、α,β−不飽和カルボニル
化合物類を製造することも考えられる。例えば、一般的
にアルコール類よりカルボニル化合物類を製造する方法
としては、銅触媒、亜鉛触媒などを充填した反応器の中
を、高温で水蒸気とともに気化させたアルコール類を、
流通させて酸化脱水素反応する方法が知られている(例
えば、特開昭51−16643号公報、特開昭51−1
3748号公報等)。しかし、これらの気相反応は高温
の反応条件にて行う必要があり、不飽和結合を有するア
リルアルコール類に応用した場合には、分解副反応が多
く、効率的な反応とはいえない。また、液相にてルテニ
ウムを触媒とし、次亜塩素酸を滴下してアルコール類を
酸化脱水素反応する方法が開示されている(例えば、特
開昭64−50836号公報、特開昭63−17494
6号公報、特開昭63−145248号公報、特開昭6
3−130552号公報、特開昭62−265244号
公報、特開昭56−22758号公報等)。しかし、こ
うした液相反応においては高価な次亜塩素酸を用いなけ
ればならず、さらには次亜塩素酸の不安定さから危険を
伴う不利がある。It is also conceivable to apply an oxidative dehydrogenation reaction for producing carbonyl compounds by extracting hydrogen from alcohols to allyl alcohols to produce α, β-unsaturated carbonyl compounds. For example, in general, as a method for producing carbonyl compounds from alcohols, alcohols vaporized with steam at high temperature in a reactor filled with a copper catalyst, a zinc catalyst, etc.
A method of circulating and conducting an oxidative dehydrogenation reaction is known (for example, JP-A-51-16643 and JP-A-51-1).
3748, etc.). However, these gas phase reactions need to be carried out under high temperature reaction conditions, and when applied to allyl alcohols having unsaturated bonds, many decomposition side reactions occur, and it cannot be said to be an efficient reaction. Further, a method has been disclosed in which ruthenium is used as a catalyst in a liquid phase and hypochlorous acid is added dropwise to carry out an oxidative dehydrogenation reaction of alcohols (for example, JP-A-64-50836 and JP-A-63-63). 17494
No. 6, JP-A-63-145248, JP-A-SHO-6
3-130552, JP-A-62-265244, JP-A-56-22758 and the like). However, in such a liquid phase reaction, expensive hypochlorous acid must be used, and further, there is a disadvantage in that hypochlorous acid is unstable because of its instability.
【0005】また最近では、アリルアルコール類を酸化
脱水素反応してα,β−不飽和カルボニル化合物類を製
造するための触媒として、イリジウムトリフェニルフォ
スフィンを用いる方法が報告されている(Journa
l of Organometallic Chemi
stry,356巻,381−8頁(1988))。し
かし、このような有機イリジウムは爆発の危険性を持っ
ており製造上の不利が大きい。また、ヘキサデカカルボ
ニル六ロジウムを酸化脱水素反応用触媒として用いる方
法(特開平3−93742号公報)も知られているが、
高価なロジウム化合物を使用すること、触媒が均一系で
あり分離、再利用が困難な点で不利がある。また、酸化
ルテニウムを酸化脱水素反応用触媒として用いる方法
(Journal of Organic Chemi
stry,49巻,3435−6頁(1984))も知
られているが、酸化ルテニウムの毒性から取り扱い上に
不利がある。また、シンナミルアルコールを、ビスマス
−白金をアルミナに担持した触媒を用いて、酸化脱水素
反応する方法(Journal of Catalys
is,131巻,131頁(1995))も知られてい
るが、ビスマスの毒性や、白金が高価なことから工業的
な製造には不利がある。Recently, a method using iridium triphenylphosphine as a catalyst for producing α, β-unsaturated carbonyl compounds by oxidative dehydrogenation of allyl alcohols has been reported (Journa).
l of Organometallic Chemi
story, 356, 381-8 (1988)). However, such organic iridium has a risk of explosion and has a large manufacturing disadvantage. A method using hexadecacarbonyl hexarhodium as a catalyst for oxidative dehydrogenation reaction (Japanese Patent Laid-Open No. 3-93742) is also known.
The use of expensive rhodium compounds is disadvantageous in that the catalyst is a homogeneous system and separation and reuse are difficult. Further, a method of using ruthenium oxide as a catalyst for oxidative dehydrogenation reaction (Journal of Organic Chemi)
Stry, Vol. 49, p. 3435-6 (1984)) is also known, but it is disadvantageous in handling because of the toxicity of ruthenium oxide. Further, a method of carrying out an oxidative dehydrogenation reaction of cinnamyl alcohol using a catalyst in which bismuth-platinum is supported on alumina (Journal of Catalysts).
is, 131, 131 (1995)), but it is disadvantageous for industrial production because of the toxicity of bismuth and the expensiveness of platinum.
【0006】[0006]
【発明が解決しようとする課題】本発明は、高価な酸化
剤を用いることなく、安全にかつ温和な反応条件で、ア
リルアルコール類よりα,β−不飽和カルボニル化合物
類を製造する方法を提供することを目的とする。DISCLOSURE OF THE INVENTION The present invention provides a method for producing α, β-unsaturated carbonyl compounds from allyl alcohols under safe and mild reaction conditions without using an expensive oxidizing agent. The purpose is to do.
【0007】[0007]
【課題を解決するための手段】本発明者らは、前記従来
技術の課題を解決すべく、酸化脱水素反応に使用する触
媒について鋭意研究を重ねた。その結果、以下に示す特
定のパラジウム化合物が、アリルアルコール類を酸化脱
水素反応してα,β−不飽和カルボニル化合物類を製造
するための触媒として高活性を有することを見出し本発
明を完成するに至った。Means for Solving the Problems In order to solve the above-mentioned problems of the prior art, the present inventors have conducted extensive studies on a catalyst used in an oxidative dehydrogenation reaction. As a result, they have found that the specific palladium compound shown below has high activity as a catalyst for producing α, β-unsaturated carbonyl compounds by oxidative dehydrogenation of allyl alcohols, thus completing the present invention. Came to.
【0008】すなわち本発明は、酢酸パラジウムと一酸
化炭素を酢酸中で反応させて得られるパラジウムカルボ
キシルアセテートに、含窒素化合物または酢酸化合物を
反応させて得られる懸濁化合物からなる、アリルアルコ
ール類を酸化脱水素反応してα,β−不飽和カルボニル
化合物類を製造するための触媒、酢酸パラジウムと一酸
化炭素を酢酸中で反応させて得られるパラジウムカルボ
キシルアセテートに、含窒素化合物または酢酸化合物を
反応させて得られる懸濁化合物に、さらに芳香族溶媒を
添加する工程と酸素に接触させる工程を経て得られる沈
殿物、および当該沈殿物からなるアリルアルコール類を
酸化脱水素反応してα,β−不飽和カルボニル化合物類
を製造するための触媒、並びに前記触媒の存在下に、ア
リルアルコール類を酸素雰囲気下で酸化脱水素反応する
ことを特徴とするα,β−不飽和カルボニル化合物類の
製造法に関する。That is, the present invention provides allyl alcohols consisting of a suspension compound obtained by reacting a palladium carboxylate acetate obtained by reacting palladium acetate with carbon monoxide in acetic acid with a nitrogen-containing compound or an acetic acid compound. Catalyst for producing α, β-unsaturated carbonyl compounds by oxidative dehydrogenation reaction, palladium carboxylacetate obtained by reacting palladium acetate with carbon monoxide in acetic acid is reacted with nitrogen-containing compound or acetic acid compound The resulting suspension compound is subjected to oxidative dehydrogenation reaction of a precipitate obtained by further adding an aromatic solvent and a step of contacting with oxygen, and allyl alcohols composed of the precipitate to obtain α, β- A catalyst for producing unsaturated carbonyl compounds, and allyl alcohols in the presence of the catalyst. α characterized by oxidative dehydrogenation reaction under hydrogen atmosphere, a process for producing β- unsaturated carbonyl compounds.
【0009】本発明のアリルアルコール類を酸化脱水素
反応してα,β−不飽和カルボニル化合物類を製造する
ための触媒は、酢酸パラジウムと一酸化炭素を酢酸中で
反応させて得られるパラジウムカルボキシルアセテート
に、含窒素化合物または酢酸化合物を反応させて得られ
る懸濁化合物である。かかる懸濁化合物は公知の方法
(I. Moiseev、Pure&Appl.Che
m.,61巻,No.10,pp.1755−176
2,1989)により調製できる。以下に、かかる懸濁
化合物の調製法を詳しく述べる。The catalyst for producing α, β-unsaturated carbonyl compounds by oxidative dehydrogenation of allyl alcohols of the present invention is a palladium carboxyl obtained by reacting palladium acetate with carbon monoxide in acetic acid. It is a suspension compound obtained by reacting acetate with a nitrogen-containing compound or an acetic acid compound. Such suspension compounds can be prepared by known methods (I. Moiseev, Pure & Appl. Che.
m. 61, No. 10, pp. 175-176
2, 1989). The method for preparing such a suspension compound will be described in detail below.
【0010】まず、酢酸パラジウムを含有する酢酸溶液
を調製する。酢酸に溶解する酢酸パラジウムの使用量
は、酢酸パラジウムが酢酸に溶解する範囲であれば特に
限定されないが、通常は、コスト面、酢酸溶液の取り扱
い性から、酢酸100重量部に対し、酢酸パラジウム1
〜100重量部程度が適当である。なお、酢酸としては
氷酢酸が好ましい。First, an acetic acid solution containing palladium acetate is prepared. The amount of palladium acetate dissolved in acetic acid is not particularly limited as long as it is within the range in which palladium acetate is dissolved in acetic acid, but usually, from the viewpoint of cost and handleability of acetic acid solution, 1 part of palladium acetate is used per 100 parts by weight of acetic acid.
About 100 parts by weight is suitable. Glacial acetic acid is preferable as acetic acid.
【0011】次いで、この酢酸パラジウムを含有する酢
酸溶液を一酸化炭素雰囲気下で反応させてパラジウムカ
ルボキシルアセテートにする。一酸化炭素の流通は、酢
酸パラジウムの全てをパラジウムカルボキシルアセテー
トにすることができれば、一酸化炭素の流通量は、特に
制限されず、通常、室温〜70℃で、1〜3時間程度、
好ましくは1.5〜2時間流通させる。なお、一酸化炭
素雰囲気下とは、酢酸溶液中の酢酸パラジウムが一酸化
炭素と接触できる状態をいい、酢酸溶液へ一酸化炭素を
バブリングする方法、一酸化炭素雰囲気中で酢酸溶液を
撹拌する方法等の方法を採用できる。Next, this acetic acid solution containing palladium acetate is reacted in a carbon monoxide atmosphere to form palladium carboxyl acetate. As for the flow of carbon monoxide, the flow amount of carbon monoxide is not particularly limited as long as all of palladium acetate can be converted to palladium carboxyl acetate, and is usually at room temperature to 70 ° C. for about 1 to 3 hours.
It is preferably distributed for 1.5 to 2 hours. The carbon monoxide atmosphere means that palladium acetate in an acetic acid solution can contact carbon monoxide, a method of bubbling carbon monoxide into an acetic acid solution, a method of stirring the acetic acid solution in a carbon monoxide atmosphere. Etc. can be adopted.
【0012】さらに得られたパラジウムカルボキシルア
セテートに、含窒素化合物または酢酸化合物を反応させ
て、酢酸中に懸濁状態で存在する懸濁化合物を得る。含
窒素化合物または酢酸化合物としては、パラジウムと反
応して結合もしくは錯体を形成しうる化合物を使用でき
る。Further, the obtained palladium carboxylacetate is reacted with a nitrogen-containing compound or an acetic acid compound to obtain a suspension compound existing in suspension in acetic acid. As the nitrogen-containing compound or acetic acid compound, a compound that can react with palladium to form a bond or a complex can be used.
【0013】このような含窒素化合物としては、3級窒
素を有する1,10−フェナントロリン、2,2−ビピ
リジン、トリエチルアミン、一般式(1):As such a nitrogen-containing compound, 1,10-phenanthroline having a tertiary nitrogen, 2,2-bipyridine, triethylamine, the general formula (1):
【0014】[0014]
【化7】 Embedded image
【0015】(式中、R1 、R2 はそれぞれに同一また
は相異なって水素原子または炭素数1〜8のアルキル基
を示す)で表されるピリジン化合物、および一般式
(2):(CH3 )2 N(CH2 )n N(CH3 )2
(式中、nは1〜10の整数)で表されるアミン化合物
などが好ましい。一般式(1)で表されるピリジン化合
物の具体例としては、ピリジン、4−メチルピリジン、
2−メチルピリジン、2,6−ジメチルピリジン等があ
げられ、一般式(2)で表されるアミン化合物として
は、1,2−ジ(N,N−ジメチルアミノ)エタン、
1,3−ジ(N,N−ジメチルアミノ)プロパン等があ
げられる。(Wherein R 1 and R 2 are the same or different and each independently represent a hydrogen atom or an alkyl group having 1 to 8 carbon atoms), and a general formula (2): (CH 3 ) 2 N (CH 2 ) n N (CH 3 ) 2
(In the formula, n is an integer of 1 to 10) and the like are preferable amine compounds. Specific examples of the pyridine compound represented by the general formula (1) include pyridine, 4-methylpyridine,
2-methylpyridine, 2,6-dimethylpyridine and the like can be mentioned, and as the amine compound represented by the general formula (2), 1,2-di (N, N-dimethylamino) ethane,
1,3-di (N, N-dimethylamino) propane and the like can be mentioned.
【0016】また、酢酸化合物としては、酢酸アルカリ
金属塩が好ましく、その具体例としては酢酸カリウム等
があげられる。The acetic acid compound is preferably an alkali metal acetate, and specific examples thereof include potassium acetate.
【0017】含窒素化合物または酢酸化合物の使用量は
パラジウムカルボキシルアセテート中のパラジウム金属
の全量が含窒素化合物または酢酸化合物と反応して結合
もしくは錯体を形成しうる理論量以上である。通常は理
論量の2〜3倍量とされる。たとえば含窒素化合物中の
窒素原子が1つの場合には、前記酢酸パラジウムの仕込
み量1モル部に対して、2モル部以上、窒素原子が2つ
の場合には1モル部以上である。また、酢酸化合物の使
用量は、前記酢酸パラジウム1モル部に対して、2モル
部以上である。The amount of the nitrogen-containing compound or acetic acid compound used is at least a theoretical amount such that the total amount of palladium metal in palladium carboxylacetate can react with the nitrogen-containing compound or acetic acid compound to form a bond or a complex. Usually, the amount is 2-3 times the theoretical amount. For example, when the nitrogen-containing compound has one nitrogen atom, the amount of palladium acetate charged is 1 part by mole or more, and when there are two nitrogen atoms, the amount is 1 part by mole or more. The amount of the acetic acid compound used is 2 parts by mole or more based on 1 part by mole of the palladium acetate.
【0018】なお、前述の報文によれば、例えば、含窒
素化合物が1,10−フェナントロリン(以下、Phe
nと略することもある)である場合、得られた懸濁化合
物は、Pd4 (Phen)2 (CO)2 (OCOCH
3 )4 という構造であることが推定されており、前述の
報文においてはかかる懸濁化合物はオレフィンのアセト
オキシ化反応に用いられている。According to the above-mentioned report, for example, the nitrogen-containing compound is 1,10-phenanthroline (hereinafter referred to as Phe).
n may be abbreviated as n), the obtained suspension compound is Pd 4 (Phen) 2 (CO) 2 (OCOCH
3 ) 4 It is estimated that the structure is 4, and in the above-mentioned paper, such a suspension compound is used in the acetoxylation reaction of an olefin.
【0019】本発明は、かかる公知の懸濁化合物を、ア
リルアルコール類からα,β−不飽和カルボニル化合物
類を製造するための酸化脱水素反応用の触媒として用い
たものである。かかる懸濁化合物は、通常、懸濁溶液
(酢酸溶液)のまま均一系の触媒として用いられる。The present invention uses such a known suspension compound as a catalyst for the oxidative dehydrogenation reaction for producing α, β-unsaturated carbonyl compounds from allyl alcohols. Such a suspension compound is usually used as a suspension system (acetic acid solution) as a homogeneous catalyst.
【0020】本発明では、前記懸濁化合物に、さらに芳
香族溶媒を添加する工程と酸素に接触させる工程を経て
得られる沈殿物を、アリルアルコール類からα,β−不
飽和カルボニル化合物類を製造するための酸化脱水素反
応用の触媒として使用することもできる。In the present invention, α, β-unsaturated carbonyl compounds are produced from allyl alcohol by using a precipitate obtained through a step of adding an aromatic solvent and a step of contacting with oxygen to the suspension compound. It can also be used as a catalyst for the oxidative dehydrogenation reaction.
【0021】芳香族溶媒としてはベンゼンが好ましく、
その使用量は前記懸濁化合物を含有する懸濁溶液(酢酸
溶液)100重量部に対して30重量部以上である。好
ましくは、100〜2000重量部である。30重量部
に満たない場合には、懸濁化合物を沈殿させることが困
難である。Benzene is preferred as the aromatic solvent,
The amount used is 30 parts by weight or more based on 100 parts by weight of a suspension solution (acetic acid solution) containing the suspension compound. Preferably, it is 100 to 2000 parts by weight. If the amount is less than 30 parts by weight, it is difficult to precipitate the suspension compound.
【0022】また、酸素に接触させる工程とは、懸濁化
合物または沈殿物を酸素と接触させることをいい、酸素
を供給して接触させる場合の他に空気中の酸素と接触す
る場合も含まれる。酸素と接触する工程は、たとえば、
懸濁化合物に芳香族溶媒を添加する際に、懸濁化合物ま
たは沈殿物と酸素が接触するような状態、また沈殿物を
分離した後に、沈殿物の空隙に酸素を含むような状態を
いう。The step of bringing into contact with oxygen means bringing the suspension compound or the precipitate into contact with oxygen, and includes the case of contacting with oxygen in the air as well as the case of supplying and contacting with oxygen. . The step of contacting with oxygen is, for example,
When the aromatic solvent is added to the suspension compound, it means a state in which the suspension compound or the precipitate comes into contact with oxygen, or a state in which after the precipitate is separated, oxygen is contained in the voids of the precipitate.
【0023】なお、沈殿物は黒色を呈し、その構造は定
かにはなっていないが、含窒素化合物が、Phenであ
る場合、Pd(Phen)(OCOCH3 )2 またはP
d4(Phen)2 (OCOCH3 )n (n=1〜3)
ではないかと推定される。Although the precipitate is black and its structure has not been clarified, when the nitrogen-containing compound is Phen, Pd (Phen) (OCOCH 3 ) 2 or P
d 4 (Phen) 2 (OCOCH 3 ) n (n = 1 to 3)
It is estimated that it may be.
【0024】このように前記懸濁化合物に、芳香族溶媒
を添加する工程と酸素に接触させる工程を経ることによ
って沈殿物を生じることは前述の報文には一切記載がな
く、本発明者が初めて見出したものであり、また、かか
る沈殿物をアリルアルコール類からα,β−不飽和カル
ボニル化合物類を製造するための酸化脱水素反応用の触
媒として用いることも、本発明者が初めて見出したもの
である。The fact that a precipitate is formed by the steps of adding an aromatic solvent and contacting with oxygen to the above-mentioned suspension compound is not described in the above-mentioned report, and the present inventor has not described it. The present inventor has also found for the first time that the precipitate is used as a catalyst for oxidative dehydrogenation reaction for producing α, β-unsaturated carbonyl compounds from allyl alcohols. It is a thing.
【0025】こうして得られた沈殿物は、酢酸溶液のま
ま、または上澄み液を除去(デカンテーション)した
後、不均一系触媒として取り扱うことが可能である。前
記懸濁化合物を含有するは懸濁溶液は、ほとんどの場合
に均一系の触媒として取り扱われ、そのまま溶液の状態
で反応系に添加されるため、酸化脱水素反応後に反応系
から触媒を分離するのは非常に困難(煩雑な操作)であ
ったが、沈殿物からなる不均一系触媒によれば酸化脱水
素反応後における反応系からの触媒分離が容易になり、
また触媒の繰り返し使用も可能である。なお、触媒の分
離は、自然沈降法、遠心分離法など各種公知の方法を採
用することができる。The thus obtained precipitate can be treated as a heterogeneous catalyst as it is as an acetic acid solution or after removing the supernatant (decantation). In most cases, the suspension solution containing the suspension compound is treated as a homogeneous catalyst and is added to the reaction system as a solution as it is, so that the catalyst is separated from the reaction system after the oxidative dehydrogenation reaction. Was very difficult (complex operation), but a heterogeneous catalyst consisting of a precipitate facilitates separation of the catalyst from the reaction system after the oxidative dehydrogenation reaction,
It is also possible to repeatedly use the catalyst. The catalyst can be separated by various known methods such as a natural sedimentation method and a centrifugal separation method.
【0026】本発明では、前記懸濁化合物または沈殿物
からなる触媒の存在下で、アリルアルコール類を酸素雰
囲気下に酸化脱水素反応してα,β−不飽和カルボニル
化合物類を製造する。In the present invention, allyl alcohols are subjected to oxidative dehydrogenation reaction in an oxygen atmosphere in the presence of a catalyst comprising the above-mentioned suspension compound or precipitate to produce α, β-unsaturated carbonyl compounds.
【0027】アリルアルコール類としては、一般式
(3):The allyl alcohols are represented by the general formula (3):
【0028】[0028]
【化8】 Embedded image
【0029】で表される構造を有する化合物であれば特
に限定はなく、アリルアルコールまたはその誘導体のよ
うな低分子量の化合物から、前記構造を一部に有する高
分子量の化合物(ポリマー)のいずれにも適用できる。
たとえば、アリルアルコール類が、一般式(4):There is no particular limitation as long as it is a compound having a structure represented by the formula (1), and it can be changed from a low molecular weight compound such as allyl alcohol or a derivative thereof to a high molecular weight compound (polymer) partially having the above structure. Can also be applied.
For example, allyl alcohols are represented by the general formula (4):
【0030】[0030]
【化9】 Embedded image
【0031】で表される化合物の場合には、R3 、R
4 、R5 およびR6 としては、それぞれに同一または相
異なって水素原子、直鎖もしくは分岐鎖の飽和脂肪族炭
化水素基または不飽和脂肪族炭化水素基、直鎖もしくは
分岐鎖の飽和脂環族炭化水素基または不飽和脂環族炭化
水素基、または芳香族炭化水素基等の各種の炭素数1〜
32の炭化水素基等(ただし、R3 またはR4 とR5 は
それぞれの一部が結合して不飽和脂環構造を形成しても
よい)や、カルボキシ基、シアノ基等の各種官能基等が
あげられる。かかるアリルアルコール類の具体例として
は、例えば、アリルアルコール、シンナミルアルコー
ル、ゲラニオール、ネロール、2−ヘキセン−1−オー
ル、3−メチル−2−ブテン−1−オール、1−ヒドロ
キシ−2,4−ジメチルメタノシクロヘキセン、4−メ
チル−3−ペンテン−2−オール、ミルテノールなどが
あげられる。In the case of the compound represented by R 3 , R 3 and R
4 , R 5 and R 6 are the same or different and each is a hydrogen atom, a linear or branched saturated aliphatic hydrocarbon group or an unsaturated aliphatic hydrocarbon group, a linear or branched saturated alicyclic group. 1 to 6 carbon atoms such as group hydrocarbon group, unsaturated alicyclic hydrocarbon group, or aromatic hydrocarbon group
32 hydrocarbon groups and the like (provided that R 3 or R 4 and R 5 are partially bonded to each other to form an unsaturated alicyclic structure), and various functional groups such as carboxy group and cyano group. Etc. Specific examples of such allyl alcohols include allyl alcohol, cinnamyl alcohol, geraniol, nerol, 2-hexen-1-ol, 3-methyl-2-buten-1-ol, 1-hydroxy-2,4. -Dimethylmethanocyclohexene, 4-methyl-3-penten-2-ol, myrtenol and the like.
【0032】また、α,β−不飽和カルボニル化合物類
としては、一般式(3)で表される構造を有するアリル
アルコール類を酸化脱水素反応した、一般式(4):As the α, β-unsaturated carbonyl compound, allyl alcohols having the structure represented by the general formula (3) are obtained by oxidative dehydrogenation reaction of the general formula (4):
【0033】[0033]
【化10】 Embedded image
【0034】で表される構造を有する化合物があげられ
る。A compound having a structure represented by
【0035】本発明の酸化脱水素反応において、前記触
媒の使用量は、原料であるアリルアルコール類に対し
て、触媒中のパラジウム含有量が、通常は0.01〜2
5モル%程度、好ましくは0.5〜10モル%である。
0.01モル%より少ない場合は、触媒効果が低いため
十分な反応速度が得られない。また25モル%を越える
場合は、触媒費用や触媒分離作業の点で不利がある。In the oxidative dehydrogenation reaction of the present invention, the amount of the catalyst used is such that the content of palladium in the catalyst is usually 0.01 to 2 with respect to the allyl alcohol as a raw material.
It is about 5 mol%, preferably 0.5 to 10 mol%.
If it is less than 0.01 mol%, a sufficient reaction rate cannot be obtained because the catalytic effect is low. On the other hand, if it exceeds 25 mol%, there are disadvantages in terms of catalyst cost and catalyst separation work.
【0036】本発明の酸化脱水素反応は、必ずしも溶媒
の存在下に行う必要はないが、得られるα,β−不飽和
カルボニル化合物類の収率の点から、有機溶媒系で行う
のが好ましい。特に、有機溶媒としては、芳香族炭化水
素類、カルボン酸類、エステル類、アルキルハライド類
およびハロゲン化炭素類から選ばれるいずれか少なくと
も1種を使用するのが好ましい。The oxidative dehydrogenation reaction of the present invention does not necessarily have to be carried out in the presence of a solvent, but it is preferably carried out in an organic solvent system from the viewpoint of the yield of the obtained α, β-unsaturated carbonyl compounds. . In particular, as the organic solvent, it is preferable to use at least one selected from aromatic hydrocarbons, carboxylic acids, esters, alkyl halides and halogenated carbons.
【0037】上記有機溶媒のうち芳香族炭化水素類とし
てはベンゼン、トルエン、キシレン、エチルベンゼン、
イソブチルベンゼン、テトラリン等を例示できる。カル
ボン酸類としては酢酸、プロピオン酸、酪酸、イソ酪酸
等を例示できる。エステル類としては酢酸メチル、酢酸
エチル、酢酸イソブチル、プロピオン酸メチル、プロピ
オン酸エチル、プロピオン酸イソブチル等を例示でき
る。アルキルハライド類としては、ジクロロメタン、ト
リクロロメタン、ジクロロエタン、トリクロロエタン、
ジクロロプロパン、ジクロロブタン、トリクロロプロパ
ン、トリクロロブタン、テトラクロロプロパン、テトラ
クロロブタン等を例示できる。ハロゲン化炭素として
は、四塩化炭素、ヘキサクロロエタン、オクタクロロプ
ロパン等を例示できる。Among the above organic solvents, aromatic hydrocarbons include benzene, toluene, xylene, ethylbenzene,
Examples thereof include isobutylbenzene and tetralin. Examples of carboxylic acids include acetic acid, propionic acid, butyric acid, isobutyric acid and the like. Examples of the esters include methyl acetate, ethyl acetate, isobutyl acetate, methyl propionate, ethyl propionate, isobutyl propionate and the like. The alkyl halides include dichloromethane, trichloromethane, dichloroethane, trichloroethane,
Examples thereof include dichloropropane, dichlorobutane, trichloropropane, trichlorobutane, tetrachloropropane and tetrachlorobutane. Examples of the halogenated carbon include carbon tetrachloride, hexachloroethane, octachloropropane and the like.
【0038】本発明のα,β−不飽和カルボニル化合物
類の製造は、通常、前記触媒を反応容器に入れ、これに
有機溶媒および反応原料であるアリルアルコール類を加
え、酸素雰囲気下に、所定の反応温度にて、所定の反応
時間、酸化脱水素反応させることにより行う。The production of the α, β-unsaturated carbonyl compound of the present invention is usually carried out by placing the catalyst in a reaction vessel, adding an organic solvent and allyl alcohol which is a reaction raw material thereto, and carrying out a predetermined reaction in an oxygen atmosphere. The reaction is carried out by carrying out the oxidative dehydrogenation reaction for a predetermined reaction time at the reaction temperature.
【0039】反応温度は、通常は5〜150℃程度であ
る。特に有機溶媒または原料のアリルアルコール類の凝
固点以上、沸点以下の温度とするのがよく、10〜80
℃が好ましい。5℃以下では有機溶媒が凝固し、反応に
不利であり、150℃を越える場合にはα,β−不飽和
カルボニル化合物類の収率が低下し、熱コスト的にも不
利である。反応時間は原料のアリルアルコール類の種類
や反応温度などにより異なるが、通常2〜30時間程度
とされる。また、酸素雰囲気下とは、空気中または酸素
ガスを供給した状態、これらをバブリングする状態等を
いう。The reaction temperature is usually about 5 to 150 ° C. In particular, it is preferable that the temperature is not lower than the freezing point and not higher than the boiling point of the organic solvent or the raw material allyl alcohol, and is 10 to 80.
C is preferred. When the temperature is lower than 5 ° C, the organic solvent is solidified, which is disadvantageous to the reaction. When the temperature exceeds 150 ° C, the yield of α, β-unsaturated carbonyl compounds is lowered, which is also disadvantageous in terms of heat cost. The reaction time varies depending on the type of allyl alcohol as a raw material and the reaction temperature, but is usually about 2 to 30 hours. The term "in an oxygen atmosphere" refers to a state in which air or oxygen gas is supplied, a state in which these are bubbled, and the like.
【0040】なお、本発明の製造法は、前記特定触媒を
採用することにより酸化脱水素反応を、常圧で行い、収
率よくα,β−不飽和カルボニル化合物類を収得できる
ことを一つの特徴とするが、加圧条件を排除するもので
はない。One of the features of the production method of the present invention is that the oxidative dehydrogenation reaction can be carried out at normal pressure by employing the above-mentioned specific catalyst to obtain α, β-unsaturated carbonyl compounds in good yield. However, the pressurizing condition is not excluded.
【0041】[0041]
【発明の効果】本発明によれば、安全で温和な条件下
に、アリルアルコール類を酸化脱水素反応してα,β−
不飽和カルボニル化合物類を60〜95モル%程度の高
収率で製造できる。また、本発明で用いる触媒のなかで
も、沈殿物からなる触媒は不均一触媒として使用でき、
反応系から容易に分離でき、廃棄操作が容易である。According to the present invention, allyl alcohols are subjected to oxidative dehydrogenation reaction under safe and mild conditions to obtain α, β-
Unsaturated carbonyl compounds can be produced in a high yield of about 60 to 95 mol%. Further, among the catalysts used in the present invention, a catalyst composed of a precipitate can be used as a heterogeneous catalyst,
It can be easily separated from the reaction system and is easily discarded.
【0042】[0042]
【実施例】以下に実施例および比較例をあげて本発明を
さらに具体的に説明するが、本発明はこれら実施例に限
定されるものではない。The present invention will be described in more detail with reference to the following examples and comparative examples, but the present invention is not limited to these examples.
【0043】実施例1(1)(酸化脱水素反応用触媒の
調製) 20mlの丸底フラスコに氷酢酸3.5ml(3.67
g)、酢酸パラジウム0.03gを入れ、一酸化炭素雰
囲気中、50℃にて1.5時間反応させ、黄色結晶のパ
ラジウムカルボキシルアセテートを得た。次いで、フラ
スコ中に存在するパラジウム金属の理論量(0.05ミ
リモル)の2倍モル相当の1,10−フェナントロリン
(0.10ミリモル)を加え、50℃にて0.5時間反
応させ、非常に細かい浮遊物のある懸濁溶液を得た。こ
の懸濁溶液を触媒Aという。Example 1 (1) (Preparation of catalyst for oxidative dehydrogenation reaction) 3.5 ml of glacial acetic acid (3.67 g) was added to a 20 ml round bottom flask.
g) and 0.03 g of palladium acetate were added, and the reaction was carried out at 50 ° C. for 1.5 hours in a carbon monoxide atmosphere to obtain yellow crystals of palladium carboxyl acetate. Then, 1,10-phenanthroline (0.10 mmol) corresponding to twice the theoretical amount of palladium metal present in the flask (0.05 mmol) was added, and the reaction was carried out at 50 ° C. for 0.5 hours, and the reaction was carried out. A suspension of fine suspension was obtained. This suspension solution is called catalyst A.
【0044】(2)(酸化脱水素反応用触媒の調製) 上記(1)で得られた触媒Aにベンゼン15mlを加え
た。徐々に沈殿物が生じ、この沈殿物を分離した後、上
澄みをデカンテーションにて除去した。分離作業は酸素
雰囲気中(空気雰囲気下)で行い、黒色の固体を得た。
得られた沈殿物を触媒Bという。(2) (Preparation of catalyst for oxidative dehydrogenation reaction) To the catalyst A obtained in (1) above, 15 ml of benzene was added. A precipitate gradually formed, and after separating this precipitate, the supernatant was removed by decantation. The separation work was performed in an oxygen atmosphere (under an air atmosphere) to obtain a black solid.
The obtained precipitate is called catalyst B.
【0045】(3)(酸化脱水素反応) 還流冷却管およびコックを備え、密封状態を保持できる
20mlのシュレンク管に、パラジウム含有量が0.0
3ミリモルの触媒B(沈殿物)を入れた後、溶媒として
ベンゼン5mlおよび反応原料のシンナミルアルコール
を1.5ミリモル加え、シュレンク管を酸素で置換した
後、コックに風船を取り付け酸素雰囲気を保った。電磁
撹拌機つきオイルバスにて撹拌しながら50℃で、24
時間反応を行った。得られたα,β−不飽和カルボニル
化合物類(シンナミルアルデヒド)の分析はガスクロマ
トグラフ法によった。転化率、収率を表1に示す。な
お、転化率とは原料が転化した割合をいい、収率とはす
べての原料のうち目的生成物に転化した割合をいう。(3) (Oxidative dehydrogenation reaction) A 20 ml Schlenk tube equipped with a reflux condenser and a cock and capable of maintaining a sealed state has a palladium content of 0.0
After adding 3 mmol of catalyst B (precipitate), 5 ml of benzene as a solvent and 1.5 mmol of cinnamyl alcohol as a reaction raw material were added, the Schlenk tube was replaced with oxygen, and a balloon was attached to the cock to keep the oxygen atmosphere. It was While stirring in an oil bath with a magnetic stirrer, at 50 ° C, 24
A time reaction was performed. The obtained α, β-unsaturated carbonyl compounds (cinnamylaldehyde) were analyzed by gas chromatography. Table 1 shows the conversion rate and the yield. The conversion rate refers to the rate of conversion of the raw materials, and the yield refers to the rate of conversion to the target product among all the raw materials.
【0046】実施例2〜23比較例1〜3 原料のアリルアルコール類の種類、触媒の種類(前記A
もしくはB、または含窒素化合物もしくは酢酸化合物の
種類)、反応温度、反応時間および溶媒のうちいずれか
少なくとも1種を表1に示すように代えた他は実施例1
と同様に行った。α,β−不飽和カルボニル化合物類へ
の転化率、選択率を表1に示す。Examples 2 to 23 Comparative Examples 1 to 3 Types of allyl alcohols as raw materials and types of catalysts (the above A)
Or B, or the type of nitrogen-containing compound or acetic acid compound), reaction temperature, reaction time, and solvent except that at least one of them is changed as shown in Table 1.
The same was done. Table 1 shows the conversion and selectivity of α, β-unsaturated carbonyl compounds.
【0047】[0047]
【表1】 [Table 1]
【0048】表1中、Pd(OAc)2 は酢酸パラジウ
ムを、PCAはパラジウムカルボキシルアセテートを、
ベンゼン酢酸はベンゼンと酢酸の1:1(重量比)混合
物をいうIn Table 1, Pd (OAc) 2 is palladium acetate, PCA is palladium carboxyl acetate,
Benzene acetic acid refers to a 1: 1 (weight ratio) mixture of benzene and acetic acid.
【手続補正書】[Procedure amendment]
【提出日】平成8年6月19日[Submission date] June 19, 1996
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】請求項9[Correction target item name] Claim 9
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【化3】 で表される構造を有する化合物であり、α,β−不飽和
カルボニル化合物類が、一般式(4) :Embedded image Wherein the α, β-unsaturated carbonyl compound is a compound having a structure represented by the following general formula (4):
【化4】 で表される構造を有する化合物である請求項1、2、3
または8記載の触媒。Embedded image A compound having a structure represented by:
Or the catalyst according to item 8.
【手続補正2】[Procedure amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】請求項12[Name of item to be corrected] Claim 12
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【化5】 で表される構造を有する化合物であり、α,β−不飽和
カルボニル化合物類が、一般式(4):Embedded image Wherein the α, β-unsaturated carbonyl compound is a compound having a structure represented by the general formula (4):
【化6】 で表される構造を有する化合物である請求項10または
11記載の製造法。Embedded image The method according to claim 10 or 11, which is a compound having a structure represented by:
【手続補正3】[Procedure 3]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0028[Correction target item name] 0028
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0028】[0028]
【化8】 Embedded image
【手続補正4】[Procedure amendment 4]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0030[Correction target item name] 0030
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0030】[0030]
【化9】 Embedded image
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 // C07B 61/00 300 C07B 61/00 300 ──────────────────────────────────────────────────続 き Continuation of the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical display location // C07B 61/00 300 C07B 61/00 300
Claims (12)
反応させて得られるパラジウムカルボキシルアセテート
に、含窒素化合物または酢酸化合物を反応させて得られ
る懸濁化合物からなる、アリルアルコール類を酸化脱水
素反応してα,β−不飽和カルボニル化合物類を製造す
るための触媒。1. Oxidative dehydrogenation of allyl alcohols comprising a suspension compound obtained by reacting palladium carboxyl acetate obtained by reacting palladium acetate with carbon monoxide in acetic acid with a nitrogen-containing compound or an acetic acid compound. A catalyst for reacting to produce α, β-unsaturated carbonyl compounds.
ロリン、2,2−ビピリジン、トリエチルアミン、一般
式(1): 【化1】 (式中、R1 、R2 はそれぞれに同一または相異なって
水素原子または炭素数1〜8のアルキル基を示す)で表
されるピリジン化合物、および一般式(2):(CH
3 )2 N(CH2 )n N(CH3 )2 (式中、nは1〜
10の整数)で表されるアミン化合物から選ばれるいず
れか少なくとも1種である請求項1記載の触媒。2. The nitrogen-containing compound is 1,10-phenanthroline, 2,2-bipyridine, triethylamine, a compound represented by the general formula (1): (In the formula, R 1 and R 2 are the same or different and each independently represent a hydrogen atom or an alkyl group having 1 to 8 carbon atoms), and a general formula (2): (CH
3 ) 2 N (CH 2 ) n N (CH 3 ) 2 (where n is 1 to
The catalyst according to claim 1, which is at least one selected from the amine compounds represented by (integer of 10).
る請求項1記載の触媒。3. The catalyst according to claim 1, wherein the acetic acid compound is an alkali metal acetate.
反応させて得られるパラジウムカルボキシルアセテート
に、含窒素化合物または酢酸化合物を反応させて得られ
る懸濁化合物に、さらに芳香族溶媒を添加する工程と酸
素に接触させる工程を経て得られる沈殿物。4. A step of further adding an aromatic solvent to a palladium carboxylacetate obtained by reacting palladium acetate and carbon monoxide in acetic acid, and a suspension compound obtained by reacting a nitrogen-containing compound or an acetic acid compound. And a precipitate obtained through the step of contacting with oxygen.
ロリン、2,2−ビピリジン、トリエチルアミン、一般
式(1): 【化2】 (式中、R1 、R2 はそれぞれに同一または相異なって
水素原子または炭素数1〜8のアルキル基を示す)で表
されるピリジン化合物、および一般式(2):(CH
3 )2 N(CH2 )n N(CH3 )2 (式中、nは1〜
10の整数)で表されるアミン化合物から選ばれるいず
れか少なくとも1種である請求項4記載の沈殿物。5. The nitrogen-containing compound is 1,10-phenanthroline, 2,2-bipyridine, triethylamine, a compound represented by the general formula (1): (In the formula, R 1 and R 2 are the same or different and each independently represent a hydrogen atom or an alkyl group having 1 to 8 carbon atoms), and a general formula (2): (CH
3 ) 2 N (CH 2 ) n N (CH 3 ) 2 (where n is 1 to
The integer according to claim 4, which is at least one selected from the amine compounds represented by the formula (10: integer).
る請求項4記載の沈殿物。6. The precipitate according to claim 4, wherein the acetic acid compound is an alkali metal acetate.
5または6記載の沈殿物。7. The aromatic solvent is benzene,
The precipitate according to 5 or 6.
からなるアリルアルコール類を酸化脱水素反応してα,
β−不飽和カルボニル化合物類を製造するための触媒。8. An allyl alcohol comprising the precipitate according to claim 4, 5, 6 or 7 is subjected to oxidative dehydrogenation reaction to obtain α,
A catalyst for producing β-unsaturated carbonyl compounds.
カルボニル化合物類が、一般式(4): 【化4】 で表される構造を有する化合物である請求項1、2、3
または8記載の触媒。9. An allyl alcohol is represented by the general formula (3): Wherein the α, β-unsaturated carbonyl compound is a compound having a structure represented by the following general formula (4): A compound having a structure represented by:
Or the catalyst according to item 8.
の存在下に、アリルアルコール類を酸素雰囲気下で酸化
脱水素反応することを特徴とするα,β−不飽和カルボ
ニル化合物類の製造法。10. An α, β-unsaturated carbonyl compound which is characterized by oxidatively dehydrogenating allyl alcohol in an oxygen atmosphere in the presence of the catalyst according to claim 1, 2, 3 or 8. Manufacturing method.
類、カルボン酸類、エステル類、アルキルハライド類お
よびハロゲン化炭素類から選ばれるいずれか少なくとも
1種の有機溶媒中で行うことを特徴とする請求項10記
載の製造法。11. The oxidative dehydrogenation reaction is carried out in at least one organic solvent selected from aromatic hydrocarbons, carboxylic acids, esters, alkyl halides and halogenated carbons. The manufacturing method according to claim 10.
(3): 【化5】 で表される構造を有する化合物であり、α,β−不飽和
カルボニル化合物類が、一般式(4): 【化6】 で表される構造を有する化合物である請求項10または
11記載の製造法。12. The allyl alcohol is represented by the general formula (3): Wherein the α, β-unsaturated carbonyl compound is a compound having a structure represented by the following general formula (4): The method according to claim 10 or 11, which is a compound having a structure represented by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18789795A JP3814840B2 (en) | 1995-06-30 | 1995-06-30 | Catalyst for oxidative dehydrogenation and process for producing α, β-unsaturated carbonyl compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18789795A JP3814840B2 (en) | 1995-06-30 | 1995-06-30 | Catalyst for oxidative dehydrogenation and process for producing α, β-unsaturated carbonyl compounds |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0910596A true JPH0910596A (en) | 1997-01-14 |
| JP3814840B2 JP3814840B2 (en) | 2006-08-30 |
Family
ID=16214115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18789795A Expired - Fee Related JP3814840B2 (en) | 1995-06-30 | 1995-06-30 | Catalyst for oxidative dehydrogenation and process for producing α, β-unsaturated carbonyl compounds |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3814840B2 (en) |
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1995
- 1995-06-30 JP JP18789795A patent/JP3814840B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP3814840B2 (en) | 2006-08-30 |
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