KR0128106B1 - Process for producing cyclopentenone with catalyst of indenglcobalt(i) compound - Google Patents

Process for producing cyclopentenone with catalyst of indenglcobalt(i) compound

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KR0128106B1
KR0128106B1 KR1019940016568A KR19940016568A KR0128106B1 KR 0128106 B1 KR0128106 B1 KR 0128106B1 KR 1019940016568 A KR1019940016568 A KR 1019940016568A KR 19940016568 A KR19940016568 A KR 19940016568A KR 0128106 B1 KR0128106 B1 KR 0128106B1
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cyclopentenone
catalyst
carbon monoxide
reaction
producing
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KR1019940016568A
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KR960004311A (en
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정영근
이분열
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정영근
이분열
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/49Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
    • C07C45/50Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/587Unsaturated compounds containing a keto groups being part of a ring
    • C07C49/597Unsaturated compounds containing a keto groups being part of a ring of a five-membered ring

Abstract

In the reaction of alkene or alkyne such as norbonadien or norbonylene with carbon monoxide, the pressure of carbon monoxide is fixed at 5-100 atmosphere, and the temperature is maintained at 50-200 degree Celsius.Indenyl cobalt(I) compound is used as catalyst, and cyclopentenone derivatives are synthesized.

Description

인데닐코발트(Ⅰ)화합물을 촉매로 사용하는 시클로펜텐온 유도체의 제조방법Method for preparing cyclopentenone derivatives using indenyl cobalt (I) compound as catalyst

본 발명은 의약품이나 향료물질과 같은 유용한 화합물을 만드는 중간물질로 이용되는 시클로펜텐온 유도체 제조방법에 관한 것이다.The present invention relates to a method for preparing a cyclopentenone derivative used as an intermediate for making a useful compound such as a pharmaceutical or a perfume.

시클로펜텐온 유도체를 제조하는 종래의 유기화학적 접근방법은 아래 [Ⅰ]식에서와 같이, 1, 4-디케톤유도체(1,4-diketone derivatives)를 염기촉매하여 고리화축합(cycloncondensation)하는 것이다.A conventional organic chemical approach to preparing cyclopentenone derivatives is to cyclocondensate by base catalyst of 1,4-diketone derivatives as shown in the following [I].

그러나 이와같은 방법에 의하여 시클로펜텐온 유도체를 제조하는 방법에서는 우선,1,4-디케톤 유도체를 얻는 것이 간단하지 않을뿐 아니라, 이들 화합물이 다양하지 않기 때문에 좀더 개념적으로 간단한 방법들이 연구되어 왔다. 즉, Organic Reactions(1991) 40호 1면, Journal of American Chemical Society(1989) 111호 3336면, Journal of Organic Chemistry(1992) 57호 5803면, Joumal of Amerecan Chemical Society(1988) 110호 1286면, Organometalics(1992) 11호 2044면에 게재된 것과 같이 전이금속을 이용하여 알켄, 알킨 및 일산화탄소를 함께 고리화함으로써 시클로펜텐온 유도체를 합성하는 아래 [2]식과 같은 반응에 대한 연구들이 있었다.However, in the method for producing a cyclopentenone derivative by such a method, it is not only simple to obtain a 1,4-diketone derivative, but more conceptually simple methods have been studied because these compounds are not diverse. That is, Organic Reactions (1991) No. 40, Journal of American Chemical Society (1989) 111, No. 3336, Journal of Organic Chemistry (1992) No. 57, 5803, Joumal of Amerecan Chemical Society (1988) No. 110, 1286, As described in page 2044 of Organometalics (1992) No. 11, there have been studies on the reaction as described in the following [2] for synthesizing cyclopentenone derivatives by cyclizing alkene, alkyne and carbon monoxide together using a transition metal.

그러나 이와같은 여러 반응에서는 반응물과 같은 양(1당량)의 전이금속을 필요로 하였으므로 공업적인 대량생산에 활용하는데 어려움이 있었다. 한편, 최근에 디코발트옥타카르보닐(dicobaltoctacarbonyl)과 코리간드(coligand)로서 트리페닐포스페이트(triphenylphosphate)를 사용하여 시클로펜텐온 유도체를 합성하는 방법이 Journal of American Chemical Society(1994) 3159면에서 공개되었으나, 이 경우도 촉매의 전환수가 작아서 많은 양의 촉매를 필요로 하며, 일산화탄소의 압력이 3기압으로 일정하여야만 반응이 진행된다는 결점이 있다.However, these reactions required the same amount (1 equivalent) of the transition metal as the reactants, which made it difficult to utilize them for industrial mass production. Recently, a method of synthesizing cyclopentenone derivatives using triphenylphosphate as dicobaltoctacarbonyl and coligand has been disclosed in Journal of American Chemical Society (1994) 3159. In this case, too, the number of conversion of the catalyst is small and a large amount of catalyst is required, and the reaction proceeds only when the pressure of carbon monoxide is constant at 3 atm.

본 발명의 목적은 인데닐코발트(I)화합물(indenyl cobalt(I) compounds) 촉매를 사용하여 수율이 높고, 비용이 적게들어 시클로펜텐온 유도체를 공업적으로 대량생산할 수 있는 제조방법을 제공하는데 있다.SUMMARY OF THE INVENTION An object of the present invention is to provide a production method for industrially mass-producing cyclopentenone derivatives with high yield and low cost by using indenyl cobalt (I) compounds catalyst. .

본 발명에 따른 시클로펜텐온 유도체의 제조방법은 분자간 반응(intermolecular reactions)에 의한 것과 분자내 반응(intermolecular reactions)에 의한 것으로 구분할 수 있다.The method for producing a cyclopentenone derivative according to the present invention can be classified into one of an intermolecular reactions and one of an intramolecular reactions.

우선 분자간 반응(intramolecular reactions)을 통한 시클로펜텐온 유도체의 합성에 관하여 살펴보면, 이는 아래 [3]과 같이 알켄, 알킨 및 일산화 탄소를 인데닐코발트(I)화합물 촉매하에 반응시킴으로써 이루어진다.First, the synthesis of cyclopentenone derivatives through intermolecular reactions is made by reacting alkenes, alkynes and carbon monoxide under an indenyl cobalt (I) compound catalyst as shown in [3] below.

여기에서 알켄은 반응성이 좋은 놀보나디엔(norbonadien)과 놀보닐랜(norbonylene)이 바람직하며, 놀보나디엔의 경우 합성된 시클로펜텐온 유도체가 아래의 반응식[4]에서와 같이 유기구리 화합물의 1, 4-부가반응(1, 4-addition reaction)과 역 딜스-알더반응(retro Diels-Alder reaction)을 통하여 유용한 입체선택적인 시클로펜텐온 유도체를 만들 수 있다.Herein, alkenes are preferably reactive norbonadiene and norbonylene, and in the case of nolvadiene, the cyclopentenone derivatives synthesized are 1, 1, or 3 of the organocopper compound as shown in Reaction [4]. Useful four-addition reactions and retro Diels-Alder reactions make useful stereoselective cyclopentenone derivatives.

상기 식[3]에서 알킨의 R1과 R2는 수소, 알콜, 아민 티올, 에테르, 아렌, 알킬; 또는 알콜, 암ㄴ, 티올, 에테르, 아렌, 알킬, 카르복실산, 알데히드, 케톤, 니트릴, 아미드 2중결합, 3중결합 중 하나 이상으로 치환된 것으로서 상기 알킨의 3중결합과 비공액인 탄화수소화합물이다.In Formula [3], R 1 and R 2 of alkyne are hydrogen, alcohol, amine thiol, ether, arene, alkyl; Or hydrocarbons unconjugated with the triple bond of the alkyne, substituted with one or more of alcohol, ammonium, thiol, ether, arene, alkyl, carboxylic acid, aldehyde, ketone, nitrile, amide double bond, triple bond Compound.

일반적으로 합성된 시클로펜텐온 유도체에서 R1, 즉 카르보닐기 옆의 탄소에 붙는 작용기는 R2보다 그 크기가 크며, R1과 R2의 크기가 비슷한 때에는 레지오선택성(regioselectivity)이 없으므로 R3, R4가 동일한 놀보나디엔을 알켄으로 사용했을 때에는 아래의 두 시클로펜텐온 유도체의 혼합물이 얻어진다.In general, in the cyclopentenone derivatives synthesized, R 1 , that is, the functional group attached to the carbon next to the carbonyl group is larger than R 2 , and when R 1 and R 2 are similar in size, there is no regioselectivity, so R 3 , R When a tetravalent same nolvonadiene is used as the alkene, a mixture of the following two cyclopentenone derivatives is obtained.

분자간 반응에 의한 시클로펜텐온 유도체 합성의 특수항 형태로서, 상기 알켄과 알킨이 한 분자내에 존재하는 화합물과 일산화탄소 및 인데닐코발트(Ⅰ)화합물 촉매를 반응시킴으로써 시클로펜텐온 유도체를 합성하는 방법이 분자내 반응(intermolecular reaction)을 통한 시클로펜텐온 유도체의 합성이다. 이와같은 분자내 반응은 일반적으로 전술한 분자간 반응에 의하여 시클로펜텐온 유도체를 합성하는 것보다 용이하며, 하기의 식 [5]에서와 같이 반응결과 두고리 시클로펜텐온 유도체(bicyclic cyclopentenon derivatives)를 만들어낸다.As a special embodiment of the synthesis of cyclopentenone derivatives by intermolecular reaction, a method of synthesizing cyclopentenone derivatives by reacting alkene and alkyne in a molecule with a catalyst of carbon monoxide and indenyl cobalt (I) Synthesis of cyclopentenone derivatives via intermolecular reaction. Such intramolecular reactions are generally easier than synthesizing cyclopentenone derivatives by the intermolecular reactions described above, and produce bicyclic cyclopentenon derivatives as a result of the reaction as shown in Equation [5]. .

본 발명에 따른 시클로펜텐온 유도체의 제조방법에 사용되는 촉매는 인데닐코발트(Ⅰ)화합물(indenyl cobalt(I) compounds)이다. 인데닐 코발트 (I )의 리간드로는 알칸, 일산화탄소, 포스핀(phosphine), 포스파이트(phosphite), 알킨, 아민 등과 같이 쉽게 떨어져 나갈 수 있는 리간드가 가능하며, 인데닐코발토센(indenylcobaltocene)과 같이 반응조건하에서 쉽게 인데닐코발발트(I)로 만들어질 수 있는 것도 가능하다. 상기 리간드를 가진 인데닐코발트( I )화함물 중에서 만들기 쉽고 안정한 화합물로는 리간드로 일산화탄소와 트리페닐포스핀(triphenyl-phosphine)을 각각 두개씩 가진 indenylco(Co(CO)2, indenylCo(PPh3)2및 1, 5-시클로옥타디엔(COD)을 리간드로 가진 indenylCo(COD)가 바람직하다.The catalyst used in the method for preparing a cyclopentenone derivative according to the present invention is an indenyl cobalt (I) compound. Indenyl cobalt (I) ligands can be easily separated off such as alkanes, carbon monoxide, phosphine, phosphite, alkynes, amines, and the like, such as indenylcobaltocene It is also possible to be easily made of indenyl cobalt (I) under the reaction conditions. Among the indenyl cobalt (I) compounds containing the ligand, compounds which are easy to make and stable are indenylco (Co (CO) 2 and indenylCo (PPh 3 ) 2 each having two carbon monoxide and triphenylphosphine as ligands. And indenylCo (COD) having 1, 5-cyclooctadiene (COD) as a ligand.

본 발명에 따른 시클로펜텐온 유도체의 제조방법에서 일산화탄소는 기체상태로 공급되며, 그 공급압력은 5기압 내지 100기압이면 가능하며,15기압 내지 50기압의 압력으로 공급되는 것이 바람직하다.In the method for producing a cyclopentenone derivative according to the present invention, carbon monoxide is supplied in a gaseous state, and the supply pressure thereof may be 5 to 100 atm, and is preferably supplied at a pressure of 15 to 50 atm.

본 발명에 따른 시클로펜텐온 유도체의 제조방법에서 이용될 수 있는 용매로는 벤젠, 톨루엔, 크실렌, 헥산, 헵탄, 옥탄, 클로로포름(CHC13), 염화메틸렌(CH2Cl2), 염화에틸렌(dichloroethane), 디에틸에테르, 뷰틸에테르, 에틸아세테이트, 아세토니트릴(CH3CN), THF(tetrahydrofurane), DME(1, 2-dimeth-oxyethane) DMF(dimethylformamide), DMSO(dimethylsulfoxide) 디클림(diglyme·diethylene glycol dimethylether)이 가능하나 DME가 가장 바람직하다.Solvents that may be used in the preparation method of the cyclopentenone derivatives according to the present invention include benzene, toluene, xylene, hexane, heptane, octane, chloroform (CHC1 3 ), methylene chloride (CH 2 Cl 2 ), and ethylene chloride (dichloroethane). ), Diethyl ether, butyl ether, ethyl acetate, acetonitrile (CH 3 CN), THF (tetrahydrofurane), DME (1, 2-dimeth-oxyethane) DMF (dimethylformamide), DMSO (dimethylsulfoxide) dicream (diglyme diethylene) glycol dimethylether) is possible, but DME is most preferred.

본 발명에 따른 시클로펜텐온 유도체의 제조방법에서 상기 반응[1]은 50℃ 내지 200℃의 온도에서 가능하지만, 상기 온도가 100℃ 내지 110℃인 것이 바람직하다.In the method for preparing a cyclopentenone derivative according to the present invention, the reaction [1] is possible at a temperature of 50 ° C. to 200 ° C., but the temperature is preferably 100 ° C. to 110 ° C.

아래에서는 본 발명에 따른 시클로펜텐온 유도체의 제조방법의 실시예에 관하여 설명하고자 한다.Hereinafter will be described with respect to an embodiment of a method for producing a cyclopentenone derivative according to the present invention.

본 발명에 따른 시클로펜텐온 유도체의 제조방법의 '실시예 I'은 분자간 반응에 의한 시클로펜텐온 유도체의 제조방법이다. 이 실시예에서 사용한 알켄은 전술한 바와같이 반응결과로 얻어지는 시클로펜텐온 유도체를 입체 선택적인 유용한 시클로펜텐온 유도체로 만들기 쉬운 놀보나디엔이었으며, 알킨은 모두 터미널알킨을 사용하였다. 이 실시예에서 알킨, 알켄 및 촉매의 당량비는 1 : 5 : 0.01이며, 그 수율은 표 1에서와 같이 85~100%이다.'Example I' of the method for producing a cyclopentenone derivative according to the present invention is a method for preparing a cyclopentenone derivative by an intermolecular reaction. Alkenes used in this example were nolvonadienes which are easy to make the cyclopentenone derivatives obtained as a result of the reaction into stereoselective useful cyclopentenone derivatives as described above, and all alkynes used terminal alkynes. In this example, the equivalent ratio of alkyne, alkene and catalyst is 1: 5: 0.01, and the yield is 85-100% as shown in Table 1.

한편 '실시예 Ⅱ'는 알켄과 알킨이 한 분자내에 들어있는 아릴프로파르길아민(allyl propargyl amine)을 이용한 분자내 반응에 의한 시클로펜텐온 유도체의 제조방법으로서 반응물과 촉매의 망량비는 1 : 0.02이며 그 수율은 90% 이상이다.Meanwhile, 'Example II' is a method for preparing a cyclopentenone derivative by intramolecular reaction using an arylpropargyl amine in which alkene and alkyne are contained in one molecule. 0.02 and the yield is more than 90%.

실시예 IExample I

반자간 반응(intermdecular reaction)Intermdecular reaction

반응용기에 놀보나다엔 2.7㎖(25mmol), 도표 1에 나타난 알킨 5mmol, 및 용매로서 및 DME(dimethoxy ethane) 10㎖를 넣는다. 용기안에 있는 공기를 제거하기 위하여 질소를 버블링(bubbling)한후, 촉매 엔데닐 코발트(Ⅰ)(indenylCo(COD)) 14mg(0.05mmol))을 넣는다. 일산화탄소의 압력을 10기압으로 하여 용기속에 있는 질소를 제거하고 용기안을 일산화탄소로 채운다. 여기에 일산화탄소의 압력을 15기압으로 하고, 100~110℃그의 온도에서 약 40시간 교반한다.Into the reaction vessel, 2.7 ml (25 mmol) of nolvondane, 5 mmol of alkyne shown in Table 1, and 10 ml of dimethoxy ethane (DME) are added as a solvent. After bubbling nitrogen to remove the air in the vessel, 14 mg (0.05 mmol) of catalyst endenyl cobalt (I) is added. The pressure of carbon monoxide is 10 atm to remove nitrogen from the vessel and fill the vessel with carbon monoxide. Here, the pressure of carbon monoxide is 15 atm, and the mixture is stirred at a temperature of 100 to 110 ° C. for about 40 hours.

반응완료후 먼저 가스를 내보낸후 용매와 잔류 놀보다디엔은 회전증발기(rotary evaporator)로 제거한 후 실리카겔 컬럼 크로마토그래피 또는 진공증류를 통하여 생성물을 얻는다. 건조후 생성물의 양 순도 및 알킨에 기초를 둔 수율은 다음의 표 1과 같다.After completion of the reaction, the gas is first discharged, and then the solvent and residual nolvadiene are removed by a rotary evaporator, and the product is obtained by silica gel column chromatography or vacuum distillation. Yield based on the purity and alkyne yield of the product after drying is shown in Table 1 below.

[표 1]TABLE 1

실시예 ⅡExample II

분자내반응(intramolecular reaction)Intramolecular reaction

반응용기에 토실그룹으로 보호된 아릴프로파르길아민(allyl propargylamine) 1.25g(5.0mmol) 및 용매로서 DME 10㎖를 넣고, 질소로 버블링하여 공기를 제거한 후 촉매 인데닐코발트(I)[indenylCo(COD)]28mg(0.1mmol)을 넣는다. 용기에 일산화탄소 10기압을 가하여 질소를 제거한후 일산화탄소의 압력을 15기압으로 하고, 100∼110℃의 온도에서 약 40시간 교반한다.Into the reaction vessel, 1.25 g (5.0 mmol) of aryl propargylamine protected with tosyl group and 10 ml of DME as a solvent were removed, followed by bubbling with nitrogen to remove air, followed by catalyst indenyl cobalt (I) [indenylCo]. (COD)] 28 mg (0.1 mmol). 10 atm of carbon monoxide was added to the vessel to remove nitrogen, and the pressure of carbon monoxide was set to 15 atm, followed by stirring at a temperature of 100 to 110 ° C for about 40 hours.

반응환료후 실리카겔 컬럼 크로마트그래피로 생성물을 얻는다. 건조후 생성물은 1.30g이다.After reaction reaction, the product is obtained by silica gel column chromatography. After drying the product is 1.30 g.

아릴프로파르길아민에 기초한 수율은 94%이다.The yield based on arylpropargylamine is 94%.

본 발명에 따른 시클로펜텐온 유도체의 제조방법은 인데닐코발트(I)화합물 촉매를 사용함으로써 종래의 시클로펜텐온 유도체의 제조방법에 비하여 촉매의 전환수를 크게 증대시켜 적은양의 촉매를 사용하면서도 수율이 높아서 의약품이나 향료물질과 같은 유용한 화합물제조에 중간체로 이용되는 시클로펜텐온 유도체의 공업적 대량생산에 이용될 수 있다.The method for preparing a cyclopentenone derivative according to the present invention uses an indenyl cobalt (I) compound catalyst to greatly increase the number of conversion of the catalyst compared to the method for preparing a cyclopentenone derivative, and thus yields a small amount of catalyst. This high level can be used for industrial mass production of cyclopentenone derivatives which are used as intermediates in the manufacture of useful compounds such as pharmaceuticals and perfumes.

Claims (8)

알킨, 알켄 및 일산호탄소로 부터 시클로펜텐온 유도체를 제조하는 방법에 있어서, 인데닐코발트(I )화합물을 촉매로 사용하는 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.A method for producing a cyclopentenone derivative from alkynes, alkenes and carbon monoxide, wherein the indenyl cobalt (I) compound is used as a catalyst. 제1항에 있어서, 상기 알켄이 놀보나디엔 또는 놀보닐렌인 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method of claim 1, wherein the alkene is nolvadiene or nolvylene. 제1항에 있어서, 상기 알킨이 하기식으로 표시되는 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method for producing a cyclopentenone derivative according to claim 1, wherein the alkyne is represented by the following formula. R1- C ≡ C - R2 R 1 -C ≡ C-R 2 (여기에서 R1과 R2는 수소, 알콜, 아민, 티올, 에테르, 아렌, 알킬; 또는 알콜, 아민, 티올, 에테르, 아렌, 알킬, 카르복실산, 알데히드, 케톤, 니트릴, 아미드, 2중결합, 3중결합 중 하나 이상으로 치환된 것으로서 상기 알킨의 3중결합과 비공액인 탄화수소 화합물)Wherein R 1 and R 2 are hydrogen, alcohol, amine, thiol, ether, arene, alkyl; or alcohol, amine, thiol, ether, arene, alkyl, carboxylic acid, aldehyde, ketone, nitrile, amide, double A hydrocarbon compound non-conjugated with a triple bond of the alkyne, substituted with at least one of a bond and a triple bond) 제1항에 있어서, 상기 알켄과 알킨이 한 분자내에 존재하는 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method of claim 1, wherein the alkene and alkyne are present in one molecule. 제1항 내지 제4항에 있어서, 상기 일산화탄소의 압력이 5기압 내지 100기압인 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method for producing a cyclopentenone derivative according to claim 1, wherein the pressure of the carbon monoxide is 5 atm to 100 atm. 제5항에 있어서, 상기 일산화탄소의 압력이 15기압 내지 50기압인 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method of claim 5, wherein the carbon monoxide has a pressure of 15 to 50 atm. 제1항에 있어서, 반응이 50℃ 내지 200℃의 온도에서 이루어지는 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method for producing a cyclopentenone derivative according to claim 1, wherein the reaction is performed at a temperature of 50 ° C to 200 ° C. 제7항에 있어서, 상기 반응이 100℃ 내지 110℃의 온도에서 이루어지는 것을 특징으로 하는 시클로펜텐온 유도체를 제조하는 방법.The method of claim 7, wherein the reaction is carried out at a temperature of 100 ℃ to 110 ℃.
KR1019940016568A 1994-07-11 1994-07-11 Process for producing cyclopentenone with catalyst of indenglcobalt(i) compound KR0128106B1 (en)

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