KR20000056308A - A process for the preparation of cinnamic acid derivatives using (S)-binaphthyl palladium complex as a catalyst - Google Patents

A process for the preparation of cinnamic acid derivatives using (S)-binaphthyl palladium complex as a catalyst Download PDF

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KR20000056308A
KR20000056308A KR1019990005518A KR19990005518A KR20000056308A KR 20000056308 A KR20000056308 A KR 20000056308A KR 1019990005518 A KR1019990005518 A KR 1019990005518A KR 19990005518 A KR19990005518 A KR 19990005518A KR 20000056308 A KR20000056308 A KR 20000056308A
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cinnamic acid
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acid derivatives
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김정수
백성인
김기석
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구광시
주식회사 코오롱
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/347Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
    • C07C51/377Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C59/00Compounds having carboxyl groups bound to acyclic carbon atoms and containing any of the groups OH, O—metal, —CHO, keto, ether, groups, groups, or groups
    • C07C59/40Unsaturated compounds
    • C07C59/58Unsaturated compounds containing ether groups, groups, groups, or groups
    • C07C59/64Unsaturated compounds containing ether groups, groups, groups, or groups containing six-membered aromatic rings

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Abstract

PURPOSE: A process of preparing cinnamic acid derivatives using a trace amount of a palladium composite catalyst is provided which needs no complicated activation process for recovering palladium. CONSTITUTION: A cinnamic acid derivatives of formula 1 are prepared by the reaction of alkoxybenzene derivatives of formula 2 and acrylic acid derivatives of the following formula; CH2=CHCOOR2 in the presence of a (S)-binaphthyl palladium composite catalyst of formula 3 and an inorganic base. In formula, X is brome or iodine, R1 is C1-8 lower alkyl, R2 is H, C1-10 straight or branched alkyl, or hydroxyalkyl, R3 is benzene or toluene. and has high color, purity products and production yield. The process produces the title compound in high purity and yields as compared with conventional ones.

Description

(S)-비나프틸팔라듐복합촉매를 이용한 신남산 유도체의 제조방법{A process for the preparation of cinnamic acid derivatives using (S)-binaphthyl palladium complex as a catalyst}A process for the preparation of cinnamic acid derivatives using (S) -binaphthyl palladium complex as a catalyst}

본 발명은 하기 화학식 1의 신남산 유도체를 제조하는 방법에 관한 것이다.The present invention relates to a method for preparing the cinnamic acid derivative of the formula (1).

1One

상기 식에서 R1은 탄소수 1 내지 8의 저급 알킬기이며, R2는 수소, 탄소수 1내지 10의 직쇄상 또는 분지상 알킬기, 또는 히드록시알킬기이다.In the above formula, R 1 is a lower alkyl group having 1 to 8 carbon atoms, R 2 is hydrogen, a linear or branched alkyl group having 1 to 10 carbon atoms, or a hydroxyalkyl group.

신남산 유도체는 자외선을 흡수하는 성질에 의해 자외선 차단 화장품의 원료로 사용되고 있으며, 이를 제조하기 위한 여러가지 방법이 보고 되어왔다.Cinnamic acid derivatives have been used as a raw material for sunscreen cosmetics by the nature of absorbing ultraviolet rays, and various methods have been reported for preparing them.

예를 들어, 미국특허 제 4,970,332에 기술된 방법에 따르면 하기 반응식 1과 같이 4-요오도아니솔이 지지체에 결합된 팔라듐 촉매와 트리알킬아민하에서 알킬 아크릴레이트와 반응시킴으로써 신남산 유도체를 제조하는 방법이 개시된 바 있다.For example, according to the method described in US Pat. No. 4,970,332, a method of preparing cinnamic acid derivatives is obtained by reacting 4-iodoanisole with alkyl acrylate under a palladium catalyst and trialkylamine bonded to a support as shown in Scheme 1 below. It has been disclosed.

상기에서 R2*는 탄소수 1 내지 10의 알킬기이다.In the above, R 2 * is an alkyl group having 1 to 10 carbon atoms.

또한, 미국특허 제 5,457,266호에 기재된 신남산 유도체의 제법은 하기 반응식 2와 같이 화학식 2의 알콕시벤젠 유도체를 팔라듐활성촉매, 알카노산 암모늄염하에서 알킬 아크릴레이트와 반응시킴으로써 화학식 1의 신남산 유도체를 제조하는 방법이 개시된 바 있다.In addition, the preparation method of cinnamic acid derivatives described in US Pat. No. 5,457,266 is prepared by reacting an alkoxybenzene derivative of formula (2) with an alkyl acrylate under a palladium active catalyst and an alkanoic acid ammonium salt as shown in Scheme 2 to prepare a cinnamic acid derivative of formula (1). The method has been disclosed.

상기에서 R1은 탄소수 1 내지 8의 저급 알킬기이며, R2는 수소, 탄소수 1 내지 10의 직쇄상 또는 분지상 알킬기, 또는 히드록시알킬기이다.R 1 is a lower alkyl group having 1 to 8 carbon atoms, and R 2 is hydrogen, a straight or branched alkyl group having 1 to 10 carbon atoms, or a hydroxyalkyl group.

그러나, 상기한 공지의 방법에 따라 화학식 1의 신남산 유도체를 제조할 경우 제조공정상 여러 가지 어려움이 있다. 즉 지지체에 결합된 팔라듐 촉매를 사용할 경우 촉매 활성이 떨어져 촉매 사용량이 많고, 반응시간이 길며, 반응수율이 낮고, 및 염기로는 트리알킬아민만으로 한정되는 것 등의 단점이 있고, 팔라듐 활성 탄소촉매하에서의 반응은 반응속도가 빠르나 촉매 사용량이 많아 반응 종결후 값이 비싼 팔라듐촉매를 회수하기 위한 까다로운 활성화 공정이 요구되는 단점이 있다. 또한, 상기의 두 반응에는 모두 염기로 암모늄염이 사용되는데 이는 목적화합물의 색상과 순도에 있어서 만족할 만한 결과를 제공하지 못하는 단점이 있다.However, when preparing the cinnamic acid derivative of the formula (1) according to the known method described above, there are various difficulties in the manufacturing process. That is, when the palladium catalyst bonded to the support is used, there are disadvantages such as low catalyst activity, high catalyst usage, long reaction time, low reaction yield, and limited to only trialkylamine as a base, and a palladium activated carbon catalyst. Under the reaction, the reaction rate is fast, but the catalyst is used a lot, so that a demanding activation process for recovering the expensive palladium catalyst after completion of the reaction is required. In addition, in both reactions, an ammonium salt is used as a base, which does not provide satisfactory results in color and purity of the target compound.

이에 본 발명자들은 상기와 같은 종래 기술의 문제점을 해결하고자 연구를 거듭한 결과, 활성이 강한 팔라듐복합촉매를 극미량 사용함으로써 팔라듐을 회수하기 위한 까다로운 활성화 공정이 필요없고, 반응성이 강하여 반응시간이 짧고, 염기로는 무기염기를 사용하여 색상, 순도 및 수율이 높은 신남산 유도체의 제조방법을 발견하여 본 발명을 완성하게 되었다.Accordingly, the present inventors have repeatedly studied to solve the problems of the prior art as a result, by using a very small amount of a highly active palladium complex catalyst, there is no need for a demanding activation process for recovering palladium, the reaction time is short, the reaction time is short, As a base, the present invention was completed by discovering a method of preparing cinnamic acid derivative having high color, purity, and yield using an inorganic base.

따라서, 본 발명은 팔라듐 복합촉매를 사용한 신규의 신남산 유도체의 제조방법을 제공하는 것을 목적으로 한다.Accordingly, an object of the present invention is to provide a method for producing a novel cinnamic acid derivative using a palladium complex catalyst.

본 발명은 화학식 2의 알콕시벤젠 유도체와 화학식 4의 아크릴산 유도체를 화학식 3의 (S)-비나프틸팔라듐복합촉매 및 무기염기 존재하에서 반응시키는 공정을 포함하는 화학식 1의 신남산 유도체의 제조방법에 관한 것이다.The present invention relates to a process for preparing a cinnamic acid derivative of formula (1) comprising a step of reacting an alkoxybenzene derivative of formula (2) and an acrylic acid derivative of formula (4) in the presence of the (S) -binafthyl palladium complex catalyst of formula (3) and an inorganic base. It is about.

상기에서 X는 브롬 또는 요오드, R1은 탄소수 1 내지 8의 저급 알킬기, R2는 수소, 탄소수 1 내지 10의 직쇄상 또는 분지상 알킬기, 또는 히드록시알킬기이고, R3는 벤젠 또는 톨루엔이다.X is bromine or iodine, R 1 is a lower alkyl group having 1 to 8 carbon atoms, R 2 is hydrogen, a straight or branched alkyl group having 1 to 10 carbon atoms, or a hydroxyalkyl group, and R 3 is benzene or toluene.

본 발명에 따른 제조방법을 반응식으로 나타내면 하기 반응식 3과 같다.The preparation method according to the present invention is represented by the following Scheme 3.

상기 반응식 3에서 X,R1및 R2는 상기에서 정의된 바와 같다.In Scheme 3, X, R 1 and R 2 are as defined above.

본 발명에 따른 제조방법에서 화학식 4의 아크릴산 유도체는 화학식 2의 알콕시벤젠 유도체에 대해 0.5 ~ 5.0당량 사용되는 것이 바람직하며, 2 내지 4당량을 사용하는 것이 더욱 바람직하다. 상기 화합물의 사용량이 화학식 2의 알콕시벤젠 유도체에 대해 0.5당량 미만일 때는 반응성이 떨어지고, 5당량을 초과할 때는 부반응이 일어 날 수 있다.In the preparation method according to the present invention, the acrylic acid derivative of Formula 4 is preferably used in an amount of 0.5 to 5.0 equivalents, more preferably 2 to 4 equivalents, relative to the alkoxybenzene derivative of Formula 2. When the amount of the compound used is less than 0.5 equivalents to the alkoxybenzene derivative of Formula 2, the reactivity decreases, and when it exceeds 5 equivalents, side reactions may occur.

본 발명에 따른 제조방법에서 화학식 3의 (S)-비나프틸팔라듐복합촉매의 사용량은 화학식 2의 알콕시벤젠 유도체에 대해 10 ~ 100ppm인 것이 바람직하며, 30 ~ 50ppm인 것이 더욱 바람직하다. 화학식 3의 (S)-비나프틸팔라듐복합촉매의 사용량이 10ppm미만일 때는 반응성이 떨어지고, 100ppm을 초과할 때에는 부반응이 일어나 경제성이 떨어질 수 있다.In the preparation method according to the present invention, the amount of the (S) -binafylpalladium complex catalyst of Formula 3 is preferably 10 to 100 ppm, more preferably 30 to 50 ppm, based on the alkoxybenzene derivative of Formula 2. When the amount of the (S) -vinaphthyl palladium complex catalyst of Formula 3 is less than 10 ppm, the reactivity may decrease, and when it exceeds 100 ppm, side reactions may occur and economic efficiency may be reduced.

본 발명에 따른 제조방법에 있어서, 무기염기는 탄산칼륨, 탄산수소칼륨, 탄산나트륨 및 탄산수소나트륨으로 이루어진 군에서 선택되는 것이 바람직하다. 무기염기의 사용량은 화학식 2의 알콕시벤젠 유도체에 대해 0.5 ~ 5.0당량을 사용하는 것이 바람직하며, 1 ~ 3당량을 사용하는 것이 더욱 바람직하다. 무기염기의 사용량이 0.5당량 미만일 때는 반응성이 떨어지고, 5당량을 초과할 때에는 부반응 및 제거의 어려움이 있다.In the production method according to the invention, the inorganic base is preferably selected from the group consisting of potassium carbonate, potassium hydrogen carbonate, sodium carbonate and sodium hydrogen carbonate. The amount of the inorganic base is preferably 0.5 to 5.0 equivalents, more preferably 1-3 equivalents to the alkoxybenzene derivative of the formula (2). When the amount of the inorganic base is less than 0.5 equivalents, the reactivity decreases, and when it exceeds 5 equivalents, there are difficulties in side reactions and removal.

본 발명에 따른 제조방법에 있어서, 반응 용매는 디메틸포름아미드, N-메틸피롤리돈 및 물로 이루어진 군에서 선택되는 것이 바람직하고, 화학식 2의 알콕시벤젠 유도체에 대해 질량비로 1 ~ 10배로 사용되는 것이 바람직하며, 2 ~ 6배를 사용하는 것이 더욱 바람직하다. 반응 용매의 사용량이 화학식 2의 알콕시벤젠 유도체에 비해 1배 미만일 때에는 부반응이 일어나며, 10배를 초과할 때에는 반응성이 떨어질 수 있다.In the production method according to the present invention, the reaction solvent is preferably selected from the group consisting of dimethylformamide, N-methylpyrrolidone and water, it is used in an amount of 1 to 10 times by mass relative to the alkoxybenzene derivative of formula (2) Preferably, it is more preferable to use 2-6 times. When the amount of the reaction solvent is less than one time compared to the alkoxybenzene derivative of Formula 2, a side reaction may occur, and when the amount of the reaction solvent exceeds 10 times, the reactivity may be deteriorated.

본 발명에 따른 제조방법에 있어서, 반응온도는 50 ~ 150℃가 바람직하며, 60 ~ 120℃가 더욱 바람직하다. 또한, 반응시간은 0.5 ~ 5시간이 바람직하며, 1 ~ 2시간이 더욱 바람직하다. 상기한 반응온도보다 낮거나 반응시간이 짧으면 반응성이 떨어지고, 반응온도보다 높거나 반응시간이 길면 부반응이 일어날 수 있다.In the production method according to the invention, the reaction temperature is preferably 50 ~ 150 ℃, more preferably 60 ~ 120 ℃. In addition, the reaction time is preferably 0.5 to 5 hours, more preferably 1 to 2 hours. If the reaction temperature is lower than the above or the reaction time is short, the reactivity is lowered, if higher than the reaction temperature or the reaction time is long side reaction may occur.

상기와 같이 화학식 2의 알콕시벤젠 유도체와 화학식 4의 아크릴산 유도체의 반응이 완결되면 반응 용액을 추출 및 농축시킨 후, 감압증류 등의 정제방법으로 생성된 화학식 1의 신남산 유도체를 순수한 상태로 수득할 수 있다.As described above, when the reaction between the alkoxybenzene derivative of Formula 2 and the acrylic acid derivative of Formula 4 is completed, the reaction solution is extracted and concentrated, and the cinnamic acid derivative of Formula 1 produced by a purification method such as distillation under reduced pressure can be obtained in a pure state. Can be.

상기와 같은 본 발명에 따른 화학식 1의 신남산 유도체의 제조방법은 극미량의 (S)-비나프틸팔라듐복합촉매 및 무기염기를 이용함으로써 고가의 팔라듐촉매를 회수하기 위한 활성화 공정이 필요없으며, 색상, 순도를 개선할 수 있을 뿐 아니라 높은 수율로 화학식 1의 신남산 유도체를 제조할 수 있다.As described above, the method for preparing the cinnamic acid derivative of Chemical Formula 1 according to the present invention does not require an activation process for recovering an expensive palladium catalyst by using a very small amount of (S) -binafylpalladium complex catalyst and inorganic base. In addition to improving the purity, it is possible to prepare a cinnamic acid derivative of Formula 1 in high yield.

이하, 본 발명을 실시예를 통하여 더욱 상세히 설명한다. 그러나, 이것이 본 발명의 범위를 제한하는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples. However, this does not limit the scope of the invention.

실시예 1Example 1

2-에틸헥실 4-메톡시신남산 에스테르의 제조Preparation of 2-ethylhexyl 4-methoxycinnamic acid ester

물 300g, 4-브로모아니솔 187.0g, 탄산갈륨 138.2g, (S)-비나프틸팔라듐복합촉매(R3=벤젠) 10mg에 2-에틸헥실 아크릴레이트 276.4g을 천천히 적가하였다. 이 용액을 100℃에서 1시간 동안 교반시킨 후 층분리를 통해 물층을 제거한 후 감압증류로 상기 목적물 275.9g을 얻었다. 상기 목적물의 수율은 95%이었으며, GC에 의한 순도는 99.9%였다. NMR에 의한 측정 데이터는 다음과 같다.300 g of water, 187.0 g of 4-bromoanisole, 138.2 g of gallium carbonate, and 276.4 g of 2-ethylhexyl acrylate were slowly added dropwise to 10 mg of (S) -vinaptyl palladium complex catalyst (R 3 = benzene). The solution was stirred at 100 ° C. for 1 hour, and then the water layer was removed by layer separation. Then, 275.9 g of the target compound was obtained by distillation under reduced pressure. The yield of the target product was 95%, the purity by GC was 99.9%. Measurement data by NMR is as follows.

1H-NMR(CDCl3, 400MHz, ppm) : 0.86-0.98(6H,m), 1.25-1.72(9H,m), 3.84(3H,s), 4.11(2H,d), 6.85-6.95(1H,m), 7.44-7.54(1H,m), 7.64(1H,d) 1 H-NMR (CDCl 3 , 400 MHz, ppm): 0.86-0.98 (6H, m), 1.25-1.72 (9H, m), 3.84 (3H, s), 4.11 (2H, d), 6.85-6.95 (1H) , m), 7.44-7.54 (1H, m), 7.64 (1H, d)

실시예 2Example 2

2-에틸헥실 4-메톡시신남산 에스테르의 제조Preparation of 2-ethylhexyl 4-methoxycinnamic acid ester

물 300g, 4-요오도아니솔 234.0g, 탄산칼륨 138.2g,(S)-비나프틸팔라듐복합촉매(R3=벤젠) 10mg에 2-에틸헥실 아크릴레이트 276.4g을 천천히 적가하였다. 이 용액을 100℃에서 1시간 동안 교반시킨 후 층분리를 통해 물층을 제거한 후 감압증류로 상기 목적물 275.9g을 얻었다. 상기 목적물의 수율은 95%이었으며, GC에 의한 순도는 99.9%이었다. NMR에 의한 측정 데이터는 다음과 같다.276.4 g of 2-ethylhexyl acrylate was slowly added dropwise to 300 g of water, 234.0 g of 4-iodoanisole, 138.2 g of potassium carbonate, and 10 mg of (S) -binafthyl palladium complex catalyst (R 3 = benzene). The solution was stirred at 100 ° C. for 1 hour, and then the water layer was removed by layer separation. Then, 275.9 g of the target compound was obtained by distillation under reduced pressure. The yield of the target product was 95%, purity by GC was 99.9%. Measurement data by NMR is as follows.

1H-NMR(CDCl3, 400MHz, ppm) : 0.86-0.98(6H,m), 1.25-1.72(9H,m), 3.84(3H,s), 4.11(2H,d), 6.85-6.95(1H,m), 7.44-7.54(1H,m), 7.64(1H,d) 1 H-NMR (CDCl 3 , 400 MHz, ppm): 0.86-0.98 (6H, m), 1.25-1.72 (9H, m), 3.84 (3H, s), 4.11 (2H, d), 6.85-6.95 (1H) , m), 7.44-7.54 (1H, m), 7.64 (1H, d)

실시예 3Example 3

2-에틸헥실 4-메톡시신남산 에스테르의 제조Preparation of 2-ethylhexyl 4-methoxycinnamic acid ester

디메틸포름아미드 300g, 4-브로모아니솔 187.0g, 탄산칼륨 138.2g, (S)-비나프틸팔라듐복합촉매(R3=벤젠) 10mg에 2-에틸헥실 아크릴레이트 276.4g을 천천히 적가하였다. 이 용액을 100℃에서 1시간 동안 교반시킨 후 층분리를 통해 물층을 제거한 후 감압증류로 상기 목적물 275.9g을 얻었다. 상기 목적물의 수율은 95%였으며, GC에 의한 순도는 99.9%였다. NMR에 의한 측정 데이터는 다음과 같다.300 g of dimethylformamide, 187.0 g of 4-bromoanisole, 138.2 g of potassium carbonate, and 276.4 g of 2-ethylhexyl acrylate were slowly added dropwise to 10 mg of the (S) -binafthyl palladium complex catalyst (R 3 = benzene). The solution was stirred at 100 ° C. for 1 hour, and then the water layer was removed by layer separation. Then, 275.9 g of the target compound was obtained by distillation under reduced pressure. The yield of the target product was 95%, the purity by GC was 99.9%. Measurement data by NMR is as follows.

1H-NMR(CDCl3, 400MHz, ppm) : 0.86-0.98(6H,m), 1.25-1.72(9H,m), 3.84(3H,s), 4.11(2H,d), 6.85-6.95(1H,m), 7.44-7.54(1H,m), 7.64(1H,d) 1 H-NMR (CDCl 3 , 400 MHz, ppm): 0.86-0.98 (6H, m), 1.25-1.72 (9H, m), 3.84 (3H, s), 4.11 (2H, d), 6.85-6.95 (1H) , m), 7.44-7.54 (1H, m), 7.64 (1H, d)

비교예Comparative example

2-에틸헥실 4-메톡시신남산 에스테르의 제조Preparation of 2-ethylhexyl 4-methoxycinnamic acid ester

미국특허 제 5,457,266호에 기술된 방법으로 제조하였다. 4-요오도아니솔 4.68g, 2-에틸헥실 아세테이트 4.05g, 트리에틸아민 2.22g, 아세트산 1.32g, 팔라듐탄소촉매 15mg을 넣고 150℃에서 3시간 교반하였다. 물과 톨루엔을 넣고 층분리 후 2N 염산용액으로 세척한 후 감압증류하여 수율 80%, GC 순도 95%로 노란색의 목적화합물 4.65g을 얻었다.It was prepared by the method described in US Pat. No. 5,457,266. 4.68 g of 4-iodoanisole, 4.05 g of 2-ethylhexyl acetate, 2.22 g of triethylamine, 1.32 g of acetic acid and 15 mg of palladium carbon catalyst were added and stirred at 150 ° C. for 3 hours. Water and toluene were added, the layers were separated, washed with 2N hydrochloric acid solution, and distilled under reduced pressure to obtain 4.65 g of a yellow target compound with a yield of 80% and GC purity of 95%.

이상의 실시예 및 비교예에서 확인된 바와 같이 본 발명의 제조방법은 기존의 방법보다 고순도 및 고수율로 화학식 1의 신남산 유도체를 얻을 수 있었다.As confirmed in the above examples and comparative examples, the production method of the present invention was able to obtain a cinnamic acid derivative of Formula 1 with higher purity and higher yield than the conventional method.

본 발명의 제조방법은 화학식 1의 신남산 유도체를 종래의 제조방법에 비해고수율, 고순도로 경제적으로 제조할 수 있다는 잇점이 있다.The production method of the present invention has the advantage that it can be economically produced in high yield, high purity compared to the conventional production method of the cinnamic acid derivative of formula (1).

Claims (7)

화학식 2의 알콕시벤젠 유도체와 화학식 4의 아크릴산 유도체를 화학식 3의 (S)-비나프틸팔라듐복합촉매 및 무기염기 존재하에서 반응시키는 공정을 포함하는 화학식 1의 신남산 유도체의 제조방법.A process for preparing a cinnamic acid derivative of formula (1) comprising the step of reacting an alkoxybenzene derivative of formula (2) and an acrylic acid derivative of formula (4) in the presence of a (S) -binafylpalladium complex catalyst of formula (3) and an inorganic base. 1One 22 33 44 상기에서 X는 브롬 또는 요오드, R1은 탄소수 1 내지 8의 저급 알킬기, R2는 수소, 탄소수 1 내지 10의 직쇄상 또는 분지상 알킬기, 또는 히드록시알킬기이고, R3는 벤젠 또는 톨루엔이다.X is bromine or iodine, R 1 is a lower alkyl group having 1 to 8 carbon atoms, R 2 is hydrogen, a straight or branched alkyl group having 1 to 10 carbon atoms, or a hydroxyalkyl group, and R 3 is benzene or toluene. 제1항에 있어서, 화학식 4의 아크릴산 유도체의 사용량이 화학식 2의 알콕시 벤젠 유도체에 대해 0.5 ~ 5.0당량인 것을 특징으로 하는 화학식 1의 신남산 유도체의 제조방법The method of claim 1, wherein the amount of the acrylic acid derivative represented by the formula (4) is 0.5 to 5.0 equivalents based on the alkoxy benzene derivative represented by the formula (2). 제1항에 있어서, 화학식 3의 (S)-비나프틸팔라듐복합촉매의 사용량이 화학식 2의 알콕시벤젠 유도체에 대해 10 ~ 100ppm인 것을 특징으로 하는 화학식 1의 신남산 유도체의 제조방법.The method of claim 1, wherein the amount of the (S) -binafylpalladium complex catalyst of the formula (3) is 10 to 100 ppm with respect to the alkoxybenzene derivative of the formula (2). 제1항에 있어서, 무기염기가 탄산칼륨, 탄산수소칼륨, 탄산나트륨 및 탄산수소나트륨으로 이루어진 군에서 선택되는 것을 특징으로 하는 화학식 1의 신남산 유도체의 제조방법.The method of claim 1, wherein the inorganic base is selected from the group consisting of potassium carbonate, potassium hydrogen carbonate, sodium carbonate and sodium hydrogen carbonate. 제4항에 있어서, 무기염기의 사용량이 화학식 2의 알콕시벤젠 유도체에 대해 0.5 ~ 5.0당량인 것을 특징으로 하는 화학식 1의 신남산 유도체의 제조방법.The method of claim 4, wherein the amount of the inorganic base is 0.5 to 5.0 equivalents based on the alkoxybenzene derivative of the formula (2). 제1항에 있어서, 반응 용매가 디메틸포름아미드, N-메틸피롤리돈 및 물로 이루어진 군에서 선택되며, 화학식 2의 알콕시벤젠 유도체에 대해 질량비로 1 ~ 10배가 사용되는 것을 특징으로 하는 화학식 1의 신남산 유도체의 제조방법.The reaction solvent of claim 1, wherein the reaction solvent is selected from the group consisting of dimethylformamide, N-methylpyrrolidone, and water, and 1 to 10 times by mass ratio is used for the alkoxybenzene derivative of Formula 2. Method for preparing cinnamic acid derivatives. 제1항에 있어서, 반응온도가 50 ~ 150℃이고, 반응시간이 0.5 ~ 5시간인 것을 특징으로 하는 화학식 1의 신남산 유도체의 제조방법.The method of claim 1, wherein the reaction temperature is 50 ~ 150 ℃, the reaction time is 0.5 to 5 hours.
KR1019990005518A 1999-02-19 1999-02-19 A process for the preparation of cinnamic acid derivatives using (S)-binaphthyl palladium complex as a catalyst KR20000056308A (en)

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