KR810000579B1 - Process for preparation of catalyst - Google Patents
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- KR810000579B1 KR810000579B1 KR1019800002264A KR800002264A KR810000579B1 KR 810000579 B1 KR810000579 B1 KR 810000579B1 KR 1019800002264 A KR1019800002264 A KR 1019800002264A KR 800002264 A KR800002264 A KR 800002264A KR 810000579 B1 KR810000579 B1 KR 810000579B1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
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Abstract
Description
본 발명은 여러 유기 인화합물을 배위자(ligand)로 하는 로듐촉매의 제조방법에 관한 것이다.The present invention relates to a method for producing a rhodium catalyst containing various organophosphorus compounds as ligands.
본 발명의 로듐촉매는 올레핀을 히드로포밀화 시켜서 상응하는 알데히드로 만들 때 사용되며, 다음 일반식(I)의 구조를 갖는다.The rhodium catalyst of the present invention is used to hydroformyl an olefin to make the corresponding aldehyde, and has the structure of the following general formula (I).
RhXCO(PR3)x……(I)RhXCO (PR 3 ) x... … (I)
여기서, R은 메틸, 부틸 및 페닐등의 알킬 및 아릴그룹이고,Wherein R is alkyl and aryl groups such as methyl, butyl and phenyl,
X는 수소 또는 할로겐이고, X는 2 내지 3의 정수이다.X is hydrogen or halogen and X is an integer from 2 to 3.
특히 일반식(I)의 촉매는 프로필렌으로부터 옥타놀을 제조하는 히드로포밀화 반응의 촉매로 많이 사용되고 있다.In particular, the catalyst of the general formula (I) is widely used as a catalyst for the hydroformylation reaction for producing octanol from propylene.
최근, 균일계 촉매반응에 로듐화합물과 유기 인화합물의 착화물을 가용성 촉매로 사용하여 올레핀, 카보닐화합물, 방향족화합물들의 수소화 또는 올레핀의 히드로포밀화, 히드로 카복시화하는 방법들이 많이 개발되고 있다.Recently, many methods have been developed for the hydrogenation of olefins, carbonyl compounds, aromatic compounds or the hydroformylation and hydrocarboxylation of olefins by using complexes of rhodium compounds and organophosphorus compounds as soluble catalysts in homogeneous catalysis.
올레핀을 히드로포밀화시켜 상응하는 알데히드로 만들 때 사용되는 종전의 촉매로는 코발트 옥타카보닐과 같은 코발트화합물이 사용되어 왔다. 그러나, 이들 코발트화합물을 사용할 경우에는 올레핀의 히드로포밀화 반응조건, 예를들면 반응압력, 반응온도가 매우 격렬해야 하며, n-알데히드와 이소알데히드의 생성비율이 낮아 결과적으로 원하는 n-알데히드의 수율이 낮은 결점을 지닌다.Cobalt compounds, such as cobalt octacarbonyl, have been used as conventional catalysts for hydroformylating olefins to make the corresponding aldehydes. However, in the case of using these cobalt compounds, the hydroformylation reaction conditions of the olefin, for example, the reaction pressure and the reaction temperature must be very violent, and the production rate of n-aldehyde and isoaldehyde is low, resulting in a desired yield of n-aldehyde. Has this low drawback.
상술한 결점을 없애기 위하여는 본 발명의 로듐촉매를 사용, 매우 온화한 반응조건에서 원하는 n-알데히드의 수율을 높일 수 있다.In order to eliminate the above-mentioned drawbacks, the rhodium catalyst of the present invention can be used to increase the desired yield of n-aldehyde under very mild reaction conditions.
본 발명을 상세히 설명하면, 배위자로 사용되는 유기인 화합물을 무수알코올 용액에 녹여 교반, 가열시킨 다음 40-50℃의 뜨거운 무수알코올에 용해시킨 로듐화합물을 가하고 카보닐기 공여체(donor group)인 알데히드와 알카리금속, 예를들면 나트륨, 칼륨을 무수알코올에 녹여 첨가하고, 격렬히 교반, 환류시켜 일반식(I)의 로듐촉매를 엊는다.DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT In detail, the organic phosphorus compound used as a ligand is dissolved in anhydrous alcohol solution, stirred and heated, and then a rhodium compound dissolved in hot anhydrous alcohol at 40-50 ° C. is added to the aldehyde, which is a carbonyl donor group. Alkali metals such as sodium and potassium are dissolved in anhydrous alcohol, added, and vigorously stirred and refluxed to remove the rhodium catalyst of the general formula (I).
본 발명의 로듐촉매를 제조함에 있어서 특기할 사항은 제조반응이 완결될 때까지 균일계 반응조건을 유지시키면서 각 화합물을 빠른속도로 연속적으로 가하면서 격렬히 저어주어 반응이 완전히 이루어지도록 하여야 한다.What should be noted in the preparation of the rhodium catalyst of the present invention is to stir vigorously while rapidly adding each compound continuously while maintaining the homogeneous reaction conditions until the production reaction is completed to complete the reaction.
만일, 이것이 잘 이루어지지 않는다면 미반응 생성물로 인하여 원하는 생성물이 오염됨으로써 최종 생성물의 수율을 저하시키게 된다.If this is not done well, the unreacted product will contaminate the desired product, resulting in lower yield of the final product.
본 발명에 사용되는 로듐화합물로는 금속로듐, 염화로듐, 초산로듐, 질산로듐 등이 있으며, 염화로듐을 사용하는 것이 바람직하다.Rhodium compounds used in the present invention include metal rhodium, rhodium chloride, rhodium acetate, rhodium nitrate, and the like, and rhodium chloride is preferably used.
또한, 배위자로 사용되는 유기인 화합물로는 PR3(여기서, R은 상기에서 정의된 바와 같다)등이 있다.In addition, organophosphorus compounds used as ligands include PR 3 (where R is as defined above) and the like.
로듐 촉매의 카보닐기 공여체(donor group)로는 탄소수 1 내지 4의 알데히드, 바람직하기로는 포름알데히드를 사용하는 것이다.The carbonyl group donor of the rhodium catalyst is an aldehyde having 1 to 4 carbon atoms, preferably formaldehyde.
또한, 로듐금속 화합물을 제조반응에 사용할 경우에 종전에는 환원제로서 히드라진과 수소화 붕소나트륨을 사용하였으나, 이는 이단계 제조반응으로 제조공정이 불편하고 생성수율이 80%정도로서 비교적 낮다.In addition, when a rhodium metal compound is used in the production reaction, hydrazine and sodium borohydride have been used as a reducing agent in the past, but this production process is inconvenient due to the two-step production reaction and the production yield is relatively low as about 80%.
그러나, 환원제로서 알카리금속, 예를들면 나트륨, 칼륨 또는 칼륨-나트륨의 합금과 무수알코올 용액을 사용함으로써 일단계 반응으로 제조공정이 간편하고 90% 이상의 수율을 얻을 수 있다.However, by using an alkali metal, for example, an alloy of sodium, potassium or potassium-sodium as the reducing agent and an anhydrous alcohol solution, the manufacturing process is simple and a yield of 90% or more can be obtained by a one-step reaction.
본 발명의 로듐촉매의 제조시에 촉매의 안정성증대 및 촉매의 성능개량등의 이유로 배위자를 금속과 착화물형성에 필요한 화학양론적 양보다 과잉으로 공존시켜 제조한다. 일반적으로 금속로듐과 배위자는 몰비로 1 : 5 내지 1: 100 정도이며, 바람직하기로는 1: 10정도이다.In the preparation of the rhodium catalyst of the present invention, the ligand is coexisted in excess of the stoichiometric amount necessary for complex formation with the metal for reasons such as increased stability of the catalyst and improved performance of the catalyst. Generally, the metal rhodium and the ligand are in a molar ratio of about 1: 5 to 1: 100, preferably about 1:10.
반응온도는 일반적으로 80 내지 100℃이다.The reaction temperature is generally 80 to 100 ° C.
다음 실시예를 들어 본 발명을 구체적으로 설명한다.The present invention is described in detail with reference to the following examples.
[실시예 1]Example 1
환류 냉각기와 질소인입기를 장치한 3구를 500ml 둥근 바닥플라스크를 500ml 가열기 안에 넣어 자력 교반기 위에 놓는다. 질소 인입기를 통해 질소를 채운 플라스크내에 무수에탄올 100ml와 트리페닐포스핀 2.62g(1.0밀리몰)을 넣어 가열, 교반하고 용해시킨 후 무수에탄올 20ml에 삼염화로듐 삼수화물 0.26g(0.1밀리몰)을 녹여 빨리 가한다. 약 30초 후에 포름알데히드 10ml를 가하고 연속적으로 무수에탄올 20ml에 나트륨금속 0.322g(14밀리몰)을 녹인 용액을 가한다.Three holes equipped with a reflux condenser and nitrogen injector were placed in a 500 ml round bottom flask in a 500 ml heater and placed on a magnetic stirrer. 100 ml of anhydrous ethanol and 2.62 g (1.0 mmol) of triphenylphosphine were added to a flask filled with nitrogen through a nitrogen inleter, heated, stirred and dissolved, followed by dissolving 0.26 g (0.1 mmol) of rhodium trichloride trihydrate in 20 ml of anhydrous ethanol. do. After about 30 seconds, 10 ml of formaldehyde is added and a solution of 0.322 g (14 mmol) of sodium metal is continuously added to 20 ml of anhydrous ethanol.
약 한시간 정도 가열, 교반하면서 환류시켜 황색 침전물을 얻는다. 미반응 생성물을 세척하기 위해 에탄올, 물, 에탄올, n-헥산의 순서로 침전물을 세척하고 건조시킨다.The mixture is heated to reflux with stirring for about an hour to obtain a yellow precipitate. The precipitate is washed and dried in the order of ethanol, water, ethanol, n-hexane to wash the unreacted product.
얻어진 생성물은 매우 순도가 높은 히드로카보닐트리스(트리페닐포스핀)로듐(I)으로서 수율은 95%이었다.The obtained product was very high-hydrocarbonyl tris (triphenylphosphine) rhodium (I), the yield was 95%.
[실시예 2]Example 2
실시예 1과 같은 실험장치에 트리페닐포스핀을 로듐화합물보다 20배 과량으로 가하고 나트륨금속대신 칼륨금속을 무수에탄올 용액에 녹여 가하여 반응시키는 이외에는 실시예 1과 동일한 방법으로 실험했다.Triphenylphosphine was added 20 times more than the rhodium compound, and potassium metal was dissolved in anhydrous ethanol solution instead of sodium metal, and the reaction was carried out in the same manner as in Example 1.
히드로카보닐트리스(트리페닐포스핀) 로듐(I)의 수율은 95%이었다.The yield of hydrocarbonyltris (triphenylphosphine) rhodium (I) was 95%.
[실시예 3]Example 3
실시예 1의 나트륨금속대신 나트륨-칼륨의 합금을 무수에탄올에 녹여 사용한 이외에는 실시예 1과 동일한 방법으로 실험을 행했다. 히드로카보닐트리스(트리페닐포핀) 로듐(I)의 수율은 95%이었다.The experiment was conducted in the same manner as in Example 1 except that the sodium-potassium alloy instead of the sodium metal of Example 1 was dissolved in anhydrous ethanol. The yield of hydrocarbonyltris (triphenylphosphine) rhodium (I) was 95%.
이상의 실시예 2,3에서 얻은 로듐촉매 RhHCO(PPh3)의 분광학적 자료 및 융점은 실시예 1과 같다.Spectroscopic data and melting point of the rhodium catalyst RhHCO (PPh 3 ) obtained in Examples 2 and 3 are the same as those in Example 1.
[실시예 4]Example 4
배위자로 트리부틸포스핀을 사용하여 실시예 1과 동일한 방법으로 일반식(I)의 촉매를 제조했다. 실시예 1과 동일한 반응장치에 트리부틸포스핀 1.0116g(0.5밀리몰)을 20ml 에탄올에 녹여 가하고 0.13g(0.05 밀리몰) 삼염화로듐 삼수화물을 10ml 에탄올에 녹여 가한 후 교반하면서 가열했다. 약 30초 후 포름알데히드 10ml와 무수에탄올 10ml에 녹인 나트륨금속 0.161g(7밀리몰)용액을 가하고 30분간 환류시켜 진한 노란색의 용액을 얻었다. 용매를 증발시킨 후 석유에테르로 결정화시켰다.Tributylphosphine was used as the ligand to prepare a catalyst of formula (I) in the same manner as in Example 1. 1.0116 g (0.5 mmol) of tributylphosphine was dissolved in 20 ml of ethanol, and 0.13 g (0.05 mmol) of rhodium trichloride was added to 10 ml of ethanol, followed by heating with stirring. After about 30 seconds, a solution of 0.161 g (7 mmol) of sodium metal dissolved in 10 ml of formaldehyde and 10 ml of anhydrous ethanol was added and refluxed for 30 minutes to obtain a dark yellow solution. The solvent was evaporated and then crystallized with petroleum ether.
히드로카보닐트리스(트리부틸포스핀) 로듐(I)의 수율은 70%이었다.The yield of hydrocarbonyltris (tributylphosphine) rhodium (I) was 70%.
I.R 데이타I.R data
용액(n-헥산, cm-1) 2040(Rh-H)Solution (n-hexane, cm -1 ) 2040 (Rh-H)
1940(CO)1940 (CO)
1150, 1220(P-Bu)1150, 1220 (P-Bu)
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