• Bulletin of the Korean Chemical Society
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• 제10권4호
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• pp.360-362
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• 1989

Catalytic isomerization of unsaturated alcohols to the corresponding carbonyl compounds with$Rh(ClO_4)(CO)(PPh_3)_2\;(1)\;and\;[Rh(CO)(PPh_3)_3]ClO_4$ (2) is faster under hydrogen (where hydrogenation also occurs to give saturated alcohols) than under nitrogen. The isomerization under hydrogen seems to occur through an alkylhydridorhodium(III) complex which also undergoes reductive elimination to give hydrogenation products, saturated alcohols. The isomerization under hydrogen is faster with 2 than with 1, which is understood by acceleration of the last step, enol formation by $PPh_3$ dissociated from 2 and present in the reaction mixture when 2 is used as catalyst. Relative rates of the isomerization observed for different unsaturated alcohols are interpreted by steric effects of substituted groups and numbers of hydrogens to be abstracted by the rhodium of the intermediate, alkylhydridorhodium(III) to undergo the reductive elimination to give enol which is then rapidly converted into a carbonyl compound. It has been observed that the hydrogenation is relatively significant when reactions occur slowly whereas the isomerization is predominant when reactions proceed rapidly.

• Bulletin of the Korean Chemical Society
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• 제7권6호
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• pp.466-468
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• 1986

Reaction of $Ir(ClO_4)(CO)(PPh_3)_2$ with trans-$C_6H_5CH$ = $CHCO_2C_2H_5$ produces a new cationic iridium(I) complex, [Ir (trans-$C_6H_5CH$ = $CHCO_2C_2H_5)(CO)(PPh_3)_2]ClO_4$ where trans-$C_6H_5CH$ = $CHCO_2C_2H_5$ seems to be coordinated through the carbonyl oxygen rather than through the $\pi$-system of the olefinic group according to the spectral data. It has been found that Ir$(ClO_4)(CO)(PPh_3)_2$ catalyzes the hydrogenation of $CH_2$ = $CHCO_2C_2H_5$, trans-$CH_3CH$ = $CHCO_2C_2H_5$ and trans-$C_6H_5CH$ = $CHCO_2C_2H_5$ to $CH_3CH_2CO_2C_2H_5$, $CH_3CH_2CH_2CO_2C_2H_5$ and $C_6H_5CH_2CH_2CO_2C_2H_5$, respectively at room temperature under the atmospheric pressure of hydrogen. The relative rates of the hydrogenation of the unsaturated esters are mostly understood in terms of steric reasons.

• Bulletin of the Korean Chemical Society
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• 제7권6호
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• pp.468-471
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• 1986

The isolated products from the reactions of $Rh(ClO_4)(CO)(PPh_3)_2$ (1) with CH_2$ = $CHCO_2C_2H_5$ (2) and trans-$CH_3CH$ = $CHCO_2C_2H_5$ (3) contain 80∼ 90% of $[Rh(CH_2 = CHCO_2C_2H_5)(CO)(PPh_3)_2]ClO_4$ (4) and [Rh(trans-$CH_3CH = CHCO_2C_2H_5(CO)(PPh_3)_2]ClO_4$ (5), respectively where 2 and 3 seem to be coordinated through the carbonyl oxygen. It has been found that complex 1 catalyzes the isomerization of $CH_2 = CH(CH_2)_8CO_2C_2H_5$ (6) to $CH_3(CH_2)_nCH = CH(CH_2)_{7-n}CO_2C_2H_5$ (n = 0∼7) under nitrogen at 25$^{\circ}C$. The isomerization of 6 is slower than that of $CH_2 = CH(CH_2)_9CH_3$ to $CH_3(CH_2)_nCH$ = $CH(CH_2)_{8-n}CH_3$ (n = 0∼8), which is understood in terms of the interactions between the carbonyl oxygen of 6 and the catalyst. It has been also observed that complex 1 catalyzes the hydrogenation of 2, 3, 6, trans-$C_6H_5CH = CHCO_2C_2H_5$ (7), $CH_3(CH_2)_7CH = CH(CH_2)_7CO_2C_2H_5$ (8) and $CH_2 = CH(CH_2)_9CH_3$ (9), and the isomerization (double bond migration) of 6 and 9 under hydrogen at 25$^{\circ}C$. The interactions between the carbonyl oxygen of the unsaturated esters and the catalyst affect the hydrogenation in such a way that the hydrogenation of the unsaturated esters becomes slower than that of simple olefins.

• Bulletin of the Korean Chemical Society
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• 제26권11호
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• pp.1682-1688
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• 2005

Using the ASED-MO (Atom Superposition and Electron Delocalization-Molecular Orbital) theory, we investigated carbon formation and carbon hydrogenation for $CO_2$ methanation on the Ni (111) surface. For carbon formation mechanism, we calculated the following activation energies, 1.27 eV for $CO_2$ dissociation, 2.97 eV for the CO, 1.93 eV for 2CO dissociation, respectively. For carbon methanation mechanism, we also calculated the following activation energies, 0.72 eV for methylidyne, 0.52 eV for methylene and 0.50 eV for methane, respectively. We found that the calculated activation energy of CO dissociation is higher than that of 2CO dissociation on the clean surface and base on these results that the CO dissociation step are the ratedetermining of the process. The C-H bond lengths of $CH_4$ the intermediate complex are 1.21 $\AA$, 1.31 $\AA$ for the C${\cdot}{\cdot}{\cdot}H_{(1)}$, and 2.82 $\AA$ for the height, with angles of 105${^{\circ}}$ for ∠ $H_{(1)}$CH and 98${^{\circ}}$ for $H_{(1)} CH _{(1)}$.

• 대한화학회지
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• 제32권5호
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• pp.501-506
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• 1988

본 연구에서는 알칼리화합물의 첨가가 Co/NaY촉매의 반응성과 선택도에 미치는 영향을 관찰하였다. 촉매는 제올라이트 NaY에 알칼리화합물을 첨가한 후 $Co_2(CO)_8$을 담지시켜 제조하였고, 온도 = 200∼$250^{\circ}C$, GHSV = 120∼$160hr^{-1}$, 압력 = 1atm, $H_2$/CO = 1 에서 반응하였다. 첨가된 알칼리이온의 염기도가 클수록 올레핀선택도, probability of chain growth(${\alpha}$), $CO_2$의 생성율은 증가하고 메탄의 생성율은 감소하였으며, 알칼리용액의 염기도가 클수록 반응활성은 증가하였다.

• 공업화학
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• 제28권3호
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• pp.326-331
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• 2017

캐스터오일은 수소화반응을 통해 계면활성제의 중간체 등 유용한 화학산업의 원료로 활용 가능하다. 본 연구에서는 캐스터오일의 수소화용 니켈촉매의 제조조건과 전처리 조건에 대한 영향을 연구하였다. 니켈촉매는 침전제와 pH를 다르게 하여 실리카 담체상에 침전법으로 담지되었고, 다시 산화와 환원의 반복된 전처리를 행하였다. 니켈촉매의 활성은 캐스터오일의 요오드 가를 측정하여 비교하였고, 니켈촉매의 분산도는 XRD, BET, TEM을 통하여 분석하였다. 니켈촉매의 활성을 CO산화반응실험을 통하여도 비교하였다. 산화와 환원 사이클의 반복에 의해 니켈의 재분산이 실리카 상에서 발생하였고, 이것이 캐스터오일 수소화반응 활성을 증진시키는데 기여하였다.

• Journal of Magnetics
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• 제8권3호
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• pp.124-127
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• 2003

HDDR (hydrogenation, disproportionation, desorption, recombination) and mechanical milling processes have been applied to the $SmCo_{5}$ alloy in an attempt to produce a highly coercive powder. The $SmCo_{5}$ alloy had very high structural stability under the hydrogen atmosphere and the 1:5 phase was only partially disproportionated under up to 10 kgf/$\textrm{cm}^2$ hydrogen gas. The partially disproportionated material was recombined not into 1:5 phase after the HDDR, but rather into multi-phase mixture consisting of 1:5, 2:17, 2:7 and 1:7 phases. The $SmCo_{5}$ alloy HDDR-treated with hydrogen up to 10 kgf/$\textrm{cm}^2$ had poor coercivity. For a useful HDDR to prepare a high coercivity $SmCo_{5}$ alloy powder, much higher hydrogen pressure well exceeding 10 kgf/$\textrm{cm}^2$ would be required. The $SmCo_{5}$ alloy lump was amorphized by an intensive mechanical milling, and it was crystallised ultra-finely by a subsequent optimum annealing. The optimally annealed material had very high coercivity, and it was found that the mechanical milling followed by an annealing was an effective way of producing highly coercive $SmCo_{5}$ alloy powder.

• Bulletin of the Korean Chemical Society
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• 제8권3호
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• pp.185-189
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• 1987

Reactions of $Ir(ClO)_4(CO)(PPh_3)_2$ with dicyano olefins, cis-NCCH = CH$CH_2$$CH_2$CN (cDC1B), trans-NCCH = CH$CH_2$$CH_2$CN (tDC1B), trans-NC$CH_2$CH = CH$CH_2$CN (tDC2B), and NC$CH_2$$CH_2$$CH_2$$CH_2$CN (DCB) produce binuclear dicationic iridium (I) complexes, $[(CO)(PPh_3)_2Ir-NC-A-CN-Ir(PPh_3)_2(CO)](ClO_4)_2$ (NC-A-CN = cDC1B (1a), tDC1B (1b), tDC2B (1c), DCB (1d)). Complexes 1a-1d react with hydrogen to give binuclear dicationic tetrahydrido iridium (Ⅲ ) complexes, $[(CO)(PPh_3)_2(H)_2Ir-NC-A-CN-Ir(H)_2(PPh_3)_2(CO)](ClO_4)_2$ (NC-A-CN = cDC1B (2a), tDC1B (2b), tDC2B (2c), DCB (2d)). Complexes 2a and 2b catalyze the hydrogenation of cDC1B and tDC1B, respectively to give DCB, while the complex 2c is catalytically active for the isomerization of tDC2B to give cDC1B and tDC1B and the hydrogenation of tDC2B to give DCB at $100^{\circ}C$.

• 한국세라믹학회지
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• 제36권5호
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• pp.504-512
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• 1999

The high-quality carbon nanofibers were prepared by chemical vapor deposition of gas mixtures of CO-H2 and C3H8-H2 over Fe-Cu and Ni-Cu bimetallic catalysts. The yield and structure of carbon nanofiber produced were altered by the change of catalyst composition and reaction temperature. The high yields were obtained around 500$^{\circ}C$ with e-Cu catalyst and around 700-750$^{\circ}C$ with Ni-Cu catalyst and the relatively higher yields were obtained with the bimetallic catalyst containing 50-90% of Ni and Fe respectively in comparison with the pure metals. The carbon nanofibers produced over the Fe-Cu catalyst at around 500$^{\circ}C$ with the maximum yields had the highest surface ares of 160-200 m2/g around 650$^{\circ}C$ which was slightly lower than the temperature for maximum yields. In order to examine the characteristics of carbon nanofibers as catalyst support Ni and Co metals were supporte on the carbon nanofibers and CO hydrogenation reaction was performed with the catalysts. The particle size distribution of Ni and Co supported over the carbon nanofibers were 6-15 nm and the CO hydrogenation reaction rate with the carbon-nanofiber supported catalysts was much higher than that over the other supports.

• 대한화학회지
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• 제40권6호
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• pp.445-452
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• 1996

Hydridonitrosyl complex의 촉매 활용 가능성과 반응 mechanism을 조사하기 위하여 $RuH(NO)(PPh_3)_3$와 RuH(NO)(etp)에 의한 ketone과 aldehyde의 수소화 반응을 연구하였다. 이 촉매들은 ketone과 aldehyde의 수소화 반응에 대하여 촉매 활성을 보이고 있으며, 활성은 기질의 입체장애 및 전자적 요인에 의존하고 있다. 즉, 입체 장애가 적을수록 촉매의 활성이 증가하며, 전자적 요인의 효과는 ketone의 경우 carbonyl carbon의 부분양전하의 양이 증가할수록, aldehyde의 경우는 carbonyl group의 double bond character가 강할수록 반응성이 증대되는 방향으로 나타나고 있다. 이러한 결과는 ketone과 aldehyde의 반응 mechanism이 다름을 반영하고 있다. 한편, RuH(NO)(etp)와 과잉의 $PPh_3$ 존재하에서 $RuH(NO)(PPh_3)_3$가 촉매 활성을 보이고 있음은 NO ligand의 결합방식의 변화를 통한 반응경로가 존재함을 확인하고 있다. 과잉의 $PPh_3$는 촉매와의 몰비가 변함에 따라 작용의 변화(ligand의 해리 방지 ${\rightarrow}$ 염기 ${\rightarrow}$ ligand)가 나타나며 촉매 활성에 영향을 미치고 있다. 이러한 결과를 이해하기 위하여 각 촉매에 대한 반응 mechanism을 제시하였다. 한편, 동일한 기질에 있어서 RuH(NO)(etp)의 활성은 항상 $RuH(NO)(PPh_3)_3$에 비하여 낮았으며 이는 주로 착물의 구조차이에 기인한 것으로 해석되며, 경쟁반응에 있어서는 olefin의 수소화 반응이 carbonyl group의 수소화 반응보다 선택적으로 진행되고 있다.