Hydrogenation of carbon dioxide catalyzed by ruthenium trimethylphosphine complexes - Effect of gas pressure and additives on rate in the liquid phase

被引:64
作者
Thomas, CA [1 ]
Bonilla, RJ [1 ]
Huang, Y [1 ]
Jessop, PG [1 ]
机构
[1] Univ Calif Davis, Dept Chem, Davis, CA 95616 USA
来源
CANADIAN JOURNAL OF CHEMISTRY-REVUE CANADIENNE DE CHIMIE | 2001年 / 79卷 / 5-6期
关键词
carbon dioxide; homogeneous catalysis; hydrogenation; formic acid; expanded liquids;
D O I
10.1139/v00-200
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Kinetic and mechanistic studies of CO(2) hydrogenation were performed in liquid triethylamine and at subcritical CO(2) pressures to avoid complications from phase behaviour that are observed under supercritical conditions. Kinetic measurements of the hydrogenation of CO(2) to formic acid, catalyzed by RuCl(O(2)CMe)(PMe(3))(4), support a CO(2) insertion mechanism. The reaction is first-order in both H(2) and CO(2) under most conditions. The rate is strongly dependent on the choice of additive, with methanol giving the greatest rates. Because only trace amounts of methanol are needed, the effect of the additive is believed to involve direct interactions with the catalyst rather than changes in the physical properties of the reaction medium. The optimized rates exceed 3500 h(-1). Addition of an inert gas affects the rate of the reaction, probably via the phenomenon of gas expansion of the liquid phase.
引用
收藏
页码:719 / 724
页数:6
相关论文
共 32 条
[1]   Complexes [(P-2)Rh(hfacac)] as model compounds for the fragment [(P-2)Rh] and as highly active catalysts for CO2 hydrogenation: The accessible molecular surface (AMS) model as an approach to quantifying the intrinsic steric properties of chelating ligands in homogeneous catalysis [J].
Angermund, K ;
Baumann, W ;
Dinjus, E ;
Fornika, R ;
Gorls, H ;
Kessler, M ;
Kruger, C ;
Leitner, W ;
Lutz, F .
CHEMISTRY-A EUROPEAN JOURNAL, 1997, 3 (05) :755-764
[2]  
[Anonymous], COMPREHENSIVE ORGANO
[3]  
BURGEMEISTER T, 1993, ANGEW CHEM INT EDIT, V32, P739, DOI 10.1002/anie.199307391
[4]   A kinetic approach for predicting diffusivities in dense fluid mixtures [J].
Dariva, C ;
Coelho, LAF ;
Oliveira, JV .
FLUID PHASE EQUILIBRIA, 1999, 158 :1045-1054
[5]   COMPLEXES [(P-2)RH(HFACAC)] (P-2=BIDENTATE CHELATING PHOSPHANE, HFACAC=HEXAFLUOROACETYLACETONATE) AS CATALYSTS FOR CO2 HYDROGENATION - CORRELATIONS BETWEEN SOLID-STATE STRUCTURES, RH-103 NMR SHIFTS AND CATALYTIC ACTIVITIES [J].
FORNIKA, R ;
GORLS, H ;
SEEMANN, B ;
LEITNER, W .
JOURNAL OF THE CHEMICAL SOCIETY-CHEMICAL COMMUNICATIONS, 1995, (14) :1479-1481
[6]   EQUILIBRIUM PHASE PROPERTIES OF THE HYDROGEN METHANE CARBON-DIOXIDE, HYDROGEN CARBON-DIOXIDE N-PENTANE AND HYDROGEN N-PENTANE SYSTEMS [J].
FREITAG, NP ;
ROBINSON, DB .
FLUID PHASE EQUILIBRIA, 1986, 31 (02) :183-201
[7]   CO2-ACTIVATION .3. HYDROGENATION OF CARBON-DIOXIDE TO FORMIC-ACID USING WATER-SOLUBLE RHODIUM CATALYSTS [J].
GASSNER, F ;
LEITNER, W .
JOURNAL OF THE CHEMICAL SOCIETY-CHEMICAL COMMUNICATIONS, 1993, (19) :1465-1466
[8]   CO2 activation .7. Formation of the catalytically active intermediate in the hydrogenation of carbon dioxide to formic acid using the [{(COD)Rh(mu-H)}(4)]/Ph(2)P(CH2)(4)PPh(2) catalyst: First direct observation of hydride migration from rhodium to coordinated 1,5-cyclooctadiene [J].
Gassner, F ;
Dinjus, E ;
Gorls, H ;
Leitner, W .
ORGANOMETALLICS, 1996, 15 (08) :2078-2082
[9]   DIRECT FORMATION OF FORMIC-ACID FROM CARBON-DIOXIDE AND DIHYDROGEN USING THE [(RH(COD)CL)2]-PH2P(CH2)4PPH2 CATALYST SYSTEM [J].
GRAF, E ;
LEITNER, W .
JOURNAL OF THE CHEMICAL SOCIETY-CHEMICAL COMMUNICATIONS, 1992, (08) :623-624
[10]  
Halmann M., 1993, CHEM FIXATION CARBON, P172