Spatially resolved catalysis in microstructured reactors by IR spectroscopy: CO oxidation over mono- and bifunctional Pt catalysts

[1]  Y. Schuurman,et al.  Kinetics and Mechanism of the Water–Gas Shift Reaction Over Platinum Supported Catalysts , 2009 .

[2]  A. Andreasen,et al.  Degree of rate control: how much the energies of intermediates and transition states control rates. , 2009, Journal of the American Chemical Society.

[3]  Yves Schuurman,et al.  Aspects of kinetic modeling of fixed bed reactors , 2008 .

[4]  G. Germani,et al.  Preparation and characterization of porous alumina-based catalyst coatings in microchannels , 2007 .

[5]  A. C. van Veen,et al.  Wall coating optimization for microchannel reactors , 2007 .

[6]  N. Dupont,et al.  Specificities of micro-structured reactors for hydrogen production and purification , 2007 .

[7]  R. Hayes,et al.  On the use of mechanistic CO oxidation models with a platinum monolith catalyst , 2007 .

[8]  F. Vogel,et al.  Optically accessible channel reactor for the kinetic investigation of hydrocarbon reforming reactions , 2006 .

[9]  G. Germani,et al.  Water-gas shift reaction kinetics over μ-structured Pt/CeO2/Al2O3 catalysts , 2006 .

[10]  G. Germani,et al.  Platinum/ceria/alumina catalysts on microstructures for carbon monoxide conversion , 2005 .

[11]  D. Vlachos,et al.  A thermodynamically consistent surface reaction mechanism for CO oxidation on Pt , 2005 .

[12]  Hai Wang,et al.  Thermodynamic consistency in microkinetic development of surface reaction mechanisms , 2003 .

[13]  F. Duprat,et al.  Light-off curve of catalytic reaction and kinetics , 2002 .

[14]  M. Daturi,et al.  IR study of polycrystalline ceria properties in oxidised and reduced states , 1999 .

[15]  Gbmm Guy Marin,et al.  Development of a transient kinetic model for the CO oxidation by O2 over a Pt/Rh/CeO2/γ-Al2O3 three-way catalyst , 1998 .

[16]  X. Verykios,et al.  Specific Features Concerning the Mechanism of Methane Reforming by Carbon Dioxide over Ni/La2O3Catalyst , 1997 .

[17]  J. Hoebink,et al.  Kinetic study of the CO oxidation over Pt/γ-Al2O3 and Pt/Rh/CeO2/γ-Al2O3 in the presence of H2O and CO2 , 1997 .

[18]  Dale F. Rudd,et al.  The Microkinetics of heterogeneous catalysis , 1993 .

[19]  M. Harold,et al.  Kinetics and multiple rate states of CO oxidation on Pt I. Model development and multiplicity analysis , 1991 .

[20]  Luis F. Razon,et al.  Intrinsically Unstable Behavior during the Oxidation of Carbon Monoxide on Platinum , 1986 .

[21]  H. C. Yao,et al.  Ceria in automotive exhaust catalysts: I. Oxygen storage , 1984 .

[22]  Gwan Kim.  Ceria-promoted three-way catalysts for auto exhaust emission control , 1982 .

[23]  Volker Hessel,et al.  System, process and plant engineering , 2009 .

[24]  Ray W. Chrisman,et al.  Comprar Micro Instrumentation: for High Throughput Experimentation and Process Intensification | Melvin V. Koch | 9783527314256 | Wiley , 2007 .

[25]  Y. Schuurman,et al.  Hydrogen production from non-stationary catalytic cracking of methane: a mechanistic study using in operando infrared spectroscopy , 2004 .

[26]  F. Dautzenberg,et al.  Process intensification using multifunctional reactors , 2001 .

[27]  C. Depecker.  La réflexion diffuse associée à la spectrométrie IRTF : une nouvelle étape dans l'analyse "in situ" des composés solides , 1988 .