Determination of adsorption and desorption parameters from ignition temperature measurements in catalytic combustion systems

被引:18
作者
Perger, T
Kovacs, T
Turányi, T
Treviño, C
机构
[1] Univ Nacl Autonoma Mexico, Fac Ciencias, Mexico City 04510, DF, Mexico
[2] Eotvos Lorand Univ, Dept Phys Chem, ELTE, H-1518 Budapest, Hungary
关键词
D O I
10.1021/jp0258208
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
When a cold catalyst is exposed to a fuel-oxygen mixture, the surface gets covered with the more effectively adsorbing species. When the temperature is increased, this species is desorbed and the ignition temperature is determined by the rate of desorption. Based on the equations for the heat balance, expressions were derived for the calculation of ignition temperature from the parameters of the experimental setup, the preexponential factor Ad and activation energy E-d of desorption, the ratio of sticking coefficients, and the ratio of adsorption orders of fuel and oxygen. Published experimental data for the catalytic ignition of CO, H-2, and CH4 were reinterpreted using the expressions obtained, and the following parameters were determined for polycrystalline platinum catalyst: E-d(H-2/Pt) = 43.3+/-5.2 kJ/mol, E-d(CO/Pt) = 107.2+/-12.7 kJ/mol, E-d(O-2/Pt) = 190 34 kJ/mol, S-H2,S-0/S-O2,S-0 = 36.7+/-9.6, S-CO,S-0/S-O2,S-0 = 41.2+/-8.5, S-O2,S-0/SCH4,0 = 5.9+/-0.3. Error limits refer to a confidence level of 0.95. The activation energy of desorption for CO and O-2 and the ratio of zero coverage sticking coefficients of O-2 and CH4 are the first experimentally based determinations of these parameters. Experimental ignition temperatures could be reproduced assuming second-order ' adsorption of CO, H-2, and O-2 on the Pt surface. These reaction orders have been debated in the literature.
引用
收藏
页码:2262 / 2274
页数:13
相关论文
共 81 条
[21]  
DEUTSCHMANN O, 1995, 15 INT C DYN EXPL RE
[22]  
Deutschmann O, 1995, 8 INT S TRANSP PHEN, P166
[23]   Two-dimensional modelling for catalytically stabilized combustion of a lean methane-air mixture with elementary homogeneous and heterogeneous chemical reactions [J].
Dogwiler, U ;
Benz, P ;
Mantzaras, J .
COMBUSTION AND FLAME, 1999, 116 (1-2) :243-258
[24]   An numerical simulation of effect of surface diffusion on hydrogen-oxygen reaction over platinum catalytic surface [J].
Enomoto, H ;
Kato, H ;
Tsue, M ;
Kono, M .
JSME INTERNATIONAL JOURNAL SERIES B-FLUIDS AND THERMAL ENGINEERING, 1999, 42 (01) :71-77
[25]   CHEMISORPTION OF CO ON PT(111) SURFACE [J].
ERTL, G ;
NEUMANN, M ;
STREIT, KM .
SURFACE SCIENCE, 1977, 64 (02) :393-410
[26]   A THEORETICAL AND EXPERIMENTAL-STUDY OF CATALYTIC IGNITION IN THE HYDROGEN OXYGEN REACTION ON PLATINUM [J].
FASSIHI, M ;
ZHDANOV, VP ;
RINNEMO, M ;
KECK, KE ;
KASEMO, B .
JOURNAL OF CATALYSIS, 1993, 141 (02) :438-452
[27]   The autothermal behavior of platinum catalyzed hydrogen oxidation: Experiments and modeling [J].
Fernandes, NE ;
Park, YK ;
Vlachos, DG .
COMBUSTION AND FLAME, 1999, 118 (1-2) :164-178
[28]   The influence of a catalytic surface on the gas-phase combustion of H2+O2 [J].
Försth, M ;
Gudmundson, F ;
Persson, JL ;
Rosén, A .
COMBUSTION AND FLAME, 1999, 119 (1-2) :144-153
[29]  
Frank-Kamenetskii D., 1969, Diffusion and heat transfer in chemical kinetics
[30]   OBSERVED KINETICS OF AN EXOTHERMIC REACTION ON A TEMPERATURE-CONTROLLED CATALYTIC WIRE [J].
GARSKE, ME ;
HAROLD, MP .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (03) :623-644