Simplified method of effectiveness factor calculations for irregular geometries of washcoats
暂无分享,去创建一个
[1] G. Rosen. The mathematical theory of diffusion and reaction in permeable catalysts , 1976 .
[2] S. Järås,et al. Numerical analysis of the transient performance of high-temperature monolith catalytic combustors: Effect of catalyst porosity , 1995 .
[3] S. Järås,et al. Catalytic combustion for gas turbine applications , 1999 .
[4] Eugene E. Petersen,et al. A general criterion for diffusion influenced chemical reactions in porous solids , 1965 .
[5] Jacob A. Moulijn,et al. Monoliths in Heterogeneous Catalysis , 1994 .
[6] Rutherford Aris,et al. On the effects of radiative heat transfer in monoliths , 1977 .
[7] W. E. Stewart,et al. Influence of coating geometry on the effectiveness of monolithic catalysts , 1986 .
[8] T. G. Smith. An examination of the isothermal pellet assumption relative to the design of nonadiabatic fixed bed catalytic reactors , 1977 .
[9] R. Aris,et al. On shape factors for irregular particles—II.: The transient problem. Heat transfer to a packed bed☆ , 1957 .
[10] O. Levenspiel. Chemical Reaction Engineering , 1972 .
[11] W. Murray. Numerical Methods for Unconstrained Optimization , 1975 .
[12] Bruce A. Finlayson,et al. Mathematical models of the monolith catalytic converter: Part II. Application to automobile exhaust , 1976 .
[13] Robert E. Hayes,et al. Diffusion limitation effects in the washcoat of a catalytic monolith reactor , 1996 .
[14] Robert E. Hayes,et al. MASS AND HEAT TRANSFER EFFECTS IN CATALYTIC MONOLITH REACTORS , 1994 .
[15] R. E. Hayes,et al. Introduction to Catalytic Combustion , 1998 .
[16] Rutherford Aris,et al. Communication. Normalization for the Thiele Modulus , 1965 .
[17] Kenneth B. Bischoff,et al. Effectiveness factors for general reaction rate forms , 1965 .