Calculations are done for a series of mathematical models for a mono-Phenomena studied include axial conduction in the wall, diffusion and conduction in the gas in a transverse direction perpendicular to the flow direction, multiple steady states, and transients giving wall temperatures exceeding the adiabatic temperature.lith catalytic converter to oxidize carbon monoxide in automobile exhaust.
SCOPEFor better or for worse, the use of catalytic converters to reduce automobile emissions of carbon monoxide and hydrocarbons has become a reality. Two types of catalytic converters are used for this application: packed beds and monoliths. The present study is concerned with mathematical models for the monolith converter. The simplest model which will give realistic predictions is determined, and the model calculations illustrate the important phenomena occurring in the device.Although conyiderable attention has been devoted to modeling packed-bed converters (Wei, 1975), little published information is available on modeling monolith Larry C. Young is with Amoco Production Company, Tulsa, Oklahoma.converters. Kuo (1973) developed a lumped parameter model for the monolith converter, which has been used by eight automobile and oil companies. Votruba et al. (1975) have also presented a similar model. Both these models include axial conduction in the wall. Hegedus (1974) neglects axial conduction. In a preliminary study, Young and Finlayson (1974) proposed and solved two models for the monolith, which cast some doubt on the validity of the simpler models. The essential question is whether or not to include diffusion and conduction in the fluid in a transverse direction perpendicular to the flow (and duct) axis, as did Young and Finlayson, or whether a simple lumped parameter model of this phenomenon, with specified Nusselt and Sherwood numbers,