英文摘要 |
The effect of the non-uniform monolith cell resistance on the flow field and pressure drop in the catalytic converter were studied numerically. The monolith with non-uniform brick resistance resulting from either non-uniform cell length or non-uniform cell size was employed. Under steady state, axisymmetric, and incompressible flow assumptions employing the standard κ-ε turbulence model, the governing equations were discretized by the finite volume and QUICK difference schemes, while the SIMPLE algorithm was used on the non-staggered grid system. In general, flow mal-distribution and pressure loss inside the catalytic converter were improved since more flow would be guided to enter the outer region and the size of the sepration bubble around the diffuser wall would be reduced. Some related parameters including the Reynolds numbers, the protrusive thickness, the monolith position, and the cell density difference between the center and the wall were studied to optimize the design of the catalytic converter. |