CAJ | 학술논문

This work tries to identify the relationship between geometric configuration of monolith catalysts, and transfer and reaction performances for selective catalytic reduction of N2O with CO. Monolith catalysts with five different channel shapes (circle, regular triangle, rectangle, square and hexagon), was investigated to make a com-prehensive comparison of their pressure drop, heat transfer Nu number, mass transfer Sh number and N2O conver-sion. It was found that monolith catalysts have a much lower pressure drop than that of traditional packed bed, and for monolith catalysts with different channel shapes, pressure drop decreases in the order of regular triangle>rec-tangle>square>hexagon>circle. The order of Nu is in regular triangle>rectangle≈square>hexagon>circle, similar to that of Sh. N2O conversion follows the order of regular triangle>rectangular≈square≈circle>hexagon. The results indicate that chemical reaction including internal diffusion is the controlling step in the selective cata-lytic reduction of N2O removal with CO. In addition, channel size and gas velocity also have influence on N2O conversion and pressure drop.