| 摘要 |
A honeycomb catalyst body includes a plugged honeycomb structure having porous partition walls, inflow side plugged portions, outflow side plugged portions, and porous projecting portions which project so as to extend from the partition walls into the cells and are formed integrally with the partition walls; and catalyst loaded onto the projecting portions of the plugged honeycomb structure. A porosity of the partition walls of the plugged honeycomb structure is 40 to 70%, a thickness of the projecting portions is from 30 to 140% of a thickness of the partition walls, and an amount of a catalyst loaded onto pore surfaces of the partition walls of the plugged honeycomb structure is smaller than an amount of the catalyst loaded onto the projecting portions. The catalyst loaded onto projecting portions is a three-way catalyst, and the catalyst loaded onto projecting portions is a selective reduction catalyst. |
| 主权项 |
1. A honeycomb catalyst body comprising:
a plugged honeycomb structure having porous partition walls which define and form a plurality of cells extending from an inflow side end surface to an outflow side end surface to become through channels of a fluid, inflow side plugged portions provided at outflow side ends of the predetermined cells, outflow side plugged portions provided at outflow side ends of the remaining cells, and porous projecting portions which project so as to extend from the partition walls into inflow cells, that are defined as the cells provided with the outflow side plugged portions, and into outflow cells, that are defined as the cells provided with the inflow side plugged portions, and which are formed integrally with the partition walls; and a catalyst loaded onto the projecting portions of the plugged honeycomb structure, wherein a porosity of the partition walls of the plugged honeycomb structure is from 40 to 70%, a thickness of the projecting portions is from 30 to 140% of a thickness of the partition walls, an amount of a catalyst loaded onto the partition walls in a cross section vertical to an extending direction of the cells is 40% or less of a total amount of the catalyst loaded onto the plugged honeycomb structure, and the amount of the catalyst loaded onto the partition walls is smaller than an amount of the catalyst loaded onto the projecting portions, and the catalyst loaded onto the projecting portions extending into the inflow cells of the plugged honeycomb structure is a three-way catalyst or an NOx adsorber catalyst, and the catalyst loaded onto the projecting portions extending into the outflow cells of the plugged honeycomb structure is a selective reduction catalyst, or the catalyst loaded onto the projecting portions extending into the inflow cells of the plugged honeycomb structure is a three-way catalyst, and the catalyst loaded onto the projecting portions extending into the outflow cells of the plugged honeycomb structure is an NOx adsorber catalyst.
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