Abstract:
There is disclosed a plugged honeycomb structure which can inhibit a temperature rise during use at high temperatures and is excellent in thermal shock resistance. A plugged honeycomb structure 100 includes a pillar-shaped honeycomb structure body 4 having porous partition walls 1 defining a plurality of cells 2 which become through channels for a fluid and extend from a first end face 11 to a second end face 12, and plugging portions 5 disposed in open ends of predetermined cells 2b in the first end face 11 and open ends of residual cells 2a in the second end face 12, and the partition walls 1 are constituted of a porous body including ±-Al 2 O 3 as a main phase and further including cordierite and Y 2 Si 2 O 7 .
Abstract:
A ceramic honeycomb structure having pluralities of flow paths partitioned by porous cell walls, (a) the cell walls having porosity of 50-63%; and (b) in a pore diameter distribution in the cell walls measured by mercury porosimetry, (i) a pore diameter at a cumulative pore volume corresponding to 2% of the total pore volume being more than 180 µm and 250 µm or less, a pore diameter at 5% being 55-150 µm, a pore diameter d10 at 10% being 17-40 µm, a pore diameter d50 at 50% being 10-20 µm, a pore diameter at 85% being 5.5-10 µm, a pore diameter d90 at 90% being 3.5-9 µm, a pore diameter d98 at 98% being 2.5 µm or less, (d10 - d90)/d50 being 1.3-2, (d50 - d90)/d50 being 0.45-0.75, and (d10 - d50)/d50 being 0.75-1.4; (ii) the difference between a logarithm of the pore diameter at a cumulative pore volume corresponding to 20% of the total pore volume and a logarithm of the pore diameter at 80% being 0.39 or less; and (iii) the volume of pores of more than 100 µm being 0.03 cm 3 /g or less.
Abstract:
A ceramic honeycomb structure having pluralities of flow paths partitioned by porous cell walls; (a) the cell walls having porosity of 50-60%; and (b) in a pore diameter distribution in the cell walls measured by mercury porosimetry, (i) a pore diameter d5 at a cumulative pore volume corresponding to 5% of the total pore volume being 22 µm or more and less than 55 µm, a pore diameter d10 at 10% being 15-35 µm, a pore diameter d50 at 50% being 10-20 µm, a pore diameter at 85% being 5-9 µm, a pore diameter d90 at 90% being 3-8 µm, a pore diameter d98 at 98% being 2.5 µm or less, (d10 - d90)/d50 being 1.3-1.8, (d50 - d90)/d50 being 0.45-0.75, and (d10 - d50)/d50 being 0.75-1.1; and (ii) the difference between a logarithm of the pore diameter at a cumulative pore volume corresponding to 20% of the total pore volume and a logarithm of the pore diameter at 80% being 0.39 or less, and its production method.
Abstract:
Provided is a honeycomb structure having low heat capacity and high thermal diffusivity, and that follows the ambient temperature change rapidly. A honeycomb structure 100 includes a pillar-shaped honeycomb structure body 4 having a porous partition wall 1. The honeycomb structure body 4 includes a plurality of cells 2 defined by the partition wall 1 so as to extend from a first end face 11 to a second end face 12 of the honeycomb structure body 4, the partition wall 1 is formed by a porous body including a silicon phase as a main phase and an oxide, and the oxide includes a first oxide made of an alkali earth metal oxide, Al 2 O 3 , and SiO 2 .
Abstract translation:本发明提供一种热容量低且热扩散性高,且随着周围温度的变化而迅速变化的蜂窝结构体。 蜂窝结构体100具备具有多孔质的隔壁1的柱状的蜂窝结构体4.蜂窝结构体4具有由隔壁1划分出的多个单元2,该多个单元2从第一端面11延伸至第二端面 蜂窝结构体4的端面12上,隔壁1由以硅相为主相的多孔体和氧化物构成,氧化物包括由碱土类金属氧化物构成的第一氧化物,Al 2 O 3, 二氧化硅。
Abstract:
There is disclosed a honeycomb structure which is suitably used as a catalyst carrier for purification of an exhaust gas. In porous partition walls of the honeycomb structure, there are formed large pores which show one distribution a in a graph illustrating a pore diameter distribution and in which a pore diameter PP1 at a maximum peak value v1 of pore volumes of the one distribution a is 12 µm or more, and small pores which show the other distribution b in the graph illustrating the pore diameter distribution and in which a pore diameter PP2 at a maximum peak value v2 of pore volumes of the other distribution b is smaller than the pore diameter PP1, the pore diameter PP1 and the pore diameter PP2 satisfy a relation of 0.91 ≤ (PP1-PP2)/PP1 ≤ 0.98, and a ratio of the pore volume of the pores having pore diameters smaller than the pore diameter PP2 to a total pore volume of the partition walls is 0.5% or more and 7% or less.
Abstract:
There is provided a honeycomb structure including: a honeycomb substrate having porous partition walls separating and forming a plurality of cells functioning as fluid passages and plugging portions disposed in openings of predetermined cells on one end face and openings of the remaining cells on the other end face, wherein the partition walls contain ceramic as a main component, the number of cells having at least one pore passing from one surface to the other surface of a partition wall and having a minimum pore size of 100 µm or more is 100 or less, and the partition walls have a permeability of 0.5×10 -12 m 2 or more and 10×10 -12 m 2 or less.
Abstract translation:本发明提供一种蜂窝结构体,该蜂窝结构体具有多孔质隔壁,该多孔质隔壁分离形成有作为流体通路发挥功能的多个单元,在一个端面上的规定的单元的开口部以及另一个端面上的剩余的单元的开口部中形成封孔部 其中,所述隔壁含有陶瓷作为主要成分,具有至少一个从分隔壁的一个表面到另一个表面穿过并且最小孔径为100μm以上的孔的孔的个数为100个以下,并且, 隔壁具有0.5×10 -12 m 2以上且10×10 -12 m 2以下的磁导率。
Abstract:
An exhaust gas purification filter includes an inflow/outflow passage through which exhaust gas flows in/out, and a partition. The outflow passage and the inflow passage is alternately arranged. The partition is configured to divide the inflow passage and the outflow passage from each other, and being porous. The partition includes a coated zone where a surface of a base of the partition is covered with a first coating layer having an average pore diameter smaller than an average pore diameter of the base, and a non-coated zone where the surface of the base is not covered with the first coating layer on a downstream side of the coated zone. The average pore diameter of the base is large enough for ash to pass through the partition, and the first coating layer is constituted by a plurality of particle groups with different average particle diameters from each other.