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    • 46. 发明申请
    • Honeycomb structure
    • 蜂窝结构
    • US20060292333A1
    • 2006-12-28
    • US11320974
    • 2005-12-30
    • Kazushige OhnoMasafumi KuniedaKazutake Ogyu
    • Kazushige OhnoMasafumi KuniedaKazutake Ogyu
    • B32B3/12
    • F01N3/2828B01D39/2086B01D39/2089F01N2450/28Y10T428/24149
    • A honeycomb structure having multiple honeycomb units united through a seal material layer, wherein each honeycomb unit has multiple through holes arranged side by side in a longitudinal direction and separated from each other by the wall surfaces of the through holes, is disclosed. The honeycomb units include at least: ceramic particles; and at least one of inorganic fibers and whiskers. At least one of the honeycomb units has a cross section perpendicular to a longitudinal direction thereof, the cross section having an area greater than or equal to about 5 cm2 and less than or equal to about 50 cm2. Each corner of each honeycomb unit has a shape of one of a substantially rounded surface and a substantially chamfered surface.
    • 公开了一种蜂窝结构体,其具有通过密封材料层结合的多个蜂窝单元,其中,每个蜂窝单元具有沿纵向并排布置并且通过通孔的壁表面彼此分离的多个通孔。 蜂窝单元至少包括:陶瓷颗粒; 和无机纤维​​和晶须中的至少一种。 蜂窝单元中的至少一个具有垂直于其纵向方向的横截面,横截面具有大于或等于约5cm 2且小于或等于约50cm 3的区域, SUP> 2 。 每个蜂窝单元的每个角都具有基本圆形的表面和基本上倒角的表面之一的形状。
    • 49. 发明授权
    • Exhaust gas conversion system and exhaust gas conversion method
    • 废气转化系统和废气转化方法
    • US08394347B2
    • 2013-03-12
    • US13314102
    • 2011-12-07
    • Masafumi KuniedaShigeaki Goto
    • Masafumi KuniedaShigeaki Goto
    • B01D53/92B01D53/94F01N3/10F01N3/24F01N3/035
    • F01N3/2066F01N3/0222F01N3/035F01N3/2828F01N13/009F01N2340/00F01N2370/04F01N2450/02F01N2450/28F01N2610/02Y02T10/24
    • An exhaust gas conversion system includes an oxide catalyst, a filter, a selective catalytic reduction catalyst and an ammonia supplying device. The filter has a honeycomb structural body including a honeycomb unit. The selective catalytic reduction catalyst has a honeycomb structural body including a honeycomb unit. The oxide catalyst, the filter and the selective catalytic reduction catalyst are sequentially arranged in a direction in which an exhaust gas flows. A ratio of an area of a cross section of the selective catalytic reduction catalyst perpendicular to a longitudinal direction of the selective catalytic reduction catalyst with respect to an area of a cross section of the filter perpendicular to a longitudinal direction of the filter is approximately 0.55 or more and approximately 0.90 or less. The area of the cross section of the filter is approximately 300 cm2 or more and approximately 1000 cm2 or less.
    • 废气转化系统包括氧化物催化剂,过滤器,选择性催化还原催化剂和氨供应装置。 过滤器具有包括蜂窝单元的蜂窝结构体。 选择性催化还原催化剂具有包括蜂窝单元的蜂窝结构体。 氧化物催化剂,过滤器和选择性催化还原催化剂依次排列在废气流动的方向上。 垂直于选择性催化还原催化剂的纵向方向的选择性催化还原催化剂的横截面面积相对于过滤器垂直于过滤器的纵向方向的横截面的面积的比率为约0.55或 大约0.90或更小。 过滤器的横截面的面积为约300cm 2以上且约1000cm 2以下。