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    • 1. 发明授权
    • Catalyst for purifying exhaust gas
    • 废气净化催化剂
    • US06335305B1
    • 2002-01-01
    • US09547347
    • 2000-04-11
    • Tadashi SuzukiAkira MorikawaHideo Sobukawa
    • Tadashi SuzukiAkira MorikawaHideo Sobukawa
    • B01J2300
    • B01D53/945B01J23/63B01J37/03Y02T10/22
    • A catalyst for purifying an exhaust gas includes a support and a noble metal loaded on the support. The support includes a mixture containing a porous oxide and a composite oxide. The composite oxide is expressed by the following formula: (Al2O3)a(CeO2)b(ZrO2)1−b in which the values “a” and “b” are molar ratios and the value “a” falls in a range of from 0.4 to 2.5 and the value “b” falls in a range of from 0.2 to 0.7. The support includes a particle having a particle diameter of 5 &mgr;m or more in an amount of 30% by volume or more. With the thus arranged support, even when the catalyst is subjected to such a severe durability test that it is heated at 1,000° C. for 10 to 20 hours, it exhibits a high purifying activity, and its coating layer is inhibited from cracking or coming off.
    • 用于净化废气的催化剂包括负载在载体上的载体和贵金属。 载体包括含有多孔氧化物和复合氧化物的混合物。 复合氧化物由下式表示:其中值“a”和“b”是摩尔比,值“a”在0.4至2.5的范围内,并且值“b”落在 从0.2到0.7。 该载体包含30体积%以上的粒径为5μm以上的粒子。 通过这样排列的支撑体,即使催化剂进行如此严格的耐久试验,即在1000℃下加热10〜20小时,显示出高的净化活性,并且其涂层被抑制开裂或开始 关闭
    • 2. 发明授权
    • Composite oxide, composite oxide carrier and catalyst
    • 复合氧化物,复合氧化物载体和催化剂
    • US06150288A
    • 2000-11-21
    • US946102
    • 1997-10-07
    • Tadashi SuzukiHideo Sobukawa
    • Tadashi SuzukiHideo Sobukawa
    • B01D53/94B01J23/10B01J37/02C04B35/48B01J23/54C04B35/50
    • B01D53/945B01D53/9413B01J23/10B01J37/0236B01D2255/1021B01D2255/1025B01D2255/2042B01D2255/2063B01D2255/2065B01D2255/2092B01D2255/908B01D2255/9202B01D2255/9207Y02T10/22
    • The composite oxide and the composite oxide carrier are manufactured by the precursor forming step and firing step. The precursor forming step includes high speed mixing means. The composite oxide catalyst is obtained by preparing a composite of catalytic components simultaneously with the formation of the precursor of composite oxide in the step of forming the precursor of composite oxide. The composite oxide and the composite oxide carrier are composed of a composite oxide in which at least one of cerium and zirconium, and aluminium disperse with extremely high homogeneity. With this structure, the heat resistance of the carrier is improved and consequently, enlargement of particles of the composite oxide defining the carrier, and sintering of adjacent particles of the composite oxide can be restrained, whereby the catalyst using the composite oxide carrier in accordance with the present invention is excellent in heat resistance. With the present invention, the carrier is not limited to a general catalyst carrier. The carrier may be interpreted to indicate general formed bodies. For example, the carrier with the present invention can be also used as materials for sensors and electrodes, optical materials, semiconductors and structure materials. Furthermore, the carrier can be used for a three-way catalyst, NOx catalyst or oxidation catalyst or a part thereof, and a promoter.
    • 复合氧化物和复合氧化物载体通过前体形成步骤和烧制步骤制造。 前体形成步骤包括高速混合装置。 复合氧化物催化剂通过在形成复合氧化物的前体的步骤中同时制备复合氧化物的前体同时制备复合材料而获得。 复合氧化物和复合氧化物载体由铈和锆中的至少一种和铝均匀分散的复合氧化物组成。 通过这种结构,能够提高载体的耐热性,可以抑制复合氧化物的粒子的扩大,能够抑制复合氧化物的相邻粒子的烧结,由此使用复合氧化物载体 本发明耐热性优异。 通过本发明,载体不限于一般的催化剂载体。 载体可以被解释为指示一般成形体。 例如,本发明的载体也可以用作传感器和电极,光学材料,半导体和结构材料的材料。 此外,载体可用于三元催化剂,NOx催化剂或氧化催化剂或其一部分和促进剂。
    • 9. 发明授权
    • Catalyst for purifying exhaust gases and process for producing the same
    • 净化废气的催化剂及其制造方法
    • US5945369A
    • 1999-08-31
    • US569396
    • 1995-12-08
    • Mareo KimuraYoriko MatsuokaHideo SobukawaMasayuki FukuiAkihiko SudaToshio KandoriYoshio Ukyo
    • Mareo KimuraYoriko MatsuokaHideo SobukawaMasayuki FukuiAkihiko SudaToshio KandoriYoshio Ukyo
    • B01D53/94B01J23/10B01J23/63B01J23/38
    • B01D53/945B01J23/10B01J23/63B01D2255/206B01D2255/20715B01D2255/40Y02T10/22
    • A catalyst for purifying exhaust gases includes a porous support; a cerium oxide or a solid solution of a cerium oxide and a zirconium oxide in a state of mutual solid solution, loaded on the porous support; and a noble metal element loaded on the porous support. The cerium oxide or the solid solution has an average particle diameter of from 5 to 100 nm. The cerium oxide is present in the solid solution in an amount of from 0.2 to 4.0 by molar ratio with respect to the zirconium oxide therein. The catalyst can be prepared by: coating and calcinating on a support substrate a slurry of a cerium oxide sol, a cerium oxide sol and a zirconium oxide sol, on a solid solution powder of a cerium oxide and a zirconium oxide in a state of mutual solid solution; and loading a noble metal element thereon. The cerium oxide or its solid solution has a surface area large enough to effect an oxygen storage function, and has an average particle diameter large enough to prevent the same from entering deeply into fine pores of a porous support, thereby providing a catalyst fully exhibiting both of the oxygen storage capability and the catalytic activity.
    • 用于净化废气的催化剂包括多孔载体; 以相互固溶态的氧化铈或氧化铈和氧化锆的固溶体装载在多孔载体上; 以及负载在多孔载体上的贵金属元素。 氧化铈或固溶体的平均粒径为5〜100nm。 相对于其中的氧化锆,氧化铈以相对于氧化锆的摩尔比为0.2〜4.0的量存在于固溶体中。 催化剂可以通过以下步骤制备:在氧化铈和氧化锆溶胶的固溶体粉末上以相互的状态将氧化铈溶胶,氧化铈溶胶和氧化锆溶胶的浆料在载体基材上涂覆和煅烧 固溶; 并在其上装载贵金属元素。 氧化铈或其固溶体具有足够大的表面积以实现储氧功能,并且具有足够大的平均粒径以防止其相当于深入多孔载体的细孔中,从而提供充分显示两者的催化剂 的储氧能力和催化活性。