Catalyst for gasoline lean burn engines with improved no oxidation activity
A catalyst and catalyst coating technology, which is applied in combustion engines, internal combustion piston engines, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of poor coordination between oxidation activity and NO oxidation activity, strong loss of catalytic activity, etc. problem, to achieve the effect of improving NO oxidation activity
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Embodiment 1
[0092] (inner layer)
[0093] Platinum in the form of a platinum tetramethylammonium hydroxide complex solution and subsequently palladium in the form of a palladium nitrate solution was impregnated with a high surface area doped with 0.4% lanthanum oxide and 15% zirconia by means of a planetary mixer (P-mixer). Gamma alumina to form a wet powder while achieving incipient wetness. The amount of Pt and Pd is chosen to achieve 10 g / ft in the catalyst layer 3 Pt and 2g / ft 3 Final concentration of Pd.
[0094] Then by adding Pt and Pd supported high surface area gamma alumina, ceria, zirconia, baria, magnesia and binder at about 33%, 44%, 3%, 11.5%, respectively based on the calcined weight of the catalyst. Concentrations of 7% and 1% combine to form an aqueous slurry with water. Zirconia was introduced as an acetate colloidal solution and barium oxide as a barium acetate solution. The resulting slurry was then ground to a 90% particle size of less than 10 μm.
[0095] The s...
Embodiment 2
[0105] (inner layer)
[0106] Platinum in the form of a platinum tetramethylammonium hydroxide complex solution and subsequently palladium in the form of a palladium nitrate solution was impregnated with a high surface area doped with 0.4% lanthanum oxide and 15% zirconia by means of a planetary mixer (P-mixer). Gamma alumina to form a wet powder while achieving incipient wetness. The amount of Pt and Pd is chosen to achieve 10 g / ft in the catalyst layer 3 Pt and 2g / ft 3 Final concentration of Pd.
[0107] Then by adding Pt and Pd supported high surface area gamma alumina, ceria, zirconia, baria, magnesia and binder at about 54%, 30%, 3%, 7%, respectively based on the calcined weight of the catalyst. Concentrations of 7% and 1% combine to form an aqueous slurry with water. Zirconia was introduced as an acetate colloidal solution and barium oxide as a barium acetate solution. The resulting slurry was then ground to a 90% particle size of less than 10 μm.
[0108] The slur...
Embodiment 3
[0118] The catalyst of Example 3 was prepared according to the procedure of Example 2, wherein to prepare the inner layer, high surface area gamma alumina doped with 0.4% lanthanum oxide and 15% zirconium oxide was loaded with Pt and Pd to achieve 13 g / m in the inner layer of the catalyst. ft 3 Pt and 3g / ft 3 Final concentration of Pd. The components present in the inner layer are Pt and Pd supported high surface area gamma alumina, ceria, Zirconia, barium oxide, magnesium oxide and binders. The total load of the inner layer is 2g / in3 .
[0119] To prepare the interlayer, high surface area gamma alumina doped with 0.4% lanthanum oxide and 15% zirconia was loaded with Pt and Pd to achieve 31 g / ft in the catalyst interlayer 3 Pt and 5g / ft 3 Final concentration of Pd. The components present in the interlayer are Pt and Pd supported high surface area gamma alumina, ceria, Zirconia, barium oxide, magnesium oxide and binders. The total load of the middle layer is 2.2g / in 3 ...
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