Gasoline car particle capturing catalyst and preparation method thereof
A particle capture and catalyst technology, which is applied in chemical instruments and methods, heterogeneous catalyst chemical elements, physical/chemical process catalysts, etc., can solve the problem of incomplete catalyst treatment, etc., to ensure the ability to resist high temperature aging and improve the ability , the preparation method is simple
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Embodiment 2
[0033] A particle trapping catalyst for gasoline vehicles, using a wall-flow honeycomb carrier with a specification of Ф118.4mm×119mm, a pore density of 300cpsi, a pore wall thickness of 12mil, a porosity of 65%, an average pore diameter of 20um, and a volume of 1.31L; One end of the first coating is coated with the first coating, the coating height of the first coating is 50% of the height of the carrier, the coating amount is 60g / L, and the loading amount of Rh in the first coating is 3g / ft 3 .
[0034] Coat the other end of the carrier with a second coating, the coating height in the second coating is 50% of the height of the carrier, the coating amount is 60g / L, and the loading amount of noble metal Pd in the second coating is 16g / ft 3 , the loading of precious metal Rh is 1g / ft 3 .
[0035] The preparation method is as follows:
[0036]Add 1500g of cerium-zirconium composite oxide and activated alumina to 6000g of deionized water in turn to prepare a suspension, wher...
Embodiment 3
[0040] A particle trapping catalyst for gasoline vehicles, using a wall-flow honeycomb carrier with a specification of Ф118.4mm×119mm, a pore density of 300cpsi, a pore wall thickness of 12mil, a porosity of 65%, an average pore diameter of 20um, and a volume of 1.31L; One end is first coated with the first coating, the coating height of the first coating is 100% of the height of the carrier, the coating amount is 60g / L, and the loading amount of precious metal Rh in the first coating is 3g / ft 3 .
[0041] Coat the other end of the carrier with a second coating, the coating height of the second coating is 100%, the coating amount is 60g / L, and the loading amount of noble metal Pd in the second coating is 16g / ft 3 , the loading of precious metal Rh is 1g / ft 3 .
[0042] The preparation method is as follows:
[0043] Add 1500g of cerium-zirconium composite oxide and activated alumina to 6000g of deionized water in turn to prepare a suspension, wherein the mass ratio of ceri...
Embodiment 4
[0047] A particle trapping catalyst for gasoline vehicles, using a wall-flow honeycomb carrier with a specification of Ф118.4mm×119mm, a pore density of 300cpsi, a pore wall thickness of 12mil, a porosity of 65%, an average pore diameter of 20um, and a volume of 1.31L; One end of the first coating is coated with the first coating, the coating height of the first coating is 100% of the height of the carrier, the coating amount is 80g / L, and the loading amount of the precious metal Rh in the first coating is 3.6g / ft 3 .
[0048] Coat the other end of the carrier with a second coating, the coating height of the second coating is 100% of the height of the carrier, the coating amount is 80g / L, and the loading amount of noble metal Pd in the second coating is 16g / ft 3 , the loading of precious metal Rh is 0.4g / ft 3 .
[0049] The preparation method is as follows:
[0050] Add 1500g of cerium-zirconium composite oxide and activated alumina to 6000g of deionized water in turn to ...
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