Improved diesel oxidation catalytic converter
A technology of catalyst and catalytic activity, which is applied in the field of oxidation catalyst and exhaust gas purification of heavy-duty trucks. It can solve the problem that the catalyst does not show NO-oxidation activity, and achieve the effect of improving heating-performance
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Embodiment 1
[0063] A catalyst according to the invention was prepared whose total noble metal content and platinum-palladium ratio corresponded to the conventional diesel oxidation catalyst of Comparative Example 1.
[0064] To this end, a first coating is first applied to the ceramic honeycomb body, which has the following composition, based on the volume of the catalyst produced:
[0065] 40g / L silicon-aluminum-mixed oxide containing up to 20% by weight SiO 2
[0066] 0.204g / L precursor platinum nitrate solution
[0067] 0.204g / L precursor palladium nitrate solution
[0068] 15 g / L commercially available beta-zeolite
[0069] The coating represents a coating that does not come into direct contact with the exhaust gases after the catalyst has been produced.
[0070] After drying and calcination of the first layer, a second layer was applied thereon, having the following composition based on the volume of the catalyst produced:
[0071] 40g / L silicon-aluminum-mixed oxide containing u...
Embodiment 2
[0096] Corresponding to the procedure described in Example 1, the catalyst K2 according to the invention was prepared with two superimposed layers of the following composition:
[0097] 1st layer = lower layer = coating not in direct contact with exhaust gases:
[0098] 92g / L silicon-aluminum-mixed oxide containing up to 20% by weight SiO 2
[0099] 0.302g / L precursor platinum nitrate solution
[0100]0.302g / L precursor palladium nitrate solution
[0101] Layer 2 = upper layer = coating in direct contact with exhaust gases:
[0102] 45g / L silicon-aluminum-mixed oxide containing up to 20% by weight SiO 2
[0103] 0.706g / L precursor platinum nitrate solution
[0104] 0.101g / L precursor palladium nitrate solution
Embodiment 3
[0106] Corresponding to the procedure described in Example 1, the catalyst K2 according to the invention was prepared with two superimposed layers of the following composition:
[0107] 1st layer = lower layer = coating not in direct contact with exhaust gases:
[0108] 40g / L silicon-aluminum-mixed oxide containing up to 20% by weight SiO 2
[0109] 0.303g / L precursor platinum nitrate solution
[0110] 0.303g / L precursor palladium nitrate solution
[0111] 15 g / L commercially available beta-zeolite
[0112] Layer 2 = upper layer = coating in direct contact with exhaust gases:
[0113] 45g / L silicon-aluminum-mixed oxide containing up to 20% by weight SiO 2
[0114] 0.706g / L precursor platinum nitrate solution
[0115] 0.101g / L precursor palladium nitrate solution
[0116] Figure 6 shows that the addition of zeolite to the coating not in direct contact with the exhaust gas has an effect on the NO of the catalyst 2 - Yield was not significantly affected.
[0117] Howe...
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