NOx ADSORBER CATALYST
一种吸附剂、催化剂的技术,应用在稀燃发动机的排放系统领域,能够解决催化剂储存功能不足等问题
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Embodiment 1
[0178] Preparation [Al 2 o 3 .Nd(13.0wt%)].Pt.Pd.[Ce.Ba(7%)](10.2mol%Al 2 o 3 .Nd; 8.7mol% Ce.Ba)
[0179] Formation of CeO from barium acetate and high surface area ceria 2 -BaCO 3 The composite was then calcined at 650°C for 1 hour.
[0180] 1.77g / in 3 [Al 2 o 3 .Nd] (prepared according to general preparation (2) above) was slurried with distilled water and ground to a d of 13-15 μm 90 . Then add 94g / ft to the slurry 3 Pt malonate and 19g / ft 3 Pd nitrate solution, and stirred until homogeneous. Make Pt / Pd in [Al 2 o 3 .Nd] on the carrier for 1 hour.
[0181] Then add 3.33g / in to it 3 CeO 2 -BaCO 3 Composite material, then 0.2g / in 3 alumina binder and stir until homogeneous to form a washcoat.
[0182] The washcoat was then applied to the ceramic or metal monolith using standard coating procedures, dried at 100°C and calcined at 500°C for 45 minutes.
[0183] Ba is present at about 4.3 wt% (4.6 mol%). Nd is present at about 0.43 wt% (4.3 mol%).
Embodiment 2
[0185] Preparation [Al 2 o 3 .Nd(0%)].Pt.Pd.[Ce.Ba(7wt%)]
[0186] Prepared as in Example 1, but using Al 2 o 3 Alternative [Al 2 o 3 .Nd].
[0187] Experimental results
[0188] by 10% H 2 O, 20% O 2 and margin N 2 In the composed gas stream, the catalysts of Example 1 and Example 2 were hydrothermally aged at 800° C. for 5 h. They were performance tested in a simulated MVEG-B emissions cycle using a 1.6-liter benchtop diesel engine. Emissions were measured before and after the catalyst. Cumulative NO x Pollutant emissions are shown in figure 1 middle. Engine output (before catalyst) NO x Emissions and NO after catalyst x Difference between emissions indicates NO removal over catalyst x amount. From figure 1 It can be seen that Example 1, which contains the neodymium-containing component, has a greater adsorption of NO than Example 2, which does not contain the neodymium-containing component. x capacity.
Embodiment 3
[0190]Preparation of Al 2 o 3 PtPd[Ce.Ba(7wt%)]
[0191] Formation of CeO from barium acetate and high surface area ceria 2 -BaCO 3 The composite was then calcined at 650°C for 1 hour.
[0192] 1.5g / in 3 Al 2 o 3 Make a slurry with distilled water and grind to a d of 13-15 μm 90 . Then add 94g / ft to the slurry 3 Pt malonate and 19g / ft 3 Pd nitrate solution, and stirred until homogeneous. Make Pt / Pd in Al 2 o 3 Adsorbed on the carrier for 1 hour.
[0193] Then add 3.27g / in CeO to it 2 -BaCO 3 Composite material, then 0.2g / in 3 alumina binder and stir until homogeneous to form a washcoat.
[0194] The washcoat was then coated onto ceramic or metal monoliths using standard procedures, dried at 100°C and calcined at 500°C for 45 minutes.
[0195] Ce is present at a loading of about 59.6 wt% (48.7 mol%). Ba is present at a loading of about 4.6 wt% (4.7 mol%).
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