US2017096923A1PendingUtilityA1
PASSIVE NOx ADSORBER
Est. expiryOct 6, 2035(~9.2 yrs left)· nominal 20-yr term from priority
B01J 2229/186B01J 37/0246B01D 53/9472F01N 2510/063B01J 2229/42F01N 2570/14B01J 37/0244B01D 53/18B01D 2255/9032B01D 2255/10B01D 53/9468B01D 2258/012F01N 2570/16B01D 2255/908F01N 2370/04F01N 13/009B01D 53/9463B01D 2255/504B01J 37/0248B01J 29/743B01J 29/7415F01N 3/0814F01N 3/0842B01D 2255/2065B01D 2255/1021B01D 53/9481B01D 2255/2061B01D 2255/20707B01D 2255/2063B01D 53/9422B01D 2255/30B01D 2255/502B01D 2255/2066B01D 2255/9022B01D 53/944B01J 23/6562F01N 3/0222B01D 2255/91B01D 2255/1023B01D 2255/407B01J 29/783B01D 2255/50F01N 13/0093B01D 2255/20776F01N 3/0821B01J 35/04Y02T10/12Y02A50/20B01J 35/19
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Claims
Abstract
A NO x absorber catalyst for treating an exhaust gas from a diesel engine. The NO x absorber catalyst comprises a first NO x absorber material comprising a molecular sieve catalyst, wherein the molecular sieve catalyst comprises a noble metal and a molecular sieve, and wherein the molecular sieve contains the noble metal; a second NO x absorber material comprising palladium (Pd) supported on an oxide of cerium; and a substrate having an inlet end and an outlet end.
Claims
exact text as granted — not AI-modified1 . A NO x absorber catalyst for treating an exhaust gas from a diesel engine comprising:
a first NO x absorber material comprising a molecular sieve catalyst, wherein the molecular sieve catalyst comprises a noble metal and a molecular sieve, and wherein the molecular sieve contains the noble metal; a second NO x absorber material comprising palladium (Pd) supported on an oxide of cerium; and a substrate having an inlet end and an outlet end.
2 . A NO x absorber catalyst according to claim 1 , wherein the noble metal comprises palladium.
3 . A NO x absorber catalyst according to claim 1 , wherein the molecular sieve has an aluminosilicate framework, an aluminophosphate framework or a silico-aluminophosphate framework.
3 . A NO x absorber catalyst according to claim 1 , wherein the molecular sieve is selected from a small pore molecular sieve, a medium pore molecular sieve and a large pore molecular sieve.
4 . A NO x absorber catalyst according to claim 1 , wherein the molecular sieve is a small pore molecular sieve having a Framework Type selected from the group consisting of ACO, AEI, AEN, AFN, AFT, AFX, ANA, APC, APD, ATT, CDO, CHA, DDR, DFT, EAB, EDI, EPI, ERI, GIS, GOO, IHW, ITE, ITW, LEV, KFI, MER, MON, NSI, OWE, PAU, PHI, RHO, RTH, SAT, SAV, SIV, THO, TSC, UEI, UFI, VNI, YUG, ZON and a mixture or intergrowth of any two or more thereof.
5 . A NO x absorber catalyst according to claim 4 , wherein the small pore molecular sieve has a Framework Type that is AEI or CHA.
6 . A NO x absorber catalyst according to claim 1 , wherein the molecular sieve has an aluminosilicate framework and a silica to alumina molar ratio of 10 to 200.
7 . A NO x absorber catalyst according to claim 1 , wherein the oxide of cerium is ceria (CeO 2 ) or a mixed or composite oxide of ceria and a second oxide selected from alumina and zirconia.
8 . A NO x absorber catalyst according to claim 1 , wherein the oxide of cerium is doped with a dopant, wherein the dopant is an element selected from the group consisting of tungsten (W), silicon (Si), titanium (Ti), lanthanum (La), praseodymium (Pr), hafnium (Hf), yttrium (Y), ytterbium (Yb), samarium (Sm), neodymium (Nd) and a combination of two or more thereof, or an oxide thereof.
9 . A NO x absorber catalyst according to claim 1 , wherein the concentration of palladium (Pd) is ≦2% by weight of the concentration of the oxide of cerium.
10 . A NO x absorber catalyst according to claim 1 , which comprises a mixture of the first NO x absorber material and the second NO x absorber material.
11 . A NO x absorber catalyst according to claim 1 , wherein the NO x absorber catalyst comprises a first zone and a second zone, wherein the first zone comprises the first NO x absorber material, and the second zone comprises the second NO x absorber material.
12 . A NO x absorber catalyst according to claim 11 , wherein the first zone is disposed upstream of the second zone or the first zone is disposed downstream of the second zone.
13 . A NO x absorber catalyst according to claim 1 , which comprises a first region and a second region, wherein the first region comprises the first NO x absorber material, and the second region comprises the second NO x absorber material, and wherein either the first region overlaps the second region or the second region overlaps the first region.
14 . A NO x absorber catalyst according to claim 1 , which comprises a first layer and a second layer, wherein the first layer comprises the first NO x absorber material, and the second layer comprises the second NO x absorber material, and wherein either the first layer is disposed on the second layer or the second layer is disposed on the first layer.
15 . A NO x absorber catalyst according to any claim 1 further comprising a diesel oxidation catalyst (DOC) region.
16 . A NO x absorber catalyst according to claim 1 , wherein the substrate is a flow-through monolith or a filtering monolith.
17 . An exhaust system comprising a NO x absorber catalyst as defined in any one of claim 1 and an emissions control device.
18 . An exhaust system according to claim 17 , wherein the emissions control device is selected from the group consisting of emissions control device selected from the group consisting of a diesel particulate filter (DPF), a lean NO x trap (LNT), a lean NO x catalyst (LNC), a selective catalytic reduction (SCR) catalyst, a diesel oxidation catalyst (DOC), a catalysed soot filter (CSF), a selective catalytic reduction filter (SCRF™) catalyst, an ammonia slip catalyst (ASC) and combinations of two or more thereof.
19 . A vehicle comprising a lean burn engine and an exhaust system as defined in claim 17 .
20 . A vehicle according to claim 19 , wherein the lean burn engine is configured to run on diesel fuel comprising ≦50 ppm of sulfur.Join the waitlist — get patent alerts
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