Diesel oxidation catalysts for ultralow NO
The present disclosure is directed to a Low Temperature NOx-Absorber (LT-NA) catalyst composition which exhibits NOx adsorption in a broad temperature and space velocity range, and shifts NOx desorption to a desired temperature range. In particular, the LT-NA composition includes a large pore zeolite containing a palladium component and a small or medium pore zeolite containing a palladium component. Further provided is a catalyst article including the LT-NA catalyst composition, an emission treatment system for treating an exhaust gas including the catalyst article, and methods for reducing a NOx level in an exhaust gas stream using the catalyst article.
1. A catalyst article for treating an exhaust stream of an internal combustion engine comprising a catalyst substrate having an inlet end and an outlet end defining an overall length, and a first Low Temperature NO x Adsorber (LT-NA) catalyst composition disposed thereon, wherein the first LT-NA catalyst composition comprises:
a first zeolite, wherein the first zeolite is a large pore zeolite and comprises a first palladium component; and
a second zeolite, wherein the second zeolite is a small pore or medium pore zeolite and comprises a second palladium component,
wherein the catalyst article comprises a total zeolite loading of from about 1 to about 5 g/in 3 .
2. The catalyst article of claim 1 , wherein the first zeolite and the second zeolite are each an aluminosilicate zeolite.
3. The catalyst article of claim 1 , wherein the silica-to-alumina ratio (SAR) of the first zeolite is from about 10 to about 50 and the SAR of the second zeolite is from about 10 to about 50.
4. The catalyst article of claim 1 , wherein the first zeolite has a framework type selected from the group consisting of AFI, AFR, AFS, AFY, ASV, ATO, ATS, BEA, BEC, BOG, BPH, BSV, CAN, CON, CZP, DFO, EMT, EON, EZT, FAU, FZU, GME, GON, IFR, ISV, ITG, IWR, IWS, IWV, IWW, JSR, LTF, LTL, MAZ, MEI, MOR, MOZ, MSE, MTW, NPO, OFF, OKO, OSI, RON, RWY, SAF, SAO, SBE, SBS, SBT, SEW, SFE, SFO, SFS, SFV, SOF, SOS, STO, SSF, SSY, USI, UWY, VET, and mixtures or intergrowths thereof.
5. The catalyst article of claim 1 , wherein the second zeolite is a small pore zeolite with a framework type selected from the group consisting of ACO, AEI, AEN, AFN, AFT, AFX, APC, APD, ATT, CDO, CHA, DDR, DFT, EAB, EDI, EPI, ERI, GIS, GOO, IHW, ITE, ITW, LEV, KFI, MER, MFI, MON, NSI, OWE, PAU, PHI, RHO, RTH, SAT, SAV, SFW, SIV, THO, TSC, UEI, UFI, VNI, YUG, ZON, and mixtures or intergrowths thereof.
6. The catalyst article of claim 1 , wherein the second zeolite is a medium pore zeolite with a framework type selected from AEL, AFO, AHT, BOF, BOZ, CGF, CGS, CHI, DAC, EUO, FER, HEU, IMF, ITH, ITR, JRY, JSR, JST, LAU, LOV, MEL, MFI, MFS, MRE, MTT, MVY, MWW, NAB, NAT, NES, OBW, PAR, PCR, PON, PUN, RRO, RSN, SFF, SFG, STF, STI, STT, STW, SVR, SZR, TER, TON, TUN, UOS, VSV, WEI, WEN, and mixtures or intergrowths thereof.
7. The catalyst article of claim 1 , wherein the second zeolite has a two-dimensional pore system.
8. The catalyst article of claim 1 , further comprising a third zeolite comprising a third palladium component.
9. The catalyst article of claim 8 , wherein the third zeolite is a large pore zeolite, and wherein the first zeolite and the third zeolite have different framework types.
10. The catalyst article of claim 8 , wherein the third zeolite is a small pore or medium pore zeolite and wherein the second zeolite and the third zeolite have different framework types.
11. The catalyst article of claim 1 , wherein the first palladium component and the second palladium component are present in an amount of about 0.5% to about 6% by weight, based on the first zeolite and the second zeolite, respectively.
12. The catalyst article of claim 1 , wherein the ratio by weight of the first zeolite to the second zeolite is from about 0.1:9.9 to about 9:1.
13. The catalyst article of claim 1 , comprising:
a first washcoat comprising the first zeolite disposed on at least a portion of the length of the catalyst substrate; and
a second washcoat comprising the second zeolite disposed on at least a portion of the length of the catalyst substrate.
14. The catalyst article of claim 1 , wherein the catalyst article comprises the first and second palladium components at a loading from about 15 to about 200 g/ft 3 .
15. The catalyst article of claim 1 , further comprising a first diesel oxidation catalyst (DOC) composition.
16. The catalyst article of claim 15 , wherein the first LT-NA catalyst composition comprises a first layer and the first DOC composition comprises a second layer.
17. An exhaust gas treatment system comprising the catalytic article of claim 1 , wherein the catalytic article is downstream of and in fluid communication with an internal combustion engine.
18. A method for reducing a NO x level in an exhaust gas stream from an internal combustion engine, the method comprising contacting the exhaust gas stream with the catalyst article of claim 1 .