Oxidation catalyst for treating a natural gas emission
A catalytic material for treating an exhaust gas produced by a natural gas engine, which catalytic material comprises a molecular sieve and a platinum group metal (PGM) supported on the molecular sieve, wherein the molecular sieve has a framework comprising silicon, oxygen and optionally germanium, and has a content of heteroatom T-atoms is ≤about 0.20 mol %.
1. An oxidation catalyst for treating an exhaust gas produced by a natural gas (NG) engine, which oxidation catalyst comprises a catalytic material for treating the exhaust gas and a substrate,
which catalytic material comprises a platinum (Pt), palladium (Pd) or a combination of platinum (Pt) and palladium (Pd) supported on a molecular sieve,
wherein the molecular sieve, ia a zeolite, and has a content of heteroatom T-atoms of ≤about 0.20 mol %, and the molecular sieve has a molar ratio of silica to alumina (SAR) of ≥1500.
2. The oxidation catalyst of claim 1 , wherein the catalytic material has a content of heteroatom T-atoms of <about 0.17 mol %.
3. The oxidation catalyst of claim 1 , wherein the heteroatom is selected from the group consisting of aluminum (Al), boron (B), gallium (Ga), titanium (Ti), zinc (Zn), iron (Fe), vanadium (V) and combinations of any two or more thereof.
4. The oxidation catalyst of claim 1 , wherein the framework comprises germanium in an amount of ≤about 10 mol %.
5. The oxidation catalyst of claim 1 , wherein the framework consists essentially of silicon, oxygen and heteroatom T-atoms.
6. The oxidation catalyst of claim 1 , wherein the molecular sieve does not have a content of heteroatom T-atoms.
7. The oxidation catalyst of claim 1 , wherein the catalytic material has a total amount of the platinum group metal (PGM) of 0.01 to 30 wt %.
8. The oxidation catalyst of claim 1 , wherein the catalytic material has a total amount of palladium of 0.1 to 20 wt %.
9. The oxidation catalyst of claim 1 , wherein the molecular sieve is in a particulate form and has a D50 of 0.1 to 20 microns.
10. The oxidation catalyst of claim 1 , wherein the substrate is a flow-through substrate or a filtering substrate.
11. The oxidation catalyst of claim 1 , wherein the catalytic material is dispersed in the substrate.
12. An exhaust system comprising the oxidation catalyst of claim 1 .
13. The exhaust system of claim 12 further comprising a sulfur trap.
14. The exhaust system of claim 13 comprising a first sulfur trap and a second sulfur trap, wherein the first sulfur trap and the second sulfur trap are arranged in parallel.
15. An apparatus comprising an engine and the exhaust system of claim 12 .
16. The apparatus of claim 15 , wherein the engine is a natural gas engine.
17. The apparatus of claim 16 , wherein the engine is a lean burn internal combustion engine.
18. The oxidation catalyst of claim 1 , wherein the zeolite is a small pore zeolite, a medium pore zeolite or a large pore zeolite.
19. The oxidation catalyst of claim 1 , wherein the zeolite has a framework type selected from the group consisting of AEI, ANA, ATS, BEA, CDO, CFI, CHA, CON, DDR, ERI, FAU, FER, GON, IFR, IFW, IFY, IHW, IMF, IRN, -IRY, IS V, ITE, ITG, -ITN, ITR, ITW, IWR, IWS, IWV, IWW, JOZ, LTA, LTF, MEL, MEP, MFI, MRE, MSE, MTF, MTN, MTT, MTW, MVY, MWW, NON, NSI, RRO, RSN, RTE, RTH, RUT, RWR, SEW, SFE, SFF, SFG, SFH, SFN, SFS, SFV, SGT, SOD, SSF, -SSO, SSY, STF, STO, STT, -SVR, SW, TON, TUN, UOS, UOV, UTL, UWY, VET, VNI.
20. The oxidation catalyst of claim 1 , wherein the molecular sieve is a small pore zeolite having an AEI, AFX, ANA, CDO, CHA, DDR, EAB, EDI, EPI, ERI, IHW, ITE, ITW, KFI, LEV, MER, NSI, PAU, PHI, RHO, RTH, UFI or VNI framework type.
21. The oxidation catalyst of claim 20 , wherein the molecular sieve is a small pore zeolite having a CHA, CDO or DDR framework type.
22. The oxidation catalyst of claim 1 , wherein the molecular sieve is a medium pore zeolite having an MFI, MEL, MWW or EUO framework type.
23. The oxidation catalyst of claim 1 , wherein the molecular sieve is a large pore zeolite having an AFI, BEA, CON, EMT, FAU, or MOR framework type.
24. The oxidation catalyst of claim 1 , wherein the molecular sieve has a BEA, CDO, CON, MEL, MWW, MFI, or FAU framework type.
25. The oxidation catalyst of claim 1 , wherein the molecular sieve has a BEA or MFI framework type.
26. A method of treating an exhaust gas comprising methane, the method comprising contacting the exhaust gas with an oxidation catalyst of claim 1 .