Single or dual layer ammonia slip catalyst
US-2016367938-A1 · Dec 22, 2016 · US
US2016101411A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016101411-A1 |
| Application number | US-201514973353-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 17, 2015 |
| Priority date | Feb 27, 2007 |
| Publication date | Apr 14, 2016 |
| Grant date | — |
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Zeolite catalysts and systems and methods for preparing and using zeolite catalysts having the CHA crystal structure are disclosed. The catalysts can be used to remove nitrogen oxides from a gaseous medium across a broad temperature range and exhibit hydrothermal stable at high reaction temperatures. The zeolite catalysts include a zeolite carrier having a silica to alumina ratio from about 15:1 to about 256:1 and a copper to alumina ratio from about 0.25:1 to about 1:1.
Opening claim text (preview).
1 - 17 . (canceled) 18 . A catalyst comprising a copper ion-exchanged aluminosilicate zeolite having a CHA crystal structure, the zeolite having a mole ratio of silica to alumina from about 20 to about 40 and an atomic ratio of copper to aluminum from about 0.25 to about 0.50. 19 . The catalyst according to claim 18 , wherein the catalyst contains ion-exchanged copper and an amount of non-exchanged copper sufficient to maintain NOx conversion performance of the catalyst in an exhaust gas stream containing nitrogen oxides after hydrothermal aging of the catalyst. 20 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 25 to about 40. 21 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 25. 22 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 26. 23 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 27. 24 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 28. 25 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 29. 26 . The catalyst according to claim 19 , wherein the mole ratio of silica to alumina is about 30. 27 . The catalyst according to claim 19 , wherein the zeolite having the CHA structure is SSZ-13. 28 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.30. 29 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.33. 30 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.38. 31 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.44. 32 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.46. 33 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.40. 34 . The catalyst according to claim 18 , further comprising a binder. 35 . The catalyst according to claim 34 , wherein the binder is ZrO 2 . 36 . The catalyst according to claim 19 , wherein the zeolite contains at least about 2.00 weight percent copper, expressed as copper oxide. 37 . An exhaust gas treatment system comprising the catalyst of claim 18 and further comprising a catalyzed soot filter. 38 . The exhaust gas treatment system of claim 37 , wherein said catalyzed soot filter is upstream of said catalyst. 39 . The exhaust gas treatment system of claim 37 , further comprising a diesel oxidation catalyst. 40 . The exhaust gas treatment system of claim 39 , wherein the diesel oxidation catalyst is upstream of the catalyst comprising the zeolite having the CHA crystal structure. 41 . A catalyst article comprising a substrate having deposited thereon the catalyst according to claim 18 . 42 . The catalyst article according to claim 41 , wherein the substrate is metal or ceramic. 43 . The catalyst article according to claim 42 , wherein the substrate is a honeycomb substrate. 44 . The catalyst article according to claim 43 , wherein the honeycomb substrate is a flow through substrate. 45 . The catalyst article according to claim 43 , wherein the honeycomb substrate is a wall flow substrate.
Wall flow filters · CPC title
Copper and noble metals · CPC title
Processes characterised by a specific catalyst · CPC title
Ammonium compounds · CPC title
Other types characterised by their X-ray diffraction pattern and their defined composition {(C01B39/023, C01B39/026, C01B39/06 take precedence)} · CPC title
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