Catalyst system for reducing nitrogen oxides
US-2017218809-A1 · Aug 3, 2017 · US
US11014077B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11014077-B2 |
| Application number | US-201716096126-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 2, 2017 |
| Priority date | May 3, 2016 |
| Publication date | May 25, 2021 |
| Grant date | May 25, 2021 |
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The invention relates to a catalyst comprising a small-pore zeolite that contains iron and copper and has a maximum ring size of eight tetrahedral atoms, characterized in that the channel width of the small-pore zeolite amounts to >3.8 Å (0.38 nm) in at least one dimension.
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The invention claimed is: 1. A catalyst comprising a small-pore zeolite that contains iron and copper and has a maximum ring size of eight tetrahedral atoms, wherein the small-pore zeolite has a structure of type EAB, ERI, ESV, JBW or LEV, and wherein a channel width of the small-pore zeolite amounts to ≥0.47 nm (4.7 Å) in at least one dimension, and wherein the small-pore zeolite comprises copper in an amount of 1.0 to 1.9 wt. %, calculated as Cu, and iron in an amount of 1.0 to 2.0 wt. %, calculated as Fe, based in each case on the total weight of the small-pore zeolite with the copper and iron, and wherein the small pore zeolite contains no further metal besides copper and iron. 2. A catalyst comprising a small-pore zeolite that contains iron and copper and has a maximum ring size of eight tetrahedral atoms, wherein the small-pore zeolite has a structure type of EAB, ERI, ESV, JBW or LEV, and wherein a channel width of the small-pore zeolite amounts to >0.38 nm (3.8 Å) in at least one dimension, and wherein the small-pore zeolite comprises copper in an amount of 1.5 wt. %, calculated as Cu, and iron in an amount of 1.3 wt. %, calculated as Fe, based in each case on the total weight of the small-pore zeolite with the copper and iron, and wherein the small pore zeolite contains no further metal besides copper and iron. 3. The catalyst according to claim 1 , wherein the small-pore zeolite is of the structure type ERI or LEV. 4. The catalyst according to claim 1 , wherein the small-pore zeolite has a SAR value of 1 to 50. 5. The catalyst according to claim 1 , wherein the small-pore zeolite is of the structure type ERI and has an SAR value of 5 to 15. 6. The catalyst according to claim 2 , wherein the molar ratio of Cu:Al is 0.03 to 0.10. 7. The catalyst according to claim 2 , wherein the molar ratio of (Cu+Fe):Al is 0.12 to 0.2. 8. The catalyst according to claim 1 , wherein the small-pore zeolite is of the structure type LEV and has a SAR value of 20 to 40. 9. The catalyst according to claim 8 , wherein a molar ratio of Cu:Al is 0.15 to 0.30. 10. The catalyst according to claim 8 , wherein a molar ratio of (Cu+Fe):A1 is 0.32 to 0.50. 11. The catalyst according to claim 1 , wherein the catalyst is present in a form of a coating on a carrier substrate. 12. The catalyst according to claim 11 , wherein the carrier substrate is a flow-through substrate or a wall-flow filter. 13. The catalyst according to claim 11 , wherein the carrier substrate is inert and consists of silicon carbide, aluminum titanate or cordierite. 14. The catalyst according to claim 11 , wherein the carrier substrate comprises a catalytically active material. 15. The catalyst according to claim 14 , wherein the carrier substrate comprises an SCR catalytically active material. 16. The catalyst according to claim 14 , wherein the catalytically active material comprises a mixed oxide containing vanadium, titanium and tungsten compounds. 17. The catalyst according to claim 1 , wherein the catalyst is present as part of a carrier substrate. 18. The catalyst according to claim 17 , wherein the carrier substrate is a flow-through substrate or a wall-flow filter. 19. The catalyst according to claim 17 , wherein the carrier substrate is coated with a catalytically active material. 20. The catalyst according to claim 2 , wherein the channel width of the small-pore zeolite is ≥0.47 nm (4.7 A) in at least one dimension. 21. A method for purifying exhaust gas of lean-operated combustion engines, wherein the exhaust gas is passed over a catalyst according to claim 1 . 22. A system for purifying exhaust gas from lean-operated combustion engines, wherein the system comprises the catalyst according to claim 1 as well as an injector for aqueous urea solution, wherein the injector is located upstream of the catalyst. 23. The system according to claim 22 , wherein the system further comprises an oxidation catalyst. 24. The system according to claim 23 , wherein the oxidation catalyst includes platinum. 25. A catalyst comprising a small-pore zeolite that contains iron and copper and has a maximum ring size of eight tetrahedral atoms, and wherein the small-pore zeolite comprises copper in an amount of 1.0 to 1.9 wt. %, calculated as Cu and iron in an amount of 1.0 to 2.0 wt. %, calculated as Fe, based in each case on the total weight of the small-pore zeolite with the copper and iron, and wherein the small pore zeolite contains no further metal besides copper and iron, wherein the small-pore zeolite has either a structure type of ERI with an SAR value of 5 to 15, or a structure type of LEV with an SAR value of 20 to 40, and wherein a channel width of the small-pore zeolite is 0.48 to 0.51 nm in at least one dimension.
Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
Control of selective catalytic reduction [SCR], e.g. by adjusting the dosing of reducing agent · CPC title
Processes characterised by a specific catalyst · CPC title
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