Copper CHA zeolite catalysts
US-9839905-B2 · Dec 12, 2017 · US
US10654031B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10654031-B2 |
| Application number | US-201715806167-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 7, 2017 |
| Priority date | Feb 27, 2007 |
| Publication date | May 19, 2020 |
| Grant date | May 19, 2020 |
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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.
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What is claimed is: 1. An ammonia SCR catalyst article comprising a substrate having deposited thereon a copper-containing aluminosilicate zeolite having a CHA crystal structure, wherein the zeolite contains at least about 2.00 weight percent copper, expressed as copper oxide, and has a mole ratio of silica to alumina from about 20 to about 40, wherein the CHA crystal structure is characterized by lattice parameters determined from an X-ray powder diffraction pattern, and wherein the hydrothermal stability of the lattice parameters of the CHA crystal structure is confirmed by a hydrothermal aging test, and wherein the hydrothermal aging test comprises subjecting the catalyst article to hydrothermal aging by aging the catalyst article in the presence of 10% H 2 O at 800° C. for 48 hours, and wherein the lattice parameters of the CHA crystal structure after said hydrothermal aging test are within 1% of the lattice parameters of the CHA crystal structure prior to said hydrothermal aging test. 2. The article according to claim 1 , wherein the d-spacings of the CHA crystal structure after hydrothermal aging are within 1% of the d-spacings of the CHA crystal structure prior to hydrothermal aging within the 15-38.5° 2Θ range. 3. The article according to claim 1 , wherein the CHA crystal structure after hydrothermal aging has a lattice parameter a of about 13.56 Å and a lattice parameter c of about 4.75 Å. 4. The article according to claim 1 , wherein the substrate is a metallic or ceramic substrate. 5. The article according to claim 1 , wherein the zeolite having the CHA structure is selected from the group consisting of SSZ-13, LZ-218, Linde D, Linde R, Phi and ZK-14. 6. The article according to claim 5 , wherein the zeolite having the CHA structure is SSZ-13. 7. The article according to claim 1 , wherein the mole ratio of silica to alumina is from about 25 to about 40. 8. The article according to claim 7 , wherein the mole ratio of silica to alumina is about 30. 9. The article according to claim 1 , wherein the substrate is a honeycomb substrate. 10. The article according to claim 9 , wherein the substrate is a wall flow substrate. 11. The article according to claim 9 , wherein the substrate is a flow through substrate. 12. The article according to claim 1 , wherein the deposited zeolite further comprises a binder. 13. The article according to claim 12 , wherein the binder is ZrO 2 . 14. The article according to claim 1 , wherein the substrate is ceramic and selected from the group consisting of cordierite, cordierite-alumina, silicon nitride, zircon mullite, spodumene, alumina-silica magnesia, zircon silicate, sillimanite, magnesium silicate, zircon, petalite, alpha-alumina, and aluminosilicate. 15. The article according to claim 1 , wherein the zeolite has an atomic ratio of copper to aluminum from about 0.30 to about 0.50.
for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas · CPC title
Processes characterised by a specific catalyst · CPC title
Iron group metals or copper · CPC title
Processes characterised by a specific catalyst · CPC title
Mixtures of different aluminosilicates · CPC title
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