Highly dispersed palladium catalysts
US-2024246067-A1 · Jul 25, 2024 · US
US10081010B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10081010-B2 |
| Application number | US-201415126171-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 15, 2014 |
| Priority date | Apr 7, 2014 |
| Publication date | Sep 25, 2018 |
| Grant date | Sep 25, 2018 |
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Method for the preparation of a metal-exchanged zeolites or mixtures of metal-exchanged zeolites, such as Cu-SSZ-13, Cu-ZSM-5, Cu-beta, or Fe-beta, comprising the steps of providing a dry mixture of a) one or more microporous zeotype materials that exhibit ion exchange capacity and b) one or more metal compounds; heating the mixture in a gaseous atmosphere containing ammonia to a temperature lower than 300° C. for a time sufficient to initiate and perform a solid state ion exchange of ions of the metal compound and ions of the zeolite material; and obtaining the metal-exchanged zeolite material.
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The invention claimed is: 1. Method for the preparation of a metal-exchanged zeolite material or mixtures of metal-exchanged zeolites materials comprising the steps of providing a dry mixture containing a) one or more zeolites starting materials that exhibit ion exchange capacity and b) one or more metal compounds; heating the mixture in a gaseous atmosphere containing ammonia at a temperature of between 150° C. and 250° C. to perform a solid state ion exchange of ions of the metal compound and ions of the one or more zeolites; and obtaining the metal-exchanged zeolite material or the mixture of metal-exchanged zeolite materials, wherein the metal compound is Cu (I) oxide. 2. Method according to claim 1 , wherein the one or more zeolite starting materials have the framework code of AEI, AFX, CHA, KFI, LTA, IMF, ITH, MEL, MFI, SZR, TUN, *BEA, BEC, FAU, FER, MOR, LEV. 3. Method according to claim 1 , wherein the one or more zeolite starting materials are selected from the group consisting of ZSM-5, zeolite Y, beta zeolite, SSZ-13, SSZ-39, SSZ-62, and Chabazite. 4. Method according to claim 1 , wherein the one or more zeolite starting materials are in the H + or NH 4 + form. 5. Method according to claim 1 , wherein the one or more zeolite starting materials contain an organic structure directing agent. 6. Method according to claim 1 , wherein the one or more metal compounds are selected from the group of metal oxides, metal nitrates and phosphates, sulfates, oxalates, acetates or combinations thereof. 7. Method according to claim 1 , wherein the content of ammonia in the atmosphere is between 1 and 5000 vol. ppm. 8. Method according to claim 1 , wherein the content of oxygen in the atmosphere is 10% or lower. 9. Method according to claim 1 , wherein the content of water in the atmosphere is 5 vol. % water or less. 10. Method according to claim 1 , wherein the mixture of one or more zeolites starting materials that exhibit ion exchange capacity and one or more metal compounds is heated in the gaseous atmosphere containing ammonia at a temperature of between 150° C. and 250° C. 11. A metal-exchanged zeolite or mixtures of metal-exchanged zeolites obtained by a method according to claim 1 . 12. A method for the removal of nitrogen oxides from exhaust gas by selective catalytic reduction with a reductant, comprising contacting the exhaust gas with a catalyst comprising a metal-exchanged zeolite or mixtures of metal-exchanged zeolites obtained by a method according to claim 1 . 13. A method according to claim 12 , wherein the reductant is ammonia or a precursor thereof. 14. A method according to claim 12 , wherein the reductant comprises hydrocarbons.
Y-type faujasite · CPC title
ZSM 5 zeolites · CPC title
Iron group metals or copper · CPC title
Aluminophosphates [APO compounds] · CPC title
CHA-type, e.g. Chabazite, LZ-218 · CPC title
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