Method for the decomposition of N
View Patent ↗The invention relates to a method for the catalytic decomposition of N 2 O in a gas containing N 2 O in the presence of a catalyst, wherein the catalyst comprises a zeolite that has been loaded with a first metal selected from the group of noble metals consisting of ruthenium, rhodium, silver, rhenium, osmium, iridium, platinum and gold, and with a second metal selected from the group of transition metals consisting of chromium, manganese, iron cobalt, nickel and copper, and wherein the loading of the zeolite with metals has been obtained by first loading the zeolite with the noble metal and then with the transition metal, as well as a catalyst for this method and a method for the preparation of this catalyst.
1. A method for the catalytic decomposition of N 2 O in a gas containing N 2 O in the presence of a catalyst, wherein the catalyst comprises a zeolite that has been loaded with a first metal selected from the group of noble metals consisting of ruthenium, rhodium, silver, rhenium, osmium, iridium, platinum and gold, and with a second metal selected from the group of transition metals consisting of vanadium, chromium, manganese, iron, cobalt, nickel and copper, wherein the loading of the zeolite with metals has been obtained by first loading the zeolite with the noble metal and then with the transition metal, and wherein the zeolite is selected from the group consisting of FER, CHA and BEA.
2. The method according to claim 1 , wherein the zeolite has been loaded with the first metal by means of ion exchange.
3. The method according to claim 1 , wherein the first metal has been selected from the group consisting of ruthenium, rhodium, osmium and iridium.
4. The method according to claim 1 , wherein the second metal has been selected from the group consisting of iron, cobalt and nickel.
5. The method according to claim 1 , wherein the zeolite loaded with metals has been selected from the group consisting of Fe—Rh-FER, Fe—Ir-FER, Fe—Ru-FER, Fe—Ru-MOR, Co—Rh-FER, Co—Ir-FER, Co—Ru-FER, Fe—Rh-BEA, Fe—Ir-BEA, Fe—Ru-BEA, Co—Rh-BEA, Co—Ir-BEA and Co—Ru-BEA.
6. The method according to claim 1 , wherein the zeolite contains 0.00001-4% (m/m) of the first metal and 0.1-10% (m/m) of the second metal.
7. The method according to claim 1 , wherein the zeolite contains 0.1-0.5% (m/m) of the first metal and 1-4% (m/m) of the second metal.
8. The method according to claim 1 , wherein the gas containing N 2 O also contains oxygen or water.
9. The method according to claim 1 , wherein the gas containing N 2 O essentially contains no hydrocarbon.
10. The method according to claim 1 , wherein the gas containing N 2 O contains less than 50 ppm hydrocarbon.
11. The method according to claim 1 , wherein the gas containing N 2 O also contains NO x , where x is equal to or greater than 1.
12. The method according to claim 11 , wherein a catalyst is also used for the removal of NO x .
13. The method according to claim 1 , wherein the gas containing N 2 O is fed through a chamber that contains the catalyst, wherein the chamber, the gas or both are heated if required.
14. A method for the preparation of a catalyst for the catalytic decomposition of N 2 O in a gas containing N 2 O, wherein the catalyst comprises a zeolite and the zeolite is first loaded with a first metal selected from the group of noble metals consisting of ruthenium, rhodium, silver, osmium and iridium, and then loaded with a second metal selected from the group of transition metals consisting of vanadium, chromium, manganese, iron, cobalt, nickel and copper.
15. The method according to claim 14 , wherein the zeolite is loaded with the first metal by means of ion exchange.
16. The method according to claim 14 , wherein the second metal is selected from the group consisting of iron, cobalt and nickel.
17. The method according to claim 14 , wherein the zeolite is selected from the group consisting of FAU, FER, CHA, MOR, MFI, BEA, EMT, CON, BOG and ITQ-7.
18. A catalyst obtained according to the method of claim 14 , wherein the zeolite is selected from the group consisting of FER, CHA and BEA.
19. The catalyst according to claim 18 , wherein the zeolite contains 0.00001-4% (m/m) of the first metal and 0.1-10% (m/m) of the second metal.
20. The catalyst according to claim 18 , wherein the catalyst comprises a zeolite based on Si and Al and wherein 2-50% of the Al has been coordinated by the first metal.
21. The catalyst according to claim 18 , wherein the zeolite has a mean first metal concentration, and wherein any local first metal concentration may have a concentration deviation of not larger than 50% of the mean first metal concentration.
22. A catalyst, comprising a zeolite, wherein the zeolite is loaded with a first metal selected from the group of noble metals consisting of ruthenium, rhodium, rhenium, osmium, iridium and gold, and with a second metal selected from the group of transition metals consisting of vanadium, chromium, manganese, iron, cobalt, nickel and copper, wherein the zeolite is selected from the group consisting of FER, CHA and BEA.
23. A catalyst for the catalytic decomposition of N 2 O in a gas containing N 2 O comprising a zeolite, wherein the zeolite is first loaded with a first metal selected from the group consisting of ruthenium, rhodium, osmium, and iridium, and wherein the zeolite is loaded with a second metal selected from the group of transition metals consisting of vanadium, chromium, manganese, iron, cobalt, nickel and copper.
24. A catalyst for the catalytic decomposition of N 2 O in a gas containing N 2 O comprising a zeolite, the zeolite is first loaded with a first metal selected from the group of noble metals consisting of ruthenium, rhodium, silver, rhenium, osmium, iridium, platinum and gold, and then loaded with a second metal selected from the group of transition metals consisting of vanadium, chromium, manganese, iron, cobalt, nickel and copper; wherein the zeolite is selected from the group consisting of FER, CHA and BEA; and wherein the zeolite loaded with metals is selected from the group consisting of Fe—Rh-FER, Fe—Ir-FER, Fe—Ru-FER, Co—Rh-FER, Co—Ir-FER, Co—Ru-FER, Fe—Rh-BEA, Fe—Ir-BEA, Fe—Ru-BEA, Co—Rh-BEA, Co—Ir-BEA and Co—Ru-BEA.