SCR catalyst device containing vanadium oxide and molecular sieve containing iron

Patent metadata

Field	Value
Publication number	US-11300029-B2
Application number	US-201716469835-A
Country	US
Kind code	B2
Filing date	Dec 20, 2017
Priority date	Dec 20, 2016
Publication date	Apr 12, 2022
Grant date	Apr 12, 2022

Abstract

The invention relates to a catalyst device for purifying exhaust gases containing nitrogen oxide by using selective catalytic reduction (SCR), the catalyst device comprising at least two catalytic layers, the first layer containing vanadium oxide and a mixed oxide comprising titanium oxide and silicon oxide and the second layer containing a molecular sieve containing iron, wherein the first layer is applied onto the second layer. The invention also relates to uses of the catalyst device and a method for purifying exhaust gases.

First claim

The invention claimed is:

1. A catalyst device for purifying exhaust gases containing nitrogen oxide by selective catalytic reduction (SCR), comprising at least two catalytic layers, the first layer comprises the following components:
(a) from 0.5 to 10 wt % vanadium oxide, calculated as V 2 O 5 ,
(b) from 0 to 17 wt % tungsten oxide, calculated as WO 3 ,
(c) from 0.2 to 10 wt % cerium oxide, calculated as CeO 2 ,
(d) from 25 to 98 wt % titanium oxide, calculated as TiO 2 ,
(e) from 0.5 to 15 wt % silicon oxide, calculated as SiO 2 ,
(f) from 0 to 15 wt % aluminum oxide, calculated as Al 2 O 3 , in each case based on the weight of the first layer, and the second layer containing a molecular sieve containing iron, wherein the first layer is applied onto the second layer.

2. The catalyst device according to claim 1 , wherein, in addition to components (a), (c), (d) and (e), the first layer contains a quantity of at least one of (b) and (f).

3. The catalyst device according to claim 1 , wherein the molecular sieve is a zeolite.

4. The catalyst device according to claim 3 , wherein the zeolite is an iron-exchanged zeolite.

5. The catalyst device according to claim 3 , wherein the zeolite has a structure, whose maximum ring size has more than 8 tetrahedra.

6. The catalyst device according to claim 3 , wherein the zeolite has a structure selected from AEL, AFI, AFO, AFR, ATO, BEA, GME, HEU, MEI, MWW, EUO, FAU, FER, LTL, MAZ, MOR, MEL, MTW, OFF and TON.

7. The catalyst device according to claim 1 , wherein the first layer is completely applied onto the second layer.

8. The catalyst device according to claim 1 , wherein the first layer is applied onto the second layer in certain regions, wherein a region which has a first, upper layer is first in the flow direction, and wherein there are regions in which the lower, second layer comes into direct contact with the exhaust gases.

9. The catalyst device according to claim 1 , wherein the second layer is applied onto an inert substrate.

10. The catalyst device according to claim 1 , wherein the first layer contains from 1 to 5 wt % vanadium oxide, calculated as V 2 O 5 .

11. The catalyst device according to claim 1 , wherein the first layer contains from 0.5 to 5 wt % cerium oxide, calculated as CeO 2 .

12. The catalyst device according to claim 1 , wherein the first layer contains from 1 to 5 wt % vanadium oxide, calculated as V 2 O 5 and from 0.2 to 5 wt % cerium oxide, calculated as CeO 2 .

13. The catalyst device according to claim 1 , wherein the first layer contains from 0.5 to 3 wt % cerium oxide, calculated as CeO 2 .

14. The catalyst device according to claim 1 , wherein the second layer comprises at least two different iron containing zeolites.

15. The catalyst device according to claim 1 wherein
(a) is from 1 to 5 wt % vanadium oxide, calculated as V 2 O 5 ,
(b) is from 1 to 15 wt % tungsten oxide, calculated as WO 3 ,
(c) is from 0.2 to 5 wt % cerium oxide, calculated as CeO 2 ,
(d) is from 73 to 98 wt % titanium oxide, calculated as TiO 2 ,
(e) is from 1 to 7 wt % silicon oxide, calculated as SiO 2 ,
(f) is from 0.5 to 15 wt % aluminum oxide, calculated as Al 2 O 3 , in each case based on the weight of the first layer.

16. A method of selective catalytic reduction (SCR), comprising utilizing a catalyst device according to claim 1 for purifying exhaust gases containing nitrogen oxide by selective catalytic reduction (SCR).

17. The method according to claim 16 , wherein formation of N 2 O downstream of the catalyst device is limited to 50 ppm or less within the temperature range of 180° C. to 450° C.

18. A method for purifying exhaust gases, comprising the steps of:
(i) providing a catalyst device according to claim 1 ,
(ii) introducing exhaust gases containing nitrogen oxides into the catalyst device,
(iii) introducing a reductant containing nitrogen into the catalyst device, and
(iv) reducing nitrogen oxides in the catalyst device by selective catalytic reduction (SCR).

19. A catalyst device for purifying exhaust gases containing nitrogen oxide by selective catalytic reduction (SCR), comprising at least two catalytic layers, the first layer containing a catalytic oxide mixture and non-catalytic metal oxide support material, and the second layer containing a molecular sieve containing iron, wherein the first layer is applied onto the second layer,
wherein the catalytic oxide mixture in the first layer comprises the following components:
(a) from 0.5 to 10 wt % vanadium oxide, calculated as V 2 O 5 ,
(b) from 0 to 17 wt % tungsten oxide, calculated as WO 3 ,
(c) from 0.2 to 10 wt % cerium oxide, calculated as CeO 2 , in each case based on the weight of the first layer,
and wherein the non-catalytic metal oxide support material in the first layer comprises the following components:
(d) from 25 to 98 wt % titanium oxide, calculated as TiO 2 ,
(e) from 0.5 to 15 wt % silicon oxide, calculated as SiO 2 ,
(f) from 0 to 15 wt % aluminum oxide, calculated as Al 2 O 3 , in each case based on the weight of the first layer.

20. The catalyst device according to claim 19 , wherein the amount of titanium oxide is greater than 50% wt % up to 86.4 wt %, the amount of vanadium oxide is 1 to 5 wt %; the amount of cerium oxide is 0.2 to 5 wt %, the amount of silicon oxide is 1 to 7 wt %, and the amount of tungsten oxide is 1 to 15 wt %.

21. The catalyst device according to claim 20 , wherein the catalyst device is operative in use to purify exhaust gases having a NO 2 /NO x ratio range of >0.5 to 0.75 while the exhaust gases temperature ranges fully within a temperature range of 180 to 450° C.

Assignees

• Umicore Ag & Co Kg

Inventors

• Malmberg Stephan
• Soeger Nicola

Classifications

• B01D2255/50

  Zeolites · CPC title

• F01N2370/04

  Zeolitic material · CPC title

• B01J2523/55

  Vanadium · CPC title

• B01J2523/47

  Titanium · CPC title

• B01J23/22

  Vanadium · CPC title