Cu-CHA/Fe-BEA mixed zeolite catalyst and process for the treatment of NO
The present invention relates to a catalyst, which may be used in selective catalytic reduction (SCR), said catalyst comprising one or more zeolites of the BEA structure type, one or more zeolites of the CHA structure type, and optionally one or more zeolites of the MFI structure type, wherein at least part of the one or more zeolites of the BEA structure type contain iron (Fe), wherein at least part of the one or more zeolites of the CHA structure type contain copper (Cu), and wherein at least part of the optional one or more zeolites of the MFI structure type contain iron (Fe). Furthermore, the present invention concerns an exhaust gas treatment system comprising said catalyst as well as a process for the treatment of a gas stream comprising NO x using said catalyst as well.
1. A selective catalytic reduction (SCR) catalyst for selective catalytic reduction, the SCR catalyst comprising:
at least one zeolite of the BEA structure type;
at least one zeolite of the CHA structure type; and
at least one zeolite of the MFI structure type;
wherein the at least one zeolite of the BEA structure type contains from 0.5 to 2.0 wt. % of iron (Fe) based on the weight of the at least one zeolite of the BEA structure type,
wherein the at least one zeolite of the CHA structure type contains from 1.5 to 5.0 wt. % of copper (Cu) based on the weight of the at least one zeolite of the CHA structure type,
wherein the at least one zeolite of the MFI structure type contains from 2.5 to 5.5 wt. % of iron (Fe) based on the weight of the at least one zeolite of the MFI structure type,
wherein a loading of the at least one zeolite of the CHA structure type present in the catalyst is from 1.5-2.5 g/in 3 , and
wherein the loading of each of the at least one zeolite of the BEA structure type and of the at least one zeolite of the MFI structure type is from 0.4 to 0.6 g/in 3 ;
wherein the total loading of the at least one zeolite of the BEA structure type and of the at least one zeolite of the MFI structure type is from 0.8 to 1.2 g/in 3 ;
wherein the at least one zeolite of the BEA structure type, the at least one zeolite of the CHA structure type, and the at least one zeolite of the MFI structure type comprise Al and Si in their respective zeolite frameworks; wherein a molar ratio of silica to alumina (SAR) in each of the at least one zeolite of the BEA and the at least one zeolite of MFI structure type is from 23 to 30; and
wherein the molar ratio of silica to alumina (SAR) in the at least one zeolite of the CHA structure type is from 25 to 35.
2. The catalyst of claim 1 , wherein a ratio of the total weight of the at least one zeolite of the BEA structure type and of the at least one zeolite of the MFI structure type to the weight of the at least one zeolite of the CHA structure type is from 0.5 to 1.
3. The catalyst of claim 1 , wherein the molar ratio of silica to alumina (SAR) in each of the at least one zeolite of the BEA and the at least one zeolite of the MFI structure type is from 25 to 27.
4. The catalyst of claim 1 , wherein the molar ratio of silica to alumina (SAR) in the at least one zeolite of the CHA structure type is from 28 to 32.
5. The catalyst of claim 1 , wherein said catalyst further comprises a substrate onto which the zeolites are provided, wherein the substrate is selected from the group consisting of a flow-through substrate and a wall-flow substrate.
6. The catalyst of claim 5 , wherein the catalyst comprises at least one layer provided on the substrate, and the zeolites are contained in one single layer or two or more separate layers.