Copper oxides supported on spinel oxides as catalysts for low temperature direct NOx decomposition
Active catalysts for the treatment of a low temperature exhaust gas stream are provided containing copper oxides dispersed on a spinel oxide for the direct, lean removal of nitrogen oxides from the exhaust gas stream. The low temperature, direct decomposition is accomplished without the need of a reductant molecule. In one example, CuO x may be dispersed as a monolayer on a metal oxide support, such as Co 3 O 4 spinel oxide, synthesized using an incipient wetness impregnation technique. The CuO x /Co 3 O 4 catalyst system converts nitric oxide to nitrogen gas with high product specificity, avoiding the production of a significant concentration of the undesirable N 2 O product.
1. A catalyst system for the direct decomposition removal of NOx from an exhaust gas stream provided at a temperature of less than about 500° C., the catalyst system comprising:
a Co 3 O 4 spinel oxide; and
a plurality of discrete island regions of CuO x supported on a surface of the Co 3 O 4 spinel oxide and configured to catalyze a reduction of the NOx to generate N 2 without the presence of a reductant, wherein each of the plurality of the discrete island regions of CuOx comprises a two-dimensional, non-crystalline structure provided with a surface density of Cu at an empirical loading level of between about 6.7 and about 7.6 Cu atoms per square nanometer (Cu/nm 2 ) as determined by ICP techniques.
2. The catalyst system according to claim 1 , wherein the discrete island regions of CuO x supported on the Co 3 O 4 spinel oxide are formed using incipient wetness impregnation techniques.
3. A catalytic converter for the direct decomposition removal of NOx from an exhaust gas stream flowing at a temperature of less than or equal to about 500° C., the catalytic converter comprising:
an inlet configured to receive the exhaust gas stream into an enclosure;
an outlet configured to allow the exhaust gas stream to exit the enclosure; and
a catalyst system contained inside the enclosure, the catalyst system comprising a plurality of discrete island regions of CuOx supported on a surface of a Co 3 O 4 spinel oxide support that is configured to catalyze a reduction of the NOx to generate N 2 without the presence of a reductant, wherein each of the plurality of the discrete island regions of CuOx comprises a two-dimensional, non-crystalline structure provided with a surface density of Cu at an empirical loading level of between about 6.7 and about 7.6 Cu atoms per square nanometer (Cu/nm 2 ) as determined by ICP techniques.
4. The catalytic converter according to claim 3 , wherein the Co 3 O 4 spinel oxide is in a nanoparticle form, having an average diameter of from about 2 to about 100 nm.
5. The catalytic converter according to claim 3 , wherein the discrete island regions of CuOx supported on the Co 3 O 4 spinel oxide are formed using incipient wetness impregnation techniques.
6. The catalytic converter according to claim 3 , wherein the catalyst system is provided with a surface density of Cu at an empirical loading level of about 6.7 Cu atoms per square nanometer (Cu/nm 2 ) as determined by ICP techniques.
7. The catalytic converter according to claim 3 , configured to flow the exhaust gas stream through the catalyst system at a temperature at or less than about 350° C. and obtaining an NOx selectivity to N 2 greater than about 20%.
8. The catalytic converter according to claim 3 , configured to flow the exhaust gas stream through the catalyst system at a temperature at or less than about 300° C. and obtaining an NOx selectivity to N 2 greater than about 15%.
9. The catalytic converter according to claim 3 , configured to exhibit an NO adsorption capacity of greater than about 200 μmol NO/g.
10. A method for direct decomposition removal of NOx from a low temperature exhaust gas stream, the method comprising:
flowing the exhaust gas stream through a catalyst system and exposing the exhaust gas stream to a plurality of discrete island regions of copper oxide supported on a Co 3 O 4 spinel oxide support, each of the plurality of the discrete island regions of CuOx comprising a two-dimensional, non-crystalline structure provided with a surface density of Cu at an empirical loading level of between about 6.7 and about 7.6 Cu atoms per square nanometer (Cu/nm 2 ) as determined by ICP techniques; and
catalyzing a reduction of the NOx to generate N 2 without the presence of a reductant.
11. The method according to claim 10 , wherein the CuOx is supported on the Co 3 O 4 spinel oxide using incipient wetness impregnation techniques.
12. The method according to claim 10 , comprising flowing the exhaust gas stream through the catalyst system at a temperature at or less than about 350° C. and obtaining an NOx selectivity to N 2 greater than about 20%.
13. The method according to claim 10 , comprising flowing the exhaust gas stream through the catalyst system at a temperature at or less than about 300° C. and obtaining an NOx selectivity to N 2 greater than about 15%.