Thermally regenerable nitric oxide adsorbent
View Patent ↗A method of reducing nitrogen oxides (NO x ) present in a lean gas stream comprising nitric oxide (NO) comprises the steps of: (i) net adsorbing NO per se from the lean gas stream in an adsorbent comprising palladium and a cerium oxide at below 200° C.; (ii) thermally net desorbing NO from the NO adsorbent in a lean gas stream at 200° C. and above; and (iii) catalytically reducing NO x on a catalyst other than the NO adsorbent with a reductant selected from the group consisting of a hydrocarbon reductant, a nitrogenous reductant, hydrogen and a mixture of any two or more thereof. A system for carrying out such a method is also disclosed.
1. A method of reducing nitrogen oxides (NO x ) present in a lean gas stream comprising nitric oxide (NO), which method comprising the steps of:
(i) net adsorbing NO per se from the lean gas stream in an adsorbent comprising palladium and a cerium oxide at below 200° C.;
(ii) thermally net desorbing NO from the NO adsorbent in a lean gas stream at 200° C. and above; and
(iii) catalytically reducing NO x on a catalyst other than the NO adsorbent with a reductant selected from the group consisting of a hydrocarbon reductant, a nitrogenous reductant, hydrogen and a mixture of any two or more thereof.
2. A method according to claim 1 , wherein the NO adsorbent consists of palladium and a cerium oxide or a mixed oxide or a composite oxide containing cerium and at least one other transition metal.
3. A method according to claim 1 , wherein the NO adsorbent includes palladium dispersed on ceria or a mixed oxide or a composite oxide containing cerium and at least one other transition metal.
4. A method according to claim 1 , wherein the NO adsorbent is combined with a thermally regenerable NO x adsorbent for net adsorbing NO x at 200° C. and below and net desorbing NO x at 250° C. and above, the thermally regenerable NO x adsorbent comprising platinum and a metal oxide.
5. A method according to claim 1 , wherein step (ii) is done in a net lean gas stream.
6. A method according to claim 1 , wherein step (iii) is done in a net lean gas stream.
7. A method according to claim 1 , wherein the step (iii) catalyst is a selective catalytic reduction (SCR) catalyst and the reductant is the nitrogenous reductant.
8. A system for reducing nitrogen oxides (NO x ) in a lean gas stream comprising nitric oxide (NO), the system comprising an adsorbent for adsorbing NO per se from the lean gas stream at below 200° C., means for contacting the NO adsorbent with a lean gas stream at 200° C. and above thereby to desorb NO from the NO adsorbent and means for reducing NO desorbed from the NO adsorbent comprising a NO reduction catalyst and a source of reductant selected from the group consisting of a hydrocarbon reductant, a nitrogenous reductant, hydrogen and mixtures of any two or more thereof, wherein the NO adsorbent comprises palladium and a cerium oxide.
9. A system according to claim 8 , wherein the NO adsorbent consists of palladium and a cerium oxide or a mixed oxide or a composite oxide containing cerium and at least one other transition metal.
10. A system according to claim 8 , wherein the NO adsorbent includes palladium dispersed on ceria or a mixed oxide or a composite oxide containing cerium and at least one other transition metal.
11. A system according to claim 9 , wherein the at least one other transition metal in the mixed oxide or composite oxide is zirconium.
12. A system according to claim 8 , wherein the palladium loading in the NO adsorbent is from 0.1 to 200 g/ft −3 .
13. A system according to claim 8 , wherein the NO adsorbent is combined with a thermally regenerable NO x adsorbent for net adsorbing NO x at below 200° C. and net desorbing NO x at 250° C. and above, the thermally regenerable NO x adsorbent comprising platinum and a metal oxide.
14. A system according to claim 13 , wherein the thermally regenerable NO x adsorbent comprises platinum dispersed on alumina, ceria and/or zirconia.
15. A system according to claim 13 , wherein the NO adsorbent is present in an underlayer and the thermally regenerable NO x adsorbent is present in a layer overlying the underlayer.
16. A system according to claim 8 , wherein the NO reduction catalyst is a selective catalytic reduction catalyst and the reducing agent is a nitrogenous reducing agent.
17. A system according to claim 8 which is an exhaust system for a lean-burn internal combustion engine, wherein the NO adsorbent is located upstream of the NO reduction catalyst or is co-located with the NO reduction catalyst and wherein the exhaust system comprises means for introducing the reductant into an exhaust gas either between the NO adsorbent and the NO reduction catalyst or upstream of both the NO adsorbent and the NO reduction catalyst.
18. An exhaust system according to claim 17 , wherein the NO adsorbent is associated with an upstream end of a particulate filter.
19. An exhaust system according to claim 18 , wherein the NO adsorbent is coated on an inlet end of the particulate filter, and wherein the reductant introducing means is located downstream of the filter and the NO reduction catalyst is located downstream of the reductant introducing means.
20. An exhaust system according to claim 19 , wherein the NO adsorbent is disposed on a separate substrate located upstream of the particulate filter wherein the particulate filter catalyst is the SCR catalyst.