Thermal management of hybrid LNT/SCR aftertreatment during desulfation
View Patent ↗In an exhaust aftertreatment system comprising a NOx adsorber-catalyst followed by an SCR catalyst, means are provided for preventing the SCR catalyst from becoming heated to near the same peak temperatures as the NOx adsorber-catalyst during desulfation. In one embodiment, the means is a thermal mass between the NOx adsorber-catalyst and the SCR catalyst. In another embodiment, the means is a valve configured to selectively divert exhaust leaving the NOx adsorber-catalyst from the SCR catalyst. In a method of the invention, the NOx adsorber-catalyst temperature is cycled during desulfation. The peaks of the cycles are within an appropriate temperature range for desulfating the NOx adsorber-catalyst, but the average temperature is below the temperature range at which the SCR catalyst is damaged. The temperature peaks are damped as they travel from the NOx adsorber-catalyst to the SCR, whereby the SCR experiences much lower peak temperatures than the NOx adsorber-catalyst.
1. An exhaust aftertreatment system, comprising:
a NOx adsorber-catalyst configured to treat an exhaust flow;
an SCR catalyst configured to adsorb ammonia released by the NOx adsorber-catalyst during denitration and to subsequently use the ammonia to reduce NOx in the exhaust;
a particulate filter located upstream of the NOx adsorber-catalyst or downstream of the SCR catalyst; and
means for preventing the SCR catalyst from becoming heated to near the same peak temperatures as the NOx adsorber-catalyst during desulfation of the NOx adsorber-catalyst, the means being disposed between the NOx adsorber-catalyst and the SCR catalyst;
wherein the means comprises a flow diverter configured to prevent the exhaust leaving the NOx adsorber-catalyst from entering the SCR catalyst during desulfation of the NOx adsorber-catalyst.
2. A method of desulfating an NOx adsorber-catalyst in an exhaust aftertreatment system comprising an NOx adsorber-catalyst followed by an SCR catalyst, comprising:
in a first step, providing a flow of gas heated to at least about 650° C. to the NOx adsorber-catalyst, wherein the flow of gas passes through the NOx adsorber-catalyst and then the SCR catalyst;
maintaining the flow until a time after the NOx adsorber-catalyst has been heated by the gas to at least about 650° C., but terminating the flow before the SCR catalyst has reached a temperature of 550° C.;
in a second step, providing a second flow of gas at a temperature of about 500° C. or less to the NOx adsorber-catalyst, wherein the second flow of gas passes through the NOx adsorber-catalyst and then the SCR catalyst;
maintaining the second flow until a time after the NOx adsorber-catalyst has been cooled by the gas to a temperature at or below about 550° C.;
repeating the first and second steps at least several times to complete the desulfation.
3. The method of claim 2 , wherein there is a device between the NOx adsorber-catalyst and the SCR catalyst, the device having a substantial thermal mass in comparison to the SCR catalyst.
4. The method of claim 3 , wherein the thermal mass is a particulate filter.
5. The method of claim 3 , wherein exhaust aftertreatment system comprises a particulate filter either upstream of the NOx adsorber-catalyst or downstream of the SCR catalyst.
6. A method of desulfating an NOx adsorber-catalyst in an exhaust aftertreatment system comprising an NOx adsorber-catalyst followed by an SCR catalyst, comprising:
cycling the temperature of the NOx adsorber-catalyst;
creating a reducing environment in the NOx adsorber-catalyst during portions of the cycles where the NOx adsorber-catalyst is at temperatures effective for desulfation;
wherein the cycles have peak temperatures in a range effective for desulfation and an average temperature that is at least 100° C. lower;
wherein peak temperature reached by the SCR catalyst during the cycles is at least 100° C. lower than the peak temperature reached by the NOx adsorber-catalyst.