# Patent

## Title
Perovskite-type compounds for use in lean NOx traps

## Abstract

An exhaust aftertreatment system for a lean-burn engine may include a lean NOX trap that comprises a catalyst material. The catalyst material may remove NOX gases from the engine-out exhaust emitted from the lean-burn engine. The catalyst material may include a NOX oxidation catalyst that comprises a perovskite compound.

## Background
CROSS-REFERENCES TO RELATED APPLICATIONS
This Application claims the benefit of U.S. Provisional Application No. 61/160,523, filed on Mar. 16, 2009, the disclosure of which is hereby incorporated by reference in its entirety.


TECHNICAL FIELD
The technical field relates generally to exhaust aftertreatment systems and, more particularly, to a catalyst material for use in a lean NOX trap.
BACKGROUND
A lean-burn engine may be supplied with a lean mixture of air and fuel (oxygen-rich mixture) as a means to improve vehicle fuel economy. The engine-out exhaust emitted from such engines during periods of lean-burn operation may include a relatively high content of oxygen (O2), a relatively low content of carbon monoxide (CO) and unburned/partially-burned hydrocarbons (hereafter HC's), and small amounts of nitrogen oxides primarily comprised of NO and NO2 (collectively referred to as NOX gases). The concentration of several of these gaseous emissions, however, may need to be decreased to the greatest extent feasible before the engine-out exhaust is expelled to the atmosphere from the vehicle's tailpipe. To this end, an exhaust aftertreatment system may be installed downstream of the vehicle engine to control and reduce the various unwanted emissions and particulate matter contained in the engine-out exhaust. A typical exhaust aftertreatment system usually aspires to (1) oxidize CO into carbon dioxide (CO2), (2) oxidize HC's into CO2 and water (H2O), (3) convert NOX gases into nitrogen (N2) and O2, and remove any other unwanted matter.
Traditional catalytic converters outfitted with a three-way catalyst (TWC) have been implemented in many exhaust aftertreatment system designs. The TWO generally includes some combination of platinum group metals (PGM) that can simultaneously oxidize CO and HC's and reduce NOX gases. Catalytic converters of this kind have been known to function quite effectively when the engine operates with a stoichiometric mixture of air and fuel. This is because the engine-out exhaust generated from the combustion of a stoichiometric air/fuel mixture generally includes an appropriate balance of reductants (CO, HC's, and H2) and oxidants (O2) to concurrently reduce the NOX gases and oxidize any CO and NC's through various coupled catalytic reactions. But TWC-equipped catalytic converters are generally not able to efficiently reduce NOX gases when the engine operates with a lean mixture of air and fuel. The low levels of reductants and the high O2 content in the engine-out exhaust make such a reaction kinetically unfavorable in most instances.
A lean NOX trap, or LNT, is but one available option that may be employed in the exhaust aftertreatment system to help remove NOX gases contained in the engine-out exhaust of a lean-burn engine. A LNT generally operates by feeding the engine-out exhaust expelled from the lean-burn engine across and/or through an LNT catalyst material that exhibits NOX gas trapping and conversion capabilities. The LNT catalyst material oxidizes NO to NO2 and simultaneously traps or “stores” NO2 as a nitrate species when the lean-burn engine is combusting a lean mixture of air and fuel. The efficiency of NOX gas removal and storage may be enhanced, in some instances, by increasing the proportion of NO2 in the total NOX emission so as to reduce the oxidative demand (NO to NO2) on the LNT catalyst material. The NOX storage capacity of the LNT catalyst material, however, is not unlimited and at some point may need to be regenerated or purged of the NOX-derived nitrate compounds. The LNT catalyst material may be regenerated by momentarily switching the mixture of air and fuel supplied to the lean-burn engine from lean to rich. The resultant delivery of a rich-burn engine-out exhaust to the LNT catalyst material causes the NOX-derived nitrate compounds to become thermodynamically unstable which, in turn, triggers the release of NOX gases and regenerates future NOX storage sites. The liberated NOX gases are then reduced, largely to N2, by the excess reductants—such as CO, HC's and/or H2— present in the rich-burn engine effluents. The overall conversion efficiency of some LNTs, aided by the appropriate cycling between a lean and rich mixture of air and fuel, have been shown to remove more than 90% of NOX gases contained in the engine-out exhaust of lean-burn engines over lengthy periods of time.
A conventional LNT typically includes a canister with an inlet that receives the engine-out exhaust emitted from the lean-burn engine and an outlet that delivers the engine-out exhaust from the canister. The canister may house a support body that communicates the engine-out exhaust from the inlet to the outlet over a catalyst material. The catalyst material is typically a mixture of PGMs and an alkali or alkaline earth metal compound dispersed within a high surface-area washcoat. The mixture of PGMs includes platinum, which catalyzes the oxidation of NO and to some extent the reduction of NOX gases, and rhodium, which primarily catalyzes the reduction of NOX gases. The alkali or alkaline earth metal compound provides trap sites for the reversible storage of NO2 as a metal nitrate. Of these various materials dispersed in the washcoat, platinum is usually present in the greatest amount. One specific LNT catalyst material known to skilled artisans includes an alumina washcoat appropriately loaded with platinum, rhodium, and barium oxide. But the use of platinum group metals, especially the relatively large amounts of platinum, in conventional LNT catalyst materials is rather expensive. Platinum has also shown a tendency to lose some catalytic activity when exposed to engine-out exhaust at higher operating temperatures.
The incorporation of a lean NOX trap into an exhaust aftertreatment system for a lean-burn engine is thus an attractive, yet challenging, option for removing unwanted emissions including NOX gases from the engine-out exhaust. Such technology is constantly in need of innovative developments and contributions that can help advance to this and other related fields of technological art.
SUMMARY OF EXEMPLARY EMBODIMENTS
An exhaust aftertreatment system for a lean-burn engine may include a lean NOX trap that comprises a catalyst material. The catalyst material may remove NOX gases from a flow of engine-out exhaust emitted from the lean-burn engine. The catalyst material may include a NOX oxidation catalyst that comprises a perovskite compound.
Other exemplary embodiments of the invention will become apparent from the detailed description provided hereinafter. It should be understood that the detailed description and specific examples, while disclosing exemplary embodiments of the invention, are intended for purposes of illustration only and are not intended to limit the scope of the invention.



BRIEF DESCRIPTION OF THE DRAWINGS
Exemplary embodiments of the invention will become more fully understood from the detailed description and the accompanying drawings, wherein:
FIG. 1 is a schematic illustration of an exhaust aftertreatment system that includes a lean NOX trap according to one embodiment of the invention.
FIG. 2 is a perspective and partial cut-away view of an exemplary embodiment of a lean NOX trap that may be included in the exhaust aftertreatment system illustrated in FIG. 1.
FIG. 3 is a partial magnified view of the lean NOX trap shown in FIG. 2 that depicts, in an idealized manner, a catalyst material carried by the support body according to one embodiment of the invention.
FIG. 4 is a partial magnified view of the lean NOX trap shown in FIG. 2 that depicts, in an idealized manner, a catalyst material carried by the support body according to one embodiment of the invention.
FIG. 5 is a graph that shows the NOX conversion profile of an exemplary catalyst material under a variety of operation conditions as well as the NOX conversion profile of a conventional LNT catalyst material.



DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS
The following description of the embodiment(s) is merely exemplary in nature and is in no way intended to limit the invention, its application, or uses.
A lean-burn engine that combusts a lean mixture of air and fuel may be fitted with an exhaust aftertreatment system to help reduce the concentration of certain unwanted emissions and particulate matter from its engine-out exhaust. Some gaseous emissions contained in the engine-out exhaust that may need to be removed include CO, HC's, and NOX gases. Catalytic converters that employ PGM metals have long been used to address this need. But the nature of the engine-out exhaust produced during lean-burn engine operation poses certain challenges for traditional catalytic converters. One specific challenge is that the relatively high content of O2 and the relatively low content of CO and HC's in the engine-out exhaust renders the reaction kinetics for the conversion of NOX gases to N2 over PGM metals quite unfavorable.
A lean NOX trap may therefore be incorporated into the exhaust aftertreatment system to help remove NOX gases from a flow of engine-out exhaust emanating from the lean-burn engine. The lean NOX trap may include a support body that comprises a surface over which at least a portion of the flow of engine-out exhaust passes. The support body may be a monolithic honeycomb structure, a wire mesh, a packed bed of many support particles, or any other feasible design. A catalyst material that comprises a NOX oxidation catalyst, a NOX storage catalyst, and a NOX reduction catalyst may be carried by the at least one surface of the support body. The NOX oxidation catalyst may include a perovskite compound. The use of platinum in the catalyst material of the lean NOX trap may, if desired, be substantially diminished or altogether eliminated as a corollary of the perovskite compound's NOX oxidation capabilities under lean-burn engine conditions.
An exemplary and schematic illustration of the relevant parts of an exhaust aftertreatment system 10 for a vehicle powered by a lean-burn engine 12 is shown in FIG. 1. The exhaust aftertreatment system 10 receives a flow of engine-out exhaust 14 from the lean-burn engine 12 and communicates a flow of treated exhaust 16 towards a vehicle tailpipe 18 for expulsion to the atmosphere. The exhaust aftertreatment system 10 may include a lean NOX trap 20 to help remove NOX gases from the flow of engine-out exhaust 14. A variety of other devices, while not expressly shown in FIG. 1, may also be included in the exhaust aftertreatment system 10 to supplement the lean NOX trap's 20 NOX removal capabilities and/or remove other unwanted gaseous emissions and/or suspended particulate matter. These devices include, for example, a diesel oxidation catalyst, a TWC-based catalytic converter, and/or a diesel particulate filter. Other devices may also be located upstream or downstream of the exhaust aftertreatment system 10. An exhaust gas recirculation line may, for example, recirculate a portion of the flow of engine-out exhaust 14 in known fashion to help lower the NOX gas emissions from the lean-burn engine 12. As another example, at least a portion of the engine-out exhaust 14 may be directed through a turbocharger turbine to increase the intake pressure of the air supplied to the lean-burn engine 12. Skilled artisans will undoubtedly know of, and understand, these and the many other devices that may be included in and around the exhaust aftertreatment system 10.
The lean-burn engine 12 may be any engine that is constructed and designed to combust, at least some of the time, a lean mixture of air and fuel 22 (hereafter “lean A/F mixture”). The lean-burn engine 12 may be coupled to an inlet manifold 24 and an exhaust manifold 26. Some particular examples of engines that may be employed as the lean-burn engine 12 include, but are not limited to, a diesel engine, a spark ignition direct injection engine (SIDI), and a homogeneous charge compression ignition engine (HCCI). The general construction and functionality of these types of engines are known to skilled artisans and, as a result, need not be discussed in detail here. Other known engine types that are designed and/or constructed to operate in a lean-burn state may also be used.
The inlet manifold 24 may supply the lean A/F mixture 22 to the lean-burn engine 12 for combustion. The lean A/F mixture 22 generally contains more air than is stoichiometrically necessary to combust the fuel. For instance, the air to fuel mass ratio of the lean A/F mixture 22 may be greater than 14.6-14.8, which is the approximate stoichiometric air/fuel mass ratio range of many gasoline and diesel fuels. Indeed, in many instances, the air to fuel mass ratio of the lean A/F mixture 22 usually lies somewhere in the range of about 20-65 depending on the operating demands of the vehicle. The lean A/F mixture 22, however, may be momentarily and periodically switched to a rich mixture of air and fuel 28 (hereafter “rich A/F mixture”) for any of a number of reasons. The air to fuel mass ratio of the rich A/F mixture 28 may be stoichiometric or less, and generally lies somewhere in the range of about 12-14. It should be noted that FIG. 1 identifies separate feeds of the lean A/F mixture 22 and the rich A/F mixture 28 for ease of description only. In actuality, the vehicle is most likely outfitted with a fuel injection system, an air induction system, and an A/F ratio control system that can accurately control the amount of air and fuel that is mixed together and simultaneously fed to the intake manifold 24. Reference to the lean A/F mixture 24 and the rich A/F mixture 28 is therefore intended as a description of the current state of the mixture of air and fuel being fed to the lean-burn engine 12 and not necessarily to distinct feed streams of air and fuel that are separately piped to the intake manifold 24.
The lean A/F mixture 22 or the rich A/F mixture 28, once introduced to the lean-burn engine 12, may be combusted to produce energy for powering the vehicle and engine-out exhaust comprised of combustion products and unreacted air and/or fuel. The engine-out exhaust generated from the combustion of the lean A/F mixture 22 generally comprises oxygen, carbon dioxide, carbon monoxide, HC's, NOX gases, possibly some particulate matter, and the balance nitrogen and water when the fuel is gasoline or diesel fuel. The NOX gas constituency of the engine-out exhaust may fluctuate between 50 and 1500 ppm and typically comprises greater than 90 wt. % NO and less than 10 wt. % NO2. The O2 content, which is relatively high, and the CO and HC's content, which are relatively low, promote an oxidizing environment in the engine-out exhaust. The engine-out exhaust generated from the combustion of the rich A/F mixture 28, on the other hand, generally comprises a higher content of CO and HC's and a much lower content of O2 than the engine-out exhaust generated from the combustion of the lean A/F mixture 22. This shift in reductant and oxygen content in the engine-out exhaust, relative to that produced by the lean A/F mixture 22, promotes a reducing environment in the engine-out exhaust. A reducing environment can, of course, be induced and/or enhanced in the engine-out exhaust through other procedures not discussed here. The engine-out exhaust produced from either the lean A/F mixture 22 or the rich A/F mixture 28, which can reach temperatures of up to about 900° C., may ultimately be expelled from the lean-burn engine 12 through the exhaust manifold 26 as the flow of engine-out exhaust 14.
The lean NOX trap 20, as shown best in FIG. 2, may comprise a canister 30 that includes a hollow chamber 32, an inlet 34, and an outlet 36. The hollow chamber 32 may be cylindrical in shape, as shown, or may assume any other desired geometry. The inlet 34 may fluidly communicate with the exhaust manifold 26 to receive the flow of engine-out exhaust 14. The outlet 36 may communicate the flow of engine-out exhaust 14 downstream of the lean NOX trap 20 for further treatment, if needed, and the eventual discharge from the exhaust aftertreatment system 10 as the flow of treated exhaust 16. The inlet 34 and the outlet 36 may be located on opposite ends of the hollow chamber 32, as shown, or in some other workable configuration. The canister 30 may be fabricated from stainless steel and joined with suitable piping to form a continuous flow path for communicating the flow of engine-out exhaust 14 through the hollow chamber 32 from the inlet 34 to the outlet 36 along a flow axis A.
A support body 38 that includes an inlet end 40 and an outlet end 42 may be housed in the hollow chamber 32. The inlet end 40 and the outlet end 42 of the support body 38 may be near the inlet 34 and the outlet 36 of the canister, respectively. The support body 38, as shown in partial cross-section, may be a monolithic honeycomb structure that fits tightly inside the hollow chamber 32. A plurality of flow-through cells 44, often numbering in the hundreds, may extend from the inlet end 40 to the outlet end 42 of the support body 38 in general parallel alignment with the flow axis A. Each of the flow-through cells 44 may be at least partially defined by a wall surface 46, shown best in FIG. 3, over which a respective portion of the flow of engine-out exhaust 14 passes while traversing the support body 38. A tight fit between the support body 38 and the hollow chamber 32 ensures that the flow-through cells 44 communicate most of the flow of engine-out exhaust 14 from the inlet 34 to the outlet 36 of the canister 30. The support body 38 may be formed from a ceramic or other material capable of withstanding the potentially high temperatures often associated with the flow of engine-out exhaust 14.
A catalyst material 48, as shown best in FIG. 3, may be carried on the wall surface 46 of one or more of the plurality of flow-through cells 44 to facilitate the removal of NOX gases from the flow of engine-out exhaust 14. The catalyst material 48 may comprise a carrier material 50 loaded with a NOX oxidation catalyst 52, a NOX storage catalyst 54, and a NOX reduction catalyst 56. Each of the catalysts 52, 54, 56, as shown, may be substantially homogeneously mixed and evenly dispersed on the carrier material 50. But other catalyst loading configurations are certainly possible. The catalysts 52, 54, 56 may, as an alternative option, be dispersed on the carrier material 50 so that a higher concentration of the NOX oxidation catalyst 52 is present near the inlet end 40 of the support body 38 and a higher concentration of the NOX reduction catalyst 56 is present near the outlet end 42.
The carrier material 50 may be directly washcoated onto the wall surface 46 of the one or more flow-through cells 44. The carrier material 50 may completely or partially cover the wall surface 46, and may exhibit a relatively high surface area with many loading or dispersion sites for accommodating the NOX oxidation, storage, and reduction catalysts 52, 54, 56. The surface area of the carrier material 50 may range, for example, from about 20 m2/gram to about 300 m2/gram. In one embodiment, the carrier material 50 may comprise a high-surface area mixed cerium and zirconium oxide material (CeO2—ZrO2). Such a material offers not only a high-surface area but also some additional relevant functionality. A variety of CeO2—ZrO2 materials, for instance, have demonstrated some ability to enhance the storage of NO2 at low temperatures, stabilize certain catalysts so that loading requirements can be reduced, and promote the water-gas shift reaction that converts CO and H2O into CO2 and H2. The carrier material 50 may also comprise alumina (Al2O3) or a zeolite either alone or in combination with a CeO2—ZrO2 material.
The NOX oxidation catalyst 52 may comprise a perovskite compound defined by the general formula ABO3 where “A” and “B” are complimentary cations of different sizes that coordinate with oxygen anions. A unit cell of the perovskite compound's ABO3 crystal structure may feature a cubic closest packing arrangement with the “A” cation, which is generally the larger of the two cations, centrally located and surrounded by eight “B” cations located in the octahedral voids of the packing arrangement. The “A” and “B” cations in such a packing arrangement respectively coordinate with twelve and six oxygen anions. The unit cell of the perovskite compounds ABO3 crystal structure, however, is not necessarily limited to a cubic closest packing arrangement. Certain combinations of the “A” and “B” cations may indeed deviate from the cubic closest packing arrangement and assume, for instance, an orthorhombic, rhombohedral, or monoclinic packing structure. Small amounts of the “A” and “B” cations of the perovskite compound may also be substituted with different, yet similar sized, “A” and “B” cations such that the perovskite compound is represented by the general formula A1XA21-XBO3, where X≦1.
A great many perovskite compounds are possible for use as the NOX oxidation catalyst 52 since no fewer than 27 cations may be employed as the “A” cation and no fewer than 36 cations may be employed as the “B” cation. A listing of the cations most frequently employed as the “A” cation includes those of calcium (Ca), strontium (Sr), barium (Ba), bismuth (Bi), cadmium (Cd), cerium (Ce), lead (Pb), yttrium (Y), and lanthanum (La) while a listing of the cations most commonly employed as the “B” cation includes those of cobalt (Co), titanium (Ti), zirconium (Zr), niobium (Nb), tin (Sn), cerium (Ce), aluminum (Al), nickel (Ni), chromium (Cr), manganese (Mn), copper (Cu), and iron (Fe). The NOX oxidation catalyst 52 may include only a single perovskite compound or a mixture of two or more different perovskite compounds. Some specific and exemplary perovskite compounds that may constitute all or part of the NOX oxidation catalyst 52 include LaCoO3, La0.9Sr0.1CoO3, LaMnO3, and La0.9Sr0.1MnO3.
The perovskite compound can catalytically oxidize NO to NO2 when exposed to the flow of engine-out exhaust 14 just as efficiently as conventional PGM metals such as platinum. While not wishing to be bound by theory, it is believed that the perovskite compound donates an oxygen anion to an NO molecule to enable the formation of NO2 while temporarily forming an oxygen vacancy in its crystal structure. Oxygen contained in the flow of engine-out exhaust 14 then disassociates to fill that oxygen vacancy and possibly oxidize an additional NO molecule. The ability of the perovskite compound(s) to efficiently oxidize NO to NO2 may significantly diminish or altogether eliminate the need to include platinum in the catalyst material 48. The catalyst material 48 may, as a result, include only trace amounts of platinum or no platinum at all.
The NOX storage catalyst 54 and the NOX reduction catalyst 56 may be any suitable material known to skilled artisans. The NOX storage catalyst 54 may generally comprise any compound that can trap and store NO2 in the oxidizing environment promoted by the combustion of the lean A/F mixture 22 and, conversely, release NOX gases in the reducing environment promoted, for example, by the combustion of the rich A/F mixture 28. A number of alkali or alkaline earth metal compounds operate in such a fashion through the reversible formation of a nitrate species and, as such, may constitute all or part of the NOX storage catalyst 54. Some specific and exemplary alkali or alkaline earth metal compounds that may be employed include BaO, BaCO3, and K2CO3. The NOX reduction catalyst 56 may generally comprise any compound that can reduce NOX gases in the reducing environment promoted, for example, by the combustion of the rich A/F mixture 28. Rhodium is an example of a material that may constitute all or part of the NOX reduction catalyst 56.
Other materials may also be dispersed on the carrier material 50 that have other catalytic functions or serve some other practical or performance-related purpose. Palladium, for example, can help oxidize any residual HC's and CO present in the flow of engine-out exhaust 14 as well as slow the rate of perovskite sulfur poisoning that may occur when sulfur-containing fuels are combusted in the lean-burn engine 12.
The NOX oxidation, storage, and reduction catalysts 52, 54, 56 work together to convert NOX gases largely into N2 in the one or more flow-through cells 44 through a multi-part reaction mechanism. The conversion of NOX gases to N2 begins when the NOX oxidation catalyst 52 oxidizes NO contained in the flow of engine-out exhaust 14 into NO2. This oxidation reaction occurs when the lean-burn engine 12 receives and combusts the lean A/F mixture 22 which, in turn, renders the flow of engine-out exhaust 14 more favorable to oxidation. At the same time the NOX storage catalyst 54 traps and stores both the originally-present and newly-generated NO2 as a nitrate species. The oxidation of NO and the storage of NO2 can occur until the NOX storage catalyst 54 reaches its NOX storage capacity. The NO2-derived nitrate species stored in the NOX storage catalyst 54 may then be removed to permit the continued removal of NOX gases from the flow of engine-out exhaust 14. The release of NOX gases from the NOX storage catalyst 54, and the simultaneous regeneration of future NO2 storage sites, may be accomplished by momentarily supplying the lean-burn engine 12 with the rich A/F mixture 28 for combustion instead of the lean A/F mixture 22. This fresh injection of additional fuel makes the flow of engine-out exhaust 14 more favorable to reduction and, as a result, renders the NOX-derived nitrate compounds thermodynamically unstable causing the liberation of NOX gases. Then, to complete the conversion of NOX gases to N2, the NOX reduction catalyst 56 reduces the liberated NOX gases largely to N2 in the presence of excess reductants contained in the flow of the engine-out exhaust 14. The excess reductants that participate in this reaction include CO, HC's and H2. Once the regeneration of the NOX storage catalyst 54 is satisfactorily achieved, the lean A/F mixture 22 may be restored to the lean-burn engine 12 and the cycle repeated. The catalyst material 48 can thus cumulatively strip a substantial portion of the NOX gases from the flow of engine-out exhaust 14, in exchange for N2, while the engine-out exhaust 14 navigates the flow-through cells 44 from the inlet end 40 to the outlet end 42 of the support body 38.
The amount of the NOX oxidation, storage, and reduction catalysts 52, 54, 56 that are loaded onto the carrier material 50 can vary based on a number of factors. But in one embodiment of the catalyst material 48, in which the loading of each material is reported in grams per liter of combined volume of the flow-through cells 44 in which the catalyst material 48 is located, the carrier material 50 may be present in an amount that ranges from about 100 g/L to about 200 g/L, the NOX oxidation catalyst 52 may be present in an amount that ranges from about 50 g/L to about 150 g/L, the NOX storage catalyst 54 may be present in an amount that ranges from about 10 g/L to about 50 g/L, and the NOX reduction catalyst 56 may be present in an amount that ranges from about 0.10 g/L to about 0.30 g/L. Palladium, if included, may be present in an amount that ranges from about 1.0 g/L to about 5.0 g/L. A specific example of the catalyst material 48 may comprise about 120 g/L of CeO2—ZrO2 with a Ce/Zr mol ratio of 75/25 as the carrier material 50, about 100 g/L of La0.9Sr0.1MnO3 as the NOX oxidation catalyst 52, about 30 g/L of BaO as the NOX storage catalyst 54, about 0.18 g/L of rhodium as the NOX reduction catalyst 56, and about 1.8 g/L of palladium. Other loading requirements may of course be employed, especially if some other combination of catalysts is used to construct the catalyst material 48 or if other materials are included therein. Skilled artisans will nonetheless be capable of determining the appropriate loading amounts of the carrier material 50 and the catalysts 52, 54, 56 that may be included in the catalyst material 48 through experience and/or routine experimentation.
An alternative embodiment of the catalyst material, depicted as numeral 48′, is shown in FIG. 4. This embodiment is similar in many respects to the embodiment shown in FIG. 3 and, as such, similar reference numerals are used to designate similar materials and/or structural details. The catalyst material 48′ of this embodiment includes the same catalysts 52, 54, 56 and removes NOX gases from the flow of engine-out exhaust 14 by way of the same catalytic mechanisms explained with respect to the catalyst material 48 described before. One difference here, however, is that the catalyst material 48′ embodies a multi-layer construction.
The catalyst material 48′ of this embodiment, as shown, may comprise a first carrier material 50a′ adjacent to the wall surface 46 of the one or more flow-through cells 44 and a second carrier material 50b′ overlying the first carrier material 50a′. The first and second carrier materials 50a′, 50b′ may be discrete material layers that have the same or different compositions. The NOX oxidation catalyst 52 may be dispersed on both the first and the second carrier materials 50a′, 50b′ to make it available for NO oxidation throughout the catalyst material 48′. The NOX storage and reduction catalysts 54, 56 may be dispersed on the first carrier material 50a′ to perform their respective catalytic functions. The absence of the NOX storage and reduction catalysts 54, 56 from the second carrier material 50b′, while not mandatory, can help promote the catalytic reactions taking place in the catalyst material 48′ and also help manage the movement of NO, NO2, and N2 between the catalyst material 48′ and the flow of engine-out exhaust 14. Palladium may also be included in either of the first or second carrier materials 50a′, 50b′ if desired. But in some instances, as shown here, palladium may only need to be dispersed on the second carrier layer 50b′ in order to sufficiently perform its intended functions. It should be noted that the exposure of the NOX oxidation, storage, and reduction catalysts 52, 54, 56, as well as the palladium, if present, to the flow of engine-out exhaust 14 is not significantly inhibited by the multi-layer construction of the catalyst material 48′. This is because the portion of the flow of engine-out exhaust 14 that traverses each flow-through cell 44 can readily permeate and diffuse through both the first and second carrier materials 50a′, 50b′ with little resistance.
The amount of the NOX oxidation, storage, and reduction catalysts 52, 54, 56 that are loaded onto the first and second carrier materials 50a′, 50b′ can vary based on a number of factors. The total amounts of materials used to make the catalyst material 48′ of this embodiment may generally be the same as the catalyst material 48 described earlier. A specific example of the catalyst material 48′ may comprise a mixture of about 40 g/L of Al2O3 and about 60 g/L of CeO2—ZrO2 (Ce/Zr mol ratio of 75/25) as the first carrier material 50a′ and about 90 g/L of Al2O3 as the second carrier material 50b′ (total of 190 g/L of carrier material in the catalyst material 48′). The catalyst material 48′ may also comprise about 30 g/L of La0.9Sr0.1MnO3 dispersed on each of the first and carrier materials 50a′ 50b′ to serve as the NOX oxidation catalyst 52 (total of about 60 g/L of NOX oxidation catalyst in the catalyst material 48′), about 10 g/L of BaO and about 0.18 g/L of rhodium dispersed on first carrier material 50a′ to serve as the NOX storage catalyst 54 and the NOX reduction catalyst 56, respectively, and about 3.5 g/L of palladium dispersed on the second carrier material 50b′, where the loading of each material is once again reported in grams per liter of combined volume of the flow-through cells 44 in which the catalyst material 48′ is located. Other loading requirements, like before, may also be employed.
A method of using the lean NOX trap 20 comprising the catalyst material 48, 48′ in the exhaust aftertreatment system 10, or variations of the exhaust aftertreatment system 10, should be apparent to a skilled artisan given the above disclosure. The method of use includes supplying the lean A/F mixture 22 to the lean-burn engine 12 for combustion by way of the inlet manifold 24. The lean A/F mixture 22 combusts inside the lean-burn engine 12 and the flow of engine-out exhaust 14 is communicated from the exhaust manifold 26 to the exhaust aftertreatment system 10. The lean NOX trap 20, which may embody the specific construction described above, receives the flow of engine-out exhaust 14 at the inlet 34 of the canister 30. The flow of engine-out exhaust 14 passes from the inlet 34 to the outlet 36 and traverses the support body 38 through the plurality flow-through cells 44. The catalyst material 48, 48′ carried on the wall surface 46 of one or more of the plurality of flow-through 44 cells oxidizes NO to NO2 and stores NO2 as a nitrate species. The method of use then includes supplying the rich A/F mixture 28 to the lean-burn engine 12 to regenerate the catalyst material 48, 48′. The introduction of rich-burn engine effluents into the flow of engine-out exhaust 14 causes the release of NOX gases from the catalyst material 48, 48′ and the reduction of those NOX gases largely to N2. The newly-generated N2 is captured by the flow of engine-out exhaust 14 and carried out of the canister 30 through the outlet 36. Next, the method of use includes ceasing the supply of the rich A/F mixture 28 to the lean-burn engine 12 and reinstating the flow of the lean A/F mixture 22.
EXAMPLE
A specific and exemplary embodiment of the catalyst material includes a CeO2—ZrO2 carrier material loaded with La0.9Sr0.1MnO3 as the NOX oxidation catalyst, BaO as the NOX storage catalyst, rhodium as the NOX reduction catalyst, and palladium.
A quantity of La0.9Sr0.1MnO3 was prepared by a citric acid method. First, appropriate amounts of La(NO3)3.6H2O, 50% Mn(NO3)2 solution, and Sr(NO3)2 were dissolved in distilled water with citric acid monohydrate. Citric acid was then added to the solution in 10 wt. % excess to ensure complete complexation of the metal ions. The solution was stirred for 1 hour at room temperature. Next, the solution was heated to 80° C. under continuous stirring to slowly evaporate the water until the solution became a viscous gel and started evolving NO/NO2 gases. The gel was then placed overnight in an oven set at 90° C. The resulting spongy material was crushed and calcined at 700° C. for about 5 hours in static air to form the perovskite oxide.
A quantity of CeO2—ZrO2 loaded with Pd—Rh and BaO was prepared by a conventional incipient wetness impregnation method. Pursuant to this method, Pd(NO3)2, Rh(NO3)3, and Ba(CH3COO)2 were co-impregnated onto CeO2—ZrO2 (Ce/Zr mol ratio of 75/25) to give a loading of 20 wt. % BaO, 1.6 wt. % Pd, and 0.16 wt. % Rh. The Pd—Rh/BaO/CeO2—ZrO2 material was then dried at 120° C. overnight and, afterwards, calcined at 550° C. for about 5 hours.
A slurry of the La0.9Sr0.1MnO3 and the Pd—Rh/BaO/CeO2—ZrO2 was then ball-milled together for about 18 hours. The pH of the slurry was maintained at approximately 9.0 by adding aqueous ammonia as needed. After ball-milling, the slurry was washcoated onto a monolithic honeycomb core sample. The core sample had a length of 1 inch, a diameter of 0.75 inches, and a flow-through cell density of about 600 flow-through cells per square inch with each cell having a wall thickness of about 0.003 inches. The targeted total loading for the catalyst material was 250 g/L with 30 g/L BaO, 100 g/L La0.9Sr0.1MnO3, 1.8 g/L Pd, 0.18 g/L Rh, and the balance CeO2—ZrO2, where the measurement of L refers to the total flow-through volume available for gas transport through the core sample. After washcoating, the catalyst material was dried and calcined at 550° C. for about 5 hours in static air.
The catalyst material was then evaluated after being hydrothermally pre-treated in an oven at 750° C. with 10 wt. % H2O/air for about 72 hours. The monolithic honeycomb core sample was tested in a vertical quartz tubular reactor operated at atmospheric pressure. A gas manifold coupled to the reactor included three banks of flow controllers that provided various gases to the reactor. The first bank, representing a rich feed, provided a feed gas that contained 1 mol % H2, 3 mol % CO, and the balance N2 at a total flow rate of 1.0 L/min. The second bank, representing a lean feed, provided a feed gas that contained 10 mol % O2 and the balance N2 at a total flow rate of 1.0 L/min. A solenoid valve cycled the flow of feed gas to the reactor at a frequency of 60 seconds from the second bank (lean) and 5 seconds from the first bank (rich). The third bank, which was not cycled, provided a feed gas at a flow rate of 2 L/min that contained NO, CO2, and N2 in mol percent proportions generally consistent with a diesel engine exhaust gas composition. The total flow rate to the reactor was thus 3 L/min (on a dry basis) corresponding to a space velocity of 50,000 h−1. The following table summarizes the feed gas testing conditions.










Model Gas Component Table












Lean Condition
Rich Condition

















NO
200
ppm
200
ppm



O2
10
mol %
0
mol %



H2O
10
mol %
10
mol %



CO2
10
mol %
10
mol %



H2
0
mol %
1
mol %



CO
0
mol %
3
mol %











N2
balance
balance













Duration
60
seconds
5
seconds



Space Velocity
50,000
h−1
50,000
h−1










The overall NOX conversion profile of the catalyst material when subjected to various gas feed temperatures in the reactor is shown as line A in FIG. 5. The NOX conversion data was calculated by the following formula using the concentrations of NO and NO2 as reported by an FTIR analyzer.




  
    x
    ⁡
    
      (
      %
      )
    
  
  =
  
    
      
        [
        
          
            Average
            ⁢
            
              
            
            ⁢
            of
            ⁢
            
              
            
            ⁢
            inlet
            ⁢
            
              
            
            ⁢
            
              (
              
                NO
                x
              
              )
            
          
          -
          
            Average
            ⁢
            
              
            
            ⁢
            of
            ⁢
            
              
            
            ⁢
            outlet
            ⁢
            
              
            
            ⁢
            
              (
              
                NO
                x
              
              )
            
          
        
        ]
      
      
        Average
        ⁢
        
          
        
        ⁢
        of
        ⁢
        
          
        
        ⁢
        inlet
        ⁢
        
          
        
        ⁢
        
          (
          
            NO
            x
          
          )
        
      
    
    ×
    100
  




The NOX conversion profile of a commercial LNT catalyst loaded on the same type of monolithic honeycomb core structure, when subjected to the same reactor conditions, is shown as line B. The commercial catalyst included a PGM catalyst loading of 2.06 g/L (1.6 g Pt/0.28 g Pd/0.18 g Rh) where the measurement of L, like before, refers to the total flow-through volume available for gas transport through the core sample. As shown in FIG. 5, the performance of the catalyst material with La0.9Sr0.1MnO3 is thus quite comparable to that of the commercial LNT catalyst that includes a relatively large amount of platinum.

FIG. 5 also shows the NOX conversion profiles of the catalyst material after sulfur loading and after desulfation. Sulfur was deposited on the catalyst material by first supplying the reactor with the lean feed gas (from the second bank) additionally containing 8 ppm SO2 for 2 hours at 300° C. This resulted in a sulfur exposure of 1 gram sulfur per liter of catalyst material. The sulfur-loaded catalyst material was then evaluated in the reactor similar to before. The NOX conversion profile of the sulfur-loaded catalyst material is shown as line C. Desulfation of the catalyst material was then achieved by supplying the reactor with the rich feed gas (from the first bank) using a temperature ramp from 300° C. to 700° C. at 10° C./minute followed by soaking at 700° C. for 30 minutes. The desulfated catalyst material was then evaluated in the reactor similar to before. The NOX conversion profile of the desulfated catalyst material is shown as line D.
The above description of embodiments is merely exemplary in nature and, thus, variations thereof are not to be regarded as a departure from the spirit and scope of the invention.

## Claims

1. A lean NOX trap for incorporation into an exhaust aftertreatment system, the lean NOX trap comprising:
a diesel particulate trap comprising a monolithic honeycomb structure having a plurality of flow-through cells, and a catalyst material carried by the monolithic honeycomb structure, the catalyst being constructed and arranged to remove nitrogen oxide gases (NOX) contained in a flow of engine-out exhaust emitted from a lean-burn engine that is supplied with a mixture of air and fuel, the catalyst material comprising a NOX oxidation catalyst that comprises a perovskite compound for catalytically oxidizing NO to NO2 when the mixture of air and fuel is lean, wherein the catalyst material further comprises a carrier material on which the NOX oxidation catalyst is dispersed, wherein the catalyst material further comprises a NOX storage catalyst that stores NO2 as a nitrate species when the mixture of air and fuel is lean and releases NOX gases when the mixture of air and fuel is rich, a NOX reduction catalyst that reduces NOX gases to N2 when the mixture of air and fuel is rich, and palladium, and wherein the NOX storage catalyst, the NOX reduction catalyst, and the palladium are dispersed on the carrier material with the NOX oxidation catalyst.

2. The lean NOX trap according to claim 1, wherein the carrier material comprises at least one of a CeO2—ZrO2 material, alumina, or a zeolite.

3. The lean NOX trap according to claim 1, wherein the NOX storage catalyst comprises an alkali or alkaline earth metal oxide and the NOX reduction catalyst comprises rhodium.

4. The lean NOX trap according to claim 1, wherein the catalyst material further comprises a first carrier material and a second carrier material overlying the first carrier material, wherein the NOX oxidation catalyst is dispersed on each of the first and second carrier materials, the catalyst material further comprising a NOX storage catalyst that stores NO2 as a nitrate species when the mixture of air and fuel is lean and releases NOX gases when the mixture of air and fuel is rich, a NOX reduction catalyst that reduces NOX gases to N2 when the mixture of air and fuel is rich, and palladium, and wherein the NOX oxidation catalyst and the NOX storage catalyst are dispersed on the first carrier material and the palladium is dispersed on the second carrier material.

5. The lean NOX trap according to claim 4, where n each of the first and second carrier materials comprises at least one of a CeO2—ZrO2 material, alumina, or a zeolite, and wherein the NOX storage catalyst comprises an alkali or alkaline earth metal oxide and the NOX reduction catalyst comprises rhodium.

6. The lean NOX trap according to claim 1, wherein the NOX oxidation catalyst comprises at least one of LaCoO3, LaMnO3, La0.9S0.1CoO3, or La0.9Sr0.1MnO3.

7. The lean NOX trap according to claim 1, wherein the catalyst material includes only trace amounts of platinum or less.

8. A lean NOX trap for incorporation into an exhaust aftertreatment system for a lean-burn engine that is supplied with and combusts a mixture of air and fuel, the lean NOX trap comprising;
a canister that comprises a hollow chamber, an inlet for receiving a flow of engine-out exhaust from the lean-burn engine and introducing the flow of engine-out exhaust to the hollow chamber, and an outlet for delivering the flow of engine-out exhaust from the hollow chamber;
a support body housed within the hollow chamber and comprising an inlet end near the inlet of the canister, an outlet end near the outlet of the canister, and at least one surface over which at least a portion of the flow of engine-out exhaust passes while the Flow of engine out exhaust traverses the support body from the inlet end to the outlet end; and
a catalyst material carried by the at least one surface of the support body that removes nitrogen oxide gases (NOX) contained in the flow of engine-out exhaust, the catalyst material comprising (1) a NOX oxidation catalyst that catalytically oxidizes NO to NO2 when the flow of engine-out exhaust promotes an oxidizing environment, (2) a NOX storage catalyst that stores NO2 when the flow of engine-out exhaust promotes an oxidizing environment and releases NOX gases when the flow of engine-out exhaust promotes a reducing environment, and (3) a NOX reduction catalyst that reduces NOX gases to N2 when the flow of engine out exhaust promotes a reducing environment;
wherein the NOX oxidation catalyst comprises a perovskite compound, the NOX storage catalyst comprises an alkali or alkaline earth metal oxide, and the NOX reduction catalyst comprises rhodium, and wherein the catalyst material includes only trace amounts of platinum or less.

9. The lean NOX trap according to claim 8, wherein the catalyst material further comprises a carrier material on which the NOX oxidation catalyst, the NOX storage catalyst, and the NOX redaction catalyst are dispersed, wherein the carrier material has a surface area ranging from about 20 m2/gram to about 300 m2/gram, and wherein the carrier material comprises at least one of a CeO2—ZrO2 material, alumina, or a zeolite.

10. The lean NOX trap according to claim 9, wherein the catalyst material further comprises palladium, and wherein the palladium is dispersed on the carrier material with the NOX oxidation catalyst, the NOX storage catalyst, and the NOX reduction catalyst.

11. The lean NOX trap according to claim 8, wherein the catalyst material further comprises a first carrier material adjacent to the at least one wall surface and a second carrier material overlying the first carrier material, wherein the each of the first and second carrier materials have a surface area ranging from about 20 m2/gram to about 300 m2/gram, wherein each of the first and second carrier materials comprise at least one of a CeO2—ZrO2 material, alumina, or a zeolite, and wherein the NOX oxidation catalyst is dispersed on each of the first and second carrier materials and the NOX storage catalyst and the NOX reduction catalyst are dispersed on first catalyst material.

12. The lean NOX trap according to claim 11, wherein the catalyst material further comprises palladium, and wherein the palladium is dispersed on the second carrier material.

13. The lean NOX trap according to claim 8, wherein the NOX oxidation catalyst comprises at least one of LaCoO3, LaMnO3, La0.9Sr0.1CoO3, or La0.9Sr0.1MnO3.

14. The lean NOX trap according to claim 8, wherein the NOX storage catalyst comprises at least one of BaO, BaCO3, or K2CO3.

15. The lean NOX trap according to claim 8, wherein the support body is a monolithic honeycomb structure that comprises a plurality of flow-through cells extending from the inlet end of the support body to the outlet end of the support body, each of the plurality of flow-through cells communicating a portion of the flow of engine-out exhaust and being at least partially defined by a wall surface over which the portion of the flow of engine-out exhaust passes when the flow of engine-out exhaust is traversing the support body from the inlet end to the outlet end, and wherein the catalyst material is carried on the wall surface of one or more of the plurality of flow-through cells.