NOx TRAP COMPOSITION

Abstract

A NO.sub.x trap composition, and its use in an exhaust system for internal combustion engines, is disclosed. NO.sub.x trap composition comprises a platinum group metal, barium, cobalt, and a magnesia-alumina support. The NO.sub.x trap composition is less prone to storage deactivation and exhibits reduced N.sub.2O formation.

Claims

1. A method for treating exhaust gas from an internal combustion engine comprising contacting the exhaust gas with a NO.sub.x trap composition comprising a platinum group metal, barium, cobalt, and a magnesia-alumina support, wherein the platinum group metal, barium, and cobalt are supported on the magnesia-alumina support.

2. The method of claim 1 wherein the platinum group metal is selected from the group consisting of platinum, palladium, rhodium, and mixtures thereof.

3. The method of claim 1 wherein the magnesia-alumina support is a magnesium aluminate spinel.

4. The method of claim 1 wherein the magnesia-alumina support comprises 5 to 40 weight percent magnesia.

5. The method of claim 1 wherein the NO.sub.x trap composition comprises 0.1 to 10 weight percent platinum group metal.

6. The method of claim 1 wherein the NO.sub.x trap composition comprises 2 to 20 weight percent cobalt.

7. The method of claim 1 wherein the NO.sub.x trap composition comprises 1 to 10 weight percent barium.

8. The method of claim 1 wherein the magnesia-alumina support is pre-calcined at a temperature greater than 600 C.

9. The method wherein the NO.sub.x trap composition of claim is supported on a metal or ceramic substrate.

10. The method of claim 9 wherein the substrate is a flow-through monolith.

11. The method of claim 9 wherein the exhaust gas is further treated by contacting the exhaust gas with at least one of an oxidation catalyst and a particulate filter.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0010] The NO.sub.x trap composition of the invention comprises a platinum group metal, barium, cobalt, and a magnesia-alumina support. The platinum group metal (PGM) is preferably platinum, palladium, rhodium, or mixtures thereof; most preferably, the PGM is platinum, palladium, or mixtures thereof.

[0011] The magnesia-alumina support is preferably a spinel, a magnesia-alumina mixed metal oxide, a hydrotalcite or hydrotalcite-like material, and combinations of two or more thereof. More preferably, the magnesia-alumina support is a spinel.

[0012] Preferably, the magnesia-alumina support comprises 5 to 40 weight percent magnesia, more preferably 10 to 30 weight percent. If the magnesia-alumina support is a hydrotalcite, the support is preferably mixed with an alumina such as boehmite to maintain the overall magnesia content to within 5 to 40 weight percent.

[0013] The spinel is preferably a magnesium aluminate spinel, preferably having an atomic ratio of Mg to Al ranging from about 0.17 to about 1, more preferably from about 0.25 to about 0.75, and most preferably from about 0.35 to about 0.65. A most preferred embodiment includes MgAl.sub.2O.sub.4.

[0014] The magnesia-alumina mixed metal oxide comprises Al.sub.2O.sub.3 and MgO. Portions of the Al.sub.2O.sub.3 and MgO may be chemically reacted or unreacted. The ratio of Mg/Al in the magnesia-alumina mixed metal oxide may preferably vary from about 0.25 to 10, more preferably from about 0.5 to about 2, and most preferably from about 0.75 to about 1.5.

[0015] The magnesia-alumina support may also be a hydrotalcite or hydrotalcite-like (HTL) material. The hydrotalcite or HTL may be collapsed, dehydrated and or dehydroxylated. Non-limiting examples and methods for making various types of hydrotalcites or HTLs are described in U.S. Pat. Nos. 4,866,019, 4,964,581, 4,952,382 6,028,023, 6,479,421, 6,929,736, and 7,112,313; which are incorporated by reference herein in their entirety.

[0016] Preferably, the magnesia-alumina support is calcined at a temperature greater than 600 C., more preferably greater than 700 C. and most preferably greater than 800 C., prior to its inclusion in the NO.sub.x trap composition. The calcination is typically performed in the presence of an oxygen-containing gas (such as air) for greater than 1 hour. The high-temperature calcination leads to the formation of spinel in the magnesia-alumina support.

[0017] The NO.sub.x trap composition of the present invention may be prepared by any suitable means. Preferably, the platinum group metal, cobalt and barium are loaded onto the magnesia-alumina support by any known means to form the NO.sub.x trap composition, the manner of addition is not considered to be particularly critical. For example, a PGM compound (such as platinum nitrate), a cobalt compound (such as cobalt nitrate), and a barium compound (such as barium nitrate) may be supported on the magnesia-alumina support by impregnation, adsorption, ion-exchange, incipient wetness, precipitation, or the like.

[0018] The order of addition of the PGM, cobalt and barium compounds to the magnesia-alumina support is not considered critical. For example, the platinum, cobalt, and barium compounds may be added to the magnesia-alumina support simultaneously, or may be added sequentially in any order. Preferably, the cobalt and barium compounds are added to the magnesia-alumina support prior to the addition of the PGM compound(s).

[0019] The NO.sub.x trap composition preferably comprises 0.1 to 10 weight percent PGM, more preferably 0.5 to 5 weight percent PGM, and most preferably 1 to 3 weight percent PGM. The NO.sub.x trap composition preferably comprises 2 to 20 weight percent cobalt, more preferably 5 to 15 weight percent cobalt, and most preferably 7 to 12 weight percent cobalt. The NO.sub.x trap composition preferably comprises 1 to 10 weight percent barium, more preferably 2 to 8 weight percent barium, and most preferably 3 to 7 weight percent barium. Preferably, the weight ratio of cobalt:barium is greater than 1, more preferably 2 or higher.

[0020] The invention also includes a NO.sub.x trap. The NO.sub.x trap comprises the NO.sub.x trap composition supported on a ceramic substrate or a metallic substrate. The ceramic substrate may be made of any suitable refractory material, e.g., alumina, silica, titania, ceria, zirconia, magnesia, zeolites, silicon nitride, silicon carbide, zirconium silicates, magnesium silicates, aluminosilicates and metallo aluminosilicates (such as cordierite and spodumene), or a mixture or mixed oxide of any two or more thereof. Cordierite, a magnesium aluminosilicate, and silicon carbide are particularly preferred.

[0021] The metallic substrate may be made of any suitable metal, and in particular heat-resistant metals and metal alloys such as titanium and stainless steel as well as ferritic alloys containing iron, nickel, chromium, and/or aluminum in addition to other trace metals.

[0022] The substrate is preferably a flow-through substrate or a filter substrate. Most preferably, the substrate is a flow-through substrate. In particular, the flow-through substrate is a flow-through monolith preferably having a honeycomb structure with many small, parallel thin-walled channels running axially through the substrate and extending throughout the substrate. The channel cross-section of the substrate may be any shape, but is preferably square, sinusoidal, triangular, rectangular, hexagonal, trapezoidal, circular, or oval.

[0023] Preferably, the NO.sub.x trap is prepared by depositing the NO.sub.x trap composition on the substrate using washcoat procedures. A representative process for preparing the NO.sub.x trap using a washcoat procedure is set forth below. It will be understood that the process below can be varied according to different embodiments of the invention.

[0024] The washcoating is preferably performed by first slurrying finely divided particles of the NO.sub.x trap composition in an appropriate solvent, preferably water, to form a slurry. The slurry preferably contains between 5 to 70 weight percent solids, more preferably between 10 to 50 weight percent. Preferably, the particles are milled or subject to another comminution process in order to ensure that substantially all of the solid particles have a particle size of less than 20 microns in an average diameter, prior to forming the slurry. Additional components, such as stabilizers or promoters may also be incorporated in the slurry as a mixture of water soluble or water-dispersible compounds or complexes.

[0025] The substrate may then be coated one or more times with the slurry such that there will be deposited on the substrate the desired loading of the NO.sub.x trap composition.

[0026] It is also possible to form the NO.sub.x trap composition on the substrate in order to produce the NO.sub.x trap. In such a procedure, a slurry of the magnesia-alumina support is washcoated onto the substrate as described above. After the magnesia-alumina support has been deposited on the substrate (and optionally calcined), the platinum group metal, cobalt and barium may then be added to the magnesia-alumina washcoat. The PGM, barium and cobalt may be added by any known means, including impregnation, adsorption, or ion-exchange of a PGM compound (such as platinum nitrate), a barium compound (such as barium nitrate), and a cobalt compound (such as cobalt nitrate). The order of this addition is not considered critical such that the platinum group metal compound, the barium compound, and the cobalt compound may be added simultaneously or sequentially in any order.

[0027] Preferably, the entire length of the substrate is coated with the NO.sub.x trap composition so that a washcoat of the NO.sub.x trap composition covers the entire surface of the substrate.

[0028] After the NO.sub.x trap composition is deposited onto the substrate, the NO.sub.x trap is typically dried by heating at an elevated temperature of preferably 80 to 150 C. and then calcined by heating at an elevated temperature. Preferably, the calcination occurs at 400 to 600 C. for approximately 1 to 8 hours.

[0029] The invention also encompasses an exhaust system for internal combustion engines that comprises the NO.sub.x trap of the invention. Preferably, the exhaust system comprises the NO.sub.x trap with an oxidation catalyst and/or a particulate filter. These after-treatment devices are well known in the art. Particulate filters are devices that reduce particulates from the exhaust of internal combustion engines. Particulate filters include catalyzed soot filters (CSF) and bare (non-catalyzed) particulate filters. Catalyzed soot filters (for diesel and gasoline applications) include metal and metal oxide components (such as Pt, Pd, Fe, Mn, Cu, and ceria) to oxidize hydrocarbons and carbon monoxide in addition to destroying soot trapped by the filter.

[0030] Particularly preferred exhaust systems include the NO.sub.x trap followed by a CSF, both close-coupled; a close-coupled NO.sub.x trap with an underfloor CSF; and a close-coupled diesel oxidation catalyst/CSF and an underfloor NO.sub.x trap.

[0031] The invention also encompasses treating an exhaust gas from an internal combustion engine, in particular for treating exhaust gas from a vehicular lean burn internal combustion engine, such as a diesel engine, a lean-burn gasoline engine, or an engine powered by liquid petroleum gas or natural gas. The method comprises contacting the exhaust gas with the NO.sub.x trap of the invention.

[0032] The following examples merely illustrate the invention. Those skilled in the art will recognize many variations that are within the spirit of the invention and scope of the claims.

EXAMPLE 1

Preparation of Catalysts

[0033] Catalyst 1A (PtPdBaCo/Magnesia-Alumina Support):

[0034] Cobalt (II) nitrate (4.92 g) and barium acetate (0.93 g) are dissolved in demineralized water (15 mL) using gentle heating. This CoBa solution is then added stepwise to magnesia-alumina support (10 g), before being dried at 105 C. for 2-3 hours, followed by calcination at 500 C. for 2 hours to form a BaCo/magnesia-alumina. The BaCo/magnesia-alumina is contacted with an aqueous solution of platinum and palladium salts (7 g solution) to add 1.5 wt. % Pt and 0.5 wt. % Pd onto the final catalyst, before being dried at 105 C. for 2-3 hours, followed by calcination at 500 C. for 2 hours to form Catalyst 1A. Catalyst 1A contains 10 wt. % Co, 5 wt. % Ba, 1.5 wt. % Pt, and 0.5 wt. % Pd.

[0035] Comparative Catalyst 1B (PtPdBa/Magnesia-Alumina Support):

[0036] Comparative Catalyst 1B is prepared according to the procedure of Catalyst 1A with the exception that cobalt nitrate is not utilized. Comparative Catalyst 1B contains 5 wt. % Ba, 1.5 wt. % Pt, and 0.5 wt. % Pd.

[0037] Comparative Catalyst 1C (PtPdBaCo/Alumina Support):

[0038] Comparative Catalyst 1C is prepared according to the procedure of Comparative Catalyst 1A with the exception that alumina is used in place of the maganesia-alumina support. Comparative Catalyst 1C contains 10 wt. % Co, 5 wt. % Ba, 1.5 wt. % Pt, and 0.5 wt. % Pd.

EXAMPLE 2

NO.SUB.x .Storage Testing Procedures

[0039] The catalyst (0.4 g) is stored at 200 C. for 5 minutes in an NO-containing gas, then the temperature is increased to 290 C. at a ramping rate of 20 C./minute to achieve a bed temperature of 275 C., and the catalyst is maintained at a 275 C. bed temperature for 5 minutes. The catalyst is then subjected to a 15 second rich purge in the presence of a rich gas, followed by Temperature Programmed Desorption (TPD) in the presence of a TPD gas until the bed temperature reaches about 500 C. in order to measure the NO.sub.x storage and N.sub.2O selectivity of the fresh catalysts (fresh cycle).

[0040] The catalyst is then thermally aged at 800 C. in air for 24 hours, and is subjected to a rich activation for 2 minutes in the presence of the rich gas at a temperature of 500 C.

[0041] The procedure is repeated in order to measure the NO.sub.x storage and N.sub.2O selectivity of the thermally aged catalyst (aged cycle).

[0042] The NO-containing gas comprises 10.5 vol. % O.sub.2, 50 ppm NO, 6 vol. % CO.sub.2, 1500 ppm CO, 100 ppm hydrocarbons and 6.3 vol. % H.sub.2O.

[0043] The rich gas comprises 1.5 vol. % O.sub.2, 6 vol. % CO.sub.2, 43,200 ppm CO, 1830 ppm hydrocarbons and 6.3 vol. % H.sub.2O.

[0044] The TPD gas comprises 10.5 vol. % O.sub.2, 6 vol. % CO.sub.2, 1500 ppm CO, 100 ppm hydrocarbons and 6.3 vol. % H.sub.2O.

[0045] The NO.sub.x storage results are shown in Table 1.

[0046] The N.sub.2O selectivity results are shown in Table 2.

[0047] The results show that the catalyst of the invention (Catalyst 1A) has higher NO.sub.x storage and good selectivity to N.sub.2O compared to Comparative Catalysts 1B and 1C. Catalyst 1A also retains good NO.sub.x storage and N.sub.2O selectivity after the high temperature aging at 800 C., as compared with Comparative Catalysts 1B and 1C which show much lower NO.sub.x storage and an increase in selectivity to N.sub.2O upon aging.

TABLE-US-00001 TABLE 1 NO.sub.x Storage Results NO.sub.x Storage (% of Input NO.sub.x stored) Catalyst Fresh Aged 1A 77 63 1B * 62 32 1C * 64 29 * Comparison Example

TABLE-US-00002 TABLE 2 Lean N.sub.2O Selectivity Results N.sub.2O Produced (ppm) Catalyst Fresh Aged 1A 21 20 1B * 21 26 1C * 18 21 * Comparison Example