Patent Application
20240238725
THIS INVENTION relates to a composition for the manufacture of a three-way catalyst for treating exhaust gas from an internal combustion engine. The present invention extends to a washcoat comprising the catalyst composition, and a catalyst article comprising the catalyst composition. The invention further extends to a method of manufacturing the catalyst article, a method of treating exhaust gas with the catalyst article, and systems comprising the catalyst article.
Three-way catalysts (TWCs) are conventionally used to convert carbon monoxide (CO), hydrocarbons (HC), and nitrogen oxides (NOx) found in the exhaust gases of gasoline fuelled internal combustion engines. These contaminants are harmful substances, and their emission is strictly controlled by environmental regulations around the world.
Three-way catalysts treat exhaust gases by simultaneously oxidising carbon monoxide and hydrocarbons and reducing nitrogen oxides. Conventional three-way catalysts typically comprise a noble metal (such as platinum, rhodium, palladium, iridium, or ruthenium) on a catalyst support. The catalyst support typically comprises a porous refractory oxide, for example, an alumina, a silica, or a ceria. The supported catalyst may then be applied to a substrate, or extruded, to form a catalyst article.
Three-way catalysts, like other exhaust gas catalysts, typically achieve very high efficiencies once they reach their operating temperature (typically, 200° C. and higher). However, these catalysts may be relatively inefficient below their operating temperature, i.e., during the cold start stage. The activity of a three-way catalyst may be measured in terms of “light-off temperature”. Improved light-off performance may be indicative of improved performance below during the cold start stage.
The term “light-off temperature” as used herein will be understood to refer to the temperature at which 50% catalytic conversion is achieved and is synonymous with “Tso”. It will be understood that the light-off temperature for different components in an exhaust gas may be different from one another. For example, a catalyst's light-off temperature for carbon monoxide may be different from its light-off temperature for nitrogen oxides.
TWCs can be exposed to extremely high temperatures of 800-1000° C. during thermal ageing. Exposure to these temperatures leads to severe sintering phenomena. This can cause a number of issues that affect TWC performance: loss of surface area, loss of available reactive oxygen within the catalyst support lattice, and further sintering of the noble metal. A TWC with improved thermal stability is therefore desired. Conventional methods used in respect of TWCs to improve thermal stability include using ceria-zirconia or the addition of other “promoter” elements, such as alkaline earth metals or any of the trivalent rare earth metals.
Due to an increase in PGM commodity prices, a TWC with a reduced noble metal loading is desired. TWC with reduced metal loadings are often associated with poor emission control performance and poor thermal stability.
Accordingly, it is an object of the present invention to provide a catalyst article which achieves improved thermal stability and improved light-off performance. It is also an objective of the present invention to provide improved CO, HC and NOx emission control performance at a significantly reduced noble metal loading.
The present inventors have found that the presence of an intermetallic compound comprising at least a transition metal selected from Fe, Ce, Y, Nb and combinations thereof, and a noble metal selected from Pt, Pd, Rh and combinations thereof, in a catalyst composition provides improved thermal stability and improved light-off performance results. The presence of the above intermetallic compound in a catalyst composition also results in improved CO, HC and NOx emission control performance at a significantly reduced noble metal loading when the composition is used in the manufacture of a catalyst article.
According to a first aspect, there is provided a catalyst composition comprising an intermetallic compound, wherein the intermetallic compound comprises:
Preferably, the intermetallic compound has a formula according to Formula I:
in which:
According to a second aspect of the invention there is provided a washcoat composition comprising a catalyst composition according to the first aspect of the invention and a liquid medium.
A third aspect of the invention provides a catalyst article comprising a substrate and a catalyst composition according to the first aspect of the present invention.
A fourth aspect of the invention provides a method of making a catalyst article of the third aspect of the invention, comprising the step of coating a substrate with a washcoat composition according to the second aspect of the invention.
A fifth aspect of the invention provides an emission treatment system for treating a flow of a combustion exhaust gas comprising the catalyst article according to the third aspect.
A sixth aspect of the invention provides a method of treating an exhaust gas from an engine, comprising contacting the exhaust gas with a catalyst article according to the third aspect.
Preferred and/or optional features of the invention will now be set out. Any aspect of the invention may be combined with any other aspect of the invention unless the context demands otherwise. Any of the preferred and/or optional features of any aspect may be combined, either singly or in combination, with any aspect of the invention unless the context demands otherwise.
The present invention is directed to the catalytic treatment of combustion exhaust gas, such as that produced by gasoline and other engines, and to related catalysts compositions, catalytic articles, and systems. More specifically, the invention relates to the simultaneous treatment of NOx, CO, and HC in a vehicular exhaust system.
The first aspect provides a catalyst composition comprising an intermetallic compound, wherein the intermetallic compound comprises:
As a skilled person would understand, the term “intermetallic compound” refers to a compound formed by at least two metals, and which has, at least partly, an ordered crystal structure which differ from the crystal structures of its constituting elements (metals). Without wishing to be bound to a specific theory, it is believed that the particular combination of electronic and crystal structure of an intermetallic compound, leads to chemical potentials of the elements not easily obtained in other compounds. The chemical potential results to a large extent from the electron transfer between the constituting elements of the intermetallic compound.
The intermetallic compound of Al—X serves as PGM platform in which PGM atoms can be homogeneously dispersed.
Preferably, the intermetallic compound may have a formula according to Formula I defined above.
In Formula I, a, b and c indicate atomic weight percentages based on total metal content of the intermetallic compound.
In Formula I, X represents the transition metal and may be selected from Fe, Ce, Y, Nb and a combination thereof. Preferably, X is Fe or Y. Most preferably, X may be Y.
In Formula I, PGM represents the noble metal and may be selected from Pt, Pd, Rh and a combination thereof. Preferably, PGM is Rh.
In Formula I, 25≤a<80, such as 60<a<80, for example a=75. It may be preferred that 74≤a≤76. It may be more preferred that 74.5≤a≤75.5.
In Formula I, 20<b<75 such as 20<b≤40 or 20<b≤35. It may be preferred that 20<b≤25. It may be preferred that b is between 24 and 25.
In Formula I, 0<c<5.0, such as 0.2≤c<3.0. It may be preferred that c is greater than or equal to 0.5, or greater than or equal to 0.6. It may be preferred that c is less than or equal to 1.0, or less than or equal to 0.7. It may be preferred that c is 0.2≤c≤0.5. It may be preferred that c is about 0.5.
As demonstrated in the examples, the provision of intermetallic compounds having formulas such as Al74.8Y25Rh0.2, Al74.5 Y25Rh0.5 and Al74.0 Y25Rh1.0, give rise to catalyst articles with improved performance. In particular, the abovementioned intermetallic compounds give rise to improved thermal stability after aging of the catalyst article. Moreover, it has been found that these catalyst articles demonstrate improved performance at significantly reduced noble metal loadings. This is particularly advantageous as conventional TWCs do not typically perform well at reduced noble metal loadings.
The term “noble metal loading” as used herein refers to a measurement in units of g/ft3 on a metal weight basis.
Various techniques may be used to prepare the intermetallic compound according to the invention. A powder metallurgical method, such as annealing for an appropriate time in an inert crucible and atmosphere to reach thermodynamic equilibrium, may be preferred.
The intermetallic compound may be prepared according to the method described hereinbelow.
An intermetallic compound according to the present invention is prepared by melting metallic Al, X and PGM particles in a furnace, such as an electric Arc furnace, under an atmosphere of Ar gas. The melting of the particles may be repeated several times, for example 5 times. The molten material may be annealed at 800° C. for 48 hours in vacuum conditions. The annealed material may then be allowed to cool down to room temperature and may subsequently be crushed to the desired particle size in a mill. The type of mill is not particularly limited and may be selected by the person skilled in the art, for example the mill may suitably be a ball mill.
Optionally, the intermetallic compound particles obtained from the method described above (also referred to as unleached intermetallic compound particles), may be further subjected to a leaching step to obtain leached intermetallic compound particles. The intermetallic compound particles may be leached in a suitable leaching solution. Preferably, the intermetallic compound particles may be leached in a 10 wt % NaOH aqueous solution or in a 10 wt % a Na2CO3 aqueous solution for 24 hours at room temperature. The leached intermetallic compound particles may be filtered and thoroughly washed with distilled water until a pH 7 was measured. The washed particles may then be dried at 313K (40° C.) for 12 hours.
In particular, Al, or substantially Al, may be leached from the intermetallic compound of Formula I. It may be preferable to leach at least 40% of the Al present in the unleached intermetallic compound particles. It may be more preferable to leach at least 50% of the Al present in the unleached intermetallic compound particles. It may be even more preferable to leach at least 60 wt % of the Al present in the unleached intermetallic compound particles, such as at least 64 wt % of the Al. It may be most preferred to leach all, or substantially all of the Al present in the unleached intermetallic compound particles, thereby leaving monodispersed PGM supported on X oxide, such as Rh/Fe2O3, or Pt/Fe2O3, Rh/Y2O3 etc.
Leaching of the intermetallic compound increases the specific surface area of the intermetallic compound. The specific surface area of the intermetallic compound may be determined by Brunauer-Emmett-Teller (BET) methods. Preferably, the BET specific surface area may be from about 90 m2/g to about 160 m2/g, more preferably from about 100 m2/g to about 160 m2/g, even more preferably from about 120 m2/g to about 150 m2/g.
The amount of intermetallic compound present in the catalyst composition may be such that the catalyst composition has a noble metal loading of between 0.5 to 5 g/ft3, preferably of between 0.5 to 4 g/ft3, even more preferably of between 0.5 to 3 g/ft3, such as 0.5 to 2 g/ft3. The noble metal loading of the catalyst composition may be 2.0 g/ft3.
The composition may comprise an oxygen storage component and/or an inorganic oxide.
The oxygen storage component may be cerium oxide, zirconium oxide, a ceria-zirconia mixed oxide, an alumina-ceria-zirconia mixed oxide, or a combination thereof. More preferably, the oxygen storage component may comprise the ceria-zirconia mixed oxide, the alumina-ceria-zirconia mixed oxide or a combination thereof. The ceria-zirconia mixed oxide may further comprise dopants, such as lanthanum, neodymium, praseodymium, yttrium oxides, etc. In some embodiments, the oxygen storage component may comprise the ceria-zirconia mixed oxide and the alumina-ceria-zirconia mixed oxide.
The oxygen storage component may be present in the catalyst composition in an amount of between 20 to 80 wt %, preferably in an amount of between 20 to 60 wt %, more preferably in an amount of between 20 to 50 wt %, relative to other components in a catalyst composition.
The inorganic oxide may be a doped or non-doped alumina, a doped or non-doped silica, a doped or non-doped ceria, or a doped or non-doped ceria-zirconia. Preferably the inorganic oxide is a lanthanum doped alumina (e.g., lanthanum stabilised alumina), wherein lanthanum is up to 10 wt %, preferably, 2 to 8, 3 to 7, or 4 to 6 wt % of the inorganic oxide. It will be understood that the inorganic oxide is different to the oxygen storage component.
The inorganic oxide may be present in the catalyst composition in an amount of between 20 to 80 wt %, preferably in an amount of between 40 to 80 wt %, more preferably to in an amount of between 50 to 80 wt %, relative to other components in a catalyst composition.
The leached or unleached intermetallic compound particles, the oxygen storage component and the inorganic oxide may be combined to obtain the catalyst composition according to the first aspect of the invention.
The catalyst composition may optionally comprise a group 1 or a group 2 metal. In particular, the catalyst composition may comprise one or more metals selected from magnesium, calcium, strontium, and barium. Preferably, the catalyst composition comprises barium. The group 1 or the group 2 metal may be supported on the oxygen storage component and/or the inorganic oxide.
The catalyst composition of the invention may be a catalyst composition for use as a three-way catalyst for treating a flow of a combustion exhaust gas by simultaneously oxidising carbon monoxide and hydrocarbons and reducing nitrogen oxides.
The catalyst composition may be applied to a substrate in the form of a washcoat. Accordingly, a further aspect of the present invention provides a washcoat comprising the catalyst composition of the first aspect and a liquid medium.
The washcoat typically has a solids content of from 20 to 45 wt %, for example 20 to 35 wt %, or about 25 wt %.
The washcoat may be prepared according to the method described hereinbelow.
The method for producing the washcoat may comprise the step of forming a slurry of the oxygen storage component. The slurry of the oxygen storage component may be prepared by suspending the oxygen storage component in a liquid medium, for example in deionised water.
The method for producing the washcoat may comprise the step of adding the leached or unleached intermetallic compound (also referred to herein as an intermetallic compound precursor) to the slurry of the oxygen storage component. The skilled person will be able to select alternative intermetallic compounds of Formula I according to the desired noble metal loading. The method for producing the washcoat may comprise the step of adding an inorganic oxide to the slurry.
The viscosity and rheology of the washcoat may be adjusted using additives known in the art.
Additives may be added in an ageing step prior to coating the washcoat onto a substrate.
The formulation of the intermetallic compound and the amount of the intermetallic compound added to form the composition used to form the washcoat can be selected by the skilled person depending upon the amount of the desired noble metal loading in a catalyst article.
It was found that a catalyst article according to the present invention displays improved thermal stability at aged conditions and improved light-off performance at a significantly reduced noble metal loading in the catalyst. Accordingly, in another aspect of the present invention there is provided a catalyst article, suitable for the treatment of exhaust gas an internal combustion engine, comprising a substrate to which the catalyst composition of the first aspect has been applied.
The substrate may be a flow-through monolith. Alternatively, the substrate can be a wall-flow filter.
The flow-through monolith substrate has a first face and a second face defining a longitudinal direction there between. The flow-through monolith substrate has a plurality of channels extending between the first face and the second face. The plurality of channels extends in the longitudinal direction and provide a plurality of inner surfaces (e.g. the surfaces of the walls defining each channel). Each of the plurality of channels has an opening at the first face and an opening at the second face. For the avoidance of doubt, the flow-through monolith substrate is not a wall flow filter.
The first face is typically at an inlet end of the substrate and the second face is at an outlet end of the substrate.
The channels may be of a constant width and each plurality of channels may have a uniform channel width.
Preferably within a plane orthogonal to the longitudinal direction, the monolith substrate has from 300 to 900 channels per square inch, preferably from 400 to 800. For example, on the first face, the density of open first channels and closed second channels is from 600 to 700 channels per square inch. The channels can have cross sections that are rectangular, square, circular, oval, triangular, hexagonal, or other polygonal shapes.
The monolith substrate acts as a support for holding catalytic material. Suitable materials for forming the monolith substrate include ceramic-like materials such as cordierite, silicon carbide, silicon nitride, zirconia, mullite, spodumene, alumina-silica magnesia or zirconium silicate, or of porous, refractory metal. Such materials and their use in the manufacture of porous monolith substrates are well known in the art.
It should be noted that the flow-through monolith substrate described herein is a single component (i.e. a single brick). Nonetheless, when forming an emission treatment system, the substrate used may be formed by adhering together a plurality of channels or by adhering together a plurality of smaller substrates as described herein. Such techniques are well known in the art, as well as suitable casings and configurations of the emission treatment system.
In embodiments wherein the catalyst article of the present invention comprises a ceramic substrate, the ceramic substrate may be made of any suitable refractory material, e.g., alumina, silica, 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.
In embodiments wherein the catalyst article of the present invention comprises a metallic substrate, 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 aluminium in addition to other trace metals.
In another aspect of the invention there is provided a method for producing a catalyst article comprising the catalyst composition of the first aspect, comprising the step of applying the washcoat of the second aspect to a substrate.
The method of producing a catalyst article may comprise the steps described above in relation to preparing a washcoat of the second aspect of the invention.
The method may comprise the step of coating the washcoat onto a substrate to form a coated substrate. The washcoat may be coated on to a substrate by any method known in the art. The amount of washcoat coated onto the substrate may be determined based upon the desired noble metal component loading on the catalyst article. The washcoat may be coated onto the substrate in one or more coating steps.
Optionally, the method may comprise the step of drying the coated substrate to form a dried coated substrate.
The method may comprise the step of calcining the coated substrate. The step of calcining the coated substrate may be carried out on a substrate which has been optionally dried, or on the coated substrate after coating. Typically, the coated substrate is calcined at a temperature in the range of 450 to 600° C. for a period of up to 2 hours. Suitably, the coated substrate is calcined in a furnace under an atmosphere of air.
It will be appreciated that the steps recited above may be performed in any suitable order and/or that some steps may be combined into a single step. For example, the drying and calcining steps may be combined.
The method for producing a catalyst article according to the invention may comprise the steps of:
According to a further aspect of the invention there is provided an exhaust system comprising a catalyst article of the third aspect of the invention.
In a further aspect of the invention there is provided a method of treating an exhaust gas from an engine comprising contacting the exhaust gas with a catalyst article according to the third aspect.
The invention will now be described further in relation to the following non-limiting examples.
Catalyst Articles 1 to 3 were prepared with catalyst compositions comprising different intermetallic compounds as shown in Table 1:
The different intermetallic compounds listed in Table 1 were prepared using a similar method.
The intermetallic compounds were prepared using an electric arc furnace under an atmosphere of Ar. The alloy samples were annealed at 1100K (827° C.) for 48 hours in vacuum and subsequently crushed to a particle size of <75 μm in a ball mill.
Catalyst compositions were prepared by the following method:
The catalyst composition may be applied to a substrate in the form of a washcoat comprising the catalyst composition of the first aspect and a liquid medium. The washcoat may be prepared according to the method described hereinbelow.
Pre-prepared inorganic oxide of lanthanum doped alumina was added to deionised water to form a slurry. To the slurry was added an intermetallic compound precursor obtained from the method described above. The resulting mixture was homogenised by stirring. A base or acid was slowly added to adjust pH in the range of about 6.0 to 7.0.
A thickening agent was added to the slurry, which was then aged to produce a washcoat suitable for coating a substrate.
The washcoat was applied to the substrate by pulling the washcoat through the channels under vacuum. The substrate was a standard cordierite foil, having a cell density of 400 cells per square inch (cpsi), an axial length of 5.00 cm and a width of 2.54 cm.
The coated substrate was then dried and calcined.
For Catalyst Articles 1 to 3, the light-off temperatures for each of carbon monoxide, nitrogen oxide, and hydrocarbons were determined using a Synthetic Catalyst Activity Test (SCAT) rig using the gas compositions shown in Table 2 under stoichiometric conditions.
Under the gas composition above, the catalyst articles were heated to 400° C. at a rate of 20° C. per minute and held at this temperature for 5 minutes. The temperature was decreased to 100° C. Light-off temperatures were measured for each catalyst article under a gas flow rate of 40 litres per minute.
Complete light-off curves for carbon monoxide, hydrocarbons, and nitrogen oxides are shown in
Comparative Catalyst A is a single-layered TWC coated on a ceramic substrate (400 cpsi, 4.0 mil wall thickness). The catalyst layer consists of Rh supported on a washcoat of La-stabilized alumina and Nd-stabilized ceria zirconia where Rh was prefixed on the alumina support. The Rh loading of Comparative Catalyst A is 0.5 g/ft3.
The method for producing a washcoat for Comparative Catalysts A to D is similar to the method for producing a washcoat according to the present invention as described above. However, the method differs from the method of the present invention in that a noble metal source is added to the slurry of the oxygen storage component instead of an intermetallic compound precursor. Suitably, the noble metal source may be added to the slurry as one or more soluble compounds of the desired noble metals in solution. Suitably, the noble metal source may be provided as nitrates of the noble metal in an aqueous solution, for example the noble metal source is added as rhodium nitrate in the preparation of Comparative Catalyst D.
Comparative Catalyst B is a single-layered TWC coated on a ceramic substrate (400 cpsi, 4.0 mil wall thickness). The catalyst layer consists of Rh supported on a washcoat of Y-doped La-stabilized alumina and Nd-stabilized ceria zirconia where Rh was prefixed on the alumina support. The Y-doped La-stabilized alumina was prepared by a wetness impregnation method by using an aqueous Y nitrate solution. The Y concentration is the same as the following Catalyst Article 4. The Rh loading of Comparative Catalyst B is 0.5 g/ft3.
Comparative Catalyst C is a single-layered TWC coated on a ceramic substrate (400 cpsi, 4.0 mil wall thickness). The catalyst layer consists of Rh supported on a washcoat of yttrium oxide, La-stabilized alumina and Nd-stabilized ceria zirconia where Rh was prefixed on the yttrium oxide support. The Y concentration in the whole washcoat is the same as the following Catalyst Article 4. The Rh loading of Comparative Catalyst C is 0.5 g/ft3.
An intermetallic compound of general formula Al74.5—Y25—Rh0.5 was prepared by using a similar method as described above.
Catalyst Article 4 with a Rh loading of 0.5 g/ft3 was prepared by following a similar method as described above in respect of Catalyst Articles 1 to 3. The Al—Y—Rh intermetallic compound precursor was mixed with La-stabilized alumina and Nd-stabilized ceria zirconia. The Y concentration in the whole washcoat is the same as Comparative Catalysts B and C.
Comparative Catalysts A to C and Catalyst Article 4 were tested separately over a SCAT rig as described above after hydrothermal aging for 4 hours at 1000° C. under air with 10% steam.
Light-off temperatures were measured with a heating rate of 30° C./min under reaction gas condition in Table 2.
The HC, CO and NOx conversion at 600° C. of the aged Comparative Catalysts A to C and Catalyst Article 4 are shown in Table 3. The data indicate that, surprisingly, Catalyst Article 4 of the present invention gave significantly improved light-off performance when compared with Comparative Catalysts A to C for the conversion of THC and NOx. It can be seen that Catalyst Article 4 achieved significantly higher conversions of THC and NOx compared to Comparative Catalysts A to C at the same temperature. This invention can save precious natural resource as a reduced noble metal loading can be used to provide cleaner-air environment through significant performance improvement of TWC to reduce air-pollutions by automobiles.
It was also surprisingly found that Catalyst Article 4 has a significantly improved thermal stability at a Rh loading of 0.5 g/ft3 compared to conventional catalyst materials at the same Rh loading. This effect is shown in
An intermetallic compound of general formula Al74.5—Y25—Rh0.5 was prepared by using a similar method as described above.
Catalyst Article 5 with a Rh loading of 2.0 g/ft3 was prepared by following a similar method as described above in respect of Catalyst Article 4.
The crushed intermetallic particles formed in the preparation of Catalyst Article 5 were leached in 10 wt % Na2CO3 aqueous solution for 24 hours at room temperature. The leached intermetallic particles were washed with distilled water until a pH˜7 was measured. The particles were then dried at 313 K (40° C.) for 12 hours. The leached intermetallic compound particles were used to prepare Catalyst Article 6 with a Rh loading of 2.0 g/ft3 by following a similar method as described above in respect of Catalyst Articles 4 and 5.
The surface area of Catalyst Articles 5 and 6 were measured by using a BET method. The surface area measurements are shown in Table 4. Leaching of the intermetallic compound particles has significantly increased the surface area of Catalyst Article 6 compared to Catalyst Article 5 which was prepared from an intermetallic compound having the same composition, but which was not leached.
Light-off test results were obtained for total hydrocarbons, and nitrogen oxides after harsh lean 1000° C., 4 hour aged under 10% steam-air balance. These results were obtained under the same conditions set out in Table 2 and by following a similar method as described above in Example 2. The light-off test results are shown in Table 5.
Leaching the intermetallic compound results in superior conversion of total hydrocarbons and nitrogen oxides at harsh lean aged conditions.
It was also found that Catalyst Article 6 has a significantly improved thermal stability compared to Catalyst Article 5. This effect is shown in
Comparative Catalyst D was prepared using a Rh precursor and Catalyst Articles 7 to 9 were prepared using intermetallic compounds according to the invention. The formulations for the Rh precursor and the respective intermetallic compounds used are shown in Table 6.
Comparative Catalyst D is a single-layered TWC coated on a ceramic substrate (400 cpsi, 4.0 mil wall thickness). The catalyst layer consists of Rh supported on a washcoat of Y-doped La-stabilized alumina and Nd, La-stabilized ceria zirconia where Rh was prefixed on the alumina support. The Y-doped La-stabilized alumina was prepared by a wetness impregnation method by using an aqueous Y nitrate solution. The Y concentration is the same as the following Catalyst Articles 7 to 9. The Rh loading of Comparative Catalyst D is 2.0 g/ft3.
An intermetallic compound of general formula Al74.8—Y25—Rh0.2 was prepared by using a similar method as described above.
The crushed intermetallic particles were leached in 10 wt % Na2CO3 aqueous solution for 24 hours at room temperature. The leached intermetallic particles were washed with distilled water until a pH˜7 was measured. The particles were then dried at 313 K (40° C.) for 12 hours. The leached intermetallic compound particles were used to prepare Catalyst Article 7 having a Rh loading of 2.0 g/ft3 by following a similar method as described above in respect of Catalyst Articles 4 to 6.
An intermetallic compound of general formula Al74.5—Y25.0—Rh0.5 was prepared by using a similar method as described above.
The crushed intermetallic particles were leached in 10 wt % Na2CO3 aqueous solution for 24 hours at room temperature. The leached intermetallic particles were washed with distilled water until a pH˜7 was measured. The particles were then dried at 313 K (40° C.) for 12 hours. The leached intermetallic compound particles were used to prepare Catalyst Article 8 having a Rh loading of 2.0 g/ft3 by following a similar method as described above in respect of Catalyst Articles 4 to 6.
An intermetallic compound of general formula Al74.0—Y25.0—Rh1.0 was prepared by using a similar method as described above.
The crushed intermetallic particles were leached in 10 wt % Na2CO3 aqueous solution for 24 hours at room temperature. The leached intermetallic particles were washed with distilled water until a pH˜7 was measured. The particles were then dried at 313 K (40° C.) for 12 hours. The leached intermetallic compound particles were used to prepare Catalyst Article 9 having a Rh loading of 2.0 g/ft3 by following a similar method as described above in respect of Catalyst Articles 4 to 6.
Light-off test results were obtained for total hydrocarbons, and nitrogen oxides. These results were obtained under the same conditions set out in Table 2 and by following a similar method as described above. The light-off test results measured after lean aged conditions are shown in Table 7. The aging comprises harsh lean aging at 1000° C. for 4 hours under air with 10% steam.
It can be seen that Catalyst Article 8, with a Rh atomic weight percentage of 0.5, achieved the best total HC conversion. Both Catalyst Article 7 with a Rh atomic weight percentage of 0.2 and Catalyst Article 8, with a Rh atomic weight percentage of 0.5, achieved good NOx conversions. The atomic weight percentage of Rh in the intermetallic compound (i.e. the value of c in Formula I provided above), may therefore be selected based on its application requirement. For example, if the application of the catalyst article is focussed on HC conversion, a formulation of Catalyst Article 8 may be preferable. If, however, the application of the catalyst article is focussed on NOx conversion, then a formulation of Catalyst Article 7 may be preferable.
| Number | Date | Country | Kind |
|---|---|---|---|
| 23152222.8 | Jan 2023 | EP | regional |
