Patent Application
20240207826
Disclosed herein are nanoparticles comprising a platinum group metal (PGM) and a base metal (BM), catalytic compositions comprising such nanoparticles and a support material, and methods of making such nanoparticles and catalytic compositions. Catalytic articles and exhaust gas treatment systems, as well as methods of treating an exhaust gas stream comprising a pollutant, are also disclosed.
Regulators worldwide are imposing increasingly stringent vehicle emission limits. Lean burn engines, e.g., diesel engines, provide vehicle users with excellent fuel economy due to their standard operation at high air/fuel ratios under fuel lean conditions. However, these engines also emit exhaust gas emissions comprising pollutants such as particulate matter (PM), unburned hydrocarbons (HC), carbon monoxide (CO), and nitrogen oxides (NO.).
Platinum group metals (PGMs) are among the most active catalyst components used in automotive emission control systems to reduce the release of pollutants. However, high-temperature exposure during operation can significantly diminish the activity of PGM catalysts due to metal particle sintering, which reduces the catalyst's specific surface area and lowers catalytic efficiency. The commonly employed PGM platinum (Pt) is especially vulnerable under high-temperature and lean (oxidizing) conditions. For example, a PGM dispersion (fraction of metal exposed) on a three-way catalyst (TWC) may be reduced to less than 5% after typical gasoline-type aging, yielding inefficient PGM utilization, increased costs, and higher noxious emissions.
Emissions control during the engine cold start period has become increasingly important as regulations become more stringent. Many catalysts used to treat the exhaust of internal combustion engines are less effective during periods of relatively low temperature operation because the engine exhaust is not at a sufficiently high temperature for efficient catalytic conversion of noxious components. Illustratively, the intrinsic activities of even state-of-the-art PGM catalysts are still too low to be effective at the low exhaust temperatures used, for example, during engine cold start, resulting in increased emissions during low temperature operation.
Accordingly, there is a need for novel catalytic compositions with enhanced PGM efficiency at low temperatures.
Disclosed herein is a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM), wherein:
In some embodiments, the PGM is selected from Pd, Pt, and combinations of the foregoing. In some embodiments, the PGM is Pt.
In some embodiments, the BM is selected from Cu, Co, Mn, Ni, and combinations of any of the foregoing. In some embodiments, the BM is Cu. In some embodiments, the BM is Co. In some embodiments, the BM is Mn. In some embodiments, the BM is Ni.
In some embodiments, the alloy comprises at least 2 at % of the BM.
In some embodiments, the molar percentage of the PGM is in the range of 25% to 75%. In some embodiments, the molar percentage of the PGM is in the range of 25% to 67%. In some embodiments, the molar percentage of the PGM is in the range of 25% to 65%. In some embodiments, the molar percentage of the PGM is in the range of 33% to 65%.
In some embodiments, the particle size is in the range of 2.5 nm to 3.5 nm.
In some embodiments, the nanoparticle consists essentially of the PGM and the BM.
Also disclosed herein is a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM), wherein:
In some embodiments, the PGM is selected from Pd, Pt, and combinations of the foregoing. In some embodiments, the PGM is Pt.
In some embodiments, the BM is selected from Cu, Co, Mn, Ni, and combinations of any of the foregoing. In some embodiments, the BM is Cu. In some embodiments, the BM is Co. In some embodiments, the BM is Mn. In some embodiments, the BM is Ni.
In some embodiments, the alloy comprises at least 2 at % of the BM.
In some embodiments, the molar percentage of the PGM is in the range of 60% to 95%. In some embodiments, the molar percentage of the PGM is in the range of 65% to 90%. In some embodiments, the molar percentage of the PGM is in the range of 67% to 88%.
In some embodiments, the particle size is in the range of 4 nm to 6 nm.
In some embodiments, the nanoparticle consists essentially of the PGM and the BM.
Also disclosed herein is a nanoparticle prepared by a process comprising:
Also disclosed herein is a catalytic composition comprising:
In some embodiments, the support material comprises alumina, silica, zirconia, titania, ceria, or a combination of any of the foregoing. In some embodiments, the support material is Al2O3. In some embodiments, the support material is lanthanum-stabilized zirconia. In some embodiments, the support material does not substantially change the electronic structure of the at least one nanoparticle.
In some embodiments, the nanoparticle comprises 0.2 wt % to 0.4 wt % of a total weight of the catalytic composition.
In some embodiments, the catalytic composition has an exposed metal surface area in the range of 0.01 m2/gcatalyst to 0.1 m2/gcatalyst.
Also disclosed herein is a catalytic composition prepared by a process comprising:
Also disclosed herein is a catalytic article comprising:
Also disclosed herein is an exhaust gas treatment system comprising a catalytic article disclosed herein, wherein the catalytic article is downstream of and in fluid communication with an internal combustion engine.
Also disclosed herein is a method of treating an exhaust gas stream comprising a pollutant, the method comprising passing the exhaust gas stream through a catalytic article disclosed herein or an exhaust gas treatment system disclosed herein.
In some embodiments, the pollutant comprises hydrocarbons.
In some embodiments, the exhaust gas stream is passed through the catalytic article or the exhaust gas treatment system at a low temperature. In some embodiments, the low temperature is in the range of 100° C. to 150° C.
As used herein, “a” or “an” entity refers to one or more of that entity, e.g., “a compound” refers to one or more compounds or at least one compound unless stated otherwise. As such, the terms “a” (or “an”), “one or more”, and “at least one” are used interchangeably herein.
As used herein, “[X] is in the range of [A] to [Z]” means that [X] can be any value in the range from [A] to [Z], including [A] or [Z].
As used herein, the term “alloy” refers to a metal created by combining two or more metallic elements.
As used herein “a molar percentage of [X] calculated based on a total number of moles of [X] and [Y],” e.g., in the context of a nanoparticle refers to a percentage calculated as:
As used herein, the term “associated” means, i.e., “equipped with,” “connected to,” or in “communication with,” e.g., “electrically connected” or in “fluid communication with” or otherwise connected in a way to perform a function. As used herein, the term “associated” may mean directly associated with or indirectly associated with, i.e., through one or more other articles or elements.
As used herein, the term “average particle size” refers to a characteristic of particles that indicates, on average, the diameter of the particles.
As used herein, the term “base metal” refers to a transition metal or lanthanide (e.g., V, Mn, Fe, Co, Ni, Cu, Zn, Ag, Au, or Sn) or an oxide thereof. For ease of reference herein, concentrations of base metal or base metal oxide materials are reported in terms of elemental metal concentration rather than the oxide form. In some embodiments, the base metal may be selected from iron (Fe), copper (Cu), manganese (Mn), chromium (Cr), cobalt (Co), nickel (Ni), tin (Sn), an oxide of any of the foregoing, and mixtures of any of the foregoing.
As used herein, the term “calcination” refers to heating a solid to an elevated temperature (i.e., an above-ambient temperature) in air or oxygen, such as, e.g., to remove impurities or volatile substances from the solid, or to fix one substance onto another.
As used herein, the term “catalyst” or “catalyst composition” refers to a material that promotes a chemical reaction. The catalyst or catalyst composition may include a catalytically active species and a support that carries or supports the catalytically active species. For example, the catalytically active species may be disposed in or on a support material through association, dispersion, impregnation, or other suitable methods, and may reside on the surface or be distributed throughout the support material.
As used herein, the term “catalytic article” refers to an article comprising a substrate having a catalyst coating composition.
As used herein, the term “coordinating solvent” refers to a solvent capable of coordinating with dissolved ions. Non-limiting examples of coordinating solvents include dimethylsulfoxide (DMSO), dimethylformamide (DMF), acetonitrile (CH3CN), nitromethane (CH3NO2), and nitrobenzene (C6H5NO2).
As used herein, the term “exhaust stream” or “exhaust gas stream” refers to any combination of flowing gas that may contain solid or liquid particulate matter. The stream may comprise gaseous components, such as, for example, exhaust of a lean burn engine, which may contain certain non-gaseous components, such as liquid droplets, solid particulates, and the like. The exhaust gas stream of a combustion engine may further comprise combustion products (CO2 and H2O), products of incomplete combustion (carbon monoxide (CO) and hydrocarbons (HC)), oxides of nitrogen (NOx), combustible and/or carbonaceous particulate matter (soot), and/or unreacted oxygen and nitrogen.
As used herein, the terms “upstream” and “downstream” refer to relative directions according to the flow of an engine exhaust gas stream from an engine toward a tailpipe, with the engine in an upstream location and the tailpipe and any pollution abatement articles, such as, e.g., filters and catalysts, being downstream from the engine. The inlet end of a substrate is synonymous with the “upstream” end or “front” end. The outlet end is synonymous with the “downstream” end or “rear” end. An upstream zone is upstream of a downstream zone. In some embodiments, an upstream zone may be closer to the engine or manifold, and a downstream zone may be further away from the engine or manifold.
As used herein, the term “in fluid communication” refers to articles positioned on the same exhaust line. Illustratively, a common exhaust stream passes through articles that are in fluid communication with each other. Articles in fluid communication may be adjacent to each other in the exhaust line. Alternatively, articles in fluid communication may be separated by one or more articles, which may be referred to as “washcoated monoliths.”
As used herein, the term “impregnated” or “impregnation” refers to permeation of a catalytic material into the porous structure of a support material.
As used herein, the term “material” refers to an element, constituent, or substance of which something is composed or can be made.
As used herein, the term “nanoparticle” refers to a particle having at least one dimension that is the range of 1 nm to 999 nm in length.
As used herein, the terms “on” and “over,” in reference to a coating layer, may be used synonymously. Illustratively, the term “directly on” means in direct contact with. In some embodiments, disclosed articles are referred to as comprising one coating layer “on” a second coating layer. Such language is intended to encompass embodiments with intervening layers, where direct contact between the coating layers is not required.
As used herein, the term “particle size” refers to the smallest diameter sphere that will completely enclose the particle, and this measurement relates to an individual particle as opposed to an agglomeration of two or more particles. Particle size may be measured by laser light scattering techniques, with dispersions or dry powders, e.g., according to ASTM method D4464. Particle size may also be measured by Scanning Electron Microscopy (SEM) or Transmission Electron Microscopy (TEM) for submicron size particles, or by a particle size analyzer for support-containing particles (micron size). In addition to TEM, carbon monoxide (CO) chemisorption may be used to determine average PGM particle size. This technique does not differentiate between various PGM species (e.g., Pt, Pd, etc., as compared to XRD, TEM, and SEM) and only determines the average particle size.
As used herein, the term “platinum group metal” (PGM) refers to a platinum group metal or an oxide thereof, such as, e.g., platinum (Pt), palladium (Pd), ruthenium (Ru), rhodium (Rh), osmium (Os), iridium (Ir), an oxide of any of the foregoing, and mixtures of any of the foregoing. In some embodiments, the PGM may be in any valence state.
As used herein, the term “room temperature” or “ambient temperature” refers to a temperature in the range of 15° C. to 25° C., such as, e.g., 20° C. to 25° C.
As used herein, the term “substantially” refers to a property having a statistical occurrence greater that 75%.
As used herein, the term “substrate” refers to a monolithic material onto which a catalyst composition, e.g., a catalytic coating, is disposed, e.g., in the form of a washcoat. In some embodiments, the substrate is selected from flow-through monoliths and monolithic wall-flow filters. As used herein, the term “flow-through substrate” refers to a substrate comprising parallel channels running in the axial direction. As used herein, the term “wall-flow substrate” refers to a substrate comprising adjacent channels, wherein the adjacent channels are alternatively plugged at each end. Flow-through and wall-flow substrates are known in the art and taught, e.g., in PCT International Application Publication No. WO 2016/070090, which is incorporated herein by reference. As used herein, a “monolithic substrate” refers to a unitary structure that is homogeneous and continuous from inlet to outlet.
As used herein, the term “support” refers to any high surface area material, e.g., refractory metal oxide material, upon which a catalytic component is applied.
As used herein, the term “washcoat” refers to a thin, adherent coating of a material applied to a substrate material. A washcoat layer includes a compositionally distinct layer of material disposed on the surface of a substrate or an underlying washcoat layer. A substrate may contain one or more washcoat layers, and each washcoat layer may be different in some way (e.g., may differ in physical properties thereof such as, e.g., particle size) and/or may differ in its chemical catalytic functions.
Without limitation, some embodiments of the disclosure include:
Some embodiments of this disclosure relate to a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM), wherein:
In some embodiments, the particle size is in the range of 2.5 nm to 3.5 nm.
In some embodiments, the PGM is selected from Pd, Pt, and combinations of the foregoing. In some embodiments, the PGM is Pt.
In some embodiments, the BM is selected from Cu, Co, Mn, Ni, and combinations of any of the foregoing. In some embodiments, the BM is Cu. In some embodiments, the BM is Co. In some embodiments, the BM is Mn. In some embodiments, the BM is Ni.
In some embodiments, the BM has a face-centered cubic (FCC) structure. In some embodiments, the BM has a hexagonal close-packed (HCP) structure. In some embodiments, the BM has a body-centered cubic structure (BCC) structure.
In some embodiments, the alloy comprises at least 2 at % of the BM. In some embodiments, the alloy comprises at least 5 at % of the BM. In some embodiments, the alloy comprises at least 10 at % of the BM. In some embodiments, the alloy comprises at least 15 at % of the BM. In some embodiments, the alloy comprises at least 20 at/o of the BM. In some embodiments, the alloy comprises at least 25 at % of the BM. In some embodiments, the alloy comprises at least 30 at/o of the BM.
In some embodiments, the molar percentage of the PGM is in the range of 25% to 75%. In some embodiments, the molar percentage of the PGM is in the range of 25% to 67%. In some embodiments, the molar percentage of the PGM is in the range of 25% to 65%. In some embodiments, the molar percentage of the PGM is in the range of 33% to 65%.
In some embodiments, the molar percentage of the PGM is in the range of 60% to 66%. In some embodiments, the molar percentage of the PGM is in the range of 45% to 55%. In some embodiments, the molar percentage of the PGM is in the range of 33% to 40%.
In some embodiments, the nanoparticle consists essentially of the PGM and the BM.
Nanoparticles with a Particle Size Ranging from 4 nm to 7 nm
Some embodiments of this disclosure relate to a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM), wherein:
In some embodiments, the particle size is in the range of 4 nm to 6 nm.
In some embodiments, the PGM is selected from palladium-group platinum-group elements and combinations thereof. In some embodiments, the PGM is selected from Pd, Pt, and combinations of the foregoing. In some embodiments, the PGM is Pt.
In some embodiments, the BM is selected from Cu, Co, Mn, Ni, and combinations of any of the foregoing. In some embodiments, the BM is Cu. In some embodiments, the BM is Co. In some embodiments, the BM is Mn. In some embodiments, the BM is Ni.
In some embodiments, the BM has a FCC structure. In some embodiments, the BM has a HCP structure. In some embodiments, the BM has a BCC structure.
In some embodiments, the alloy comprises at least 2 at % of the BM. In some embodiments, the alloy comprises at least 5 at % of the BM. In some embodiments, the alloy comprises at least 10 at % of the BM. In some embodiments, the alloy comprises at least 15 at % of the BM. In some embodiments, the alloy comprises at least 20 at % of the BM. In some embodiments, the alloy comprises at least 25 at % of the BM. In some embodiments, the alloy comprises at least 30 at % of the BM.
In some embodiments, the molar percentage of the PGM is in the range of 60% to 95%. In some embodiments, the molar percentage of the PGM is in the range of 65% to 90%. In some embodiments, the molar percentage of the PGM is in the range of 67% to 88%. In some embodiments, the molar percentage of the PGM is in the range of 80% to 90%. In some embodiments, the molar percentage of the PGM is in the range of 65% to 75%.
In some embodiments, the nanoparticle consists essentially of the PGM and the BM.
Some embodiments of this disclosure relate to a catalytic composition comprising:
In some embodiments, the support material comprises alumina, silica, zirconia, titania, ceria, or a combination of any of the foregoing. In some embodiments, the support material is Al2O3. In some embodiments, the support material is lanthanum-stabilized zirconia. In some embodiments, the support material does not substantially change the electronic structure of the at least one nanoparticle.
In some embodiments, the nanoparticle comprises 0.2 wt % to 0.4 wt % of a total weight of the catalytic composition. In some embodiments, the nanoparticle comprises 0.3 wt % of a total weight of the catalytic composition.
In some embodiments, the nanoparticle is disposed in or on the at least one support material through association or dispersion. In some embodiments, the nanoparticle is disposed in or on the at least one support material through association. In some embodiments, the nanoparticle is disposed in or on the at least one support material through dispersion.
In some embodiments, the nanoparticle is impregnated in or on the at least one support material.
In some embodiments, the catalytic composition has an exposed metal surface area in the range of 0.01 m2/gcatalyst to 0.1 m2/gcatalyst.
Some embodiments of this disclosure relate to a catalytic article comprising:
In some embodiments, the catalytic article has a zoned configuration.
In some embodiments, the catalytic article has a layered configuration.
In some embodiments, the substrate is selected from flow-through substrates and wall-flow substrates. In some embodiments, the substrate is selected from flow-through substrates. In some embodiments, the substrate is selected from wall-flow substrates.
In some embodiments, the substrate is selected from monolithic substrates. In some embodiments, the substrate is selected from flow-through monoliths and monolithic wall-flow filters. In some embodiments, the substrate is selected from flow-through monoliths. In some embodiments, the substrate is selected from monolithic wall-flow filters.
Some embodiments of this disclosure relate to an exhaust gas treatment system comprising a catalytic article disclosed herein, wherein the catalytic article is downstream of and in fluid communication with an internal combustion engine.
In some embodiments, the internal combustion engine is a diesel engine. In some embodiments, the internal combustion engine is a diesel engine which operates at combustion conditions with air in excess of that required for stoichiometric combustion, i.e., lean conditions.
In some embodiments, the internal combustion engine is a gasoline engine (e.g., a lean burn gasoline engine) or an engine associated with a stationary source (e.g., electricity generators or pumping stations). In some embodiments, the internal combustion engine is a gasoline engine. In some embodiments, the internal combustion engine is a lean burn gasoline engine. In some embodiments, the internal combustion engine is associated with a stationary source. In some embodiments, the internal combustion engine is associated with an electricity generator. In some embodiments, the internal combustion engine is associated with a pumping station.
Exhaust gas treatment systems disclosed herein may contain more than one catalytic article positioned downstream from the internal combustion engine in fluid communication with the exhaust gas stream.
In some embodiments, the exhaust gas treatment system may further comprise a soot filter and/or an ammonia oxidation catalyst. In some embodiments, the soot filter may be uncatalyzed. In some embodiments, the soot filter may be catalyzed.
The relative placement of the various catalytic components present within the exhaust gas treatment system can vary. In some embodiments, the exhaust gas stream is received into the catalytic article(s) or exhaust gas treatment system(s) by entering the upstream end and exiting the downstream end.
Some embodiments of this disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM), the method comprising:
In some embodiments, the PGM is selected from palladium-group platinum-group elements and combinations thereof. In some embodiments, the PGM is selected from Pd, Pt, and combinations of the foregoing. In some embodiments, the PGM is Pt.
In some embodiments, the seeds of the PGM have particle sizes in the range of 1.5 nm to 3.5 nm. In some embodiments, a molar percentage of the PGM in the second mixture is in the range of 25% to 95%, calculated based on a total number of moles of the PGM and the BM in the second mixture. In some embodiments, a molar percentage of the PGM in the second mixture is 63%, calculated based on a total number of moles of the PGM and the BM in the second mixture. In some embodiments, a molar percentage of the PGM in the second mixture is 49%, calculated based on a total number of moles of the PGM and the BM in the second mixture. In some embodiments, a molar percentage of the PGM in the second mixture is 37%, calculated based on a total number of moles of the PGM and the BM in the second mixture.
In some embodiments, the seeds of the PGM have particle sizes in the range of 4 nm to 6 nm. In some embodiments, a molar percentage of the PGM in the second mixture is in the range of 50% to 95%, calculated based on a total number of moles of the PGM and the BM in the second mixture. In some embodiments, a molar percentage of the PGM in the second mixture is 69%, calculated based on a total number of moles of the PGM and the BM in the second mixture. In some embodiments, a molar percentage of the PGM in the second mixture is 86%, calculated based on a total number of moles of the PGM and the BM in the second mixture.
In some embodiments, the PGM is Pd. In some embodiments, the seeds of the PGM have particle sizes in the range of 2.5 nm to 4.5 nm.
In some embodiments, the organic solvent is selected from hexanes, dichloromethane, diethyl ether, chloroform, heptanes, tetrahydrofuran, and acetonitrile. In some embodiments, the organic solvent is hexanes.
In some embodiments, the BM precursor is selected from Co(acac)2, Mn(acac)3, Ni(acac)2, Cu(acac)2, and combinations of any of the foregoing. In some embodiments, the BM precursor is Co(acac)2. In some embodiments, the BM precursor is Mn(acac)3. In some embodiments, the BM precursor is Ni(acac)2. In some embodiments, the BM precursor is Cu(acac)2.
In some embodiments, the coordinating solvent is selected from non-phosphine solvents. In some embodiments, the coordinating solvent is selected from oleylamine, oleic acid, 1-octadecene, trioctylamine, and combinations of any of the foregoing. In some embodiments, the coordinating solvent is oleylamine.
In some embodiments, rapidly heating comprises heating at a rate of 40° C. min−1.
In some embodiments, the high temperature is in the range of 250° C. to 300° C. In some embodiments, the high temperature is 280° C.
In some embodiments, the time period is 30 minutes.
In some embodiments, isolating the nanoparticle comprises a round of precipitation using at least one antisolvent. In some embodiments, the antisolvent is selected from toluene, isopropanol, ethanol, and combinations of any of the foregoing.
In some embodiments, isolating the nanoparticle comprises two rounds of precipitation.
In some embodiments, isolating the nanoparticle further comprises centrifugation.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising laser vaporization of an alloy rod, a mixed metallic powder, or two monometallic targets.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising pulsed laser ablation in a liquid.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising vaporization of bimetallic targets by passing an intense electrical discharge through the bimetallic targets.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising a step of microwave synthesis.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising a step of atomic layer deposition.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising a step of electrochemical synthesis.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising thermal decomposition of metal complexes.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising chemical reduction of a mixture of salts in a solution.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising successive reduction of chemical complexes.
Some embodiments of the present disclosure relate to a method of preparing a nanoparticle comprising a platinum group metal (PGM) and a base metal (BM) comprising co-reduction of chemical complexes.
Also disclosed herein is a nanoparticle prepared by a process described herein.
Some embodiments of this disclosure relate to a method of preparing a catalytic composition, the method comprising:
In some embodiments, the nanoparticle comprises 0.3 wt % of a total weight of the nanoparticle and the support material.
In some embodiments, the first organic solvent is selected from hexanes, dichloromethane, diethyl ether, chloroform, heptanes, tetrahydrofuran, and acetonitrile. In some embodiments, the first organic solvent is hexanes.
In some embodiments, the support material comprises alumina, silica, zirconia, titania, ceria, or a combination of any of the foregoing. In some embodiments, the support material is Al2O3. In some embodiments, the support material is lanthanum-stabilized zirconia. In some embodiments, the support material does not substantially change the electronic structure of the at least one nanoparticle.
In some embodiments, the second organic solvent is selected from hexanes, dichloromethane, diethyl ether, chloroform, heptanes, tetrahydrofuran, and acetonitrile. In some embodiments, the second organic solvent is hexanes.
In some embodiments, the time period is at least 8 hours.
In some embodiments, isolating the catalytic composition comprises centrifuging the mixture to isolate a catalytic solid. In some embodiments, centrifuging the mixture comprises centrifuging the mixture at 8000 rpm for 3 minutes to isolate the catalytic solid.
In some embodiments, isolating the catalytic composition further comprises drying the catalytic solid. In some embodiments, drying the catalytic solid comprises drying the catalytic solid at 80° C. for at least 8 hours.
In some embodiments, isolating the catalytic composition further comprises sieving the catalytic solid to isolate the catalytic composition.
Also disclosed herein is a catalytic composition prepared by a process described herein.
Some embodiments of this disclosure relate to a method of treating an exhaust gas stream comprising a pollutant, the method comprising passing the exhaust gas stream through a catalytic article disclosed herein or an exhaust gas treatment system disclosed herein.
In some embodiments, the pollutant comprises hydrocarbons. In some embodiments, the pollutant comprises propene.
In some embodiments, the exhaust gas stream is passed through the catalytic article or the exhaust gas treatment system at a low temperature. In some embodiments, the low temperature is in the range of 100° C. to 150° C.
Claims or descriptions that include “or” or “and/or” between at least one members of a group are considered satisfied if one, more than one, or all of the group members are present in, employed in, or otherwise relevant to a given product or process unless indicated to the contrary or otherwise evident from the context. The disclosure includes embodiments in which exactly one member of the group is present in, employed in, or otherwise relevant to a given product or process. The disclosure includes embodiments in which more than one, or all the group members are present in, employed in, or otherwise relevant to a given product or process.
Furthermore, the disclosure encompasses all variations, combinations, and permutations in which at least one limitation, element, clause, and descriptive term from at least one of the listed claims is introduced into another claim. For example, any claim that is dependent on another claim can be modified to include at least one limitation found in any other claim that is dependent on the same base claim. Where elements are presented as lists, such as, e.g., in Markush group format, each subgroup of the elements is also disclosed, and any element(s) can be removed from the group. It should be understood that, in general, where the disclosure, or aspects of the disclosure, is/are referred to as comprising particular elements and/or features, embodiments of the disclosure or aspects of the disclosure consist, or consist essentially of, such elements and/or features. For purposes of simplicity, those embodiments have not been specifically set forth in haec verba herein. Where ranges are given (such as, e.g., from [X] to [Y]), endpoints (such as, e.g., [X] and [Y] in the phrase “from [X] to [Y]”) are included unless otherwise indicated. Furthermore, unless otherwise indicated or otherwise evident from the context and understanding of one of ordinary skill in the art, values that are expressed as ranges can assume any specific value or sub-range within the stated ranges in different embodiments of the disclosure, to the tenth of the unit of the lower limit of the range, unless the context clearly dictates otherwise.
Those of ordinary skill in the art will recognize or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the disclosure described herein. Such equivalents are intended to be encompassed by the following claims.
The following examples are intended to be illustrative and are not meant in any way to limit the scope of the disclosure.
All syntheses were performed using standard air-free Schlenk techniques. 0.20 mmol of platinum(II) acetylacetonate (Pt(acac)2, 97%, Sigma-Aldrich) was combined with 10 mL trioctylamine (TOA, 97%, Acros Organics), 2.5 mL oleic acid (OLAC, 90%, Sigma-Aldrich), and 0.66 mL oleylamine (OLAM, 70%, Sigma-Aldrich) in a three-neck flask and placed under magnetic stirring. The mixture was evacuated at room temperature for 15 minutes, after which an appropriate amount (50 μL for 2 nm NPs and 220 μL for 5 nm NPs) of trioctylphosphine (TOP, 97%, Sigma-Aldrich) was added. The mixture was then evacuated for an additional 30 minutes at 120° C. to remove any low boiling point impurities. At this point, the reaction mixture was a translucent pale yellow solution. The reaction vessel was then flushed with nitrogen and heated quickly (˜40° C. min−1) to a high temperature (250° C. for 2 nm NPs, and 350° C. for 5 nm NPs). After 30 minutes of reaction at high temperature, the solution was cooled rapidly to room temperature. The particles were isolated by two rounds of precipitation using isopropanol, ethanol, acetone, and methanol as antisolvents and separated by centrifugation (8000 rpm, 3 minutes). The particles were then dispersed in hexanes.
PtxM100-x nanoparticles (NPs) with varying Pt/M ratios were synthesized using a seed-mediated alloying approach. In a three-neck flask, Pt seed (0.1 mmol Pt) dispersed in hexanes was combined with variable quantities of specific metal acetylacetonate precursors to achieve specific Pt/M ratios using two different Pt seed sizes (Table 1). In Table 1, the recited material compositions (PtxM100-x) were determined by ICP-OES.
OLAM (8 mL) was added to the flask, and the mixture was placed under magnetic stirring and evacuated at 70° C. for 30 minutes to remove hexanes and low-boiling point impurities. The reaction mixture was then flushed with nitrogen and heated quickly (˜40° C. min−1) to 280° C. After 30 minutes of reaction at high temperature, the solution was cooled rapidly to room temperature. The particles were then isolated by two rounds of precipitation using toluene, isopropanol, and ethanol as antisolvents and separated by centrifugation (8000 rpm, 3 minutes). Finally, the particles were dispersed in hexanes. NPs were rapidly impregnated onto supports to prevent any leaching of base metal out of the NPs.
The metal concentration in the colloidal NP solutions was determined by thermogravimetric analysis (TGA). 300 μL of NP solution was drop-cast into an aluminum pan, and solvents were evaporated on a hot plate. The pan was transferred in a static air furnace and heated to 500° C. for 20 minutes to completely remove the ligands. Dividing the final mass of product by the initial solution volume provided the metal concentration. An appropriate amount of metal NPs to achieve 0.3 wt % was added to a dispersion of stirred supports in hexane. The mixture was left stirring overnight to ensure full adsorption of NPs onto the support material. The solid was then recovered by centrifugation (8000 rpm, 3 minutes). Final powders were dried at 80° C. overnight and sieved below 180 μm grain size. All samples were fast-treated at 700° C. for 30 seconds in a furnace to remove ligands from the colloidal synthesis following a routine procedure.
To evaluate the effects of Pt/Cu ratio, three different Pt/Cu ratios (3/1, 1/1, and 1/3) were used during synthesis. Additionally, to study the effect of NP size, two Pt NP sizes (2.6 nm (“2 nm”) and 5.1 nm (“5 nm”)) were employed as starting seeds.
After the Pt/M NPs were deposited on a Al2O3 support, ICP-OES analysis and CO chemisorption were used to find the Pt/M ratios and exposed metallic surface areas (Table 2). In Table 2, the material composition and total (Pt+M) wt % were determined using ICP-OES, while the exposed metal surface area was evaluated using CO chemisorption. The final Pt/M compositions were in close agreement with the Pt seed/M precursor ratio used in synthesis. Additionally, it was observed that as Cu content increased, the exposed metal area decreased, demonstrating that the surface was enriched by Cu as more Cu was present in the NPs.
EDS mapping was used to determine the presence of Pt and Cu for the 5 nm Pt/Cu NPs supported on Al2O3(
To determine the alloying extent of the synthesized Pt/M NPs, grazing incidence XRD spectra were measured on NPs that were drop-cast on microscope slides. From the shift of the FCC (111) peak on Pt, the degree of alloying was determined (Table 3). In Table 3, (a) is used to note that the theoretical FCC lattice constant was calculated from the difference in atomic number between Cu/M and Ni/M.
Since Cu and Ni both possess FCC structures, the amount of Cu or Ni that was alloyed with Pt was determined using Vegard's law. For PtCu, 33 at % of Cu was calculated to alloy with Pt, which is consistent with the value determined by ICP-OES (Pt63Cu37). For PtNi, 4 at % of Ni was alloyed with Pt. Because the XRD patterns for PtCo and PtMn resembled the FCC lattice structure, the theoretical FCC lattice constants for Co and Mn were calculated using the difference in atomic number between Cu, Ni, and the target metal using Vegard's law (Table 3).
Another support, lanthanum-stabilized zirconia (LSZ), was also employed in the preparation of supported catalysts. Specifically, 2 nm Pt/Cu NPs were deposited on LSZ. Representative TEM images of the Pt49Cu51 NPs supported on Al2O3 and LSZ are shown in
To avoid thermal and mass gradients in the catalytic bed, the following differential conditions were maintained for catalytic tests: Pt/M nanoparticles were diluted with Al2O3 powder (<180 μm) and reactants were highly diluted (inert gas >90%). Catalytic tests at different space velocities ensured that rates were obtained under strict kinetic control. For light-off curves, 8-40 mg of catalyst was diluted with alumina (calcined at 900° C. for 24 hours) to achieve a total 200 mg of powder for each test. The 200 mg catalyst was packed between acid-washed silica sand layers inside a quartz reactor tube with an internal diameter of 10 mm mounted inside a high-temperature furnace. The sample was pretreated at 300° C. under 02 (5 vol. %)/Ar for 30 minutes. Catalysts were cooled under Ar to 50° C. where the reaction mixture was introduced. The reaction mixture consisted of C3H6 (0.15 vol. %)/Ar, O2 (3 vol. %)/Ar and H2O (10 vol. %)/Ar. Gas Hourly Space Velocity (GHSV) was held at 100,000 mL gcatalyst−1 h−1, and the total flow rate was 50 mL min−1. H2O was introduced by heating a water saturator to 47° C. and flowing Ar carrier through it. The catalyst was then heated to 300° C. at 10° C. min−1 and cooled back down to room temperature in the reaction mixture. The gas composition was monitored using a mass spectroscopy (Hiden HPR20) following the parent molecular ions for C3H6 (41 amu), C3H8 (29 amu), O2 (32 amu), CO2 (44 amu), and H2O (18 amu).
For kinetic experiments, 10-40 mg of catalyst was diluted with alumina to achieve a total 200 mg of powder for each test. Kinetic measurements were conducted using the same pretreatment conditions described for light-off experiments. However, the final conversion was kept below 10% to ensure differential conditions. The reaction mixture was composed of C3H6 (0.15 vol. %)/Ar, O2 (3 vol. %)/Ar and H2O (10 vol. %)/Ar. The kinetic measurements were collected above 100° C. to avoid liquid water condensation. The gas composition was measured by a gas chromatograph (Buck Scientific model 910) using flame ionization detector with a methanizer and thermal conductivity detector with Ar as the carrier gas.
On a Pt-mass basis, all 2 nm Pt/Cu samples showed 2-fold higher CO2 formation rates relative to pure 2 nm Pt sample (
PdCu NPs with a Pd/Cu ratio of 3 were similarly synthesized using pre-formed uniform Pd seeds. The uniformity was maintained on PdCu NPs (
Table 4 compiles a list of alumina supported Pt/Cu bimetallic NP catalysts, Pt NP catalysts, and Pt reference catalysts evaluated. The Pt and Pt/Cu nanoparticles were synthesized according to the procedures described in Examples 1 and 2 and supported on an alumina support based on the procedure described in Example 3. These catalysts are further grouped into two subgroups of samples based on their average metal particle size, 2 nm and 5 nm, respectively. The total metal concentrations of these samples are 1% by weight. The actual Pt concentrations of the bimetallic samples were measured by ICP-OES and are indicated in Table 4. To compare these catalysts with the conventional Pt catalysts, three reference Pt samples were prepared by the incipient wetness technique with Pt concentrations of 1%, 0.8% and 0.6% by weight, respectively.
These two groups of catalysts along with the Pt reference catalysts were evaluated in a simulated automotive exhaust stream to measure their effectiveness in converting carbon monoxide, hydrocarbons and nitric oxide. Before activity measurement, the powder samples were shaped to minimize pressure drop in reactor. A powder sample was first dispersed in deionized water to form a slurry of about 30% solid content. An alumina-based binder, about 5% by weight, was added to the slurry. The slurry was continuously stirred at 100° C. until dry. The dried slurry was calcined at 550° C. for 1 hour in air. The calcined powder was crushed and sieved to 250-500 micrometer fraction. The obtained sample is designated as the fresh sample. A portion of the obtained sample was hydrothermally aged at 650° C. for 50 hours in 10% steam/air mixture, which is designated as the aged sample.
The samples in Table 4 were tested in a separate reactor from the one described in Example 4 under different reaction conditions. The feed gas simulated the exhaust stream of a diesel-powered vehicle, consisting of 500 ppm CO, 167 ppm propene (C3H6), 200 ppm NO, 10% CO2. 10% H2O and balance N2. The concentrations of all components in the feed gas are expressed based on their volume (or molar) concentrations. A 100-mg of sample, diluted with corundum to a volume of 1 mL, was loaded into the reactor, which is equivalent to a monolithic space velocity of 50,000 h−1 assuming 2 g/in3 washcoat loading. Steady-state activity measurement was conducted at temperatures from 125 to 350° C. in 25° C. increment. FTIR and HC analyzers were used to obtain the conversions of CO, C3H6 and NO. This type of measurement allows us to construct a conversion—temperature plot (or light-off curve) similar to that shown
| Number | Date | Country | Kind |
|---|---|---|---|
| 21168990.6 | Apr 2021 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2022/024947 | 4/15/2022 | WO |
