HIGHLY ACTIVE METAL OXIDE SUPPORTED ATOMICALLY DISPERSED PLATINUM GROUP METAL CATALYSTS

Abstract

A nanocatalyst including single atoms of platinum dispersed on a nanoscale metal oxide, and the nanocatalyst comprises 0.01 wt % to 1 wt % platinum. Preparing the nanocatalyst includes combining a solution comprising a nanoscale metal oxide and a compound containing a Group 10 metal to yield a mixture, aging the mixture for a length of time, filtering the mixture to yield a solid, washing the solid to eliminate water soluble anions, and calcining the solid to yield a nanocatalyst including single atoms or clusters of atoms of the Group 10 metal on the nanoscale metal oxide.

Claims

1. A method of preparing a nanocatalyst, the method comprising: combining a solution comprising a nanoscale metal oxide and a compound containing a Group 10 metal to yield a mixture; aging the mixture for a length of time; filtering the mixture to yield a solid; washing the solid to eliminate water soluble anions; and calcining the solid to yield a nanocatalyst comprising single atoms of the Group 10 metal or atom clusters of the Group 10 metal on the nanoscale metal oxide.

2. The method of claim 1, wherein the Group 10 metal is platinum.

3. The method of claim 2, wherein the compound containing the Group 10 metal is a Group 10 metal salt comprising an anion.

4. The method of claim 3, wherein the anion comprises chloride, nitrate, or acetate.

5. The method of claim 3, wherein the compound containing the Group 10 metal salt comprises H.sub.2PtCl.sub.4, H.sub.2PtCl.sub.6, Pt(NH.sub.3).sub.2Cl.sub.4, Pt(NH.sub.3).sub.2Cl.sub.2, H.sub.2Pt(OH).sub.6, or Pt(NH.sub.3).sub.4(NO.sub.3).sub.2.

6. The method of claim 2, wherein a concentration of the platinum is in a range of 0.001 wt % to 5 wt % or 0.01 wt % to 0.5 wt % of the metal oxide.

7. The method of claim 1, wherein the nanoscale metal oxide comprises one or more of Fe.sub.2O.sub.3, FeO.sub.x, CeO.sub.2, CeO.sub.x, TiO.sub.2, TiO.sub.x, CoO.sub.x, Co.sub.3O.sub.4, NiO, Cu.sub.2O, CuO, CuO.sub.x, ZrO.sub.x, NbO.sub.x, MnO.sub.x, and VO.sub.x.

8. The method of claim 1, wherein a pH of the solution is in a range of 0.5 to 7.

9. The method of claim 8, wherein the compound containing the Group 10 metal is H.sub.2PtCl.sub.4 or H.sub.2PtCl.sub.6, and the pH is in a range of 2 to 5.

10. The method of claim 8, wherein the nanoscale metal oxide is Fe.sub.2O.sub.3 and a pH of the solution is in a range of 1 to 6 or 3 to 5.

11. The method of claim 8, wherein the nanoscale metal oxide is CeO.sub.2, the compound containing the Group 10 metal is H.sub.2PtCl.sub.4 or H.sub.2PtCl.sub.6 and a pH of the solution is in a range of 1 to 5.

12. The method of claim 1, wherein the nanoscale metal oxide is Fe.sub.2O.sub.3, the compound containing the Group 10 metal is Pt(NH.sub.3).sub.4(NO.sub.3).sub.2, and a pH of the solution is greater than 10.

13. The method of claim 1, wherein the nanoscale metal oxide is CeO.sub.2, the compound containing the Group 10 metal is Pt(NH.sub.3).sub.4(NO.sub.3).sub.2, and a pH of the solution is greater than 10.

14. The method of claim 1, wherein aging comprises aging the mixture at a temperature between room temperature and 60 C.

15. The method of claim 1, further comprising drying the solid at a temperature less than 120 C. before calcining the solid.

16. The method of claim 1, wherein the nanocatalyst comprises 0.001 wt % to 5 wt % of the Group 10 metal, or 0.005 wt % to 1 wt % of the Group 10 metal, or 0.01 wt % to 0.5 wt % Group 10 metal.

17. The method of claim 1, wherein the nanoscale metal oxide is in powder form.

18. The method of claim 1, wherein the nanoscale metal oxide is in the form of nanocrystallites.

19. The method of claim 1, wherein each atom cluster of the Group 10 metal comprises two to about 10 atoms of the Group 10 metal.

20. The method of claim 19, wherein each atom cluster has a largest dimension of less than 1 nm.

21. A nanocatalyst comprising: single atoms of platinum dispersed on a nanoscale metal oxide, wherein the nanocatalyst comprises 0.01 wt % to 1 wt % platinum.

22. The nanocatalyst of claim 21, wherein the nanoscale metal oxide comprises one or more of Fe.sub.2O.sub.3, FeO.sub.x, CeO.sub.2, CeO.sub.x, TiO.sub.2, TiO.sub.x, CoO.sub.x, Co.sub.3O.sub.4, NiO, Cu.sub.2O, CuO, CuO.sub.x, ZrO.sub.x, NbO.sub.x, MnO.sub.x, and VO.sub.x.

23. The nanocatalyst of claim 21, wherein the nanoscale metal oxide is supported on a refractory oxide comprising one or both of Al.sub.2O.sub.3 and SiO.sub.2, mixtures of Al.sub.2O.sub.3 and SiO.sub.2, cordierites, or mullites.

24. The nanocatalyst of claim 21, wherein the nanoscale metal oxide is Fe.sub.2O.sub.3 or FeO.sub.x and a turnover frequency for CO oxidation at 350 C. exceeds 500/s or 1500/s.

25. The nanocatalyst of claim 21, wherein the nanoscale metal oxide is CeO.sub.2 or CeO.sub.x and a turnover frequency for CO oxidation at 350 C. exceeds 400/s or 1300/s.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0017] FIGS. 1A and 1B depict oxidation of carbon monoxide in the presence of Pt single-atom catalysts (SACs) and cluster catalysts, respectively.

[0018] FIGS. 2A-2D show aberration-corrected high-angle annular dark-field images of used (after CO oxidation at 350 C.) and freshly fabricated Pt.sub.1/Fe.sub.2O.sub.3 and used (after CO oxidation at 350 C.) and freshly fabricated Pt.sub.1/CeO.sub.2 SACs, respectively.

[0019] FIG. 3 shows specific reaction rates of Pt.sub.1 SACs (Pt.sub.1/Fe.sub.2O.sub.3, Pt.sub.1/CeO.sub.2, and Pt.sub.1/-Al.sub.2O.sub.3) and their nanoparticle counterparts (nano-Pt/CeO.sub.2 and nano-Pt/Fe.sub.2O.sub.3) for CO oxidation versus reaction temperature with a feed gas of 1 vol % CO, 4 vol % O.sub.2, and He balance, a space velocity of 9,000 L/gh to 45,000 L/gh, and a pressure of 0.1 MPa.

[0020] FIG. 4A shows the turnover frequency (TOF) of Pt.sub.1/Fe.sub.2O.sub.3 SAC and nano-Pt/Fe.sub.2O.sub.3 catalyst. FIG. 4B shows the TOF of Pt.sub.1/CeO.sub.2 SAC and nano-Pt/CeO.sub.2 catalyst.

DETAILED DESCRIPTION

[0021] Atomically dispersed Group 10 (platinum group metal or PGM) catalysts are synthesized via a modified adsorption method by finely tuning wet chemistry processing parameters including solution pH value, treatment of support materials, volume ratio of metal salt to H.sub.2O, solution temperature, and degree of solution mixing. The optimized synthesis protocols depend at least in part on the specific PGM and the chosen support material.

[0022] In one example, Fe.sub.2O.sub.3 and CeO.sub.2 nanocrystallites were synthesized by a precipitation method in which 10.0 gram iron (III) nitrate nonahydrate (Fe(NO.sub.3).sub.3.9H.sub.2O, Sigma-Aldrich) or 10.0 gram cerium(III) nitrate hexahydrate (Ce(NO.sub.3).sub.3.9H.sub.2O, Sigma-Aldrich) was used as a precursor salt and dissolved into 200 ml deionized (DI) H.sub.2O. 4.7 gram sodium carbonate (Na.sub.2CO.sub.3, Sigma-Aldrich) was dissolved in 200 ml DI H.sub.2O as a precipitant. The sodium carbonate solution was slowly added into the Fe(NO.sub.3).9H.sub.2O solution under rigorous stirring. The addition rate of the Na.sub.2CO.sub.3 aqueous solution was maintained at 1.25 ml/min or lower. The resultant solid powder precipitates were dried at 60 C. for 12 hours in air. The Fe.sub.2O.sub.3 powders were then calcined at 350 C. for 4 hours in air. The CeO.sub.2 powders were calcined at 400 C. for 5 hours in air. The -Al.sub.2O.sub.3 powders were used as control support materials and were purchased from Inframat Advanced Materials.

[0023] Isolated single Pt atoms were dispersed onto the surfaces of Fe.sub.2O.sub.3, CeO.sub.2, and -Al.sub.2O.sub.3 by a strong electrostatic adsorption method. In one example, 500 mg calcined Fe.sub.2O.sub.3 powders were dispersed into 120 ml DI H.sub.2O and the solution pH value was adjusted to 3.0 by adding dilute HCl solution. The appropriately controlled pH value of the salt solution facilitates the adsorption of isolated single Pt atoms and at least in part determines the total amount of Pt atoms that can be adsorbed onto the support surfaces. The corresponding amount (calculated based on the desired weight % of Pt in the catalyst) of chloroplatinic acid hexahydrate (H.sub.2PtCl.sub.6) was dissolved into 50 ml DI H.sub.2O. Then the H.sub.2PtCl.sub.6 aqueous solution was slowly added into the Fe.sub.2O.sub.3 solution under rigorous stirring. The addition rate of the H.sub.2PtCl.sub.6 aqueous solution was maintained at 0.42 ml/min or slower. After completing the addition of the H.sub.2PtCl.sub.6 aqueous solution into the Fe.sub.2O.sub.3 solution, the mixed solution was aged for 2 hours at room temperature. Then the solid precipitates were filtered and dried at 60 C. for 12 hours in air. The precipitant was filtered and washed by DI H.sub.2O until there were no Cl.sup. ions detected by saturated AgNO.sub.3 solution. The powders were then calcined at 300 C. for 2 hours in air with a heating rate of 1 C./min from room temperature to 300 C.

[0024] Similar processes were used to prepare the Pt/-Al.sub.2O.sub.3 and Pt/CeO.sub.2 single-atom catalysts. The actual loadings of the adsorbed Pt can be measured by ICP-MS (Inductively Coupled Plasma-Mass Spectrometry). In one example, the Pt loadings were determined to be 0.029 wt %, 0.013 wt %, and 0.034 wt % on the Fe.sub.2O.sub.3, CeO.sub.2, and -Al.sub.2O.sub.3 support surfaces, respectively.

[0025] In another example, isolated single Pd atoms were dispersed onto the surfaces of Fe.sub.2O.sub.3 powders by a strong electrostatic adsorption method. The corresponding amount of Pd (PdCl.sub.2, Sigma-Aldrich) was first deposited onto the surfaces of the fabricated Fe.sub.2O.sub.3 powders. The pH value of the Pd-containing solution was finely controlled to tune the adsorption amount. After being aged at room temperature for 2 hours and filtered, the solid powders were dried at 60 C. for 12 hours in air. The Pd/Fe.sub.2O.sub.3 powders were then thoroughly washed with DI water and calcined at 300 C. for 2 hours in air. In one example, the actual loading of the Pd on the Fe.sub.2O.sub.3 surfaces was 0.17 wt % by ICP-MS.

[0026] For preparation of control catalysts, colloidal Pt particles were dispersed onto the surfaces of the fabricated Fe.sub.2O.sub.3 and CeO.sub.2 powders. In one example, NaOH (2.32 mmol) and H.sub.2PtCl.sub.6.6H.sub.2O (5.16 mol) was added into 13.3 mL glycol solution under stirring for 1 hour at ambient temperature. The resulting solution was then heated to 140 C. and maintained at 140 C. for 4 hours to produce a brownish colloidal solution. After the colloidal solution was cooled down to room temperature, 100 mg Fe.sub.2O.sub.3 (or CeO.sub.2) powders were dispersed into the colloidal solution under rigorous stirring. After being stirred for 2 hours, the precipitate was filtered and washed thoroughly with distilled water until the filtrate was free of chloride ions (tested by saturated AgNO.sub.3 solution). The resultant precipitate powders were then dried at 60 C. for 12 hours in air and subsequently were calcined at 350 C. for 4 hours in air.

[0027] Table 1 shows the calculated specific reaction rates of Pt at 350 C. (mmol CO/(g Pt.Math.s)) for different O.sub.2/CO ratios.

TABLE-US-00001 TABLE 1 Specific reaction rates of Pt at 350 C. (mmol CO/(g.sub.pt*s)) for different O.sub.2/CO ratios. Samples O.sub.2/CO = 4.0 O.sub.2/CO = 1.0 O.sub.2/CO = 0.5 Pt.sub.1/Fe.sub.2O.sub.3 SAC 7344.2 7908.3 2844.2 Nano-Pt/Fe.sub.2O.sub.3 39.3 193.2 85.6 Pt.sub.1/CeO.sub.2 SAC 3906.6 7121.5 4370 Pt/Al.sub.2O.sub.3 / 0.2 / Pt/CeO.sub.2/Fe.sub.2O.sub.3 / 1.0 / The specific reaction rates of Pt.sub.1 atoms and Pt particles were measured with feed gas of 1.0 vol. % CO, 4.0 vol. % O.sub.2 and He balance (O.sub.2/CO = 4.0); 2.5 vol. % CO, 2.5 vol. % O.sub.2 and He balance (O.sub.2/CO = 1.0); and 2.5 vol. % CO, 1.25 vol. % O.sub.2 and He balance (O.sub.2/CO = 0.5).

[0028] FIGS. 1A and 1B depict oxidation of carbon monoxide in the presence of platinum nanoscale catalysts (or nanocatalysts), including single-atom catalysts (SACs) 100 and cluster catalysts 110, respectively. Single-atom catalyst 100 includes one or more single platinum atoms 102 on metal oxide 104. Cluster catalyst 110 includes one or more platinum clusters 112 on metal oxide 104. Each platinum cluster 112 includes at least two (e.g., two to about ten) platinum atoms. Clusters 112 may be referred to as subnanoclusters with a largest dimension (e.g., diameter) of less than 1 nm. In comparison, platinum nanoparticles are understood to have a smallest dimension (e.g., a diameter) exceeding 2 nm. Platinum single-atom catalysts 100 and cluster catalysts 110 typically include 0.01 wt % to 1 wt % platinum.

[0029] Metal oxide 104 is a nanoscale metal oxide in the form of nanoparticles, nanorods, nanoplates, or other types of nanostructures having one or more dimensions (e.g., all dimensions) in the range of 3 nm to 100 nm. In some cases, metal oxide 104 is typically in the form of crystallites (e.g., nanocrystallites). Metal oxide 104 is typically a metal oxide, preferably a reducible metal oxide. Examples of suitable metal oxides include Fe.sub.2O.sub.3, FeO.sub.x, CeO.sub.2, CeO.sub.x, TiO.sub.2, TiO.sub.x, CoO.sub.x, Co.sub.3O.sub.4, NiO, NiO.sub.x, Cu.sub.2O, CuO, CuO.sub.x, ZrO.sub.2, ZrO.sub.x, NbO.sub.x, MnO.sub.x, and VO.sub.x.

[0030] In some cases, platinum single-atom catalysts 100 and cluster catalysts 110 are on a high-surface-area (at least 50 m.sup.2/g or at least 100 m.sup.2/g) support 114. Examples of suitable supports for nanoscale metal oxides include refractory oxides, such as Al.sub.2O.sub.3, SiO.sub.2, MgO, ZrO.sub.2, cordierites, mullites, or a combination thereof.

[0031] FIGS. 2A-2D show aberration-corrected high-angle annular dark-field images of used (after CO oxidation at 350 C.) and freshly fabricated Pt.sub.1/Fe.sub.2O.sub.3 and used and freshly fabricated Pt.sub.1/CeO.sub.2 SACs, respectively.

[0032] FIG. 3 shows specific reaction rates of single Pt.sub.1 atoms (Pt.sub.1/Fe.sub.2O.sub.3 SAC, Pt.sub.1/CeO.sub.2 SAC and Pt.sub.1/-Al.sub.2O.sub.3SAC) and nanoparticle Pt (nano-Pt/CeO.sub.2 and nano-Pt/Fe.sub.2O.sub.3) catalysts for CO oxidation versus reaction temperature with a feed gas of 1 vol % CO, 4 vol % O.sub.2, and He balance, a space velocity of 9,000 L/gh to 45,000 L/gh, and a pressure of 0.1 MPa.

[0033] FIG. 4A shows the TOF of Pt.sub.1/Fe.sub.2O.sub.3 SAC and nano-Pt/Fe.sub.2O.sub.3 catalyst. FIG. 4B shows the TOF of Pt.sub.1/CeO.sub.2 SAC and nano-Pt/CeO.sub.2 catalyst.

[0034] Although this disclosure contains many specific embodiment details, these should not be construed as limitations on the scope of the subject matter or on the scope of what may be claimed, but rather as descriptions of features that may be specific to particular embodiments. Certain features that are described in this disclosure in the context of separate embodiments can also be implemented, in combination, in a single embodiment. Conversely, various features that are described in the context of a single embodiment can also be implemented in multiple embodiments, separately, or in any suitable sub-combination. Moreover, although previously described features may be described as acting in certain combinations and even initially claimed as such, one or more features from a claimed combination can, in some cases, be excised from the combination, and the claimed combination may be directed to a sub-combination or variation of a sub-combination.

[0035] Particular embodiments of the subject matter have been described. Other embodiments, alterations, and permutations of the described embodiments are within the scope of the following claims as will be apparent to those skilled in the art. While operations are depicted in the drawings or claims in a particular order, this should not be understood as requiring that such operations be performed in the particular order shown or in sequential order, or that all illustrated operations be performed (some operations may be considered optional), to achieve desirable results.

[0036] Accordingly, the previously described example embodiments do not define or constrain this disclosure. Other changes, substitutions, and alterations are also possible without departing from the spirit and scope of this disclosure.