Patent Application
20230366111
The present invention relates to single-atom catalysts and their manufacture. More specifically, the present invention is concerned with low noble metal loading without compromising their mass activities.
With the depletion of fossil fuels (coal, oil, and natural gas), serious environmental pollution, and global warming, the exploration of safe, clean, efficient, sustainable, and environmental-friendly energy sources has become a major social and technological pursuit in the twenty-first century. Hydrogen is regarded as a real clean energy alternative to fossil fuels owing to its high-energy but carbon-free content. The realization of the hydrogen economy has led to the need for efficient and sustainable methods of generation of hydrogen. One of the most attractive technologies is direct electrocatalysis water splitting. Water splitting is thus the main process in clean energy technologies,[A1-5] such as proton exchange membrane (PEM) water electrolyzers and conventional alkaline water electrolyzers.
The process of water electrolysis is based upon two half-reactions: one reaction is oxygen evolution reaction (OER) to generate oxygen, and the other reaction is hydrogen evolution reaction (HER) to produce hydrogen. In the process of HER, an advanced catalyst is required to decrease the overpotential (q) to obtain high efficiency. Up to now, platinum (Pt) group metal-based (PGM-based) materials are generally considered as state-of-the-art electrocatalysts for the HER. Nevertheless, their high cost and limited reservation seriously limit PGM-based materials' large-scale application. Hydrogen evolution reaction (HER) is thus an essential step in water splitting for sustainable hydrogen generation, but the use of rare and expensive precious metal catalysts seriously limits the widespread commercialization of these clean energy devices.[A6-11] In this regard, extensive efforts have been devoted to developing non-Pt and low-Pt electrocatalysts for HER.
On one hand, the past few years have witnessed a rapid development of earth-abundant non-Pt materials (Fe-, Co-, Ni-, Mo-, Cu-, W-, Al-, Zn-, and Mn-based compounds) for efficient HER catalysis in acidic, neutral and alkaline solutions.[A12-20] Nevertheless, for the non-noble compounds, it remains a big challenge to achieve a Pt-like catalytic activity.
Therefore, the development of low-loading, high-activity, and high stability PGM-based catalysts is essential for the widespread commercialization of electrocatalysis water-splitting technology.
To address this issue, developing low-PGM electrocatalysts for HER are highly desired. Lowering the dosage of Pt, using supported Pt nanoparticles on a substrate is a general way to increase the Pt catalytic activity and improve the utilization efficiency. However, the geometry of nanoparticles limits the majority of the Pt atoms to the particle core, making them ineffective, as only the surface atoms are involved in the chemical reaction.[A21]
So far, there have been mainly two different ways to solve this problem. First, alloying Pt together with other 3d transition metals (M=Pd, Ag, Ru, Rh, Fe, Co, Ni, Cu, Cr, Ti, V, Pb, Mn, etc.). Second, downsizing the Pt nanoparticles to single-atom catalysts (SACs) is one of the most effective strategies for improving the Pt utilization efficiency and, therefore, lowering the cost of catalyst materials.
Theoretically, downsizing the platinum particles to single atoms is one of the most effective strategies for improving the Pt utilization efficiency and, therefore, lowering the cost of catalyst materials. It has been proved that single-atom catalysts (SACs) with only isolated single atoms dispersed on a support surface are more reactive than metal particles or clusters in some cases.[A22,23] Indeed, several groups have successfully prepared Pt-based SACs to minimize the amount of Pt metal required to catalyze the HER and other reactions efficiently.[A21,24-27]
In general, there are five important strategies to prepare SACs, including the wet-chemistry method,[A28] atomic layer deposition (ALD),[A29] metal-organic framework (MOF)-derived method,[A30] high-temperature atom trapping from bulk particles,[A31] and vacancies/defects immobilization.[A32′33] However, these methods suffer from severe drawbacks such as low metal loading, high equipment costs, high pyrolysis temperature, and low yields.[A34]
Overall, SACs with ultralow loading, high activity, good selectivity, and high atom utilization efficiency (up to 100%) have attracted much attention in various catalytic fields. However, developing a simple, facile and practical approach to synthesizing SACs material with well-defined sites is very challenging.
EMBODIMENT 1. A single-atom catalyst comprising nanofibers of a conductive material and a plurality of single-atom metal sites uniformly dispersed on the surface of each of the nanofibers, wherein each single-atom metal site comprises (preferably consists of) a single atom of each of one or more metal adsorbed on the surface of one of the nanofibers, and wherein the single-atom metal sites contain the same metal(s) or different metals.
EMBODIMENT 2. The catalyst of embodiment 1, wherein the one or more metal are selected from transition metals (e.g., Co, Mo, W, Ni, Fe, Mn, Cu, Sn, In, etc.), rare earth metals (e.g., La, Y, Sc, Ce, Er, Pr, Nd, Dy, etc.), precious/rare metals (e.g., Pt, Ru, Ir, Rh, Au, Pd, etc.), more preferably Pt, Ru, or Ir, and most preferably Pt.
EMBODIMENT 3. The catalyst of 1 or 2, wherein each single-atom metal site comprises (preferably consists of) a single atom of one metal.
EMBODIMENT 4. The catalyst of embodiment 3, wherein the one metal is a transition metal, a rare earth metal, Ru, Pd, or Pt, more preferably Ru, Pd, or Pt, and most preferably Pt.
EMBODIMENT 5. The catalyst of any one of embodiments 2 to 4, wherein the Pt in the catalyst has an oxidation state (δ+) of 4>δ+>0, preferably 3>δ+>1, and more preferably of about 2.
EMBODIMENT 6. The catalyst of any one of embodiments 1 to 5, having a mass loading of the metal of at least about 1.2, preferably at least about 2, more preferably at least about 2.5, yet more preferably at least about 2.6, even more preferably at least about 2.7, and most preferably at least about 2.8 μg cm-2 (μg of metal per cm2 of surface of the nanofibers).
EMBODIMENT 7. The catalyst of any one of embodiments 1 to 6, wherein the nanofibers are between about 50 nm and about 500 nm, preferably about 100 nm and about 300 nm, and most preferably about 200 nm in average diameter.
EMBODIMENT 8. The catalyst of any one of embodiments 1 to 7, wherein the conductive material is a metal, a conductive oxide-based porous material, a conductive carbon material, or a conductive polymer, preferably a conductive polymer.
EMBODIMENT 9. The catalyst of embodiment 8, wherein the oxide-based porous material is TiO2, Fe2O3, Fe3O4, ZnO, CeO2, Al2O3, ZrO2, CuO, WO3, Co3O4, MgO, preferably TiO2, Fe2O3, or ZnO.
EMBODIMENT 10. The catalyst of embodiment 8 or 9, wherein the conductive carbon material is graphene, graphdiyne, carbon nanotubes, or carbon black, preferably graphene.
EMBODIMENT 11. The catalyst of any one of embodiments 8 to 12, wherein the conductive polymer is poly(pyrrole), polycarbazole, polyindole, polyazepines, polyaniline, poly (3,4-ethylenedioxythiophene), poly(p-phenylene sulfide), preferably poly(pyrrole), or polyaniline, and most preferably polyaniline.
EMBODIMENT 12. The catalyst of any one of embodiments 1 to 11, wherein the nanofibers are nanofibers of a conductive polymer.
EMBODIMENT 13. The catalyst of any one of embodiments 1 to 12, wherein the nanofibers are interconnected with each other.
EMBODIMENT 14. The catalyst of any one of embodiments 1 to 13, wherein the nanofibers form a three-dimensional macroporous structure.
EMBODIMENT 15. The catalyst of any one of embodiments 1 to 14, wherein the surface of each of the nanofibers is rough, preferably the surface of each of the nanofibers bears protrusions, more preferably pointed protrusions.
EMBODIMENT 16. The catalyst of any one of embodiments 1 to 5, wherein the surface of each of the nanofibers is free or substantially free from all materials except the plurality of single-atom metal sites.
EMBODIMENT 17. The catalyst of any one of embodiments 1 to 16, wherein the nanofibers are supported onto a conductive substrate, more preferably a current collector.
EMBODIMENT 18. The catalyst of embodiment 17, wherein the conductive substrate is Ni, Co, Fe, Cu, Ti, Mo, a metal-based foam, plate, or mesh, carbon cloth, carbon paper, or graphite foam, preferably a Ti mesh, Cu foam, Ni foam, or carbon cloth, and most preferably carbon cloth.
EMBODIMENT 19. The catalyst of embodiment 17 or 18, wherein a surface of the conductive substrate is uniformly covered by the nanofibers.
EMBODIMENT 20. The catalyst of any one of embodiments 1 to 19, exhibiting an X-ray diffraction (XRD) pattern that is free of diffraction peaks related to clusters or nanoparticles of the metal(s); preferably when the metal is Pt, the XRD pattern of the catalyst is free of diffraction peaks related to clusters or nanoparticles of Pt at 39.6, 47.4, and 67.1°; more preferably the XRD pattern of the catalyst is as shown in
EMBODIMENT 21. The catalyst of any one of embodiments 1 to 20, wherein when observed by high-resolution transmission electron microscopy (HRTEM), the catalyst appears free of clusters or nanoparticles of the metal(s).
EMBODIMENT 22. The catalyst of any one of embodiments 1 to 21, exhibiting a Fourier Transform Extended X-ray Absorption Fine Structure (FT-EXAFS) spectrum free of a peak related to a metal-metal bond and/or free of a peak related to a metal-chlorine bond; preferably when the metal is Pt, the FT-EXAFS spectrum is free of a peak related to the metal-metal (Pt—Pt) bond at ˜2.7 Å.
EMBODIMENT 23. The catalyst of any one of embodiments 1 to 22, wherein the metal(s) are anchored on nitrogen atoms at the surface of the nanofibers.
EMBODIMENT 24. The catalyst of any one of embodiments 1 to 23, wherein the conductive material comprises a lone electron pair on a N atom.
EMBODIMENT 25. The catalyst of embodiment 24, wherein the conductive material is poly(pyrrole), polycarbazole, polyindole, polyazepine, or polyaniline, preferably poly(pyrrole), or polyaniline, and most preferably polyaniline.
EMBODIMENT 26. The catalyst of embodiment 24 or 25, wherein the N atoms and the single-atom metal sites are homogeneously dispersed on the surface of each of the nanofibers.
EMBODIMENT 27. The catalyst of any one of embodiments 1 to 26, exhibiting a FT-EXAFS spectrum comprising a peak related to a metal-N bond; preferably when the metal is Pt, the peak related to the metal-N bond (Pt—N bond) is at about 1.8 Å and more preferably the catalyst exhibits a FT-EXAFS spectrum as shown in
EMBODIMENT 28. A method of manufacturing a single-atom catalyst, the method comprising the steps of:
EMBODIMENT 29. The method of embodiment 28, wherein the nanostructures are subnano-clusters, nanoparticles, or nanofibers, preferably nanofibers.
EMBODIMENT 30. The method of embodiment 28 or 29, wherein the catalyst is a catalyst as defined in any one of embodiments 1 to 27.
EMBODIMENT 31. The method of any one of embodiments 28 to 30, wherein step B comprises drop-casting a suspension of the nanostructures of a conductive material on the substrate.
EMBODIMENT 32. The method of embodiment 31, wherein step B comprises preparing a suspension of the nanostructure in a volatile solvent, such as ethanol, drop-casting the suspension on the substrate, and allowing the solvent to evaporate.
EMBODIMENT 33. The method of any one of embodiments 28 to 30, wherein step B comprises electrodepositing nanostructures of a conductive material on the substrate.
EMBODIMENT 34. The method of embodiment 33, wherein step B comprises electrodepositing the nanofibers using a three-electrode assembly comprising an electrolyte, the conductive substrate as a working electrode, a graphite electrode as a counter electrode, and an Ag/AgCl electrode as the reference electrode.
EMBODIMENT 35. The method of embodiment 34, wherein a potential of about 0.6 to about 1.2 V vs. Ag/AgCl, preferably about 0.7 to about 0.9 V vs. Ag/AgCl is applied to the working electrode for a period of about 1 min to about 60 min, preferably about for about 5 to about 30 minutes.
EMBODIMENT 36. The method of embodiment 34 or 35, wherein the electrolyte comprises the conductive material or a monomer of the conductive materiel.
EMBODIMENT 37. The method of any one of embodiments 34 to 36, wherein the conductive material is polyaniline, and the electrolyte comprises aniline, preferably about 1 to about 10 v/v % of aniline, and more preferably about 2 to about 5 v/v % of aniline, based on the totally volume of the electrolyte.
EMBODIMENT 38. The method of any one of embodiments 34 to 37, wherein the electrolyte further comprises an acid, preferably HCl, HNO3, H2SO4, HClO4, or phytic acid, and more preferably HCl; preferably between about 1 to about 20 v/v % of the acid, and more preferably between about 4 to about 10 v/v % of the acid, based on the totally volume of the electrolyte.
EMBODIMENT 39. The method of any one of embodiments 34 to 37, further comprising the step of washing, and then preferably drying, the conductive substrate with the electrodeposited nanofibers, wherein water is preferably used for said washing, and wherein the drying is preferably at a temperature of 60 to about 100° C.
EMBODIMENT 40. The method of any one of embodiments 28 to 40, wherein step C comprises immersing the conductive substrate with the nanostructures in a solution comprising the above-mentioned complex ions, and allowing the complex ions to adsorb on the surface of the nanostructures.
EMBODIMENT 41. The method of embodiment 40, wherein the complex ions are: FeF63−, Co(SCN)42−, Cr(CN)63−, Co(CN)63−, Fe(CN)63−, Ni(CN)42−, [Cu(NH3)Cl5]3−, [CuCl3(H2O)]−, RuCl62−, AuCl4−, IrCl62−, PtCl62−, and/or PdCl42−.
EMBODIMENT 42. The method of embodiment 40 or 41, further comprising the step of preparing the solution comprising the complex ions by adding a compound comprising the complex ion to a solvent.
EMBODIMENT 43. The method of embodiment 42, wherein the solvent is methanol, alcohol and water, preferably water, more preferably deionized water.
EMBODIMENT 44. The method of embodiment 42 or 43, wherein the compound comprising the complex ion is an acid or a salt.
EMBODIMENT 45. The method of any one of embodiments 28 to 44, further comprising between step C and D, the step of washing, and then drying the conductive substrate after the complex ions have adsorbed on the surface of the nanostructures, wherein water is preferably used for said washing.
EMBODIMENT 46. The method of any one of embodiments 28 to 45, wherein step D comprises electrochemically reducing the metal(s) using one linear sweep voltammetry (LSV) scan on the.
EMBODIMENT 47. The method of embodiment 46, wherein a voltage is scanned from about 0.2 to about −1.0 V, preferably from about 0 to about −0.8 V, and more preferably from about 0 to about −0.5 V.
EMBODIMENT 48. The method of embodiment 46 or 47, wherein a scan rate of about 0.1 to about 200 mV s−1, preferably of about 1 to about 5 mV s−1 is used.
EMBODIMENT 49. The method of any one of embodiments 46 to 48, wherein a solution of H2SO4, HClO4, KOH, or NaOH, or a phosphoric acid buffer, and more preferably a solution of H2SO4, is used as an electrolyte.
In the appended drawings:
Turning now to the invention in more details, there is provided a single-atom catalyst (SAC) comprising nanofibers of a conductive material and a plurality of single-atom metal sites uniformly dispersed on the surface of each of the nanofibers, wherein each single-atom metal site comprises a single atom of each of one or more metal adsorbed on the surface of one of the nanofibers, and wherein the single-atom metal sites contain the same metal(s) or different metals.
It has been unexpectedly found that such catalysts, particularly those according to preferred embodiments of the invention, can have mass activities for HER that are nearly 50 times higher than that of commercial catalysts of the same type (see in the Examples below PANI-Pt-10/CC vs commercial Pt/C). Hence, the catalytic activity for HER is significantly enhanced, while the noble metal usage is drastically reduced.
The PANI-Pt-10/CC material also exhibits good catalytic activity under neutral and basic conditions. That is, this single-atom-based material could find its applications in a wide pH range (pH 0-14), which can be easily adapted to the various water electrolyzers such as proton exchange membrane (PEM) and anion exchange membrane (AEM) water electrolyzers, conventional alkaline water electrolyzers, neutral electrolyzers, even hybrid ones (e.g., acid-base, neutral-base).
By changing the nature of the metal(s), the catalysts of the invention can be used for many applications, such as:
As noted above, the single-atom catalyst of the invention comprises nanofibers of a conductive material and a plurality of single-atom metal sites uniformly dispersed on the surface of each of the nanofibers, wherein each single-atom metal site comprises (preferably consists of) a single atom of each of one or more metal adsorbed on the surface of one of the nanofibers, and wherein the single-atom metal sites contain the same metal(s) or different metals.
For certainty, “a single atom of each of one or more metal” means that the single-atom metal sites may comprise a single atom of one metal (e.g., one atom of Pt), a single atom of each of two metals (e.g., one atom of Pt+one atom of Au), a single atom of each of three metals (e.g., one atom of Pt+one atom of Au+one atom of Ir), etc.
As noted above, the single-atom metal sites in the catalyst of the invention contain the same metal(s) or different metals. This means that a catalyst can comprise sites with one atom of a metal (e.g., Au), sites with one atom of another metal (e.g., Pt), and even sites with one atom of each of two metals (Au+Ir).
Preferably, the single-atom metal sites contain the same metal(s).
As noted, the single-atom metal sites are uniformly dispersed on the surface of each of the nanofibers. Herein, “uniformly dispersed” means that the distribution the single-atom metal sites is constant throughout the surface.
The one or more metals are selected from all metals that are useful as a catalyst, preferably they are selected from transition metals (e.g., Co, Mo, W, Ni, Fe, Mn, Cu, Sn, In, etc.), rare earth metals (e.g., La, Y, Sc, Ce, Er, Pr, Nd, Dy, etc.), precious/rare metals (e.g., Pt, Ru, Ir, Rh, Au, Pd, etc.), more preferably Pt, Ru, or Ir, and most preferably Pt.
In preferred embodiments, each single-atom metal site comprises (preferably consists of) a single atom of one metal. Preferably, the one metal is a transition metal, a rare earth metal, Ru, Pd, or Pt, more preferably Ru, Pd, or Pt, and most preferably Pt.
In preferred embodiments, the Pt in the catalyst has an oxidation state (5′) of 4>δ+>0, preferably 3>δ+>1, and more preferably of about 2.
In preferred embodiments, the catalyst has a mass loading of the metal of at least about 1.2, preferably at least about 2, more preferably at least about 2.5, yet more preferably at least about 2.6, even more preferably at least about 2.7, and most preferably at least about 2.8 μg cm−2 (lig of metal per cm2 of surface of the nanofibers).
In embodiments, the conductive material forming the nanofibers is a metal, a conductive oxide-based porous material, a conductive carbon material, or a conductive polymer, preferably a conductive polymer.
In embodiments, the oxide-based porous material is TiO2, Fe2O3, Fe3O4, ZnO, CeO2, Al2O3, ZrO2, CuO, WO3, Co3O4, MgO, preferably TiO2, Fe2O3, or ZnO.
In embodiments, the conductive carbon material is graphene, graphdiyne, carbon nanotubes, or carbon black, preferably graphene.
In embodiments, the conductive polymer is poly(pyrrole), polycarbazole, polyindole, polyazepines, polyaniline, poly (3,4-ethylenedioxythiophene), poly(p-phenylene sulfide), preferably poly(pyrrole), or polyaniline, and most preferably polyaniline.
In preferred embodiments, the nanofibers are nanofibers of a conductive polymer. In preferred embodiments, the nanofibers are between about 50 nm and about 500 nm, preferably about 100 nm and about 300 nm, and most preferably about 200 nm in average diameter.
In preferred embodiments, the nanofibers are interconnected with each other.
In preferred embodiments, the nanofibers form a three-dimensional macroporous structure.
In preferred embodiments, the surface of each of the nanofibers is rough, which is beneficial for the absorption of the metal ions during the manufacture of the catalyst. In more preferred embodiments, the surface of each of the nanofibers bears protrusions, preferably pointed protrusions. In other words, it can be said that the surface of each of the nanofibers is jagged. This phenomenon can increase the active surface area of the catalyst, which is further beneficial for improving the catalytic activity.
In preferred embodiments, only the plurality of single-atom metal sites is present on the surface of each of the nanofibers. In other words, the surface of each of the nanofibers is free or substantially free from all materials except the plurality of single-atom metal sites.
In preferred embodiments, the nanofibers of the conductive material are supported onto a conductive substrate, more preferably a current collector. In embodiments, the conductive substrate is Ni, Co, Fe, Cu, Ti, Mo, etc. metal-based foam/plate/mesh, carbon cloth, carbon paper, or graphite foam, preferably Ti mesh, Cu foam, Ni foam, or carbon cloth, and most preferably carbon cloth.
In preferred embodiments, a surface of the conductive substrate is uniformly covered by the nanofibers.
As noted above, each single-atom metal site comprises (preferably consists of) a single isolated atom of each or one or more metal. For more certainty, the single-atom metal sites do not comprise the metal(s) as part of nanoparticles or clusters of metal atoms. In other words, the metal sites are atomically dispersed on the surface of the nanostructures.
In preferred embodiments, the catalyst exhibits an XRD pattern that is free of diffraction peaks related to clusters or nanoparticles of the metal(s). In such embodiments, when the metal is Pt, the XRD pattern of the catalyst would be free of diffraction peaks related to clusters or nanoparticles of Pt, which would be at 39.6, 47.4, and 67.1°. In preferred such embodiments, the XRD pattern of the catalyst is as shown in
In preferred embodiments, when observed by high-resolution transmission electron microscopy (HRTEM), the catalyst appears free of clusters or nanoparticles of the metal(s).
In embodiments, the catalyst exhibits a FT-EXAFS spectrum free of a peak related to a metal-metal bond and/or free of a peak related to a metal-chlorine bond. In embodiments in which the metal is Pt, the peak related to the metal-metal (Pt—Pt) bond would be about at ˜2.7 Å (see
In preferred embodiments, the metal(s) are anchored on nitrogen atoms at the surface of the nanofibers.
In preferred such embodiments, the conductive material (preferably the conductive polymer) comprises a lone electron pair on a N atom. In embodiments, the conductive material comprising a lone electron pair on a N atom is poly(pyrrole), polycarbazole, a polyindole, a polyazepine, or polyaniline, preferably poly(pyrrole), or polyaniline, and most preferably polyaniline.
Such conductive materials with a lone electron pair on a N atom can effectively capture the H+ from hydronium ions to form protonated amine groups that can be electro-reduced easily into atomically dispersed metal sites.
In preferred such embodiments, the catalyst exhibits a FT-EXAFS spectrum comprising a peak related to a metal-N bond. In embodiments in which the metal is Pt, the peak related to the metal-N bond (Pt—N bond) is at about 1.8 Å. In more preferred embodiments, the catalyst exhibits a FT-EXAFS spectrum as shown in
In preferred such embodiments, the N atoms and the single-atom metal sites are homogeneously dispersed on the surface of each of the nanofibers. Herein, “homogenously dispersed” means that the composition of the surface, when considering the N atoms and the single-atom metal sites, is uniform throughout the surface. In preferred such embodiments, the Other advantages of polyaniline include having a high electrochemical conductivity, being easily prepared in an aqueous medium, being chemically stable, and being highly conductive in acidic media.
More importantly, Pt—N coordination can be confirmed by N K-edge XANES results. As shown in
In another related aspect of the invention, there is provided a method of manufacturing a single-atom catalyst of the invention comprises nanostructures of a conductive material and a plurality of single-atom metal sites uniformly dispersed on the surface of each of the nanofibers, wherein each single-atom metal site comprises (preferably consists of) a single atom of each of one or more metal adsorbed on the surface of one of the nanofibers, and wherein the single-atom metal sites contain the same metal(s) or different metals.
In embodiments, the nanostructures are subnano-clusters, nanoparticles, nanorods, nanowires, nanosheets, nanocubes, nanospheres, nanoflowers, or nanofibers, preferably nanofibers.
In preferred embodiments, the method is a method of manufacturing the above catalyst.
This method allows producing catalysts with the above mentioned good catalytic activity for HER, while drastically reducing noble metal usage. Even more interestingly, this method is useful to produce single-atom catalysts containing various metals useful for various purposes. Hence, this method is a universal strategy that opens up a new avenue for the design of atomically dispersed metal sites supported on conducting materials. The method of the invention is a simple, facile, fast and in-situ strategy to synthesize a series of atomically dispersed metal sites including Pt, Ru and Pd on e.g., polyamine (PANI) nanofibers. Finally, the absence of any other chemical reducing agent or surfactant when creating the single-atom metal sites in the method of the invention results in a clean surface, offering maximum exposure of active sites.
The method of the invention comprises the steps of:
In this method, the conductive substrate, the conductive material, the nanofibers, and the metals are as described in the previous sections, including the preferred embodiments thereof.
In preferred embodiment, the conductive substrate is carbon cloth.
In embodiments, step B comprises drop-casting a suspension of the nanostructures of a conductive material on the substrate. Preferably, step B comprises preparing a suspension of the nanostructure in a volatile solvent, such as ethanol, drop-casting the suspension on the substrate, and allowing the solvent to evaporate.
In alternative and preferred embodiments, step B comprises electrodepositing nanostructures of a conductive material on the substrate. Preferably, step B comprises electrodepositing the nanofibers using a three-electrode assembly comprising an electrolyte, the conductive substrate as a working electrode, a graphite electrode as a counter electrode, and an Ag/AgCl electrode as the reference electrode.
In preferred embodiments, a potential of about 0.6 to about 1.2 V vs. Ag/AgCl, preferably about 0.7 to about 0.9 V vs. Ag/AgCl is applied to the working electrode for a period of about 1 min to about 60 min, preferably about 5 to about 30 minutes.
In preferred embodiments, the electrolyte comprises the conductive material or a monomer of the conductive materiel.
Preferably, the conductive material is polyaniline, and the electrolyte comprises aniline. In preferred embodiments, the electrolyte comprises about 1 to about 10 v/v %, preferably about 2 to about 5 v/v % of aniline, based on the totally volume of the electrolyte.
In preferred embodiments, the electrolyte further comprises an acid. Preferably, the acid is HCl, HNO3, H2SO4, HClO4, or phytic acid, preferably HCl. In preferred embodiments, the electrolyte comprises between about 1 to about 20 v/v %, preferably between about 4 to about 10 v/v % of the acid, based on the totally volume of the electrolyte.
This step advantageous yields rough nanofibers as described above.
In embodiment, the method further comprises the step of washing, and then preferably drying, the conductive substrate with the electrodeposited nanofibers. In embodiments, water is used for said washing. In embodiments, the drying is at 60-100° C.
In embodiments, step B comprises immersing the conductive substrate with the electrodeposited nanofibers in a solution comprising the above-mentioned complex ions, and allowing the complex ions to adsorb on the surface of the electrodeposited nanofibers.
As well known in the art, “complex ions” are ions comprising one or more ligands attached to a central metal cation (often a transition metal)—more rarely to two or more central metal cations—with a dative bond. It can be said that a complex ion is the charged version of a coordination complex. Also, a “ligand” is a species which can use its lone pair of electrons to form a dative covalent bond with a transition metal.
In the method of the invention, the complex ions comprise a single atom of each of one or more metal, preferably a single atom of one metal, this would be the abovementioned central metal cation. This single atom of the metal is attached to one or more ligands. Also, as noted above, the complex ions have a total negative charge. Thus, it can be said that these complex ions are of formula:
[Mx+(ligand)y]z−,
The ligands in the complex ion can be identical to one another or the complex ion can comprise two or more different ligands. It will be apparent to the skilled person that since the complex ion has a total negative charge and the single atom(s) of the metal(s) bear(s) a positive charge, at least some of the ligands in the complex ion must be negatively charged.
In preferred embodiments, all the ligands are the same and are negatively charged.
Non-limiting examples of ligands are F−, H2O, NH3, Cl−, SCN−, and CN−, preferably Cl−.
Non-limiting examples of complex ions include: FeF63−, Co(SCN)42−, Cr(CN)63−, Co(CN)63−, Fe(CN)63−, Ni(CN)42−, [Cu(NH3)Cl5]3−, [CuCl3(H2O)]−, RuCl62−, AuCl4−, IrCl62−, PtCl62−, and PdCl42−.
To make a catalyst in which all the single-atom metal sites comprise a single atom of a same metal, complex ions comprising a single atom of a single metal can be used. When all the metal sites comprise a single atom of each of two metals, complex ions comprising a single atom of each of two metals can be used or complex ions comprising a single atom of each of two metals can be used, etc. To make a catalyst comprising different metal sites, a combination of complex ions is used, each complex ion comprising the metal(s) to be found at each metal site.
In embodiments, step C further comprises the step of preparing the solution comprising the complex ions by adding a compound comprising the complex ion to a solvent. Preferred solvents include methanol, alcohol and water, preferably water, more preferably deionized water. The compound comprising the complex ion can be an acid or a salt. The acid would be of formula:
Hz[Mx+(ligand)y]z−
while the salt would be of formula:
Cw[Mx+(ligand)y]z−
wherein Cw represent one or more cation with a total charge of z+.
In embodiments, the method further comprises between step C and D, the step of washing, and then drying the conductive substrate after the complex ions have adsorbed on the surface of the nanostructures. In embodiments, water is used for said washing.
In embodiments, step D comprises electrochemically reducing the metal(s) using one linear sweep voltammetry (LSV) scan.
In this step, the voltage is scanned from an upper limit to a lower limit, preferably from about 0.2 to about −1.0 V, preferably from about 0 to about −0.8 V, and most preferably from about 0 to about −0.5 V.
In preferred embodiments, a scan rate of about 0.1 to about 200 mV s−1, preferably of about 1 to about 5 mV s−1 is used.
In preferred embodiments, the electrolyte is an acidic, neutral, or alkaline aqueous solution, preferably a solution of H2SO4, HClO4, KOH, or NaOH, phosphoric acid buffer, and most preferably a solution of H2SO4.
In conclusion, a preferred method of the invention, as described above, has the following advantages:
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context.
The terms “comprising”, “having”, “including”, and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to”) unless otherwise noted. In contrast, the phrase “consisting of” excludes any unspecified element, step, ingredient, or the like. The phrase “consisting essentially of” limits the scope to the specified materials or steps and those that do not materially affect the basic and novel characteristic(s) of the invention.
Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All subsets of values within the ranges are also incorporated into the specification as if they were individually recited herein.
All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context.
The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed.
No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Herein, the term “about” has its ordinary meaning. In embodiments, it may mean plus or minus 10% or plus or minus 5% of the numerical value qualified.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.
Other objects, advantages and features of the present invention will become more apparent upon reading of the following non-restrictive description of specific embodiments thereof, given by way of example only with reference to the accompanying drawings.
The present invention is illustrated in further details by the following non-limiting examples.
For hydrogen evolution reaction (HER), the development of efficient and robust non-Pt and low-Pt catalysts with equivalent or even superior performance to commercial Pt-based catalysts are highly desired, yet remains a grand challenge.
Herein, we report a facile and fast in-situ electrochemical strategy to synthesize atomically dispersed metal sites including platinum (Pt), ruthenium (Ru) and palladium (Pd) on the surface of polyaniline (PANI) supported on carbon cloth (PANI-M/CC).
Indeed, catalytic materials are stabilized onto certain substrates in order to adequately expose their active sites. PANI not only possesses high electrochemical conductivity but also can effectively capture the H+ from hydronium ions to form protonated amine groups that can be electro-reduced easily on atomically dispersed metal sites. Conducting polymers such as PANI is easily prepared in an aqueous medium. Particularly, it is chemically stable and highly conductive in acidic media. More importantly, PANI can effectively capture protons from solutions to form protonated amine groups, which can subsequently be electro-reduced easily to generate H2 during the HER process.[A35]
As an example, the atomically dispersed Pt sites anchored on carbon cloth supported PANI (PANI-Pt/CC) exhibited superior activity and stability toward HER. In fact, the mass activity of PANI-Pt-10/CC reached 25 Å mgPt−1, which is a nearly 50-fold increase over the mass activity of the commercial 20 wt % Pt/C catalyst, and a much lower overpotential.
We attribute this outstanding performance to the following features:
This work provides a universal strategy to design atomically dispersed metal sites/conducting polymer heterostructures for highly efficient catalysts toward HER and beyond.
All the chemicals were purchased from Sigma-Aldrich® (AR grade) and were used as received without further purification. Aniline, H2PtCl6·H2O, (NH4)2PdCl4, (NH4)2RuCl6, HClO4, HNO3, HCl, Nafion® (5 wt %) and Pt/C (20 wt %) were all purchased from Sigma-Aldrich®. Ultrapure deionized water (DI Water, 18 MO cm-1) supplied by a Millipore® system.
CC was cleaned with mixed aqueous solutions of HCl (19 wt. %) and HNO3 (10 wt. %), followed by washing with deionized water repeatedly.
PANI was prepared by electrodeposition using a three-electrode configuration with CC (1×5 cm2), graphite plate and Ag/AgCl as the working electrode, the counter electrode and the reference electrode, respectively. The electrolyte was prepared by dissolving 8.0 mL HCl in 88 mL H2O and then adding 4.0 mL aniline to form a uniform solution after stirring for half an hour. A constant potential of 0.8 V vs. Ag/AgCl was applied to the CC electrode for 10 min.
After that, PANI/CC was washed with water, followed by drying at 80° C. for 1 h and then immersed in different concentrations of H2PtCl6·H2O solution for 4 h. The H2PtCl6·H2O solutions were prepared using 5, 10, 20 and 30 mg H2PtCl6·H2O in 20 mL of deionized water. Next, excess solution was removed and the PANI-H2PtCl6/CC hybrid was dried.
Finally, the as-prepared PANI-Pt-5/CC, PANI-Pt-10/CC, PANI-Pt-20/CC, and PANI-Pt-30/CC was prepared by in-situ electrochemical reduction. The reduction process was conducted with one linear sweep voltammetry (LSV) scan in 0.5 M H2SO4 solutions at a scan rate of 2 mV s−1.
Note that the PANI-Ru/CC and PANI-Pd/CC were also made under the same condition except replacing H2PtCl6·H2O with (NH4)2RuCl6 or (NH4)2PdCl4, respectively.
X-ray powder diffraction (XRD) patterns were collected on a Rigaku X-ray diffractometer equipped with a Cu Kα radiation source.
Scanning electron microscopy (SEM) measurements were carried out on a XL30 ESEM FEG scanning electron microscope at an accelerating voltage of 20 kV.
Transmission electron microscopy (TEM) measurements were performed on a HITACHI H-8100 electron microscopy (Hitachi, Tokyo, Japan) with an accelerating voltage of 200 kV.
X-ray photoelectron spectroscopy (XPS) was obtained on an ESCALABMK II X-ray photoelectron spectrometer; the peak energies were calibrated by placing the principal C1s peak at 284.6 eV.
Element composition was analyzed by inductively coupled plasma optical emission spectroscopy (ICP-OES) on Prodigy 7 and ANALYZER(CHNSO) on Vario EL cube. The ICP-OES elemental analyses were performed to obtain the Pt, Ru and Pd amount in the samples.
The X-ray absorption near-edge structure data (Pt L3-edge) were collected on the 061D-1 Hard X-ray MicroAnalysis (HXMA) beamline at the Canadian Light Source (CLS, operated at 2.9 GeV with a maximum current 250 mA). Measurements were made at room temperature using a 32-element Ge detector. The XANES spectra at N K-edge were obtained at the spherical grating monochromator (SGM) beamline 11ID-1 with an energy resolution of E/ΔE≥5000. The spectra were recorded in partial X-ray fluorescence yield (PFY) mode using four silicon drift detectors (SDD) under 10−6 Torr with a beam spot size of 25 μm. Data were first normalized to the incident photon flux I0 measured with a refreshed gold mesh at SGM before the measurement. The spectra were normalized with respect to the edge height after subtracting the pre-edge and post-edge backgrounds, and then the data was converted from energy space to k space using ATHENA software.
The HER electrochemical measurements were performed in a standard three-electrode with a two-compartment cell on an electrochemical workstation (CHI 760E). The acidic (0.5 M H2SO4) electrochemical measurements were performed using a saturated calomel electrode (SCE) as the reference electrode. A graphite plate was used as the counter electrode in all measurements. Polarization data were obtained at a scan rate of 2 mV s−1. In all measurements, the reference electrode was calibrated with respect to the reversible hydrogen electrode (RHE). The calibration was performed in the high purity H2-saturated electrolyte with a Pt electrode as the working electrode. The current-voltage was run at a scan rate of 2 mV s−1, and the average of the two potentials at which the current crossed zero was taken to be the thermodynamic potential for the hydrogen electrode reactions. All polarization curves were iR-corrected. Electrochemical impedance spectroscopy (EIS) measurements were carried out in the frequency range of 100 kHz-0.1 Hz with an AC amplitude of 5 mV. The iR-corrected potential was obtained after the correction of internal resistance measured by EIS following the equation: Eactual=Etest−iR×100%, where Etest is the original potential, R is the internal resistance, i is the corresponding current, and Eactual is the iR-corrected potential.
A commercial 20 wt % Pt/C catalyst ink was prepared by dispersing 5 mg catalyst in 990 μL mixed solution of isopropyl alcohol and water (volume ratio 5:5) and 10 μL 5 wt % Nafion® solutions. The mixed solutions were dispersed for 15 min by ultrasonic cell disruptor, and then 5 μL homogeneous catalyst ink was deposited on a glassy carbon electrode (diameter: 3.0 mm), the electrode was allowed to dry at room temperature for 15 min to form a smooth catalyst ring.
As illustrated in
A smooth CC was used as a current collector and a substrate for PANI nanofibers growth (
PANI nanofibers were first decorated on the bare CC substrate by electrochemical deposition in an acid aniline solution. As shown in
After that, the negatively charged PtCl62− ions were adsorbed on the positively charged PANI nanofibers via a solution-phase electrostatic assembly and absorption.[A36]
Finally, the adsorbed PtCl62− ions were in-situ reduced into atomically dispersed Pt sites under a voltage where hydrogen evolution occurs. The reduction process was conducted with one LSV scan in 0.5 M H2SO4 solutions at a scan rate of 2 mV s−1. It is worthwhile to mention that the absence of any other chemical reducing agent would result in a clean surface of the obtained single-atom catalysts (SACs) which offers maximum exposure of active sites.[A32]
The structure of the obtained product was first studied by XRD. As shown in
XPS was first conducted to investigate the chemical state of the Pt in PANI-Pt-10/CC. As shown in
Additionally, a series of PANI-Pt/CC samples with atomically dispersed Pt sites anchored on PANI were obtained with several quantities (5, 20, and 30 mg) of H2PtCl6·H2O. The loadings of Pt in these samples were measured via ICP-OES. As illustrated in Table 1, the Pt content is increased in a range between 1.24 to 2.82 μg cm-2 and then remained nearly constant even with a further addition of H2PtCl6·H2O by 30 mg. The XRD patterns with SEM and AC-HAADF-STEM images (
Importantly, this in-situ electrochemical strategy can be extended to synthesizing other atomically dispersed metal sites such as Pd and Ru (
The electrocatalytic activity of the obtained atomically dispersed Pt samples was evaluated by LSV in H2-saturated acid media (0.5 M H2SO4) with a scan rate of 2 mV s−1 at room temperature. Before the tests, the SCE was calibrated in a high purity H2-saturated 0.5 M H2SO4 solutions electrolyte with a Pt electrode as the working electrode (
To achieve a current density of 10 mA cm−2 (j10), the PANI-Pt-5/CC, PANI-Pt-10/CC, PANI-Pt-20/CC and PANI-Pt-30/CC display overpotentials (η) of 23, 16 (23 mV without iR correction,
It is worth mentioning that the catalyst of Pt nanoparticles (Pt NPs) on the surface of PANI supported on carbon cloth (PANI-Pt NPs/CC) has been prepared by H2 reduction at 200° C. As illustrated in
Durability is another important parameter in evaluating HER catalysts. The stability of commercial Pt/C and PANI-Pt-10/CC was evaluated by continuous cyclic voltammetry (CV) cycles under 0.5 M H2SO4 solutions. As shown in
In conclusion, a facile, simple and fast in-situ electrochemical reduction method was reported, for the first time, for the synthesis of a series of atomically dispersed metal sites on PANI nanofibers. For example, the atomically dispersed Pt sites anchored on PANI (PANI-Pt/CC) exhibit a higher HER catalytic activity and better durability than a commercial Pt/C catalyst in acid solutions. To attain a current density of 20 mA cm′, the PANI-Pt-10/CC only needs an overpotential of 25 mV. More importantly, the mass activity for PANI-Pt-10/CC at η=50 mV is nearly 50 times higher than that of commercial 20 wt % Pt/C. This universal in-situ electrochemical reduction strategy opens up a new avenue for the design of atomically dispersed metal sites supported on conducting polymers toward HER and beyond.
The scope of the claims should not be limited by the preferred embodiments set forth in the examples, but should be given the broadest interpretation consistent with the description as a whole.
The present description refers to a number of documents, the content of which is herein incorporated by reference in their entirety. These documents include, but are not limited to, the following:
A17. C. Ray, S. Dutta, Y. Negishi, T. Pal, Chem. Commun. 2016, 52, 6095-6098.
A18. R. Zhang, C. Tang, R. Kong, G. Du, A. M. Asiri, L. Chen, X. Sun, Nanoscale, 2017, 9, 4793-4800.
This application claims benefit, under 35 U.S.C. § 119(e), of U.S. provisional application Ser. No. 63/364,662, filed on May 13, 2022.
| Number | Date | Country | |
|---|---|---|---|
| 63364662 | May 2022 | US |
