The present invention generally relates to synthesis of high-entropy alloy (HEA) nanostructures. More specifically the present invention relates synthesis of unconventional phase high-entropy alloy nanowires and nanosheets for highly efficient electrocatalysis.
As an advanced route for clean and sustainable energy conversion, electrocatalysis provides a solution to the worldwide problems on energy crisis and environmental pollution. For instance, H2 is an efficient clean energy carrier with high-energy density, and has been considered as the most promising clean energy to replace traditional fossil fuels which lead to the depletion of energy resources and severe environmental issues (e.g., global warming and air pollution). As clean and efficient technology, electrochemical water splitting shows great potential in replacing the traditional technology for H2 production (e.g., steam reforming of natural gas or other light hydrocarbons) in the future world, owing to the advantages of high efficiency, excellent adaptability, and nearly zero carbon emissions. A typical reaction route of water electrolysis includes cathodic hydrogen evolution reaction (HER) and anodic oxygen evolution reaction (OER), and different electrochemical reactions occur in different electrolytes.
The rational synthesis and development of advanced catalysts with high performance are of great importance to efficiently turn raw materials into useful products. To date, the well-established proton exchange membrane (PEM)-based water electrolysis, which operates under acidic conditions, possesses many advantages compared to alkaline water electrolysis, such as compact design, higher voltage efficiency and higher gas purity. However, PEM-based water electrolysis is hampered by the low efficiency, instability and high cost of anodic electrocatalysts for OER. To overcome these disadvantages, more highly active electrocatalysts for both HER and OER are required. As benchmark commercial materials, noble metal catalysts (Pt/C) and noble-metal oxide catalysts (IrO2 and RuO2) exhibit satisfying HER and OER performance, respectively. However, their high cost and rare reserves remain limiting the large-scale applications. Furthermore, noble-metal catalysts always suffer from operational instability (e.g., dissolution, agglomeration, and show poor tolerance for poisoning) during HER/OER at high-current densities. Therefore, it is desirable to develop low-cost, high-efficiency, earth-abundant, economical electrocatalysts to substitute the noble-metal-based catalysts.
Noble metal nanomaterials have been extensively used as highly efficient catalysts in diverse electrochemical reactions. Taking the electrochemical HER as an example, platinum-group noble metals, such as Pt, are considered as highly efficient catalysts for HER. However, commercial platinum-group noble metal catalysts, e.g., Pt/C, still suffer from the scarcity, high cost, and poor catalytic stability, hindering their widespread use in practical applications. It is thus imperative to design and develop advanced noble metal catalysts with superior catalytic activity and stability to further enhance the utilization efficiency of noble metal atoms. To date, to the best of the knowledge, most reported catalysts on the market are noble-metal-based nanostructures with relatively simple compositions (i.e., one to three elements). In comparison, as promising catalysts in heterogeneous catalysis, HEAs generally consist of five or more metals, which display structure-dependent synergistic effects and enhanced catalytic performance in terms of activity and durability. Moreover, HEAs can largely decrease the usage of noble metals and thus reduce the cost of catalysts, which have attracted increasing research interests. Therefore, with the development of nanotechnology, HEA catalysts have made great progress in the field of electrocatalysis.
Impressively, the crystal phase has emerged as an increasingly significant structural parameter in determining the physicochemical properties and functionalities of nanomaterials. In particular, unconventional phases could endow nanomaterials with intriguing properties and superior performance in electrocatalysis. Although some research groups reported the HEA nanostructures with thermodynamically stable fcc phase for HER or OER, there is still no commercial technology for the preparation of novel HEA nanocatalysts with unconventional phases.
To date, alkaline water electrolysis technologies have been well developed and even commercially available for industrial H2 production. In contrast, the well-established PEM electrolysis with faster response, lower Ohmic losses, higher voltage efficiency and gas purity requires to be operated in acidic environment. However, the PEM-based water electrolysis is hampered by the low efficiency, instability and high cost of anodic electrocatalysts for OER. Many OER electrocatalysts are prone to dissolution and/or surface structure transformation under the oxidizing OER potentials in the harsh acidic environment, finally leading to a drastic decrease in catalytic performance.
Recently, HEAs containing five or more elements with similar atomic ratios have aroused extensive research interest in electrocatalysis for their enhanced catalytic activity and stability. Compared with nanomaterials with relatively simple compositions (i.e., one to three elements), HEAs exhibit unique and intriguing advantages, including adjustable compositions, distorted lattices, sluggish diffusion, and synergistic effect between various elements. To date, various advanced synthetic techniques/strategies, such as the thermal-shock-based method, moving bed pyrolysis, acute chemical reduction, sputtering, transient electrosynthesis, and wet-chemical method, etc. have been developed to prepare HEA nanomaterials. However, most of these existing synthetic approaches still suffer from harsh synthetic conditions and complicated synthetic protocols, and are only adopted to prepare HEA nanomaterials with specific components. In addition, although great efforts have been devoted to rational designing HEA nanostructures with tailored compositions, sizes, dimensions and morphologies, the research towards finely tuning the crystal phase of HEA nanomaterials is still lacking, i.e., the rational design and synthesis of HEA electrocatalysts with unconventional phases remain a great challenge.
According to a first aspect of the present invention, a method for synthesizing high-entropy alloy (HEA) nanostructures, each having a HEA shell uniformly grown on a nanocore, is provided. The method comprises: mixing nanostructure seeds, a plurality of metal precursors, one or more reducing agents and a surfactant in a solvent to form a first mixture; subjecting the first mixture to ultrasonication under an ultrasonication temperature; degassing the first mixture upon heating at a degassing temperature under vacuum with magnetic stirring; purging the first mixture with an inert gas; and keeping the first mixture at a growth temperature for a growth time to form the HEA nanostructures.
According to a second aspect of the present invention, a high-entropy alloy (HEA) nanostructure having a HEA shell uniformly grown on a nanocore is provided. The HEA nanostructure is fabricated by the method according to the first aspect of the present invention.
According to a third aspect of the present invention, a bifunctional catalyst comprising HEA nanostructures according to the second aspect of the present invention is provided.
According to a fourth aspect of the present invention, a proton exchange membrane-based electrolyzer comprising an anode and a cathode, both applied with bifunctional catalyst according to the third aspect of the present invention is provided.
In some embodiments of the present invention, the nanostructure seeds are 4H—Au nanowire seeds such that the nanocore is a nanowire formed of 4H—Au.
In some embodiments of the present invention, the nanostructure seeds are 2H/fcc-Au nanosheet seeds such that the nanocore is a nanosheet formed of 2H/fcc-Au.
In some embodiments of the present invention, the plurality of metal precursors includes Pt-based compound, Ir-based compound, Ni-based compound, Co-based compound, and Fe-based compound such that the HEA shell is formed of quinary 4H—IrPtNiCoFe.
In some embodiments of the present invention, the Pt-based compound, Ir-based compound, Ni-based compound, Co-based compound and Fe-based compound are Pt(acac)2, Ir(acac)3, Ni(acac)2, Co(acac)3 and Fe(acac)3, respectively.
In some embodiments of the present invention, the 4H—Au nanowire seeds, the metal precursors Pt(acac)2, Ir(acac)3, Ni(acac)2, Co(acac)3, and Fe(acac)3 have weight ratio of 5:5:2:3:3.
The method provided by the present invention is a low-temperature, facile, general, wet-chemical, seeded epitaxial growth method which can synthesize a library of unconventional-phase HEA nanostructures, e.g., 4H—Au@HEA nanowires (NWs) and 2H/fcc-Au@HEA nanosheets (NSs) with 5-10 components by using 4H—Au NWs and 2H/fcc-Au NSs as seeds respectively. As a result, a library of 4H—Au@HEA core-shell nanostructures composed of up to ten metallic elements (Ir, Pt, Ni, Fe, Co, Rh, Pd, Ru, Cu, and Mn) can be synthesized by simply tuning the synthetic parameters.
The present invention has the following advantages:
First, compared with traditional thermal-shock-based approaches with higher synthetic temperatures (e.g., 2000 K), the as-developed synthetic strategy is a relatively low-temperature and rapid wet-chemical synthetic method, which greatly simplifies the synthetic protocols, reduces the cost, and increases the reproducibility. This synthetic method can be readily scaled up by amplifying the amounts of reactants and the volume of reactors, showing great potential in the large-scale production of a series of HEA nanostructures with unconventional phases, e.g., 4H—Au@HEA NWs and 2H/fcc-Au@HEA NSs. To a great extent, the protocol simplifies the synthetic strategies for HEA catalysts.
Second, the as-developed synthetic strategy is a general and robust method for the controlled synthesis of a library of HEA nanostructures with different morphologies and dimensions. For example, the provided epitaxial growth strategy can prepare the one-dimensional (1D) HEA nanostructures, i.e., 4H—Au@HEA core-shell NWs with 5-10 components, including quinary 4H—IrPtNiCoFe, senary 4H—IrPtNiCoFeRh, septenary 4H—IrPtNiCoFeRhPd, octonary 4H—IrPtNiCoFeRhPdRu, novenary 4H—IrPtNiCoFeRhPdRuCu and denary 4H—IrPtNiCoFeRhPdRuCuMn HEA on 4H—Au NWs, as well as the two-dimensional (2D) HEA nanostructures, i.e., 2H/fcc-Au@HEA NSs, including quinary 2H/fcc-IrPtNiCoFe, senary 2H/fcc-IrPtNiCoFeRh, septenary 2H/fcc-IrPtNiCoFeRhPd, octonary 2H/fcc-IrPtNiCoFeRhPdRu, novenary 2H/fcc-IrPtNiCoFeRhPdRuCu and denary 2H/fcc-IrPtNiCoFeRhPdRuCuMn HEA on 2H/fcc-Au NSs. Noted that the combination of the metal elements (i.e., Ir, Pt, Ni, Co, Fe, Rh, Pd, Ru, Cu and Mn) in HEA nanostructures can be randomly tuned to achieve different uses. The invention enriches the library of HEA nanostructures with different components, morphologies, dimensions and crystal phases.
Third, the as-prepared HEA nanostructures possess unconventional phases, i.e., HEA NWs with an unconventional 4H phase and HEA NSs with an unconventional 2H/fcc heterophase. To date, to the best of the knowledge, almost all the reported HEA nanostructures possess the thermodynamically stable fcc phase. Moreover, a phase-dependent study of electrocatalytic performance has been systematically investigated. It is found that the bifunctional 4H—Au@IrPtNiCoFe NWs exhibit better HER and OER catalytic performance than that of fcc-IrPtNiCoFe NWs.
Fourth, the as-prepared 4H—Au@HEA core-shell NWs can be used as effective surface enhanced Raman scattering (SERS) platform to in situ detect the Raman signals of molecule absorption and desorption to unravel the real-time HER and OER mechanism. The 4H-HEA shell on 4H—Au is relatively thin (<2 nm), which can be used to “borrow” the electromagnetic field of the SERS-active core (i.e., 4H—Au) to enhance the Raman signals of molecules on or near the shell surface. Therefore, the reactions catalyzed by the 4H-HEA shell can be easily detected and monitored by the in situ SERS method.
Fifth, the 4H—Au@HEA NWs can be used as advanced electrocatalysts with high activity and good long-term stability towards diverse electrochemical reactions such as HER, OER, oxygen reduction reaction (ORR), alcohol oxidation reaction (AOR), and formic acid oxidation reaction (FAOR). Taking the quinary 4H—Au@IrPtNiCoFe HEA NW as an example, the bifunctional 4H—Au@IrPtNiCoFe HEA nanocatalysts exhibit the excellent HER and OER performance, among the best bifunctional multielement alloy catalysts for water splitting in the world. Impressively, the as-prepared 4H—Au@IrPtNiCoFe HEA catalysts exhibit superior catalytic activity and stability at a large current density, showing great potential in industrial-level water splitting. We also applied them as both the anode and cathode catalysts in a PEM electrolyzer to simulate the overall water splitting condition at the industrial level. And the bifunctional 4H—Au@IrPtNiCoFe HEA catalysts exhibit superior industrial-level catalytic activity and stability.
Sixth, the bifunctional 4H—Au@IrPtNiCoFe HEA is a pH-universal catalyst for overall water splitting, which can be used in both alkaline (1 M KOH) and acidic (0.5 M H2SO4) conditions. Noted that the 4H—Au core could stabilize the structure of the 4H-HEA shell during the large-current-density water electrolysis via an epitaxial growth manner. After 70 h overall water splitting in 0.5 M H2SO4, the structure of 4H—Au@IrPtNiCoFe HEA NWs still maintains, while the structure of fcc-IrPtNiCoFe HEA NWs is severely distorted and aggregated, severely decreasing the catalytic stability. It indicates that the bifunctional 4H—Au@IrPtNiCoFe HEA nanocatalysts can overcome the structural instability problem during electrolysis in the acidic condition, showing great potential in acidic PEM-based electrolyzer.
Therefore, due to the advantage of high-entropy effect (i.e., adjustable compositions, distorted lattice, sluggish diffusion, and synergistic effect between various elements) and unconventional phase, the bifunctional 4H—Au@IrPtNiCoFe HEA catalysts exhibit the world-best performance for HER and OER in both alkaline and acidic conditions. And the 4H—Au@IrPtNiCoFe HEA catalysts show great potential in the pH-universal overall water splitting at the industrial level.
Embodiments of the invention are described in more details hereinafter with reference to the drawings, in which:
In the following description, embodiments of the present invention are set forth as preferred examples. It will be apparent to those skilled in the art that modifications, including additions and/or substitutions may be made without departing from the scope and spirit of the invention. Specific details may be omitted so as not to obscure the invention; however, the disclosure is written to enable one skilled in the art to practice the teachings herein without undue experimentation.
A facile and general wet-chemical synthetic method is developed to achieve the controlled synthesis of a series of HEA nanomaterials with unconventional phases, including 4H—Au@HEA NWs and 2H/fcc-Au@HEA NSs. All the starting chemicals including solvents, precursors and surfactants are available from commercial sources.
Exemplary chemicals used in the synthetic method include: Iridium (III) acetylacetonate (Ir(acac)3, 97%), Platinum (II) acetylacetonate (Pt(acac)2, 97%), nickel (II) acetylacetonate (Ni(acac)2, 97%), cobalt (III) acetylacetonate (Co(acac)3, 97%), iron (III) acetylacetonate (Fe(acac)3, 97%), rhodium (III) acetylacetonate (Rh(acac)3, 97%), palladium (II) acetylacetonate (Pd(acac)2, 97%), ruthenium (III) acetylacetonate (Ru(acac)3, 97%), copper (II) acetylacetonate (Cu(acac)2, 97%), manganese (III) acetylacetonate (Mn(acac)3, 97%), tungsten hexacarbonyl (W(CO)6, 99%), glucose, oleylamine (OM, 70%), oleylamine (OM, ≥98%), (1-Hexadecyl) trimethylammonium chloride (CTAC, 99%), stearyl trimethyl ammonium bromide (STAB), gold (III) chloride hydrate (HAuCl4·3H2O, ˜49% Au basis), N-ethylcyclohexylamine (99%), 1,2-dichloropropane (99%), hexane (technical grade), toluene (technical grade, ≥99%) and ethanol (technical grade) were purchased from Sigma-Aldrich.
Briefly, the method used for the synthesis of 4H-HEA NWs comprises the usage of 4H—Au NWs as template, metal (Ir, Pt, Ni, Co, Fe, Rh, Pd, Ru, Cu and Mn) salts as precursors, oleylamine (OAm) as solvent, (1-Hexadecyl) trimethylammonium chloride (CTAC) as surfactant as well as W(CO)6 and glucose as reducing agents. After sonicating for 1 h, the above-mentioned mixture was heated to a relatively low temperature and reacted for 1 h. Then a library of 4H—Au@HEA core-shell NWs with 5-10 components can be successfully synthesized, including quinary 4H—IrPtNiCoFe, senary 4H—IrPtNiCoFeRh, septenary 4H—IrPtNiCoFeRhPd, octonary 4H—IrPtNiCoFeRhPdRu, novenary 4H—IrPtNiCoFeRhPdRuCu and denary 4H—IrPtNiCoFeRhPdRuCuMn HEA on 4H—Au NWs via an epitaxial growth strategy.
The synthesis of 2H/fcc-Au@HEA NSs, including quinary 2H/fcc-IrPtNiCoFe, senary 2H/fcc-IrPtNiCoFeRh, septenary 2H/fcc-IrPtNiCoFeRhPd, octonary 2H/fcc-IrPtNiCoFeRhPdRu, novenary 2H/fcc-IrPtNiCoFeRhPdRuCu and denary 2H/fcc-IrPtNiCoFeRhPdRuCuMn HEA on 2H/fcc-Au NSs via an epitaxial growth strategy, is similar to that of 4H—Au@HEA NWs except using 2H/fcc-Au NSs as seeding templates.
In a typical synthetic protocol for 4H—Au NWs, 20 mg of HAuCl4·3H2O, 1.5 mL of oleylamine (98%), 400 μl of N-ethylcyclohexylamine, 20 mL of hexane and 200 μl of 1,2-dichloropropane were thoroughly mixed in a 40 mL glass vial. The vial was then sealed with PTFE tape and parafilm before being heated for 48 h in an oil bath pre-set at 57° C. The product was collected by centrifugation at 4000 rpm for 3 min, and washed with toluene for three times and then redispersed in 10 mL of toluene. The yield of 4H—Au NWs was about 2.5 mg.
In a typical synthetic protocol for 2H/fcc-Au NSs, 10 mg of HAuCl4·3H2O, 3 mL of 4-tert-butylpyridine, 4 mL of OAm (98%) and 5 mL of heptane were thoroughly mixed in a 20 mL glass vial. The vial was then sealed with PTFE tape and parafilm before being heated for 4 h in an oil bath pre-set at 80° C. The product was collected by centrifugation at 3000 rpm for 3 min, and washed with toluene for three times and then redispersed in 10 mL of toluene. The yield of 2H/fcc-Au NSs was about 1 mg.
As depicted in
As shown in
In a typical synthesis of quinary 4H—Au@IrPtNiCoFe HEA core-shell NWs, 5 mg of as-prepared 4H—Au NWs, 5 mg of Pt(acac)2, 5 mg of Ir(acac)3, 2 mg of Ni(acac)2, 3 mg of Co(acac)3, 3 mg of Fe(acac)3, 30 mg of W(CO)6, 60 mg of glucose and 40 mg of CTAC were dissolved in 5 mL of oleylamine (OAm), followed by ultrasonication for 1 h at 30° C. The mixture was degassed upon heating at 50° C. under vacuum with vigorous magnetic stirring for 10 minutes. Then, the mixture was purged with Ar and heated to 250° C. for 1 h. The cooled product was collected by centrifugation at 4000 rpm for 3 min and washed three times with a toluene/ethanol (v/v=4:1) mixture. After that, the 4H—Au@IrPtNiCoFe HEA NWs were collected by centrifugation, and then redispersed in 10 mL toluene for storage.
The method can be extended to synthesize a library of 4H—Au@HEA core-shell NWs with 6-10 components, including senary 4H—Au@IrPtNiCoFeRh, septenary 4H—Au@ IrPtNiCoFeRhPd, octonary 4H—Au@IrPtNiCoFeRhPdRu, novenary 4H—Au@ IrPtNiCoFeRhPdRuCu and denary 4H—Au@IrPtNiCoFeRhPdRuCuMn HEA NWs, via changing the precursor ratio, reaction temperature, and time. The content of each metal salt was different in the precursor solutions, which were summarized in Table 1.
It is worth mentioning that the synthetic conditions for the preparation of 4H—Au@ HEA NWs are tunable. The metal precursor can be chosen from the salt of acetylacetonate, chloride and nitrate (e.g., Nickel salts can be chosen from Ni(acac)2, NiCl2 and Ni(NO3)2). The reducing reagents can be chosen from W(CO)6, Mo(CO)6, formaldehyde and CO flow (CO molecule released from those reagents can facilitate the reducing reaction) as well as glucose. The surfactants can be chosen from CTAC and dodecyl trimethyl ammonium chloride (DTAC). Noted that only chloride surfactant is suitable, while bromide surfactant could induce the phase transition of Au NWs from 4H to fcc, and iodide surfactant could etch the Au NWs. The reaction temperature ranges from about 250° C. to about 280° C., while the reaction time can be in the range from 60 min to 90 min. Noted that some metal elements (e.g., Ru and Mn) are relatively difficult to be reduced, it is appropriate to increase the reaction temperature and prolong the reaction time. The synthetic process can be conducted under an inert atmosphere which can be either an Ar atmosphere or a N2 atmosphere. The synthesis of 4H—Au@HEA NWs can be readily scaled up by proportionally increasing the amounts of reactants, including 4H—Au NWs, reducing reagents, solvent, metal precursors and surfactants.
By changing the 4H—Au NWs to 2H/fcc-Au NSs as seeding templates, the above synthetic method may be used to synthesize a library of 2H/fcc-Au@HEA core-shell NSs with 5-10 components, including quinary 2H/fcc-Au@IrPtNiCoFe, senary 2H/fcc-Au@IrPtNiCoFeRh, septenary 2H/fcc-Au@IrPtNiCoFeRhPd, octonary 2H/fcc-Au@IrPtNiCoFeRhPdRu, novenary 2H/fcc-Au@IrPtNiCoFeRhPdRuCu and denary 2H/fcc-Au@IrPtNiCoFeRhPdRuCuMn HEA NSs.
In a typical synthesis of quinary fcc-IrPtNiCoFe HEA NWs, 5 mg of Pt(acac)2, 5 mg of Ir(acac)3, 4 mg of Ni(acac)2, 7 mg of Co(acac)3, 7 mg of Fe(acac)3, 10 mg of W(CO)6, 60 mg of glucose, and 40 mg of stearyl trimethyl ammonium bromide (STAB) were dissolved in 5 mL of OAm, followed by ultrasonication for 1 h at 30° C. The mixture was degassed upon heating at 50° C. under vacuum with vigorous magnetic stirring for 10 minutes. Then, the mixture was purged with Ar and heated to 210° C. for 5 h. The cooled product was collected by centrifugation at 8000 rpm for 5 min and washed three times with a toluene/ethanol (v/v=1:2) mixture. After that, the fcc-IrPtNiCoFe HEA NWs were collected by centrifugation, and then redispersed in 10 mL toluene for storage.
Transmission electron microscopy (TEM) and dark-field scanning TEM (DF-STEM) images were obtained by using JEOL 2100F (Japan) operated at 200 kV. The high-angle annular DF-STEM (HAADF-STEM) images, annular bright-field STEM (ABF-STEM) images, and energy dispersive X-ray spectroscopy (EDS) results were obtained by JEOL ARM200F (JEOL, Tokyo, Japan) operated at 200 kV and equipped with double spherical aberration (Cs) correctors. Scanning electron microscope (SEM) images were recorded on a scanning electron microscope (Thermo Fisher Scientific, QUATTRO S). Rigaku SmartLab and Bruker D8 ADVANCE X-ray powder diffractometers with Cu Kα radiation sthece (λ=1.5406 Å) were used to record the X-ray diffraction (XRD) patterns of samples. The concentration of Au was measured by ICP-OES (PerkinElmer, Optima 8000DV). X-ray photoelectron spectroscopy (XPS) measurements were carried out on a VG ESCALAB 220I-XL system. C is peak (284.8 eV) was used to calibrate the binding energy of other elements. Raman measurements were conducted on a Renishaw inVia™ conformal Raman microscope with an excitation wavelength of 532 nm and a low power density of <5 mW/um−2.
As shown in the scanning SEM image (
The XPS was used to characterize the chemical valence of metal elements in the quinary 4H—Au@IrPtNiFeCo HEA NWs (
To investigate the formation process of 4H—IrPtNiFeCo HEAs on 4H—Au NWs, time-dependent experiments were conducted at the reaction time of 5 min, 20 min and 60 min, and the corresponding products were characterized by HAADF-STEM and SEM-EDS (
Notably, the as-developed synthetic strategy is a general and robust method for the controlled synthesis of a library of 4H—Au@HEA core-shell NWs with an unconventional 4H phase, including senary 4H—Au@IrPtNiFeCoRh (
In addition, a library of 2D HEA nanostructures, i.e., 2H/fcc-Au@HEA core-shell NSs, including quinary 2H/fcc-IrPtNiCoFe, senary 2H/fcc-IrPtNiCoFeRh, septenary 2H/fcc-IrPtNiCoFeRhPd, octonary 2H/fcc-IrPtNiCoFeRhPdRu, novenary 2H/fcc-IrPtNiCoFeRhPdRuCu and denary 2H/fcc-IrPtNiCoFeRhPdRuCuMn HEA on 2H/fcc-Au NSs (
As known, HEA nanomaterials with tailored compositions, sizes, dimensions and morphologies are promising catalysts for various electrochemical reactions, including HER, OER, ORR, AOR and CO2RR. However, to date, the crystal-phase-dependent study of HEA nanomaterials in electrocatalysis has been hardly reported.
As a proof-of-concept application, the HER performance of 4H—Au@IrPtNiFeCo HEA NWs with an Ir/Pt/Ni/Fe/Co ratio of ˜1.12/1.19/1.24/1.13/1 was investigated by a three-electrode system in acidic media. The three-electrode system includes a carbon paper electrode coated with a catalyst, the graphite rod, and the Ag/AgCl (saturated KCl) was employed as the working electrode, counter electrode, and reference electrode, respectively. The Ag/AgCl electrode was calibrated with respect to a reversible hydrogen electrode (RHE). All electrochemical measurements were conducted in N2-saturated 0.5 M H2SO4 aqueous solution, or performed on a CHI750e electrochemical workstation (Shanghai Chenhua Instrument Corporation, China) at room temperature.
A catalyst ink was prepared. Firstly, the as-prepared catalysts were subsequently stirred for 3 days at room temperature. The catalyst containing 1 mg of 4H—Au@IrPtNiFeCo HEA NWs was re-dispersed in a mixed solution of isopropanol (700 μl) and Milli-Q water (280 μl). Subsequently, 20 μl of Nafion solution (5%) was added into the mixture which was then sonicated for 30 min to obtain the catalyst ink.
The working electrode was prepared by drop-casting 250 μg of the prepared catalyst ink (containing 4H—Au@IrPtNiFeCo HEA NWs) on a 0.5×0.5 cm carbon paper electrode (the mass loading of the catalyst is 1 mg cm−2). The obtained working electrode was dried under ambient conditions until the solvent was completely evaporated.
A Hg/HgO electrode may be used as the reference electrode, and Pt mesh (1.0×1.0 cm) as the counter electrode. Before the test, highly pure O2 (99.999%) was bubbled into the electrolyte for 15 min. linear sweep voltammetry was conducted at a scan rate of 5 mV s−1 between 1.2 and 1.8 V versus RHE.
Before electrocatalytic measurements, cyclic voltammetry (CV) was employed at a potential range of 0.05-0.8 V (vs. RHE) to remove the capping agents on the surface of catalysts. All the polarization curves were measured at room temperature with a scan rate of 5 mV s−1 between −0.4 and 0.05 V versus RHE. For the accelerated durability test of 4H—Au@IrPtNiFeCo HEA NWs catalyst in N2-saturated 0.5 M H2SO4 electrolyte, chronopotentiometry was measured under a constant current density of 10 mA cm−2 at room temperature. Electrochemical impedance spectroscopy (EIS) measurements were carried out in the frequency range of 0.1 Hz-100 kHz with 10 mV amplitude to obtain the solution resistance (Rs). All the polarization curves were corrected by 90% iRs compensation. Current densities were normalized by the geometric area of the electrode.
To investigate the crystal-phase-dependent performance of HEA nanomaterials, fcc-IrPtNiFeCo HEA NWs (
The HER polarization curves of these catalysts were recorded in N2-saturated 0.5 M H2SO4 at a scan rate of 5 mV s−1 (
It is worth mentioning that the fcc-IrPtNiFeCo HEA NWs, which possess similar composition, dimension and morphology with the 4H—Au@IrPtNiFeCo HEA NWs, require a higher overpotential of 5 mV to achieve the current density of 10 mA cm−2, indicating the significant role of unconventional 4H phase in boosting the HER performance of HEA catalysts. Such low overpotential (7 mV) of the 4H—Au@IrPtNiFeCo HEA catalyst to drive the current density of 10 mA cm−2 toward HER is among the best of the reported multielement-alloy-based HER catalysts under acidic conditions (
Moreover,
In addition, the double-layer capacitance (Cdl) was obtained by recording CV curves at different scanning rates from 20 to 100 mV s−1 (
The EIS curves shown in (
Finally, the long-term electrochemical stability of 4H—Au@IrPtNiFeCo HEA catalyst in 0.5 M H2SO4 was also investigated by the chronoamperometric test. The current density in the chronoamperometric curve shows a negligible variation under a constant current density of 10 mA cm−2 during the HER test for 80 h, indicating the good catalytic stability of the 4H—Au@IrPtNiFeCo HEA for HER under acidic conditions (
Moreover, TEM images and FFT patterns of 4H—Au@IrPtNiFeCo HEA after the durability test show that the wire-like morphology and the 4H phase still maintain (
In comparison, the fcc-IrPtNiFeCo HEA NWs are severely distorted and aggregated, resulting in relatively poor HER stability (
Impressively, the 4H—Au@IrPtNiFeCo HEA NWs can also exhibit crystal-phase-dependent OER performances in acidic media. For comparison, the fcc-IrPtNiFeCo HEA NWs and commercial IrO2 (
As shown in the polarization curves in
Furthermore, the Tafel slope of 4H—Au@IrPtNiFeCo HEA is as low as 46.8 mV dec−1, which is lower than those of fcc-IrPtNiFeCo HEA (53.1 mV dec−1) and commercial IrO2 (63.0 mV dec−1), implying the fastest reaction kinetics of 4H—Au@IrPtNiFeCo HEA toward acidic OER (
Finally, the stability of the 4H—Au@IrPtNiFeCo HEA catalyst was evaluated via a long-term durability test in 0.5 M H2SO4. The current density in the chronoamperometric curve shows a negligible variation under a constant current density of 10 mA cm−2 during the OER test for 70 h, implying the good catalytic stability of the 4H—Au@IrPtNiFeCo HEA for OER under acidic condition (
Moreover, TEM images and FFT patterns of 4H—Au@IrPtNiFeCo HEA after the durability test show that the wire-like morphology and the 4H phase still maintain (
In comparison, the fcc-IrPtNiFeCo HEA NWs are severely distorted and aggregated, resulting in relatively poor OER stability (
The superior HER and OER performances of the 4H—Au@IrPtNiFeCo HEA catalyst could be explained as follows.
First, compared with the thermodynamically stable fcc phase, the unconventional 4H phase in the HEA catalyst could contribute to the enhancement of its catalytic activity. As evidenced by the previous studies, the unconventional 4H phase in metal nanomaterials can serve as undercoordinated active sites for electrocatalysis owing to the optimized electronic structure deriving from the unique atomic arrangements. For example, the 4H—Au nanoribbons display advantages in both activity and selectivity over fcc-Au nanorods in electrocatalytic CO2RR.
Second, the 4H—IrPtNiFeCo HEA nanostructure exhibits unique intrinsic advantages, including adjustable compositions, distorted lattice, sluggish diffusion, and synergistic effect between various elements, resulting in enhanced electrocatalytic performance.
Third, the electronic structures of core-shell heterostructures can also be modified by the internal strain arising from the lattice mismatch between the 4H—Au core and 4H—IrPtNiFeCo HEA shell with lattice distortion, leading to the optimized adsorption free energy of hydrogen on the catalyst surface.
Fourth, the 4H—Au core in the 4H—Au@IrPtNiFeCo HEA catalyst can serve as a solid framework, which supports the 4H—IrPtNiFeCo HEA nanostructure without distortion and aggregation during the long-term electrocatalysis, resulting in the outstanding catalytic stability of the 4H—Au@IrPtNiFeCo HEA catalyst.
To further evaluate the overall water splitting performance of the bifunctional 4H—Au@IrPtNiFeCo HEA catalyst in industrial operating systems, a prototype PEM electrolyzer with 4H—Au@IrPtNiFeCo HEA NWs as both the anode and cathode catalysts (
First, the Nafion 117 membranes (DuPont) were sequentially treated with 3 wt % H2O2, 0.5 M H2SO4, and Milli-Q water at 80° C. for 1 h. After cooling to room temperature, the treated N117 membranes were washed and preserved in Milli-Q water. The 4H—Au@IrPtNiFeCo HEA catalysts were used as both the cathode and anode materials for the PEM electrolyzer. The as-prepared catalyst ink was then dropped on the carbon cloth (FuelCellStore, USA) and dried in the vacuum overnight. After the membrane electrode assembly (MEA) was constructed with the 4H—Au@IrPtNiFeCo HEA NWs or Pt/C-coated carbon cloth (cathode), treated Nafion 117 membrane (separator), and the 4H—Au@IrPtNiFeCo HEA NWs or commercial IrO2/carbon paper electrode (anode), it was applied in the PEM electrolyzer.
The PEM electrolyzer was operated at room temperature using 0.5 M H2SO4 as the electrolyte solution under the flowing rate of 8 mL min−1. LSV curves were measured at a scan rate of 5 mV s−1. The stability of the PEM electrolyzer using 4H—Au@IrPtNiFeCo HEA NWs as both cathode and anode catalyst, denoted as 4H—Au@IrPtNiFeCo∥4H—Au@IrPtNiFeCo electrode couple, was evaluated by measuring chronopotentiometry at 100 mA cm−2 for 70 h.
The fcc-IrPtNiFeCo∥fcc-IrPtNiFeCo and the benchmark Pt/C∥IrO2 electrode couples were used as comparisons. The polarization curves indicate that the cell voltages of 4H—Au@IrPtNiFeCo∥4H—Au@IrPtNiFeCo electrode couple required only 1.43 V and 1.63 V to reach a current of 10 mA and 100 mA, respectively, which are lower than those of the fcc-IrPtNiFeCo∥fcc-IrPtNiFeCo electrode couple (1.52 V and 1.67 V) and the benchmark Pt/C∥IrO2 electrode couple (1.57 V and 1.75 V) (
The embodiments may be chosen and described in order to best explain the principles of the invention and its practical application, thereby enabling others skilled in the art to understand the invention for various embodiments and with various modifications that are suited to the particular use contemplated. While the methods disclosed herein have been described with reference to particular operations performed in a particular order, it will be understood that these operations may be combined, sub-divided, or re-ordered to form an equivalent method without departing from the teachings of the present disclosure. Accordingly, unless specifically indicated herein, the order and grouping of the operations are not limitations. While the apparatuses disclosed herein have been described with reference to particular structures, shapes, materials, composition of matter and relationships . . . etc., these descriptions and illustrations are not limiting. Modifications may be made to adapt a particular situation to the objective, spirit and scope of the present disclosure. All such modifications are intended to be within the scope of the claims appended hereto.
A portion of the disclosure of this patent document contains material, which is subject to copyright protection. The copyright owner has no objection to the facsimile reproduction by anyone of the patent document or the patent disclosure, as it appears in the Patent and Trademark Office patent file or records, but otherwise reserves all copyright rights whatsoever. The present application claims priority from the U.S. Provisional Patent Application No. 63/492,785 filed on 29 March, 2023, the disclosure of which is incorporated herein by reference in its entirety.
Number | Date | Country | |
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63492785 | Mar 2023 | US |