Pengyi
Lu†
ab,
Jingwen
Zhou†
ab,
Yukun
Hu†
e,
Jinwen
Yin
a,
Yunhao
Wang
a,
Jinli
Yu
a,
Yangbo
Ma
a,
Zonglong
Zhu
a,
Zhiyuan
Zeng
d and
Zhanxi
Fan
*abc
aDepartment of Chemistry, City University of Hong Kong, Hong Kong, China. E-mail: zhanxi.fan@cityu.edu.hk; Fax: +852-34420522; Web: https://fanlab-cityu.wixsite.com/group
bHong Kong Branch of National Precious Metals Material Engineering Research Center (NPMM), City University of Hong Kong, Hong Kong, China
cCity University of Hong Kong Shenzhen Research Institute, Shenzhen, Guangdong, China
dDepartment of Materials Science and Engineering, City University of Hong Kong, Hong Kong, China
eSchool of Physics, Beihang University, Beijing 100191, China
First published on 9th June 2021
Over the past few decades, gold-based materials have drawn extensive attention due to their intriguing physical/chemical properties and excellent performance in a broad range of applications. In particular, the remarkable technical progress in synthesis and characterization is promoting the rapid development of gold-based nanoalloys, which are of great significance in catalysis. In this review, we provide a brief overview of the recently reported gold-based nanoalloys, focusing on their general synthetic methods and potential catalytic applications. In particular, the general relationships between material structures/compositions and catalytic performances are discussed in representative chemical reactions, such as the carbon dioxide reduction reaction (CO2RR), oxygen reduction reaction (ORR), hydrogen evolution reaction (HER), oxygen evolution reaction (OER), small organic molecule oxidation reaction, carbon monoxide oxidation reaction, and typical heterogeneous catalytic reactions in chemical engineering. Furthermore, critical challenges and potential opportunities facing gold-based nanoalloys are proposed to provide possible inspiration for future material design towards high performance applications.
As a representative of metal-based catalysts, gold (Au), an element of group IB in the periodic table of elements, has gained enormous attention owing to its intriguing physicochemical properties and great performance in a broad range of applications. Because of the contracted 6s orbital and completely filled 4f and 5d orbitals, Au commonly exists in a stable state of elementary substance in nature, which is different from the majority of metals that are regarded as high-performance catalyst components.15–19 Despite this feature, it was observed that Au is capable of catalyzing some important chemical reactions.20,21 For example, Haruta et al. found that Au is an outstanding catalyst for low-temperature CO oxidation.22 After that, Au has been gaining increasing popularity in catalytic studies, and several other Au-catalyzed reactions have also been developed. Along with more extensive investigations on Au, the significance of Au and Au-based materials has been continuously highlighted in the field of catalysis.23–30
Although the catalytic applications of Au and Au-based materials have been well-developed in the past few decades, it is admitted that their catalytic activity gradually cannot meet the rapidly increasing requirements of various heterogeneous catalytic reactions owing to the thermodynamically stable crystal and electronic structures.31,32 This is particularly the case when electrocatalysis proposed in recent years has been taken into account. To date, different modification strategies such as morphology, structure and composition regulations have been applied to Au and Au-based materials to improve their catalytic activity, selectivity and stability. Among various strategies, nanostructure engineering and alloying have demonstrated a remarkable enhancement of catalyst performance on average. Nanostructure engineering enables nanostructured catalysts to expose abundant low-coordinated atoms on the surface which possess a higher catalytic activity, while alloying with other metals possessing inherent high catalytic activity can effectively take advantage of both added metals with high performance and Au with high stability. Benefitting from the aforementioned two favorable features, Au-based nanoalloys have emerged as a promising kind of catalyst.33–38
Usually, microstructure and composition are two key factors that determine the physical and chemical properties of Au-based nanoalloys. Different microstructures and compositions of catalysts could lead to obvious discrepancies in reaction pathways and energy barriers even in the same catalytic reaction. Based on this point, various Au-based nanoalloys with well-designed microstructures and compositions have been synthesized by different methods. Importantly, most of the aforementioned Au-based nanoalloys have demonstrated much enhanced catalytic activity, selectivity and durability in many catalytic applications.33–36
In this review, we summarize the general synthetic methods and dominant catalytic applications of Au-based nanoalloys. First, we give a brief introduction of nanoalloys from the aspects of size, composition and crystal phase, along with the highlights of the effects of these factors on the catalytic properties. Then, we introduce general methods used in recent years for the synthesis of Au-based nanoalloys. Subsequently, the catalytic applications of Au-based nanoalloys, along with the discussion on catalytically active sites and the effect of structures and components on the catalytic performance, in various chemical reactions are also presented. Finally, we provide some perspectives on the current challenges and opportunities facing Au-based nanoalloys, aiming to accelerate the development of high-performance Au-based catalysts towards practical applications.
(a) Direct synthesis. This strategy commonly involves the introduction of alloying elements before the nucleation of nanoseeds. Au and alloying elements will simultaneously precipitate, nucleate, grow and then generate Au-based nanoalloys. The direct synthesis strategy usually includes a series of methods such as the co-reduction method, electrochemical deposition, thermal shock, laser ablation in liquid technique, scanning probe block copolymer lithography, etc.
(b) Elemental diffusion. In contrast to the aforementioned strategy, elemental diffusion is typically carried out step by step. The alloy structure starts to form on the surface or interface, and the morphology of the final products will partially inherit the characteristics of initial nanostructures. The elemental diffusion strategy mainly includes methods such as seed-mediated diffusion and thermal diffusion.
In this section, we will discuss the widely used synthetic methods of Au-based nanoalloys in recent years. Table 1 summarises the advantages and disadvantages of different synthetic methods. Specifically, the reaction principles, synthetic processes as well as typical alloy microstructures and components will be described. Some representative studies will be highlighted here to illustrate the key factors of each synthetic method.
Methods | Advantages | Disadvantages |
---|---|---|
Co-reduction method | Facile operation; low equipment requirement; low cost | The composition of products is typically limited to classically miscible metals |
Seed-mediated diffusion | Products with a narrow size distribution and well-defined structure | Time consuming; kinds of products are limited by the seeds |
Electrochemical deposition | High-purity products; quick reaction | Involves templates; high cost |
Thermal diffusion | Facile operation; low equipment requirement | High temperature; energy consuming |
Thermal shock | Not limited to immiscible metals; uniform dispersion of elements; narrow size distribution; applicable to multi-element alloys; quick reaction | Ultra-high temperature; special equipment |
Laser ablation in liquid technique | Facilitate the synthesis of metastable phases and defect-rich products | Kinds of products are limited by the targets; high equipment requirements; potential safety issues associated with the laser |
Scanning probe block copolymer lithography | The composition and position of products are precisely controllable; good substrate adaptability; accessible to multi-element alloys | Complex operation; high equipment requirements |
Fig. 2 Co-reduction method for the synthesis of Au-based nanoalloys. (a) The scheme depicting the growth process of Au100−xPtx NPs. (b) TEM image of Au60Pt40 NPs with the particle size distribution in the inset. (c) HRTEM image of Au60Pt40 NPs. Reproduced with permission.102 Copyright 2013, Royal Society of Chemistry. (d–g) HRTEM image (d), elemental mappings of (e) Ni and (f) Au, and (g) EDX line-scanning profiles (inset shows the HAADF-STEM image of the corresponding NPs; scale bar, 10 nm) of Ni43Au57 NPs. Reproduced with permission.36 Copyright 2015, American Chemical Society. (h and i) SEM image (h) and TEM image (i) of hexoctahedral Au–Pd nanocrystals. (j) Schematic illustration of the relationship between the morphology of Au–Pd nanocrystals and their growth kinetics. Reproduced with permission.106 Copyright 2013, Wiley-VCH. (k) The scheme for the generation process of fcc and hcp AuRu3 nanocrystals. RRu and RAu represent the reduction rates of Ru and Au precursors, respectively. Reproduced with permission.34 Copyright 2018, Springer Nature. |
Recently, Sun et al. obtained NiAu alloy NPs by the co-reduction of HAuCl4·3H2O and Ni(acac)2 (acac denotes acetylacetonate) in the presence of oleic acid and oleylamine.36 Remarkably, it was found that the first reduction of HAuCl4·3H2O to Au facilitates Ni(acac)2 reduction at low temperature, overcoming the difficulties of a large Ni/Au miscibility gap and reduction potential gap in generating NiAu nanoalloys. A higher reaction temperature led to more Au content in NiAu alloy NPs. Specifically, the increase of the reaction temperature from 150 to 200 °C induced the formation of products ranging from Ni48Au52 to Ni43Au57. The HRTEM image (Fig. 2d), elemental mappings (Fig. 2e and f) and EDX line scanning profiles (Fig. 2g) were used to confirm the alloy nature of NiAu NPs. In addition, by changing the non-noble metal precursor from Ni(acac)2 to Co(acac)2 or Fe(acac)2, this method can also be readily extended to the synthesis of CoAu and FeAu alloy NPs.
By tuning the reaction kinetics with reductants, Au-based nanoalloys enclosed by high-index facets could also be obtained. As a representative study, Lee et al. co-reduced the HAuCl4/K2PdCl4 metal precursors in the presence of cetyltrimethylammonium chloride (CTAC) to obtain the hexoctahedral Au–Pd alloy nanocrystals enclosed by high-index {541} facets by using AA as the reductant.106Fig. 2h and i show the typical SEM and TEM images of the resultant hexoctahedral Au–Pd nanocrystals. When CTAC was used to reduce the metal precursors in the absence of AA, Au octahedra enclosed by {111} facets were first produced, followed by epitaxial growth of Pd layers on the preformed Au octahedra, generating the Au@Pd core–shell nanocrystals. After adding AA, alloy nanostructures were generated due to the enhanced reaction kinetics. Furthermore, through increasing the concentration ratio of AA to metal precursors, the nanocrystal growth behavior was transformed from thermodynamically controlled growth to kinetically controlled growth, as shown in Fig. 2j. Specifically, as the concentration ratio of AA to metal precursors was increased from 0.75 to 1, 4 and 20, the shape/morphology of Au–Pd alloy nanocrystals changed from octahedron (enclosed with {111} facets) to rhombic dodecahedron (enclosed with {110} facets), hexoctahedron (enclosed with high-index {541} facets) and quasi-flower/dendrites, respectively.
By precisely adjusting the reduction rate of metal precursors, nanoalloys with different crystal phases could also be obtained in the presence of specific surfactants. As a typical study, Kitagawa et al. found that AuRu3 nanoalloys with both fcc and hexagonal close-packed (hcp) phases were synthesized by controlling the reduction speed of appropriate Au and Ru precursors in the presence of CTAB (Fig. 2k).34 Specifically, by using diethylene glycol and ethylene glycol as reductants, the Au precursor (i.e., HAuBr4) was reduced slightly faster than the Ru precursor (i.e., K2Ru(NO)Cl5), which favored the production of fcc AuRu3 NPs. In contrast, when diethylene glycol was selected as the reducing agent, the Ru precursor (i.e., RuCl3) was reduced slightly faster than the Au precursor (i.e., HAuBr4) in the presence of CTAB, leading to the generation of hcp AuRu3 NPs.
Here we illustrate the general process of seed-mediated diffusion using a representative study by Li et al., as shown in Fig. 3a.114 In this study, the pre-synthesized Au NPs (i.e., seeds) and Cu(CH3COO)2·H2O (i.e., Cu precursor) were first mixed in a solution containing oleic acid and tri-n-octylamine. Then, Cu2+ ions were reduced to highly reactive Cu atoms or clusters with oleic acid and tri-n-octylamine at 70 °C. Meanwhile, surfactants on the surface of Au seeds could desorb, leaving more active sites. When Cu atoms or clusters came into contact with these surface active sites, they diffused into Au seeds and formed Cu–Au nanoalloys. To be specific, when the Cu/Au atomic ratio was 3/1, ordered Cu3Au NPs were obtained by using 6.3 nm Au seeds at 300 °C (Fig. 3b). Meanwhile, intermetallic CuAu NPs were generated using 8.5–9.5 nm Au seeds at 280 °C when the Cu/Au atomic ratio was 1/1. Moreover, by using Au seeds with different sizes of 3.5 nm, 4.9 nm, and 6.3 nm, ordered AuCu NPs with the sizes of 4.2 ± 0.2 nm, 6.0 ± 0.2 nm, and 7.4 ± 0.3 nm were obtained, respectively. This work provides an effective protocol to synthesize intermetallic nanoalloys with well-defined compositions, sizes and structures.
Fig. 3 Seed-mediated diffusion for the synthesis of Au-based nanoalloys. (a) The scheme depicting the formation mechanism of intermetallic Cu–Au nanocrystals. (b) XRD patterns of CuAu and Cu3Au nanocrystals. Reproduced with permission.114 Copyright 2010, Wiley-VCH. (c–f) HAADF-STEM images of AuCu alloy NPs with the (c and d) fcc and (e and f) fct phases. Reproduced with permission.115 Copyright 2017, American Chemical Society. |
The reaction conditions such as temperature and time in the seed-mediated diffusion also play an important role in the formation of nanoalloys with different crystal phases. For instance, Zhu et al. synthesized fcc AuCu and face-centered tetragonal (fct) AuCu alloy NPs using Au NPs as the seed at different reaction temperatures.115 Specifically, the final products were mainly fcc AuCu alloy NPs at 210 °C, while fct AuCu alloy NPs were obtained when the temperature was increased to 290 °C. The HAADF-STEM characterization confirmed the formation of the uniform spherical fcc AuCu (Fig. 3c, d) and fct AuCu (Fig. 3e and f) alloy NPs. In another study, Yang et al. also synthesized fct Au–Cu alloy NPs in the presence of Au seeds.116 It was found that increasing the temperature and prolonging the time promote the generation of the fct phase.
The research work done by Nugraha et al. will be described here to elucidate a typical procedure of electrochemical deposition to obtain a mesoporous alloy film.120 In this work, an aqueous solution containing multiple kinds of metal precursors including HAuCl4, CuSO4 and NiCl2 was first mixed with the pre-prepared polymeric micelle assembly to generate the electrolyte solution. At a certain potential, the metal precursors in the mixed electrolyte solution were simultaneously reduced to their metallic states to form a mesoporous AuCuNi alloy film with an average pore size of about 28 nm. After that, the organic template was removed by solvent extraction (Fig. 4a). The composition of the final products can be easily adjusted by changing the metal precursor ratio in the initial electrolyte solution, while the thickness of the products can be readily controlled by adjusting the reaction time. Cross-sectional characterization indicated that a well-defined mesoporous structure of the AuCuNi film formed on the surface as well as throughout the whole cross-sectional area (Fig. 4b and c). And the HRTEM image (Fig. 4d) further confirmed the high crystallinity of the mesoporous AuCuNi membrane. Furthermore, all metal elements were uniformly distributed in the alloy film (Fig. 4e–j), proving that the resultant mesoporous AuCuNi membrane is free of phase segregation.
Fig. 4 Electrochemical deposition of Au-based nanoalloys. (a) The schematic illustration of electrodeposition of mesoporous AuCuNi nanoalloy films. (b–d) SEM image (b), TEM image (c), and HRTEM image (d) of the cross-section of the Au60Cu35Ni5 mesoporous film that is obtained at the applied potential of −0.9 V (vs. Ag/AgCl). (e) SEM image of the top surface of the mesoporous Au60Cu35Ni5 film. (f–j) HAADF-STEM image (f) of the Au60Cu35Ni5 film and the corresponding EDX elemental mappings: (g) Au, (h) Cu, (i) Ni, and merged (j). Reproduced with permission.120 Copyright 2018, Wiley-VCH. |
Lyotropic liquid crystal (LLC) assisted electrodeposition is another promising method to synthesize Au-based nanoalloys with mesoporous and controllable structures.119 It is known that micelles can be generated when the concentration of amphiphilic surfactants is higher than the critical micelle concentration (CMC). Further increasing the concentration will lead to the formation of LLCs, in which the micelles adopt a specific arrangement. In the LLC solution,125 metal ions coordinate with the surfactants to generate a stable mesoporous structure. After electrochemical reduction, mesoporous alloy films can be obtained. As a typical study, Yamauchi et al. produced mesoporous Pt–Au binary nanoalloys by LLC-assisted electrodeposition.126 Specifically, the metal precursor solution containing H2PtCl6·6H2O, HAuCl4·4H2O, H2O, C16H33(OCH2CH2)8OH and ethanol was cast onto a conductive substrate to form LLCs after the evaporation of volatile solvents, followed by electrochemical deposition to generate mesoporous Pt–Au nanoalloys. Moreover, the framework composition of mesoporous Pt–Au nanoalloys could be easily modulated by changing the feed ratio of metal precursors in the solution. Generally, low Au content will generate well-ordered 2D hexagonal mesoporous nanostructures, while increasing the Au content would decrease the mesostructural order of bimetallic nanoalloys.
The elemental distribution of metal materials can be tuned by thermal annealing, making it feasible to prepare nanoalloys from pre-synthesized bi-/multi-nary metal nanostructures. For example, by using silica-coated Au@Ag core–shell nanorods with a fixed composition and element distribution as the research object, Hoeven et al. studied their atomic redistribution (i.e., alloying) during the heating process.131 EDX mappings showed that the boundary between the Au core and the Ag shell became blurred and then overlapped along with the temperature increase from 25 °C to 475 °C (Fig. 5a). Interestingly, alloying usually happened at a certain temperature which corresponded to the steep change in the alloying degree–temperature curves (Fig. 5b and c). Moreover, the degree of alloying depended on the volume and composition of particles. For particles with a similar composition (i.e., similar Ag content), the smaller the volume, the lower the temperature required for complete alloying (Fig. 5b), which is ascribed to the increased atomic mobility at smaller particle dimensions. For particles with a similar volume, the decrease of Ag content led to a significant drop in the starting temperature for alloying (Fig. 5c). This work indicated that both metal composition and nanoscale dimension should be considered in order to obtain desirable atomic redistribution by thermal diffusion. Recently, Zhang et al. observed a reversible transformation between the core–shell and alloy structures in Ni–Au NPs during the CO2 hydrogenation.35 The initial NPs adopted the Ni–Au core–shell structure that consisted of an fcc Ni core and 2–3 atomic layers of the Au shell. When the temperature was increased to 600 °C during CO2 hydrogenation, the structure of Ni–Au NPs changed from core–shell to alloy (Fig. 5d). Interestingly, when the temperature was brought down to 400 °C, an Au atomic layer epitaxially re-segregated along the Ni (200) plane (Fig. 5e), which proved the reversibility of this alloying/dealloying process.
Fig. 5 Thermal diffusion for the preparation of Au-based nanoalloys. (a) EDX elemental maps of silica-coated Au@Ag core–shell nanorods acquired at 25 °C, 400 °C, 450 °C, and 475 °C, respectively. (b) The dependence of the alloying degree on the particle volume for silica-coated Au@Ag nanorods. (c) The alloying degree with respect to Ag-content in silica-coated Au@Ag nanorods. Reproduced with permission.131 Copyright 2018, American Chemical Society. (d) From left to right, the HRTEM image (scale bar: 2 nm) with a Thon ring in the inset, enlarged HRTEM image of the surface region, schematic atomic structure, and point analysis of the electron energy loss spectra with a HAADF-STEM image (scale bar: 2 nm) of a Ni–Au NP at 600 °C in the inset. (e) From left to right, the HRTEM image (scale bar: 2 nm) with a Thon ring in the inset, enlarged HRTEM image of the surface region, and phase-contrast profile of a Ni–Au NP at 400 °C. Reproduced with permission.35 Copyright 2020, Springer Nature. |
As a representative study, a metastable RuAu single atom alloy (SAA) was prepared via vaporizing the immersed Ru target and reducing HAuCl4 in aqueous solutions using a laser with a pulse width of 7 ns (Fig. 6a).135 It was found that the HAuCl4 aqueous solution with different concentrations could lead to products with different compositions. When the concentration of HAuCl4 was 0.2 mM, the obtained RuAu NPs exhibited an average size of 8 nm (Fig. 6b), in which Au and Ru were uniformly distributed throughout the particles (Fig. 6c). The high resolution HAADF-STEM images showed that the individual Au atoms (marked by red circles with higher pixel intensity) occupied some positions of Ru lattices, indicating the SAA feature of the resultant RuAu NPs (Fig. 6d and e). This work suggested that LALT is an effective technique to generate SAAs despite their components being immiscible at the bulk scale.
Fig. 6 Synthesis of Au-based nanoalloys with the laser ablation in liquid technique. (a) Schematic illustration of LALT in the synthesis of RuAu SAA NPs. (b) TEM image of RuAu NPs (scale bar: 50 nm) with particle size distribution in the inset. (c) HAADF-STEM image (scale bar: 5 nm) and elemental mappings of Ru, Au and the overlap. (d and e) High-resolution HAADF-STEM image of RuAu NPs (d), in which Au atoms are marked with red circles (scale bar: 1 nm), and (e) the enlarged image of the red dashed rectangle of (d). Reproduced with permission.135 Copyright 2019, Wiley-VCH. |
Due to the strong quenching effect, LALT is a unique technique that can overcome the inherent composition limitations of synthetic alloys. For instance, Vassalini et al. successfully synthesized Au–Fe nanoalloys through the laser irradiation of a kinetically stable Au–Fe bulk alloy (i.e., the solid target) in ethanol solution.141 It was observed that the electronic structure of Fe was significantly modified in the Au–Fe nanoalloy, while the Au electronic structure remained quite similar to that of pure Au. Notably, there were up to 11 at% Fe atoms that were stably and homogeneously incorporated into the Au lattice, which far exceeded the thermodynamic limit of Fe-doped Au nanomaterials under ambient conditions.
Generally, compared with the other synthetic methods of Au-based nanoalloys, LALT possesses the advantages of faster reaction speed and higher degree of alloying. However, due to the utilization of lasers, high requirements on the experimental setup and potential safety issues might limit the wide application of this technique.
Here we use a binary alloy reported by Chen et al. as an example to illustrate the general working principle of SPBCL.148 In a typical process, the ink composed of metal precursors (e.g., HAuCl4/Na2PdCl4) and poly(ethylene oxide)-block-poly(2-vinylpyridine) was first deposited onto the specific position of the substrate with the AFM tips. Later, after annealing in Ar at 150 °C for 48 h, and successively in H2 at 500 °C for 12 h, binary alloy NPs (e.g., Au–Pd) with good crystallinity and homogeneous elemental distribution were in situ formed on the substrate. Besides, SPBCL also provides a general synthetic strategy for the structure and composition control of multicomponent nanoalloys.149,150
Catalysts | Electrolyte | Major products and maximum FE | Stability | Ref. |
---|---|---|---|---|
a SCA, submicrocone arrays; NCF, nanoporous Cu film; SCE, saturated calomel electrode; Ag/AgCl, Ag/AgCl reference electrode; CNFs, carbon nanofibers; CSNP, core–shell nanoparticle. | ||||
AuCu/Cu-SCA | 0.5 M KHCO3 | C2H5OH (29 ± 4%) and C2H4 (16 ± 4%) at −1.0 VRHE | No obvious decrease after 24 h at −1.0 VRHE | 212 |
Au1Sn2 NPs | 0.1 M NaHCO3 | HCOOH (42%) at −1.1 VRHE | Slight increase after 10 h at −1.0 VRHE | 165 |
Ordered AuCu NPs | 0.1 M KHCO3 | CO (∼80%) at −0.77 VRHE | No obvious decrease after 12 h at −0.76 VRHE | 116 |
Cu63.9Au36.1/NCF | 0.5 M KHCO3 | CH3OH (15.9%) and C2H5OH (12%) at −1.1 VSCE | — | 213 |
Pd5@Au95 NPs | 0.1 M KHCO3 | CO (∼80%) at −0.5 VRHE | — | 52 |
Twisted Pd0.8Au nanowires | 0.5 M KHCO3 | CO (94.3%) at −0.6 VRHE | 15.7% decrease after 8 h at −0.6 VRHE | 214 |
Au3Cu nanocubes | 0.5 M KHCO3 | CO (90.2%) at −0.38 VRHE | No obvious decrease after 30 h at −0.38 VRHE | 215 |
AgPd-edged Au nanoprisms | 0.1 M HClO4 | HCOOH (49%) at −0.18 VRHE | No obvious decrease after 12 h at −0.18 VRHE | 216 |
Au75Pd25 NPs | 0.1 M KHCO3 | CO (∼80%) at −0.5 VRHE | — | 217 |
Au1Ni1-CNFs | 0.1 M KHCO3 | CO (92%) at −0.98 VRHE | No obvious decrease after 16 h at −0.98 VRHE | 218 |
AuFe-CSNP | 0.5 M KHCO3 | CO (97.6%) at −0.4 VRHE | No obvious decrease after 90 h at −0.5 VRHE | 219 |
Pd@Pd3Au7 nanocubes | 0.1 M KHCO3 | CO (94%) at −0.5 VRHE | No obvious decrease after 8 h at −0.7 VRHE | 161 |
Au94Pd6 NPs | 0.1 M HClO4 | CO (94.7%) at −0.6 VRHE | No obvious decrease after 12 h at −0.6 VRHE | 163 |
Cu3Au nanowire arrays | 0.1 M KHCO3 | C2H5OH (48%) at −0.5 VRHE | 14% decrease after 8 h at −0.7 VRHE | 166 |
AuAgPtPdCu NPs | 0.5 M K2SO4 | CH4 (38.0%) and C2H4 (29.5%) at −0.9 VAg/AgCl | Steady decrease after 1 h at −0.8 VAg/AgCl | 167 |
Pd–Au electrode | 0.1 M KH2PO4/0.1 M K2HPO4 | CO (30.9%) at −0.6 VRHE | — | 168 |
For the electrocatalytic reduction of CO2, the first step is the adsorption of CO2 onto the surface of electrocatalysts. In addition to the physical adsorption, CO2 molecules can be partially charged and be adsorbed chemically.155 Owing to the lone pair of electrons of the O atom and the positively charged C atom, CO2 molecules can be easily adsorbed on the electrocatalyst surface by donating the lone pair of electrons to the Lewis acid centers or accepting electrons from the Lewis base centers, weakening the CO bonds and lowering the activation energy for subsequent electrochemical processes.156 Based on previous studies, the generation of different CO2-reduction products (e.g., C1 and C2+ products) usually involves distinct reaction pathways, which are closely associated with the formation of different intermediate species.157,158 For the generation of C1 products such as CO, methane, methanol and formic acid, the CO2 reduction could adopt different pathways, in which the formation of different intermediates (e.g., *CO2˙−, *CO, and *COOH) on the surface of electrocatalysts is likely responsible for generation of the ultimate products. For the production of C2 products such as glyoxal, glycolaldehyde, ethylene glycol and acetaldehyde, the formation of *CO and its further hydrogenation to form *CHO and *COCHO may give rise to the final products. For the production of C3 products such as propionaldehyde, n-propanol and acetone, it was hypothesized that the intermolecular C–C coupling between C1 and C2 intermediates and the following proton/electron transfer result in the formation of advanced products. Obviously, the CO2RR typically involves a series of distinct intermediates on the catalyst surface. And the intermediates are very sensitive to the electronic structure and surface state of electrocatalysts. The ideal electrocatalysts are supposed to bind with the key intermediates moderately. This is because very weak binding impedes the beginning of the reaction while the excessively strong binding results in the difficulty for further reactions. Therefore, by tuning the binding capacity of electrocatalysts to the different intermediates, the selective synthesis of particular fuels/chemicals could be well achieved. Based on this idea, abundant efforts have been devoted to selectively reducing CO2 to high-value fuels and chemicals with electrocatalysts, such as nanoalloy electrocatalysts.
As for nanoalloy electrocatalysts, two notable effects, i.e., the electronic effect and geometric effect, play crucial roles in determining the electrocatalytic CO2 reduction performance. As for the electronic effect, the interaction of d-bands of transition metals with adsorbates governs the binding strength (the lower d-band center relative to the Fermi level indicates the weaker binding strength for the occupancy of anti-bonding states159), and thus largely determines whether the catalytic reaction occurs and how it proceeds. As for the geometric effect, the interaction ability of metal atoms with adsorbates would be altered if the environment around the atoms gets changed.160 For example, more content of Cu in Au–Cu alloy NPs results in a higher d-band center, which is capable of interacting with more kinds of reaction intermediates. Importantly, it was found that having a Cu atom adjacent to an Au–C bond will stabilize *COOH while that with *CO remains unchanged, resulting in enhanced CO production activity.159 Based on this point, Gong et al. synthesized ultrathin Pd–Au shells on Pd nanocubes to catalyze the reduction of CO2 to CO with a Faradaic efficiency (FE) close to 100% in a potential range from −0.6 to −0.9 V (vs. the reversible hydrogen electrode (RHE)).161 With the addition of Au atoms, the d-band center of Pd atoms moves down relative to the Fermi level, which weakens the strong Pd–C bond and makes it easy to desorb *CO. In addition, the electron transfer between Au and Pd atoms facilitates the generation of *COOH on the surface of the ultrathin Pd–Au shell. The results indicated that the Pd–Au nanoalloy with an appropriate composition exhibits superior CO2RR performance to pure Au and Pd.
At present, most of the Au-based nanoalloy catalysts are in favor of generating C1 products, especially CO.162,163 As a typical study, Smith et al. synthesized Au–Pt bimetallic thin films with different compositions and morphologies for electrocatalytic reduction of CO2.164 It revealed the general relationship between the formation of CO (main product)/HCOOH and the catalyst composition. The highest FE of CO for pure Au is about 77% at a potential of −0.6 V (vs. RHE, Fig. 7a), while it shows a decreasing trend with the increase of Pt content. To gain a deep understanding of the relationship between the alloy composition and CO2RR performance, the FE and partial current density for CO at various potentials were measured (Fig. 7b and c). It can be seen that the FE for CO (Fig. 7b) increases while the onset potential for CO positively shifts (Fig. 7c) as the Au content increases, suggesting that the composition of Au-based nanoalloys does have an obvious effect on their CO2RR performance. Specifically, with the increase of Au content, the d-band center will be shifted away from the Fermi level, which decreases the binding energy of *COOH and *CO and thus changes the CO2-reduction performance. Besides, for HCOOH, the FEs corresponding to all the catalysts with different compositions were always below 5%. In another study, Janáky et al. used Au–Sn NPs as electrocatalysts for the CO2RR, in which the final products also only contain HCOOH, CO and H2 (Fig. 7d).165 When the atomic ratio of Au/Sn reached 1/2, the Au–Sn nanoalloy exhibited the lowest overpotential and best stability. Specifically, the current density was relatively stable at about 8 mA cm−2 within 10 h of testing at −1.0 V (vs. RHE, Fig. 7e).
Fig. 7 The electrocatalytic performance of Au-based nanoalloys towards the CO2RR. (a) The FE of CO and H2 on Au, Pt and Au–Pt alloys in CO2-saturated 0.1 M KHCO3 solution (pH = 6.8) at −0.65 V (vs. RHE). (b) The FE of CO on Au and Au–Pt alloys at different potentials. (c) The partial current density for CO on Au and Au–Pt alloys at different potentials. Inset: zoom-in profiles of the CO partial current density plots. Reproduced with permission.164 Copyright 2017, Elsevier. (d) The partial current densities of CO, HCOOH and H2 of the Au1Sn2 catalyst at different potentials in the CO2RR. (e) Long-term durability profile of the Au1Sn2 catalyst in CO2-saturated 0.1 M NaHCO3 solution at −1.0 V (vs. RHE). Reproduced with permission.165 Copyright 2018, American Chemical Society. (f) The FE of CO, CH4, C2H4 and H2, and (g) chronoamperometric responses of a high-entropy alloy (i.e., AuAgPtPdCu NPs) in CO2-saturated K2SO4 solution at different potentials (Inset: the corresponding current densities at different potentials). Reproduced with permission.167 Copyright 2020, American Chemical Society. (h) Generation of H2, CH4, C2H4, C3 and C4 hydrocarbons on the Pd–Au alloy electrode in 0.1 M KH2PO4/K2HPO4 buffer electrolyte (pH = 6.7). Reproduced with permission.168 Copyright 2016, Royal Society of Chemistry. |
In contrast to C1 products, the selective electroreduction of CO2 to high-value C2+ products (e.g., hydrocarbons and alcohols) is more challenging due to the difficulty in C–C coupling and subsequent complex reaction pathways. Cu and Cu-based catalysts are considered to be the dominant metal-based materials that can selectively reduce CO2 to C2+ products with a relatively high efficiency. Considering its merits, Cu has been introduced into Au to adjust the electronic structure of Au-based nanoalloys, aiming at optimizing the CO2RR activity and selectivity towards C2+ products. For example, He et al. used constant-potential pulse electrodeposition to prepare CuxAuy nanowire arrays (NWAs) with a high aspect ratio.166 When employed as electrocatalysts for the CO2RR, it was found that CuxAuy NWAs could significantly reduce the onset potential of alcohols. As for the Cu3Au NWAs with an optimized composition, they can selectively reduce CO2 to ethanol with an FE of up to ∼48% at a low potential of −0.5 V (vs. RHE). The superior ethanol selectivity of Cu3Au NWAs might arise from the synergistic effects of the electronic structure and morphology that increase the adsorption of *CO on the nanowire surface and promote the following reduction of *CO to ethanol through a dimerization process.
Apart from the binary Au–Cu alloys, multi-nary Au–Cu–M nanoalloys have also been developed in order to drive the CO2RR towards the formation of more kinds of C2+ products. In a typical study by Biswas et al., a high-entropy alloy containing five metal elements (i.e., AuAgPtPdCu NPs) was prepared, which can effectively catalyze the conversion of CO2 to hydrocarbon products using 0.5 M K2SO4 as the electrolyte.167 As shown in Fig. 7f, methane (CH4) and ethylene (C2H4) are the main products in a potential range from −0.7 to −0.9 V (vs. Ag/AgCl). Importantly, the FE of C2H4 reached the highest value of 29.5% at −0.9 V (vs. Ag/AgCl). In the chronoamperometric response measurements, the steady-state current densities within the initial 1000 s are −6.83, −10.31 and −13.81 mA cm−2 at various potentials of −0.7, −0.8, and −0.9 V (vs. Ag/AgCl), respectively (Fig. 7g). It was proposed that the excellent CO2RR performance of high-entropy AuAgPtPdCu NPs is attributed to the existence of redox-active Cu and the synergistic effect between multiple metal elements. This study demonstrated the feasibility of improving the CO2RR performance through the design and synthesis of high-entropy alloys.
Besides Cu, the combination of other metals with Au to form Au-based nanoalloys can also promote the formation of C2+ products in the CO2RR. As a representative study, Koper et al. reported that Pd–Au alloys formed by electrochemical deposition could electrochemically reduce CO2 to various hydrocarbons ranging from C1 to C5 products.168 Since the potential for reducing *CO to hydrocarbons is much lower than that for reducing CO2 to hydrocarbons, *CO is a key reaction intermediate for the generation of hydrocarbons. By alloying Au (with weak binding to *CO) with Pd (with strong binding to *CO), it achieved a precise and balanced control of *CO binding on the catalyst surface during the CO2RR. The online electrochemical mass spectrometry (OLEMS) indicated that the CO2-reduction products on Pd–Au alloys contain hydrogen, C1 (CH4, HCOOH and methanol), C2 (C2H4, ethane, ethanol and acetic acid), C3 (propane and propylene), C4 (1-butene, isobutane and butane) and C5 (2-methyl-butane, pentane and pentene) species (Fig. 7h). This work suggested the possibility of obtaining higher hydrocarbons (e.g., C3 to C5) from CO2 reduction by fine tuning the binding energy of *CO on the catalyst surface.
To better modulate the ORR pathway, it is significant to understand the reaction mechanisms, especially the 2-electron and 4-electron pathways. As indicated by previous studies, the adsorption mode of O2 on the catalysts plays a crucial role in controlling the reaction pathway. To be specific, three kinds of adsorption models have been reported, including the Pauling model (end-on adsorption), Griffiths model (side-on adsorption) and Bridge model (bridge-on adsorption).172,173 In the Pauling model, only one atom of the O2 molecule interacts with the active site of electrocatalysts, which is favorable to maintain the O–O bonding and thus desirable for the formation of *OOH via the 2-electron pathway. As for the Griffiths model, two atoms of the O2 molecule interact with one active site, which will weaken the O–O bond and favor the 4-electron pathway. If the active sites of electrocatalysts strongly interact with O2, the bridge-on adsorption will occur, in which both atoms of O2 interact with two active sites simultaneously. In this situation, the O–O bonding is easily broken to produce two O* through the 4e-electron pathway. Moreover, the interaction capability of electrocatalysts with different intermediates generated in the ORR, such as oxygenated (O*), hydroxyl (OH*) and superhydroxyl (OOH*) species, also influences the reaction thermodynamics and kinetics, resulting in different products (i.e., selectivity) and current densities (i.e., activity). Hence, for nanoalloy electrocatalysts, it is feasible to manipulate the ORR pathway by tuning their size, composition and structure, considering the unique electronic effect and geometric effect in alloys. Table 3 shows the catalytic performance of different Au-based nanoalloys for the ORR.
Catalysts | Electrolyte | Catalytic activity | Stability | Ref. |
---|---|---|---|---|
a NWNs, nanowire-networks; MA, mass activity; SA, specific activity; E1/2, half-wave potential; pTBA, poly(benzoic acid-2,2′:5′,2′′-terthiophene); NAs, nanothorn assemblies; ECSA, electrochemically active surface area. | ||||
S-doped AuPbPt NWNs | 0.1 M HClO4 | MA (0.59 A mg−1) and SA (0.42 mA cm−2) at 0.9 VRHE | 47 mV increase of E1/2 after 15000 cycles (0.6–1.0 VRHE) | 220 |
Pt–Au10–Co25 NPs | 0.1 M HClO4 | SA (0.75 mA cm−2) at 0.95 VRHE | 25% loss of SA after 100000 cycles (0.6–1.0 VRHE) | 221 |
Au@Ni2Pt2 NPs | 0.1 M HClO4 | MA (560 mA mgPt−1) and SA (0.8 mA cmpt−2) at 0.9 VRHE | <20% loss of MA after 20000 cycles (0.6–1.1 VRHE) | 222 |
AuNi@pTBA | 0.1 M NaOH | SA (0.59 mA cm−2) at −0.2 VAg/AgCl | 21% loss of current density after 30000 cycles (−0.9–0.2 VAg/AgCl) | 223 |
PtAu NPs | 0.1 M HClO4 | MA (33.2 A gPt−1) and SA (1.74 mA cmPt−2) at 0.9 VRHE | — | 224 |
AuCu@Pt NPs | 0.1 M HClO4 | MA (0.571 A mgPt−1) at 0.9 VRHE | 12% loss of MA after 30000 cycles (0.6–1.1 VRHE) | 225 |
PdCuAu NAs | 0.1 M HClO4 | E 1/2 (0.86 VRHE) | ∼11.9% loss of current density at 0.6 VRHE after 5 h | 226 |
Au0.01–Pt3Ni nanowires | 0.1 M HClO4 | MA (3.08 A mgPt−1) and SA (5.74 mA cm−2) at 0.9 VRHE | No obvious loss of MA after 20000 cycles (0.1–1.1 VRHE) | 227 |
FePtAu/FePt-0.8 nanowires | 0.1 M HClO4 | SA (1.69 mA cm−2) at 0.5 VAg/AgCl | No obvious shift of E1/2 after 5000 cycles (0.4–0.8 VAg/AgCl) | 228 |
Au/CuPt NPs | 0.1 M HClO4 | MA (1.5 A mgPt−1) and SA (2.72 mA cm−2) at 0.9 VRHE | 7.8% loss of ECSA after 5000 sweeps (0.60–1.10 VRHE) | 229 |
PtCuAu0.0005/C NPs | 0.1 M HClO4 | MA (1.00 mA μgPt−1) and SA (3.88 mA cm−2) at 0.90 VRHE | 8% loss of MA after 10000 cycles (0.60–1.0 VRHE) | 230 |
AuCu3/C NPs | 0.1 M KOH | MA (523 mA mgAu−1) at 0.80 VRHE | <5% loss of current after 12 h at 0.77 VRHE | 231 |
Because of the moderate stability and high catalytic efficiency, platinum/carbon (Pt/C) is widely utilized as a commercial catalyst in the field of the ORR. Considering that noble metal Pt is relatively rare and extremely expensive, great efforts have been devoted to decreasing the content of Pt in ORR catalysts, while achieving a higher activity, higher selectivity and higher stability. Recent studies showed that Au at the nanoscale possesses good catalytic activity for the ORR, and the addition of Au could significantly improve the stability of Pt catalysts.174 Based on this idea, current research work mainly focuses on adjusting the compositions and microstructures of Au–Pt alloys. For examples, He et al. synthesized Pt–Au string-bead chain nanonetworks, whose area specific activity (SA) and mass activity (MA) are 2.28 and 1.74 times that of commercial Pt/C catalysts in the ORR, respectively.175 Wang et al. synthesized bimetallic Pt–Au superlattice arrays, which show both high catalytic activity (SA and MA are 2.18 and 2.24 times that of commercial Pt/C catalysts, respectively) and excellent stability (MA still remains 96.4% after 1000 cycles) towards the ORR.176 Stamenkovic et al. coated a layer of nanoscale Au thin film on the surface of ultra-high vacuum cleaned glassy carbon (GC), which then guided the overgrowth of Pt atoms with a unique (111) structure.177 Significantly, the introduction of Au underlayers can eliminate the undesirable Pt dissolution in the ORR. To extend this concept, Pt3Au alloy NPs supported on carbon (denoted as Pt3Au/C) were also synthesized and used as ORR catalysts. It was observed that Pt3Au/C showed a 30-fold improvement in durability in comparison with Pt/C in a wide potential range of up to 1.2 V (Fig. 8a). It was proposed that the presence of Au can selectively protect the low-coordinated Pt sites, maximizing the stability of catalysts while minimizing the negative impact on the ORR activity. The aforementioned work highlights the positive implications of alloying Pt with Au towards the preparation of advanced ORR catalysts.
Fig. 8 The electrocatalytic performance of Au-based nanoalloys towards the ORR. (a) CV curves (top panel) and the corresponding Pt dissolution plots (bottom panel) of Pt/C and Pt3Au/C in 0.1 M HClO4 solution (50 mV s−1, 25 °C and 100 rpm). Inset: the comparison of Pt dissolution at various positive potential limits for Pt/C and Pt3Au/C in 0.1 M HClO4 solution at 50 mV s−1. Reproduced with permission.177 Copyright 2020, Springer Nature. (b) Positive ORR polarization curves of commercial Pt/C, NPG–Pt and fresh NPG–Pd–Pt in O2-saturated 0.1 M HClO4 solution (10 mV s−1, 25 °C and 1600 rpm.) (c) Mass activity of Pt/C and NPG–Pd–Pt at 0.9 V (vs. RHE) at various stages of durability measurements. Reproduced with permission.33 Copyright 2017, Springer Nature. (d and e) ORR polarization curves (d) and the corresponding mass activity at 0.9 V (e) of O–PdZn and Au–O–PdZn catalysts before and after 30000 potential cycles. Reproduced with permission.180 Copyright 2019, American Chemical Society. |
To promote the synergistic effects between different metal elements, researchers have extended the ORR catalysts from bimetallic alloys to multi-metallic alloys. As a typical study, Li et al. reported a new type of electrocatalyst in which Pt–Pd nanoshells with a sub-nanometer thickness were coated on nano-porous Au (denoted as NPG–Pd–Pt).33 It was found that the half-wave potential of the NPG–Pd–Pt catalyst showed a positive shift of about 46 mV compared to that of commercial Pt/C in the ORR polarization curve (Fig. 8b), indicating its higher activity. As for cycling stability, the NPG–Pd–Pt catalyst showed an obvious increase of mass activity, i.e., 1.632 A mgPt−1 after 10000 cycles (Fig. 8c). Moreover, its performance after 100000 cycles remained almost the same as that after 30000 cycles, which indicates the excellent cycling stability. Delicate structural characterization revealed that the surface evolution of the NPG–Pd–Pt catalyst happened in the long-term cycling process and eventually a stable structure of the Pt–Pd–Au alloy was formed to achieve such a superior stability. Inspired by this work, core–shell NPs have also become a popular candidate for ORR electrocatalysts in the past few years.
In order to decrease the cost of ORR catalysts, researchers have also tried to combine other cheap transition metals (e.g., Ni, Cu, Co and Fe) with noble metals such as Au. For instance, Johnston et al. prepared bimetallic Au–Ni nanodendrites through one-pot electrochemical deposition and dealloying methods.178 The Au–Ni nanodendrites exhibited higher half-wave potential, excellent catalytic activity and good durability up to 5000 cycles in the ORR. It was proposed that the unique nanodendritic structure with the Au-rich surface and the electronic effect in Au–Ni nanodendrites are the main factors enhancing their ORR performance. In another study, Au–Cu alloy aerogels were also synthesized for the ORR.179 The presence of Cu would shift the d-band center of Au, which leads to more catalytically active sites and higher activity. Specifically, compared with commercial Pt/C, the SA and MA of Au–Cu alloy aerogels increased by 4.5 and 6.3 times, respectively. Apart from the aforementioned binary alloy catalysts, Wang et al. prepared a ternary alloy catalyst through incorporating Au into ordered intermetallic PdZn supported on carbon (denoted as Au–O–PdZn/C), and used it as a Pt-free ORR electrocatalyst.180 Compared to the control samples, the half-wave potential of Au–O–PdZn/C showed the most positive shift (50 mV), which only dropped by 6 mV after 30000 cycles. Meanwhile, the MA realized a high current density of 0.105 A mgAu+Pd−1 at 0.9 V, and only decreased by 9.5% after 30000 cycles (Fig. 8d and e). It was suggested that, Au atoms, which partially replace the original Pd or Zn atoms and are located on the surface or the inside of PdZn, should be responsible for enhancing the ORR activity and durability.
For improving the production of H2O2 in the ORR via the 2-electron pathway, numerous studies have been conducted by virtue of surface engineering of catalysts. By modulating the adsorption behaviors of O2 or *OOH on catalyst surfaces, a better performance towards H2O2 generation can be achieved. For example, Au is regarded as a promising electrocatalyst for H2O2 production because of its low over-potential and unique 2e-ORR on the (111) and (110) surfaces.181 However, the poor adsorption capability of O2 on Au limits its ORR activity.182 By rationally modulating the adsorption behavior of O2, Au can be transformed into an excellent 2e-ORR electrocatalyst by introducing other noble metal atoms such as Pd, Pt or Rh to its surface.183 The introduction of a moderate amount of other noble metals that can strongly interact with the O2 molecule is propitious to the adsorption of O2 while maintaining the end-on adsorption mode and inhibiting the O–O bonding cleavage owing to the inertness of Au, which will improve the 2e-ORR activity and maintain the selectivity as well. Considering the preferable adsorption ability of Ni and Pt to O2, Amal et al. introduced Ni and Pt to the surface of Au nanorods by epitaxial growth to generate Au–Ni core–shell nanorods and Au–Pt–Ni core-sandwich-shell nanorods, which exhibited higher activity and selectivity towards H2O2 production than pure Au nanorods.184 Apart from the O2 adsorption adjustment, the manipulation of the adsorption behavior of *OOH proves another route to enhance the 2e-ORR activity.185 As the key intermediate for H2O2 production, *OOH is supposed to be quickly released from the active site to undergo the following proton-coupled electron transfer. Therefore, materials that possess weak *OOH adsorption ability can also be employed to improve the H2O2 production. For instance, combining 4e-ORR metals such as Pt and Pd with other metals with a weak *OOH adsorption ability such as Hg is an efficient way to enhance the 2e-ORR performance.186
Up to now, many Au-based nanoalloys have been designed and shown comparable catalytic activity to Pt for the HER due to the synergistic effects between different metals. Table 4 shows the catalytic performance of different Au-based nanoalloys for the HER. For instance, Sun et al. prepared NiAu/Au core/shell NPs that exhibited Pt-like activity for the HER.36 Specifically, it was found that the HER activity of the Ni43Au57 nanoalloy can be greatly enhanced after continuous potential cycling from 0.6 to 1.0 V. After potential cycling, the surface Ni in Ni43Au57 NPs was leached away, leading to formation of NiAu/Au core/shell NPs. By using 0.5 M H2SO4 solution as the electrolyte, Ni43Au57 NPs showed a relatively low onset potential of about −70 mV (Fig. 9a). After over 5000 potential cycles, the onset potential of Ni43Au57 NPs was greatly decreased due to the formation of NiAu/Au core/shell NPs (Fig. 9b). Furthermore, after 10000 potential sweeps between −0.3 and 0.9 V, the NiAu/Au core/shell NPs exhibited no obvious decrease in HER activity, which is much superior to that of the commercial Pt/C catalyst (Fig. 9c). Considering the recombination of two adsorbed H atoms as the rate-determining step (based on the calculated Tafel slope), this unique NiAu/Au core/shell structure has the Pt-like activity and is even more stable than the Pt catalyst. Theoretical calculations indicated that the leaching of surface Ni decreases the coordination number of surface Au atoms, which could significantly increase the HER activity. In another study, Wang et al. synthesized multiply-twinned Au–Ag nanocrystals supported on reduced graphene oxide, which exhibited excellent HER activities in various pH environments, including acidic, neutral and basic electrolytes.189
Catalysts | Electrolyte | E onset (mVRHE) | η 10 (mV) | Tafel slope (mV s−1) | Stability | Ref. |
---|---|---|---|---|---|---|
a E onset, onset potential; η10, overpotential at 10 mA cm−2; CSSSD, core–shell star-shaped decahedra; η, overpotential; rGO, reduced graphene oxide. | ||||||
Au75Rh25 CSSSD | 0.5 M H2SO4 | — | 64.1 | 33.8 | η increases during 500 cycles (0–1.1 VRHE) | 232 |
S-doped AuPbPt NWNs | 0.5 M H2SO4 | −2 | 12 | 17.7 | No obvious change of η10 after 5000 cycles (0–1.35 VRHE) | 220 |
Au@Zn–Fe–C | 0.5 M H2SO4 | −80 | — | 130 | No obvious change of current density after 12 h at −0.15 VRHE | 233 |
Au–Pd NPs/rGO | 0.5 M H2SO4 | ∼ −0.8 | — | 29 | Current density increases over 24 h at −0.7 VSCE | 234 |
Au–Ag icosahedra/rGO | 0.5 M H2SO4 | ∼ −10 | — | 39 | Potential (at 25 mA cm–2) increases by 12 mV after 10000 cycles (−0.2–1.0 VRHE) | 189 |
C–Ni43Au57 NPs | 0.5 M H2SO4 | ∼ −70 | — | 43 | E onset decreases to ∼ −7 mV after 10000 cycles (0.6–1.0 VRHE) | 36 |
RuAu-0.2 SAA | 1 M KOH | — | 24 | 37 | η increases by ∼2 mV after 1000 cycles (−0.26–0.14 VRHE) | 135 |
Fig. 9 The electrocatalytic performance of Au-based nanoalloys towards the HER. (a–c) Linear sweep voltammetry (LSV) polarization curves of (a) different catalysts such as Ni NPs, Au NPs, NixAuy NPs and commercial Pt, (b) Ni43Au57 NPs before and after different numbers of potential cycles, and (c) NiAu/Au core/shell NPs and commercial Pt before and after 10000 potential cycles in 0.5 M H2SO4 solution. Reproduced with permission.36 Copyright 2015, American Chemical Society. (d) LSV polarization curves of Au, Ru, Pt/C and Ru/Au-0.2 at the scanning rate of 5 mV s−1. (e) TOF of Ru, Pt/C and Ru/Au-0.2 at the overpotential of 50 mV. (f) Chronoamperometric plot (left axis) and FE (right axis) of the RuAu SAA. Reproduced with permission.135 Copyright 2019, Wiley-VCH. |
The particle size is also closely related to the HER activity. The reduction of the catalyst size can significantly increase the specific surface area and expose more active sites, thereby increasing the catalytic activity. In particular, single-atom catalysts (SACs), isolated atoms that are well dispersed on supports, exhibit outstanding catalytic activity, selectivity and stability. As a typical study, Chen et al. synthesized Ru–Au bimetallic SAAs as HER catalysts and tested in 1 M KOH solution.135 The Ru–Au SAA exhibited a quite low overpotential of 24 mV at 10 mA cm−2, which is much lower compared to those of the Au SAC, Ru SAC and commercial Pt/C (Fig. 9d). The calculated turnover frequency (TOF) of the Ru–Au SAA at −50 mV reached up to 2.18 s−1, which is 3.0 and 3.6 times those of Pt/C and the Ru SAA, respectively (Fig. 9e). After the long-term stability test for 10 h, the Ru–Au SAA only showed a small decrease of 8% in current density, which further proved the excellent electrochemical stability of the Ru–Au SAA (Fig. 9f). In addition, during the stability test, the Faradaic yield remained 100%, indicating that the observed current was entirely attributed to the HER. Theoretical and experimental investigations suggested that the superior HER performance of the Ru–Au SAA is attributed to the relay catalysis, in which the Ru atom captures and splits water molecules and subsequently the Au atom adsorbs protons and facilitates the H2 production.
Catalysts | Electrolyte | Overpotential (mV) | Tafel slope (mV s−1) | Stability | Ref. |
---|---|---|---|---|---|
Au0.89Fe0.11 NPs | 1 M KOH | ∼800 (at 10 mA cm−2) | 46 | 63% loss of current after 1000 cycles (0.57 to 1.87 VRHE) | 141 |
Au–Ru branched NPs | 0.1 M HClO4 | 220 (at 10 mA cm−2) | 62 | 67% loss of activity after 1000 cycles at 1.46 VRHE | 235 |
NiFe LDH@Au/Ni foam | 30 wt% KOH | 221 (at 50 mA cm−2) | 60.8 | Overpotential increases by 15 mV after 5000 cycles | 236 |
AuCuCo NPs | 0.1 M KOH | 596 (at 10 mA cm−2) | 65.0 | <20% loss of relative current after 4 h at 0.765 VRHE | 192 |
Combining Au with some highly active metal components is an important way to prepare high-performance OER catalysts. As a representative study, Lu et al. synthesized PtAu NPs as the cathode electrocatalyst for rechargeable Li–O2 batteries, in which the OER kinetics can be significantly enhanced and the charge voltage could be effectively reduced to 3.4 V in 0.5 M H2SO4.191 Recently, to further decrease the cost of preparing efficient OER catalysts, great efforts have been devoted to introducing earth-abundant metal elements in Au-based nanoalloys. For example, Yang et al. synthesized self-supported AuCuCo nanostructures and evaluated their OER activity in 0.1 M KOH solution.192 Owing to the special 3D structure, electronic structure variation of Au via alloying and the presence of abundant twin structures, the OER activity of AuCuCo nanostructures was comparable with that of commercial Pt/C and IrO2/C catalysts. Moreover, AuCuCo nanostructures showed better catalytic durability than both Pt/C and IrO2/C.
Besides Cu and Co, alloying other early transition metals such as Fe with Au can also increase their catalytic activity towards the OER. For instance, Alessandri et al. prepared Au–Fe nanoalloys with a large content of Fe (up to 11 at%) using LALT and tested in 1 M KOH.141 The cyclic voltammetry (CV) results showed that Au0.89Fe0.11 NPs exhibited the highest OER activity (Fig. 10a), which was much better than that of Au and FeOx NPs. Notably, at a current density of 10 mA cm−2, Au0.89Fe0.11 NPs showed the lowest overpotential of about 0.8 V, in comparison with Au NPs, FeOx NPs and their physical mixture (Fig. 10b). Meanwhile, the OER onset potential of Au0.89Fe0.11 NPs was also remarkably shifted to a lower potential compared to those of Au NPs, FeOx NPs and their physical mixture (Fig. 10c). Furthermore, at a potential of 1.82 V (vs. RHE), the Au0.89Fe0.11 nanoalloy exhibited a current density of ∼4 mA cm−2, which was around 23, 13 and 30 times larger than those of Au NPs, FeOx NPs and their physical mixture, respectively (Fig. 10d). It was suggested that the enhanced OER performance of Au0.89Fe0.11 NPs could be attributed to the strong chemical and electronic interactions between Au and Fe atoms.
Fig. 10 The electrocatalytic performance of Au-based nanoalloys towards the OER. (a) CV curves of AuxFey nanoalloys, Au NPs, FeOx NPs, and the mixture of Au and FeOx NPs in 1 M KOH. (b) Comparison of the overpotentials needed to obtain a current density of 10 mA cm−2 for different nanocatalysts. (c) Zoom of CV curves within the potential range of 1.40–1.87 V (vs. RHE). (d) Comparison of the current densities obtained at a potential of 1.82 V (vs. RHE) for different nanocatalysts. ITO is short for indium tin oxide. Reproduced with permission.141 Copyright 2017, Wiley-VCH. |
The combination of Au with other noble metals is an efficient strategy to prepare high-performance electrocatalysts for the oxidation of small organic molecules. Recently, Wang et al. synthesized PdAu/Pt trimetallic NPs supported on carbon nanotubes (denoted as CNTs-PdAu/Pt) and evaluated their catalytic performance towards the MOR in alkaline electrolyte.201 It was found that within 500 CV cycles, the CNTs-PdAu/Pt catalyst showed the highest mass activity (refer to Pt) and stability (the retention rate is 76%) in comparison with CNTs-Pd/Pt, CNTs-Au/Pt and commercial Pt/C catalysts. The enhanced MOR performance of the CNTs-PdAu/Pt catalyst was attributed to the synergistic effects between Au, Pd and Pt. Specifically, alloying Pd and Au with Pt generated numerous small Pt ensembles that were catalytically active for the MOR. Alternatively, the addition of Au could stabilize Pt from surface oxidation. Furthermore, introducing Pd might induce remarkable electron transfer from Pd to Pt, which could lead to the downshift of the Pt d-band center and thus decrease the interaction between Pt and poisoning species such as CO.
Besides noble metals, alloying Au with other early transition metals could be another effective and economic way to improve the electrocatalytic performance towards small organic molecule oxidation. As a typical study, Nugraha et al. prepared mesoporous Au41Cu46Ni13 ternary alloy films with different compositions towards the MOR.120 It was observed that the mesoporous ternary alloy film with a composition of Au41Cu46Ni13 demonstrated superior catalytic activity (current density: 3.8 mA cm−2; mass activity: 1.7 A mg−1) and excellent stability (no obvious changes in both catalytic activity and the structure were observed after working for 1200 s at 0.65 V (vs. Ag/AgCl)) as well.
Au is particularly active in catalyzing CO oxidation.22 But in order to further increase the catalytic stability and/or activity of Au, binary or ternary Au-based nanoalloys have been extensively investigated. For example, Han et al. synthesized a series of binary Pd–Au nanoalloys that showed excellent catalytic performance towards CO oxidation.45 When the atomic ratio of Pd:Au was 4:1, optimum catalytic activity was obtained among all Pd–Au nanoalloys (Fig. 11a). The activation energy of Pd4Au1 is 65.6 kJ mol−1, which is much smaller than that of the other Pd–Au nanoalloys (Fig. 11b). Significantly, the cycling stability of Pd4Au1 is significantly better compared to that of pure Au (Fig. 11c). Specifically, in an ideal exhaust gas at 353 K for 10 h, the pure Au catalyst lost 50% of its catalytic performance while only a 5% loss was found for the Pd4Au1 nanoalloy. Experimental observations suggested that the superior catalytic performance of Pd–Au nanoalloys could arise from the presence of abundant surface defects (e.g., metal vacancies) as well as alloying-induced electronic structure modifications of Au and Pd atoms.
Fig. 11 The electrocatalytic performance of Au-based nanoalloys towards the CO oxidation reaction. (a and b) Temperature-dependent CO oxidation (a) and Arrhenius plots of the reaction rate (b) of Au, Pd and PdxAuy alloys. (c) Time-dependent CO oxidation on Au/SiO2 and Pd4Au1/SiO2 in the ideal exhaust gas (filled symbol) or the simulated exhaust gas (hollow symbol). Reproduced with permission.45 Copyright 2010, American Chemical Society. (d) Temperature-dependent CO oxidation on LDHs, Cu/LDHs, Au/LDHs and AuxCuy/LDHs. (e) Arrhenius plots of LDHs, Au/LDHs and AuxCuy/LDHs. (f) CO conversion versus time for LDHs, Au/LDHs and Au2M1/LDHs (M = Cu, Ni, Pt). Reproduced with permission.204 Copyright 2020, Elsevier. |
Catalyst supports can also greatly affect the catalytic CO oxidation performance of Au-based nanoalloys through the well-known metal–support interaction.202 Recently, researchers have tried to load Au-based nanoalloys on different supports to achieve highly efficient and stable catalysts for CO oxidation. For instance, Li et al. used TiO2 as the support for Pt–Au binary nanoalloys to improve the catalytic CO oxidation performance.203 Specifically, TiO2 can facilitate the dispersion and restrict the growth/aggregation of Pt–Au NPs, which allows sufficient and stable active sites for CO oxidation. In another study, Xia et al. employed layered double hydroxides (LDHs) as the support for a variety of binary Au-M (M = Ni, Cu, Pt) nanoalloys.204 It was found that the Au2Cu1 nanoalloy supported on LDHs (denoted as Au2Cu1/LDHs) showed the highest catalytic activity and lowest activation energy among various Au–M/LDH nanoalloys, Au/LDHs and LDHs (Fig. 11d and e). Moreover, after 48 h of continuous catalytic reaction, the CO conversion rate of all catalysts decreased slightly, and Au2Cu1/LDHs remained to be the optimum catalyst (Fig. 11f). In addition, Au2Cu1/LDHs also demonstrated a very good recyclability for CO oxidation, showing no obvious deactivation after three cycles (3 h per cycle). This work suggested that LDHs are a kind of stable, highly active and low-cost supporting material for Au-based nanoalloys towards the CO oxidation reaction.
Although glycerol (GLY) is a by-product during the industrial production of biomass fuels, various value-added chemicals can be generated through the selective aerobic oxidation of GLY. Thus, how to facilitate GLY conversion and improve the selectivity to specific chemicals rather than the overoxidation products (e.g., CO2) are critically important. In this regard, Ebitani et al. synthesized Pt60Au40 alloy NPs supported on hydrotalcites (denoted as Pt60Au40–starch/HT) and explored the catalytic performance of GLY oxidation in an alkali-free aqueous solution.205 The major product of GLY oxidation is glyceric acid (GA) with a high selectivity of 87% at the reaction time of 1 h, and the GA selectivity can be maintained over 70% after reacting for 10 h (Fig. 12a). During the recycling measurement, although the catalytic activity of Pt60Au40–starch/HT slightly decreased, the high selectivity towards GA production was maintained (Fig. 12b). Experimental results indicated that the electronic and geometric modifications of Pt active sites by neighboring Au atoms and surface starch ligand result in the improvement of both activity and selectivity.
Fig. 12 The catalytic performance of Au-based nanoalloys towards typical heterogeneous catalytic reactions in chemical engineering. (a) GLY conversion, product yield and GA selectivity in GLY oxidation catalysed by Pt60Au40–starch/HT. (b) Recycling of the Pt60Au–starch/HT catalyst towards GLY oxidation. Reproduced with permission.205 Copyright 2013, American Chemical Society. (c) TOF plots for the catalytic cyclohexene hydrogenation on SiO2-supported Au, Pd and PdxAu100−x NPs. (d and e) Comparison of the catalytic hydrogenation activity of PdxAu100−x NPs that are (d) obtained with two different synthetic methods or (e) supported on different substrates. Reproduced with permission.206 Copyright 2016, American Chemical Society. |
Recently, vapor-phase catalytic hydrogenation of cyclohexene by PVP-capped PdxAu100−x NPs with various compositions was studied by Humphrey et al.206 It was found that Pd59Au41 NPs showed the highest catalytic cyclohexene hydrogenation activity among various PdxAu100−x NPs, Pd NPs and Au NPs (Fig. 12c). The steady-state TOF was usually reached after 4–5 h. Interestingly, the preparation method of PdxAu100−x NPs can also greatly affect their catalytic activity towards cyclohexene hydrogenation (Fig. 12d). Specifically, PdxAu100−x NPs obtained under microwave irradiation (μwI) tend to possess much higher catalytic hydrogenation activity than those obtained with conventional heating (CvH). Moreover, the steady-state TOF of PdxAu100−x (i.e., close to Pd60Au40) catalysts supported on different substrates showed no obvious differences (Fig. 12e), indicating that the catalyst substrate is not the key factor here. Theoretical calculations suggested that long range electronic effects and local ensemble effects in the PdxAu100−x alloy could contribute to the enhanced catalytic hydrogenation activity.
At present, it is widely accepted that the key factors affecting the catalytic performances of Au-based nanoalloys include composition, size, shape, crystal phase, support and so on. Therefore, the ultimate goal is to achieve precise control of the aforementioned factors through facile regulation methods and reveal the general structure/component-performance relationships, which will direct the synthesis of ideal Au-based nanoalloys with favorable features for a range of catalytic reactions. Although the studies on Au-based nanoalloys have obtained notable progress, there are still some challenges needed to be overcome in this research direction. In general, current investigations on Au-based nanoalloys are still in the initial stage, mainly focusing on their composition design and morphology control. In the future, more attention should be paid to how to precisely control the arrangement of different metal elements in alloys at the atomic scale, and then synthesize catalysts with desirable atomic and electronic structures. Considering that recent investigations have proven the crystal phase-dependent catalytic activity and selectivity in metal and alloy-based nanomaterials, synthesis of Au-based nanoalloys with different, unusual and even novel crystal phases is of great significance for future studies.65,88,207–211 Crystal phase control could be a promising strategy for further improving the catalytic performance of Au-based nanoalloys.
Furthermore, more advanced synthetic technologies are expected to be developed for Au-based nanoalloys with new microstructures and optimum compositions. At present, the effective synthetic methods for Au-based nanoalloys mainly concentrated on the co-reduction of metal precursors, which shows the advantages of low cost and high yield and the disadvantages of limited metal precursors that can be simultaneously reduced. Comparatively, few other effective synthetic methods are widely utilized to produce Au-based nanoalloys. Despite several unconventional strategies, such as polymer nanoreactor mediated synthesis and the cast cum cryo-milling process, have proven to be promising, their low yield cannot meet the requirements of large-scale industrial production. Therefore, it is quite important and urgent to promote the current or even develop novel synthetic strategies to precisely modulate the microstructure and composition of Au-based nanoalloys while enabling large-scale productivity to satisfy the large quantity demand in a wide range of practical applications including catalysis.
Footnote |
† These authors contributed equally to this work. |
This journal is © The Royal Society of Chemistry 2021 |