Cu-based bimetallic catalysts for electrochemical CO2 reduction: before and beyond the tandem effect

Dimiao Luo a, Weidong Dai a, Keying Wu a, Siyuan Liu a, Chiyao Tang b, Yanjuan Sun b, Fan Dong a and Chang Long *a
aResearch Center for Carbon-Neutral Environmental & Energy Technology, Institute of Fundamental and Frontier Sciences, University of Electronic Science and Technology of China, Chengdu 611731, Sichuan, P. R. China. E-mail: longch@uestc.edu.cn
bSchool of Resources and Environment, University of Electronic Science and Technology of China, Chengdu 611731, Sichuan, P. R. China

Received 15th November 2024 , Accepted 3rd March 2025

First published on 10th March 2025


Abstract

Electrochemical CO2 reduction reaction (CO2RR) is a promising approach for carbon reduction and the production of high-value chemicals. Among the various catalysts, Cu-based bimetallic catalysts have recently attracted significant attention due to their superior catalytic activity, often outperforming pure Cu counterparts, owing to the discovery of the tandem effect. This review provides an in-depth discussion of the development of Cu-based bimetallic catalysts for CO2RR over the past decades, with the discovery, understanding, and evolution of the tandem effect serving as the central thematic thread. Important milestone works have been reviewed and organized in a roughly historical manner to highlight the development of cutting-edge understanding and the remaining challenges in this field. We believe this review will help the research community clearly track the progress from the original to the latest findings and identify key insights for Cu-based bimetallic catalysts for CO2RR.


image file: d4nr04790g-p1.tif

Chang Long

Chang Long is currently an associate professor at the Institute of Fundamental and Frontier Sciences, University of Electronic Science and Technology of China (UESTC). He earned his BS (2015) and PhD (2021) in materials chemistry from Harbin Institute of Technology under the guidance of Prof. Zhiyong Tang and Prof. Shaoqin Liu. During his PhD, he was a joint student at the National Center for Nanoscience and Technology, Beijing. From 2021 to 2023, he conducted postdoctoral research with Prof. Chunhua Cui and Prof. Fan Dong at UESTC. His research focuses on nanomaterial interfaces and electrochemical applications.


1. Introduction

Excessive anthropogenic emissions of carbon dioxide (CO2) have severely disrupted the Earth's intrinsic carbon cycle, exacerbating global climate change and posing a significant threat to the sustainability of ecosystems and human society.1–4 Fortunately, electrochemical CO2 reduction (CO2RR) shows great promise in addressing this problem by leveraging renewable electricity to convert CO2 into chemical feedstocks, such as ethylene, ethanol, and n-propanol.5,6 Moreover, recent techno-economic analyses highlighted the foreseeable economic margins, leading to further increased research attention in CO2RR.7–13

Over the past decades, significant progress has been made in the selective synthesis of mono-carbon (C1) products in CO2RR, such as CO and formic acid.14–18 However, for multi-carbon (C2+) products, the performance in terms of current density, long-term stability, and especially product-specific selectivity still shows a considerable gap between the theoretical potential and numerous empirical outcomes.19–22 Cu-based materials remain the only realistic catalysts for efficient C2+ production.23–25 Furthermore, Cu-based bimetallic catalysts have shown outstanding promise for the practical application of electrosynthesis of C2+ products in CO2RR since Kenis et al.26 and Jaramillo et al.27 independently identified phase-dependent selective product formation and the now well-known tandem effect, respectively. However, advancing this field towards industrial applications remains a significant challenge, as it is still in its early stages, with much progress yet to be made. The application of the tandem effect in Cu-based bimetallic catalysts for CO2RR not only refines the adsorption and reaction pathways of the crucial intermediate CO, thereby enhancing its efficiency,28–30 but also facilitates C–C coupling, increasing the probability of long-chain hydrocarbon formation and significantly boosting the selectivity for C2+ products.31–33 A comprehensive understanding of the historical evolution of the tandem effect will offer critical perspectives for elucidating its structure–activity relationships at the catalyst surface/interface in catalytic processes.

In this review, we focus on Cu-based bimetallic catalysts for CO2RR. Unlike other closely related reviews that focus on classifying the types, structures, and synthesis strategies of tandem catalysts, designing or predicting active structures based on the tandem effect, or summarizing prior research,34–41 this review examines the tandem effect in Cu-based bimetallic catalysts. It identifies the most representative historical milestones in CO2RR involving Cu-based bimetallic catalysts, outlines the underlying development patterns over the past decades, and finally highlights the foreseeable challenges in this field. In addition, numerous reviews have already provided an extensive discussion on the industrial and economic aspects of Cu-based catalysts for CO2RR.42–46 Therefore, our review focuses on the understanding and development of the catalytic process–surface/interface structure–activity relationships of Cu-based tandem catalysts for CO2RR. We believe that this review can provide the research community with a clear and in-depth roadmap regarding Cu-based bimetallic catalysts for CO2RR.

2. Early research in CO2RR: metal-dependent product selectivity and crucial intermediate

2.1 The key classification of metal electrodes for CO2RR

In the early research on CO2RR, various metal electrodes were screened for their catalytic performance, providing numerous building block clues for the research community.47–49 Importantly, in 1986, Hori firstly comprehensively summarized the previous trial-and-error. Innovatively, at that time, regardless of the poor understanding, he explicitly highlighted the element-dependent CO2RR product selectivity and classified the metal electrodes regarding their product selectivity.50,51 Specifically, his summary suggested that most common metal electrodes can be roughly classified into metals such as Au, Ag, and Zn that produce CO, metals such as Sn, In, and Pb that produce formic acid (or formate), metals such as Pt, Ti, Fe, and Ni that produce H2, and the only metal, Cu, that generates both C1 and C2+ products (Table 1). This classification not only establishes Cu as the only monometallic catalyst capable of facilitating the formation of both C1 and C2+ products, thereby driving further exploration into C2+ production mechanisms, but also serves as a fundamental guideline for the strategic design of Cu-based tandem catalysts.
Table 1 CO2 reduction products corresponding to different metal electrodes. Reprinted with permission from Hori et al.50 Copyright 1994, Elsevier
Electrode Potential vs. NHE Current density (mA cm−2) Faradaic efficiency (%)
CH4 C2H4 EtOH PrOH CO HCOO H2 Total
Electrolyte: 0.1 M KHCO3; temperature: 18.5 °C ± 0.5 °C.a The total value contains C3H5OH (1.4%), CH3CHO (1.1%) and C2H5CHO (2.3%) in addition to the tabulated substances.b The total value contains C2H6 (0.2%).
Cu −1.44 5.0 33.3 25.5 5.7 3.0 1.3 9.4 20.5 103.5a
 
Au −1.14 5.0 0.0 0.0 0.0 0.0 87.1 0.7 10.2 98.0
Ag −1.37 5.0 0.0 0.0 0.0 0.0 81.5 0.8 12.4 94.6
Zn −1.54 5.0 0.0 0.0 0.0 0.0 79.4 6.1 9.9 95.4
Pd −1.20 5.0 2.9 0.0 0.0 0.0 28.3 2.8 26.2 60.2
Ga −1.24 5.0 0.0 0.0 0.0 0.0 23.2 0.0 79.0 102.0
 
Pb −1.63 5.0 0.0 0.0 0.0 0.0 0.0 97.4 5.0 102.4
Hg −1.51 0.5 0.0 0.0 0.0 0.0 0.0 99.5 0.0 99.5
In −1.55 5.0 0.0 0.0 0.0 0.0 2.1 94.9 3.3 100.3
Sn −1.48 5.0 0.0 0.0 0.0 0.0 7.1 88.4 4.6 100.1
Cd −1.63 5.0 1.3 0.0 0.0 0.0 13.9 78.4 9.4 103.0
Tl −1.60 5.0 0.0 0.0 0.0 0.0 0.0 95.1 6.2 101.3
 
Ni −1.48 5.0 1.8 0.1 0.0 0.0 0.0 1.4 88.9 92.4b
Fe −0.91 5.0 0.0 0.0 0.0 0.0 0.0 0.0 94.8 94.8
Pt −1.07 5.0 0.0 0.0 0.0 0.0 0.0 0.1 95.7 95.8
Ti −1.60 5.0 0.0 0.0 0.0 0.0 tr. 0.0 99.7 99.7


2.2 The CO intermediate for CO2RR

To determine the fundamentals of the metal-dependent CO2RR selectivity, Hori et al.,52 in 1989, further examined the correlation between the potential and the selectivity for CO2RR products on Cu electrodes. As shown in Fig. 1a, the faradaic efficiencies (FEs) of CO and formate were disclosed to have an inverse correlation with that of CH4 and C2H4, indicating that both CO and formate may be the crucial intermediates for the further reduced products. Evidently, CO was shown be reduced to CH4 and C2H4 in other early studies.53,54 However, when Cook et al.55 directly and merely introduced formate into the electrolyte, they found that formate could not be reduced into any products such as CH4, C2H4, and other multi-carbons. These experiments collectively indicate that CO should be the intermediate, instead of formate, which is further derived into other reduced products. Soon afterwards, Hori et al.56 conclusively confirmed this deduction through in situ infrared spectroscopy during CO2RR on a Cu electrode. As shown in Fig. 1b, a characteristic signal of CO adsorption emerged at 1900–2100 cm−1 when the potential reached −0.7 V vs. reversible hydrogen electrode (RHE). When CO2 was replaced with CO, the in situ infrared spectra reproduced the CO binding signals observed in CO2RR (Fig. 1c). Furthermore, metal electrodes such as Pt were then confirmed to have stronger CO binding strength, causing surface poisoning to occur and H2 becomes the major product.57 Reasonably, metal electrodes producing CO or formate were deduced to have a lower CO binding strength according to experimental results.50,58,59 Since then, different metals have also been screened for their CO binding property, leading to the consensus that the CO binding strength on the metal surface is significant in terms of the CO2RR product selectivity. Subsequently, an in-depth theoretical understanding was provided by Bagger et al.60 As shown in Fig. 1d, the binding energies of CO* and H* (where * represents the adsorbed intermediates) were introduced as descriptors to explain the metal-dependent CO2RR selectivity. This calculation aligns well with the previous deduction from experiments and conveys a vital message that *CO and *H bind neither too strong nor too weak on and only on the Cu surface, leading to the probability of C–C coupling51 for the generation of C2+ products on Cu. These early studies on the metal-dependent CO2RR selectivity and the identification of *CO as the key intermediate for C2+ products have laid the foundation for the recent development of Cu-based materials in CO2RR. The pivotal role of *CO as the key intermediate in CO2 reduction on the surface of Cu has been rigorously validated through both experimental evidence and theoretical calculations. This compelling confirmation has further stimulated extensive research interest, driving deeper exploration into this field.
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Fig. 1 (a) FE variations of CO2 reduction products in 0.1 M KHCO3 at 19 °C. (b) In situ IR spectra of adsorbed species on Cu during CO electroreduction at different potentials in 0.2 M KHCO3. (c) In situ IR spectra of adsorbed species on Cu during CO2 electroreduction at different potentials in 0.1 M KHCO3. (d) *CO and *H binding energies set Cu apart from other metals. (a) Reprinted with permission from Hori et al.52 Copyright 1989, the Royal Society of Chemistry. (b and c) Reprinted with permission from Hori et al.56 Copyright 1995, Elsevier. (d) Reprinted with permission from Bagger et al.60 Copyright 2017, John Wiley and Sons.

3. Bimetallic Cu-based catalysts: the discovery of phase-dependent pathway and tandem effect

3.1 Breaking the scaling relationship on monometallic Cu-based materials by alloying

As discussed above, Cu-based materials are the only and most promising catalysts for CO2RR to C2+ products, and thus significant research efforts have been devoted to Cu-based materials in this field.61–64 However, in the early stage, the performance of monometallic Cu was rather poor, largely due to the linear relationship between different adsorbed intermediates or the so-called scaling relationship (Fig. 2a).65 This suggests that if a catalyst exhibits stronger binding strength to one intermediate, the binding strength to other intermediates is correspondingly enhanced, making it difficult to simultaneously achieve both high selectivity and high activity.66,67 Thus, to break the scaling relationship and promote the selectivity as well as the activity, Nørskov et al.65 theoretically proposed alloying Cu with a secondary metal to tune the binding strength or configuration of adsorbed intermediates on the catalyst surface. Thereafter, Cu-based bimetallic catalysts have become a focal point of research in this field, with researchers actively exploring their potential in enhancing the efficiency and selectivity of CO2RR.68–70 As expected, many bimetallic Cu-based catalysts showed a promoted performance compared to their monometallic counterparts. For instance, in 2014, Takanabe et al.71 prepared a Cu–In alloy by in situ reducing Cu2O in an InSO4-containing electrolyte (Fig. 2b). The X-ray diffraction (XRD) patterns and elemental mapping of the Cu–In bimetallic alloy confirmed the formation of Cu11In9 featuring an In-rich surface and Cu-rich core. Moreover, Cu11In9 outperformed its oxide-derived Cu (OD-Cu) counterpart in terms of activity and selective CO production. Specifically, it was observed that OD-Cu primarily produces H2 at −0.3 V vs. RHE, and as the potential becomes more negative, the products gradually shift to CO and HCOOH (Fig. 2c). In contrast, the Cu11In9 exhibits the highly efficient conversion of CO2 to CO, while suppressing H2 formation (Fig. 2d). Furthermore, Han et al.72 developed a series of compositionally tunable PdxCuy bimetallic aerogels using a template-free self-assembly approach. These aerogels, characterized by their three-dimensional porous architecture and high specific surface area, exhibited an exceptional electrocatalytic performance. Remarkably, they achieved an FE as high as 80.0% and a current density of 31.8 mA cm−2 for the electrochemical reduction of CO2 to methanol, together with excellent stability under extended electrolysis conditions. Additionally, Huang et al.73 developed a CuSn bimetallic catalyst with Cu and Sn uniformly distributed on its surface (Fig. 2e and f), which showed a superior selective formate production to monometallic Cu nanoparticles (Fig. 2g and h). Notably, numerous experimental reports also suggest that in bimetallic Cu-based catalysts, the secondary metal element largely impacts the final major product. Results show that when secondary metals are present in CO or formate producing metals, such as In, Sn, and Pd, bimetallic Cu-based materials predominantly produce CO74,75 or formate,76,77 while C2+ products are frequently generated on bimetallic CuAu, CuAg, and CuZn catalysts.78–80 Typically, Ren et al.80 developed a series of bimetallic CuZn catalysts (Cu10Zn, Cu4Zn, and Cu2Zn) (Fig. 2i and j), finding that the doping level of Zn could effectively steer ethanol production, and the best Cu4Zn catalyst exhibited a roughly 2-fold improvement in ethanol FE than its Cu counterpart (Fig. 2k and l). Additionally, Cao et al.81 fabricated an Ag–Cu2O interfacial catalyst through a one-pot seed-mediated approach, which demonstrated an exceptional performance in the electrochemical reduction of CO2 to C2H4 under neutral conditions. This catalyst achieved an impressive FE of 66.0% and a partial current density reaching 429.1 mA cm−2. Insights from in situ Raman spectroscopy and theoretical calculations revealed that the Ag/Cu2O interface effectively increases the *CO coverage and accelerates C–C coupling, thereby enhancing the generation of C2H4.
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Fig. 2 (a) Linear relationships between different reaction intermediates (scaling relationships). (b1 and b2) EDS elemental mapping and XRD spectrum of Cu–In alloy, respectively. (c and d) FE of OD-Cu and Cu–In alloy for different products at various potentials, respectively. (e) Schematic of Cu–Sn alloy. (f1–f4) HAADF-STEM image and EDS elemental mapping of Cu–Sn alloy. Scale bar: 5 nm. (g and h) FE of different products for Cu and Cu1Sn1 alloy as a function of potential, respectively, with error bars representing the standard deviation from three independent measurements. (i) XRD patterns of Cu, Cu10Zn, Cu4Zn, and Cu2Zn bimetallic catalysts. (j1 and j2) SEM images of Cu and the optimal catalyst Cu4Zn, respectively. (k and l) FE of different products for Cu and Cu4Zn alloy as a function of potential, respectively. (a) Reprinted with permission from Nørskov et al.65 Copyright 2012, the American Chemical Society. (b and d) Reprinted with permission from Takanabe et al.71 Copyright 2014, John Wiley and Sons. (e–h) Reprinted with permission from Huang et al.73 Copyright 2021, the American Chemical Society. (i and l) Reprinted with permission from Ren et al.80 Copyright 2016, the American Chemical Society.

3.2 Phase-dependent CO2RR on bimetallic Cu-based catalysts and tandem effect

Regardless of the fact that bimetallic CuAu, CuAg, and CuZn catalysts can selectively convert CO2 into C2+ products, there was an interesting puzzle that bimetallic CuAu, CuAg, and CuZn catalysts do not always produce C2+ products.82–86 As a classic example, in 2014, Yang et al.87 prepared a group of homogeneous AuCu bimetallic nanoparticles with varying Au/Cu ratios, which exhibited tunable selectivity, but merely generated CO, formate and H2. Furthermore, Huang et al.88 employed a two-step synthesis method to prepare CuAg nanowires (CuAgNWs) featuring atomic-scale Cu–Ag interfaces. These nanowires demonstrated remarkable selectivity toward methane (CH4) in the electrochemical reduction of CO2, achieving an impressive maximum FE of 72%. In parallel, Lim et al.,89 through advanced density functional theory (DFT) calculations, highlighted the significant potential of the Cu3Zn alloy catalyst for efficiently converting CO2 into CH4. These cases have brought widespread attention to the question of how to selectively generate C2+ products over bimetallic Cu-based catalysts. A milestone work conducted by Kenis et al.26 directly addressed this puzzle by using CuPd catalysts with distinguished phases for the CO2RR. As shown in Fig. 3a–c, three types of CuPd catalysts, including phase-segregated, disordered solid solution, and atomically ordered phases, were prepared, respectively. Although their compositions are nearly identical, their phase differences caused selective C2+ production on phase-segregated CuPd nanoparticles, and dominant C1 production on atomic ordered CuPd nanoparticles, respectively. Although the disordered CuPd nanoparticles enabled the catalytic production of both C1 and C2+ with lower FEs than their other two counterparts (Fig. 3d). The phase-segregated CuPd intrinsically exhibited the properties of both monometallic Pd and Cu, and thus the CuPd nanoparticles did not significantly lower the d-band center, leading to the selective production of C2+. Soon after, Jaramillo et al.27 innovatively proposed the combination of metal producing CO and Cu to create a tandem effect. Specifically, an AuCu hybrid with phase-segregated state was utilized for the CO2RR (Fig. 3e). Owing to the presence of Au and Cu components, which can effectively convert CO2 to CO and CO to C2+, the AuCu hybrid electrode exhibited a large enhancement regarding the selective production of C2+ products compared to monometallic Cu (Fig. 3f and g). This tandem effect fundamentally takes advantages of Au nanoparticles for CO2 reduction to CO, generating a high local concentration of CO on the adjacent Cu surface, where the migrated CO can be further reduced into C2+ products such as alcohols on the Cu surface. This work paves the way for the application of bimetallic Cu-based catalysts for C2+ production in CO2RR, especially CuAu, CuAg, and CuZn, where the secondary metal characteristic is active for CO2-to-CO conversion. As a supplementary to this finding, in 2019, Strasser et al.90 extended the secondary metals to other components that can convert CO2 into CO, such as Ni–N–C, which we now usually classify as metal–nitrogen–carbon based (M–N–C) materials.91–94 The introduction of the tandem effect marks a groundbreaking advancement that has profoundly influenced the development of Cu-based bimetallic catalysts for CO2RR, elevating research on C2+ products to unprecedented levels. Following these pivotal discoveries, researchers began designing Cu-based bimetallic materials specifically to harness the advantages of the tandem effect, further advancing this field.95–99 For instance, Yang et al.95 prepared a CuAg tandem catalyst by physically mixing Cu and Ag nano-powders on a carbon paper substrate. Subsequently, this catalyst was employed in a gas diffusion flow cell for high-current CO2 electrolysis, resulting in a C2+ current density of 160 mA cm−2 on the Cu surface. Moreover, the C2+ production rate was four times higher than that of pure Cu. Moreover, Shen et al.100 employed an enhanced polyethylene glycol method combined with subsequent electrochemical reduction to fabricate Ag–Cu bimetallic surface alloys with adjustable surface chemical compositions, varying from Cu-rich to Ag-rich. These materials exhibited tunable product selectivity in the electrochemical reduction of CO2, presenting an innovative approach for developing catalysts with precisely controlled product outcomes. This breakthrough provides promising prospects for improving the efficiency of industrial CO2 conversion and utilization. Also, these remarkable results further underscore the industrial potential of the tandem effect.
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Fig. 3 (a and b) Schematic of Cu–Pd nanoalloys with ordered, disordered, and phase-separated structures, along with their corresponding XRD spectra. (c1–c3) EDS elemental mapping of three distinct Cu–Pd nanoalloys with ordered, disordered, and phase-separated structures, respectively, showing Cu (red) and Pd (green). (d) FEs of CO, CH4, C2H4, and C2H5OH under three distinct structural configurations. (e) Schematic of CO2RR over CuAu hybrid with a phase-separated state. (f) CO2 consumption and CO2 production rate as a function of applied potential. (g) Current efficiency and partial current density of alcohols in CO2 reduction products corresponding to Cu, Au, and CuAu hybrids. (a–d) Reprinted with permission from Kenis et al.26 Copyright 2017, the American Chemical Society. (f–g) Reprinted with permission from Jaramillo et al.27 Copyright 2018, Springer Nature.

4. Tandem effect is still not perfect

4.1 Reactor/cell design to address the problems of CO utilization and potential misalignment in tandem effect

The finding of the tandem effect based on phase segregation in bimetallic Cu-based catalysts has significantly propelled the advancements in this field. Nevertheless, this does not mean that the tandem effect is the ultimate solution of CO2RR. Usually, if we merely combine CO-producing metals/components (e.g., Ag, Au, and Zn or M–N–C) and Cu, the production of C2+ can be promoted to a great extent. However, the C2+ promotion in previous reports are not all satisfactory.101–104

As a matter of fact, two important issues have been encountered with the tandem effect. The first issue is CO utilization. Looking carefully at the scenario of CO2RR on bimetallic Cu-based catalysts, there is still an open question of can the CO generated on Au, for example, can be fully used for further reduction on Cu? Or will the CO generated initially flash through the cell before it can effectively bind on the Cu surface? The outcome probably is concerning, as evidenced by the CO production rate or partial current density of CO in previous bimetallic Cu-based systems.105–107 Thus, to address this concern, Wu et al.108 recently designed a segmented gas diffusion electrode (s-GDE) (Fig. 4a). In the fabrication of s-GDE, firstly uniform Cu catalyst layer (CL) segments were applied on the GDE, working as C2+ selective segments. Then, Ag CL segments were concentrated near the inlet, functioning as the CO selective segments. The area and positioning of the Ag CL segments were precisely controlled by a template. The CO-selective (Ag) CL segment near the inlet extended the retention time of CO in the subsequent C2+ selective (Cu) segments, thus enhancing the utilization of CO and final C2+ production (Fig. 4b). This tiny change brought about a significant difference.


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Fig. 4 (a) Schematic of the s-GDE preparation process, showing the geometries of six s-GDEs (from E1 to E6), where the Ag catalyst layer (CL) size is constant, while the Cu catalyst layer size varies. (b) Schematic of the reduction in C2+ mass activity and CO concentration. (c) Schematic of the two-step electrolysis process for converting CO2 into C2+ products using CO2 and H2O as reactants. (a and b) Reprinted with permission from Zhang et al.108 Copyright 2022, Springer Nature. (c) Reprinted with permission from Jiao et al.110 Copyright 2019, Springer Nature.

Besides the CO utilization issue, the other problem of tandem effect regarding C2+ promotion is the potential misalignment. Specifically, the optimal potential for CO2-to-CO conversion on the secondary component in most cases does not match well with the optimal potential for the CO-to-C2+ process on Cu. This issue can be partially addressed by rationally designing catalyst pairs (Cu and a secondary CO-producing component) that share a mutual optimal electrochemical window. For example, Liu et al.109 demonstrated this approach with their Ni single-atom-catalyst/Cu-R (R for reduction state) hybrid. However, this technique typically requires extensive trial-and-error. This circumstance makes it challenging to push the tandem effect to its ideal promotion limit. Therefore, in 2019, Jiao et al.110 proposed an unprecedented alternative solution by using a divided cell system, where the CO2-to-CO and CO-to-C2+ processes can be operated in two cells independently. Basically, the first cell can use CO-producing catalysts such as Ag, Au, Zn, and M–N–C catalysts, while CO is fed as a cascade in the second cell equipped with Cu catalysts (Fig. 4c). Our group111 even demonstrated that with this strategy, the not only the total C2+ production could be improved, the specific C2+ product (acetate in our case) could also be custom-tailored via facile selection of the Cu catalyst. Employing this divided cell system, the potential misalignment can be largely alleviated. Another bonus of this system should be the promising promotion of carbon efficiency and current density by custom-tailoring the electrolyte pH in each cell. This is because acidic and alkaline electrolytes have been well studied as the optimal condition for CO2 utilization and CO reduction, respectively.112–115 As previously discussed, the electrolyte is a crucial factor influencing the CO2RR performance. Thus, to explore this aspect, our group116 conducted experiments, which revealed that during the electrochemical CO2 reduction reaction, the Cuδ+ species on the surface of OD-Cu undergo dynamic reduction and reoxidation in KHCO3 electrolyte due to the presence of hydroxyl radicals (˙OH). Based on these findings, we proposed the “seesaw effect” to elucidate the dynamic equilibrium of the Cuδ+ chemical states and concentrations, further underscoring the pivotal role of electrolyte composition in governing the CO2RR performance. Leveraging the tandem effect to optimize the reactor/cell design not only offers significant advantages in enhancing the selectivity and catalytic activity for C2+ products but also presents new opportunities for exploring its industrial feasibility. By precisely regulating the reaction microenvironment, this strategy holds great promise for overcoming existing technological bottlenecks, further improving the energy conversion efficiency and accelerating the industrialization of CO2RR, ultimately enabling large-scale and stable production.

4.2 Pushing the understanding limit beyond the tandem effect regarding detailed product

According to the discussion above, it is well recognized that the total C2+ production benefits from the tandem effect. However, the tandem effect theory fails when we investigated in detail the single C2+ product. In many works employing bimetallic Cu-based catalysts having close or even identical components, their reported C2+ products in CO2RR exhibited a totally different distribution for ethylene, ethanol, acetate, and/or n-propanol.117–122 Taking CuAg catalysts as an example, Grätzel et al.117 fabricated CuAg bimetallic tandem catalysts through the electrochemical substitution of Cu(I) ions in Cu2O nanowires with Ag(I) ions from an AgNO3 solution. Alternatively, Sargent et al.118 prepared CuAg tandem catalysts by co-sputtering Cu and Ag on a polytetrafluoroethylene (PTFE) substrate. These two approaches have led to an improvement in the selective production of ethylene (with an FE of 52% at −1.05 V vs. RHE) and ethanol (with a FE of 41% at −0.67 V vs. RHE), respectively. This sort of phenomena cannot be easily understood/explained by merely the tandem effect theory. The observed disparities in C2+ product distribution can be attributed to the structural characteristics in the catalyst. In particular, the facet orientation in Cu-based catalysts plays a crucial role in determining the product selectivity. For instance, Cu (100) facets are reported to favor C–C coupling, leading to enhanced ethylene production, whereas Cu (111) facets promote oxygenate formation, resulting in increased ethanol yields.123 In addition to catalyst structure, external reaction conditions also play a pivotal role in modulating the C2+ product selectivity. Specifically, the applied potential plays a pivotal role in modulating the adsorption and activation of CO2, thereby exerting a significant influence on product selectivity in CO2RR. At lower potentials, CO2 adsorption and activation are more favorable, leading to an increased CO yield. In contrast, higher potentials tend to promote the hydrogen evolution reaction (HER), which competes with CO2RR, and ultimately diminishes its selectivity.124 Furthermore, we hypothesize that this discrepancy may arise from the intrinsic susceptibility of Cu-based catalysts to oxidation, leading to the formation of surface or bulk oxides/oxide layers during their synthesis or storage. Upon reduction, these oxides undergo reconstruction, creating new active sites, commonly referred to as OD-Cu. In this reconstruction process, the secondary metal or other components may exert a significant influence on the behavior and properties of the reconstructed sites.125 Accordingly, investigating the reconstruction behavior of OD-Cu is imperative and should not be neglected.

This fundamental puzzle also has driven research attention to further determine the mechanism (or structure–performance correlation) beyond the tandem effect. To obtain an in-depth understanding of the structure-dependent impact of bimetallic Cu-based catalysts on their CO2RR performance, Buonsanti et al.126 selected CuAg as a platform and synthesized three CuAg bimetallic nanodimers (NDs) with different Cu/Ag inter-contacting areas (Ag1Cu0.4 NDs, Ag1Cu1.1 NDs, and Ag1Cu3.2 NDs) for CO2RR (Fig. 5a). As expected based on the tandem effect, a physical mixture of Ag NPs and Cu NPs used as an electrocatalyst for CO2RR exhibited a 1.5-fold FE for C2H4 compared to that of Cu NPs alone (Fig. 5b). However, surprisingly, the CuAg bimetallic NDs did not show a superior C2H4 FE than its mixture counterpart or even Cu NPs (Fig. 5b), directly reflecting something plays a role beyond the tandem effect. According to the XPS profiles of CuAg NDs, the authors proposed that as the Cu domain size increases, the binding energy of Ag3d in the Ag–Cu ND is continuously blue-shifted, indicating that the transfer of electrons from the Cu domain to the Ag domain will dominantly steer the final pathway to C2H4 (Fig. 5c). Moreover, considering that Cu-based materials always undergo reconstruction under electrocatalysis,127,128 naturally researchers suspect that the secondary metal probably influences the reconstruction of the Cu component during the reaction. Thus, to test this hypothesis, more recently, our group129 employed a CuO/Au hybrid as a platform to investigate the reconstruction behavior of Cu-based components when decorated with/without Au (Fig. 5d). Interestingly, it was found that the local Cu atoms surrounding Au tended to rearrange into disordered layers, rather than forming the densely packed Cu (111) plane observed on bare CuO (Fig. 5e). Meanwhile, the disordered Cu species near Au in the reconstructed Cu/Au exhibited abundant undercoordinated atoms compared to the reconstructed Cu (Fig. 5f). Consequently, these undercoordinated Cu sites boost the selective electrosynthesis of n-propanol (Fig. 5g and h). In addition, our group130 investigated the reconstruction behavior of OD-Cu in electrochemical CO2 reduction through molecular dynamics simulations and experimental studies. We found that Cu derived from CuO (CuOD-Cu) exhibits a higher density of low-coordinated Cu sites and greater surface Cu atom density compared to Cu derived from Cu2O (Cu2OD-Cu). As a result, CuOD-Cu demonstrated a superior FE for n-propanol in CO2RR, reaching up to 17.9%. These three representative works may inspire more efforts for the understanding beyond the tandem effect theory.


image file: d4nr04790g-f5.tif
Fig. 5 (a) Schematic, HAADF-STEM images, and corresponding EDS elemental mappings of three Ag–Cu NDs, showing Cu (orange) and Ag (yellow). (b) FE of C2H4 obtained on three different Ag–Cu NDs, with error bars representing the standard deviation from at least three independent measurements. (c) XPS spectra of three different Ag–Cu NDs. (d1 and d2) XRD patterns of CuO and CuO/Au, with PDF cards corresponding to Au (No. 65-8601) and CuO (No. 80-1916), along with the HR-TEM image of CuO/Au, respectively. (e1 and e2) Snapshots of the simulated reconstruction process from CuO to R–Cu and from CuO/Au to R–Cu/Au, respectively. Cu (blue), O (red), Au (yellow). (f) Analysis of surface Cu coordination environments in R–Cu and R–Cu/Au systems, with statistical distribution of coordination numbers. Dark/light green indicate Cu atoms with distinct coordination states, yellow denotes Au atoms. (g and h) Partial current densities of different CORR products and the FE of n-propanol on R–Cu/Au and R–Cu in a flow cell with CO-saturated 1.0 M KOH as the electrolyte, respectively. (a–c) Reprinted with permission from Buonsanti et al.126 Copyright 2019, the American Chemical Society. (d–h) Reprinted with permission from Cui et al.129 Copyright 2024, the American Chemical Society.

5. Conclusion and outlooks

In this review, we comprehensively and insightfully summarized the historical development of the tandem effect in Cu-based bimetallic CO2 reduction. We covered its origin, relevant applications, and in-depth exploration of its limitations (Fig. 6). The discovery of the tandem effect has significantly transformed the challenges of low selectivity, poor yield, and high overpotential in electrochemical CO2 reduction to C2+ products. This has laid a theoretical foundation for achieving stable CO2 conversion into C2, C3, and even higher-order carbon-based products. Although the large-scale industrial implementation of the tandem effect is presently limited by technological and economic challenges, it remains a highly promising strategy for C2+ production, with the potential to revolutionize traditional industrial processes. With continued technological advancements and progressive cost reductions, the tandem effect is poised to play a transformative role in future industrial applications. Given the critical role of electrochemical CO2 reduction in addressing climate change and facilitating the transition to sustainable energy, research in this field is of paramount urgency and significance. However, greater emphasis on economic viability will be essential in future industrial adoption to ensure that it not only drives the green energy transition and achieves carbon neutrality goals but also delivers tangible commercial value. In future industrial applications, although Cu is relatively inexpensive, the use of noble metals as secondary components will inevitably increase the overall cost. Thus, minimizing the dependence on noble metals will be crucial for ensuring economic feasibility. Additionally, tandem reactors can significantly improve the CO2 utilization, enhancing CO production under acidic conditions and increasing the current density for CO to C2+ conversion under alkaline conditions. However, each additional reactor unit increases the system costs, which can present a substantial economic challenge for large-scale implementation. In addition to the aforementioned aspects, factors such as catalyst stability,131 energy efficiency,132 loading strategy,133 and reaction conditions134 also play crucial roles in influencing the performance of the tandem effect. These factors interact synergistically, collectively determining the manifestation of the tandem effect in the CO2RR process, as well as the selectivity and conversion efficiency of the final products. Furthermore, based on our in-depth evaluation of the fundamental underlying mechanisms for the tandem effect, we have identified two critical challenges in its application that demand further resolution and optimization. Firstly, the efficient utilization of CO intermediates for conversion to C2+ products, which represents a key bottleneck in achieving high catalytic efficiency based on this effect. The efficiency of CO intermediate conversion is not only dependent on the activity of the catalytic sites but also closely linked to the stability of the intermediates on the catalyst surface. Addressing this challenge will require the development of catalyst systems capable of effectively modulating CO adsorption and desorption behaviors. In particular, precise control of the reaction pathways of the CO intermediates on the surface of copper is anticipated to be a focal point for future research efforts. Secondly, the potential mismatch between Cu and the secondary metal is another critical factor that merits attention. This potential mismatch may adversely affect the overall performance of the catalyst, specifically by constraining the efficient conversion of CO intermediates on its surface and hindering the effective formation of C2+ products. Consequently, this diminishes the synergistic effects inherent to the bimetallic system, further limiting its catalytic efficiency. Additionally, we attributed the observed differences in the distribution and trends of deep reduction products, even among Cu-based bimetallic systems with similar or identical compositions, to the reconstruction of Cu induced by the second metal. This reconstruction alters the product distribution and remains an area where the detailed mechanisms require further investigation. Here, we outlook several key scientific questions that merit deeper exploration in future research (Fig. 7).
image file: d4nr04790g-f6.tif
Fig. 6 Schematic of the milestones in the historical development of the tandem effect.

image file: d4nr04790g-f7.tif
Fig. 7 Advancing Cu-based bimetallic catalysts for optimizing the tandem effect in CO2RR: future research directions: (a) generation and utilization of CO: sources and pathways. (b) Cu reconstruction and tailoring of product selectivity. (c) Disparity and misalignment in electrochemical potential windows for CO2-to-CO and CO-to-C2+ pathways.

1. In Cu-based bimetallic CO2RR, is all the CO generated by the secondary metal utilized for further reduction to C2+ products on Cu? Can this be quantitatively analyzed? Alternatively, does all the CO involved in deep reduction on Cu originate exclusively from the CO2 reduction occurring on the secondary metal?

2. There exists a significant potential mismatch between the optimal potentials for CO generation by the secondary metal and the deep reduction of CO to C2+ products by Cu, resulting in insufficient tandem effect gains. Besides exploring catalysts with broad potential windows, can the optimal potentials for both processes be aligned through external environmental adjustments?

3. There is currently no unified theory on how the introduction of a secondary metal induces Cu reconstruction and does this reconstruction favorably influence the selectivity toward C2+ products?

Author contributions

C. L. and F. D. obtained financial support. C. L. conceptualized and supervised the project. D. L. and C. L. drafted the manuscript. W. D. and D. L. visualized the figures. All authors commented on and edited the manuscript.

Data availability

No primary research results, software or code have been included and no new data were generated or analyzed as part of this review.

Conflicts of interest

There are no conflicts to declare.

Acknowledgements

This work was supported by the National Natural Science Foundation of China (22202034, to C. L.; 22225606 and 22176029 to F. D.), and the China Postdoctoral Science Foundation (2022 M720657, to C. L.).

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