Andrea
Conte
,
Marco
Baron
,
Sara
Bonacchi
*,
Sabrina
Antonello
* and
Alessandro
Aliprandi
*
University of Padova, Department of Chemistry, Via Marzolo 1, I-35131 Padova, Italy. E-mail: alessandro.aliprandi@unipd.it; sabrina.antonello@unipd.it; sara.bonacchi@unipd.it
First published on 19th January 2023
Copper and silver nanowires have been extensively investigated as the next generation of transparent conductive electrodes (TCEs) due to their ability to form percolating networks. Recently, they have been exploited as electrocatalysts for CO2 reduction. In this review, we present the most recent advances in this field summarizing different strategies used for the synthesis and functionalization/activation of copper and silver nanowires, as well as, the state of the art of their electrochemical performance with particular emphasis on the effect of the nanowire morphology. Novel perspectives for the development of highly efficient, selective, and stable electrocatalysts for CO2 reduction arise from the translation of NW-based TCEs in this challenging field.
In this broad scenario, the combination of sustainable-renewable energy resources such as, solar and wind energy with electrochemical catalytic CO2 conversion, minimizing the high thermodynamic activation barrier of CO2 reduction and speeding up the reactions, has emerged as a pivotal strategy to obtain add-valued multi-carbon feedstocks within a pure circular economy paradigm.2 Obviously, this approach must consider the performance required to reach economic viability in terms of products, market size and price, operational costs, efficiency, stability, etc.3 The majority of existing CO2 reduction electrocatalysts can be divided into three groups, i.e., metallic, non-metallic, and molecular catalysts, each presenting advantages and drawbacks in terms of efficiency, robustness and selectivity, but their discussion is not the focus of this mini-review.4 Herein, we aim to provide an overview of a particular class of nanomaterials, metallic nanowires (NWs), which have been employed in the last decade as transparent conductive electrodes (TCE),5 as electrocatalysts for the electrochemical reduction of CO2. As TCE, the metallic NWs6 have already found application in working devices such as organic light-emitting diodes (OLEDs),7 organic photovoltaic modules,8 and electrochromic displays.9 Only recently, metallic NWs have been considered as promising materials for the CO2 electrochemical reduction reaction (CO2RR). Research endeavours have also been devoted to the selection of the most suitable metal in terms of electrochemical CO2RR efficiency, highlighting that noble metals such as Ag,10 Au,11 and Pd12 are efficient electrocatalysts for CO2 reduction with good selectivity towards CO but only Cu is of particular interest as a unique metal with remarkable selectivity towards formic acid, methane, methanol, and other multi-carbon oxygenates and hydrocarbons (denoted as C2+) due to the moderate binding energy between the Cu metal and the reaction intermediates.13–15 Considering these scientific breakthroughs, this abundant metal has been exploited to form inexpensive CuNWs as potential highly active and selective nanostructured materials for the electrochemical CO2RR at ambient temperature and pressure. Besides, AgNWs also show versatile properties as catalysts for the electrochemical CO2RR. Interestingly, the doping of these metals NWs with heteroatoms has been recently demonstrated to be an effective approach to increase the NWs' electrocatalytic efficiency,16 since they have a profound effect on the electronic structure of the metal NWs and on binding properties of the chemical species that participate in the reaction as reagents, products, or intermediates. Ultimately, alloying also plays a crucial role in increasing the wire resistance to poisoning processes.17
The importance of this mini-review is to provide a comprehensive understanding of the recent developments of the more promising metal NWs towards catalytic applications in the field of electrochemical CO2RR. In the first section, we describe the main recent methodologies to synthesize NWs, while in the second section, we present insights into the electrocatalytic performance of NWs toward the CO2RR.
Hereafter, we summarize the most relevant CuNW synthetic procedures developed in the last few years. Pure oleylamine (OAm) has been used as a reducing and capping agent at the same time, but high temperature (200 °C) and inert atmosphere are required.27 Water can be used as an environment-friendly alternative to organic solvents, but Cu ions need to be properly stabilized in aqueous conditions to form a nanocrystalline material upon reduction. This requirement has been achieved in alkaline conditions and using hydrazine as a reducing agent.28 Under alkaline conditions, the use of natural amino acids as capping agents has been exploited to obtained Cu-based nanostructures. Indeed, amino acids such as lysine, tryptophan, and glycine assist the formation of well-defined CuNWs.29 However, this approach is limited by the necessity of using the highly toxic hydrazine as a reducing agent. Nowadays, the most used procedure for the synthesis of CuNWs is the hydrothermal method under neutral conditions, which is much cheaper and safer, and thus attractive for large-scale production. The optimized procedures employ glucose as a mild reducing agent together with aliphatic amines such as hexadecylamine (HDA) and octadecylamine (ODA) at temperatures slightly above 100 °C.30 Under the latter conditions, the reaction mechanism starting from a Cu(II) precursor and resulting in the formation of CuNWs has been recently elucidated by Sue and coworkers, which involves a stepwise reduction through Cu(I)–alkylamine species.26 Consequently, mild reducing agents can be used stoichiometrically with respect the Cu(II) precursor because they are necessary to promote the reduction from Cu(I) to Cu(0). Notably, the morphology of the so-obtained CuNWs can be tuned by changing the type and quantity of alkylamine. For instance, by reducing the amine quantity from four to three equivalents with respect to the Cu(II) source, the diameter of the CuNWs increases. The same behaviour is observed by changing the alkylamine from ODA to HDA; however, the formation of thicker NWs is often accompanied by the formation of impurities such as nanoparticles.26 As reported by Sue and coworkers,31 phenylenediamines can be also employed instead of alkylamines as capping agents to produce very stable CuNWs due to the thin coating layer of conducting polyphenylenediamine, thus exhibiting excellent anti-oxidation properties even in water. Overall, the Cu(II) reduction mechanism strongly depends on the temperature, where the Maillard reaction, which produces species (reductones) with strong reducing power, is the dominant mechanism only if the synthesis is carried out at low temperature and using excess glucose.30,32 Alternatively, at a temperature higher than 100 °C, the Cu(I)–alkylamine mechanism prevails when a stoichiometric amount of glucose is used,26 as shown in Fig. 1.
Fig. 1 Proposed dominant mechanism for the synthesis of Cu nanowires below and above 100 °C. Reproduced with permission from ref. 26. Copyright 2020, The Royal Chemical Society. |
Fig. 2 shows a schematic representation of the synthesis outcomes by varying the AgNO3 concentration in the aspect ratio of AgNWs by the polyol method. In this synthesis, the effect of AgNO3 concentration on the morphology of AgNWs is investigated by changing the concentration of AgNO3 without changing the PVP concentration.
Fig. 2 Effect of the different concentrations of silver nitrate on the silver nanowire diameter. Reproduced with permission from ref. 38. Copyright 2019, MDPI. |
Others critical variables that can be exploited to maximize the yield of AgNWs are the reaction time, temperature and molecular weight of PVP. Unalan and coworkers showed that the use of PVP with different length chains results in the production of AgNWs with tuneable aspect ratios.41 Alternatively, when ethylene glycol is employed as the polyol reducing agent, the reduction efficiency of Ag ions is strongly affected by the temperature due to the highly temperature dependence oxidation efficiency of this agent.
Wiley and coworkers carried out a series of Ag nanowire synthesis at various temperatures to study the dependency of the reducing ability of ethylene glycol in terms of temperature,42 showing that the longest Ag NWs with also the largest diameters (40–70 nm) were produced when the reaction was carried out at the lowest temperature (130 °C). Increasing the temperature led to shorter and thinner NWs. The diameter of the NWs is affected by a variety of other elements in addition to temperature. Zhan and coworkers described that increasing the quantity of AgNO3 induced an increase in the diameter of the AgNWs,43 while decreasing the concentration of AgNO3 but keeping the quantity of PVP constant led to the formation of AgNWs with higher aspect-ratio values.39
The presence of chloride ions also affects the generation of AgNWs by stabilizing the silver nanoparticles44 and by lowering the concentration of free silver ions in the solution via the production of AgCl, ultimately slowing the reduction of Ag(I), and then allowing the growth of NWs despite the presence of Ag nanoparticles.40 Positively, in the case of AgNWs, highly conductive percolating networks can be obtained without any post treatment process due to the absence of an insulating oxide layer.
The H-cell is the typical divided electrochemical cell used for testing the electrocatalytic activity and selectivity of supported nanostructured materials with respect to the CO2RR. The main advantage of this type of cell refers to the presence of two compartments connected through a conductive membrane, with one containing the working and the reference electrodes and the other, the counter electrode this setup allows the conversion of a massive amount of CO2 into add-value products without the interference of anodic reaction products. As a conductive membrane, Nafion represents the most widely employed polymer although a better choice is represented by anion exchange membranes, which limit the polarization losses and detrimental proton concentration on the catholyte.47 Typically, an aqueous solution of 0.1 M in KHCO3 is employed for both voltammetric and controlled potential electrolysis (CPE) experiments. In particular, the activity of the catalyst is evaluated by cyclic voltammetry (CV) experiments, enabling the measurement of the current density (j) as the current normalized over the electroactive electrode surface at a given potential value, E, which is directly correlated with the electron transfer (ET) event promoting the CO2RR. In terms of chemical transformation, the faradaic efficiency (FE) provides information on the electrochemical CO2RR efficiency given that it is directly correlated with the charge amount consumed during the electrolysis and the concentration of products detected. Analytical tools such as gas chromatography (GC) and nuclear magnetic resonance (NMR) are the most widely employed for the qualitative and quantitative estimation of the electrogenerated gaseous and liquid products, respectively, and thus for the proper evaluation of the activity (i.e., efficiency and selectivity) of the different catalysts.48 Ionic chromatography and conductivity measurements have also been used for the estimation of charged products such as formate. FE is calculated by using, for liquid products, the equation FE = (ZnF/Q) × 100, where Z = number of electrons involved in the reaction, n = number of moles generated for any specific product, F = Faraday constant = 96485 C mol−1, and Q = total charge passed during the bulk electrolysis (C). In the case of gaseous products, other parameters such as the gas flow rate and the volume of gas produced should be considered for the calculation of FE, as reported by Nu and coworkers.49
In this framework, another important aspect to consider is the preparation of the working electrode. A simple but effective technique usually utilized for the preparation of NW-based electrodes is the spray coating of an ethanolic dispersion of NWs on selected substrates. This non-covalent approach has the advantage of being extremely versatile given that any type of substrate can be potentially explored, while preserving the electrochemical properties of the pristine NWs. Alternatively, this electrode preparation strategy poses the challenge of maximizing the physisorption adhesion between the substrate and the NWs to minimize their leaking in the solution during the electrolysis, as well as increasing the mechanical performances (i.e., the robustness to scratches), thus strengthening the overall durability. For instance, a glassy carbon electrode (diameter of about 5–10 mm) was used as a support for drop-casting a suspension of ethanol and 5% Nafion with a CuNW concentration of 2 mg mL−1. Interestingly, the authors observed that the use of Nafion resulted in enhanced stability of the as-obtained electrode without affecting the electrochemical CO2RR performance.50 Finally, it is also important to emphasize that the use of different preparation methods to assemble NW-based electrodes and different potentials for the CPE can affect both the FE and the selectivity, therefore hindering the effective comparison of the experimental data reported in the literature to date. To guide the readers in this field, some of the most relevant results involving metal and alloy NWs as electrocatalysts for the electrochemical CO2RR are summarized in Table 1 with the aim to provide a brief glance of the catalyst performance as a function of its composition. Subsequently, all the potential values refer to the reversible hydrogen electrode (RHE).
Catalyst | Applied potential (V vs. RHE) | Current density (mA cm−2) | FE (%) | Electrolyte | Major products | Ref. |
---|---|---|---|---|---|---|
CuNWs | −1.01 | −17.3 | 77.40 | 0.1 M KHCO3 | C2H4 | 35 |
PTFE–CuNW | −0.6 | 6 | 68 | 0.1 M KHCO3 | HCOOH | 76 |
CuNWs | −1.1 | 4.25 (A g−1) | 35 (C2H4) | 0.1 M KHCO3 | C2H4, C2H6 | 84 |
25 (C2H6) | ||||||
R-CuO | −1.3 | −25 | 40 (H2) | 0.1 M KHCO3 | H2, CO, HCOOH, C2H4 | 77 |
10 (CO) | ||||||
15 (HCOOH) | ||||||
10 (C2H4) | ||||||
R-CuO-Nafion-60 | −1.3 | −25 | 30 (H2) | 0.1 M KHCO3 | H2, CO, HCOOH, C2H4 | 77 |
35 (CO) | ||||||
15 (HCOOH) | ||||||
10 (C2H4) | ||||||
CuCuxONWs | −1.03 | −24.1 | 78.4 (C2+ products) | 0.1 M KHCO3 | C2H4 | 50 |
Cu68Ag32NWs | −1.17 | −50 | 80 (C1+ and C2+ products) | 0.5 M KHCO3 | CH4 | 55 |
OD-CuNWs | −0.5 | −4 | 70 | 0.1 M KHCO3 | H2, CO | 85 |
CuO/Cu2ONWs | −0.7 | −18 | 60 (H2) | 0.1 M KHCO3 | H2, CO, HCOOH | 49 |
15 (CO) | ||||||
10 (HCOOH) | ||||||
Cu2SbNWs | −0.90 | −6 | 86.5 | 0.1 M KHCO3 | CO | 63 |
Cu9AgNWs | −1.2 | −2.7 | 66 (CH4) | 0.1 M KHCO3 | H2, C2H4, CH4 | 58 |
25 (H2) | ||||||
8 (C2H4) | ||||||
CuNWs | −1.25 | −7.5 | 55 (CH4) | 0.1 M KHCO3 | CH4 | 86 |
CuNWsPDA | −0.93 | −20 | 29 (CH4) | 0.5 M NaHCO3 | CH4 | 83 |
Au-Bypi-CuNWs | −0.9 | −13 | 25 (CH3CHO) | 0.1 M KHCO3 | CH3CHO | 87 |
Ag/CNWs | −0.67 | −0.23 | 100 (CO) | 0.1 M KHCO3 | CO | 68 |
AgAu | −1.2 | −5.61 | 99.65 (CO) | 0.1 M KCl | CO | 88 |
Ag/PTFE-PE-200NWs | −0.9 | −62 | 85 (CO) | 0.5 M NaHCO3 | H2, CO | 89 |
15 (H2) | ||||||
AgNWs | −0.9 | −0.10 | 88 (H2) | 0.1 M KHCO3 | H2, CO, CH4 | 90 |
6 (CO) | ||||||
2 (CH4) | ||||||
AgPdNWs | −0.4 | 7 | 94 | 0.1 M KHCO3 | HCOO− | 91 |
AgNWs | −1.75 (Ag/AgCl) | 16 (CO) | 98 (CO) | 0.5 M NaHCO3 | CO, H2 | 92 |
1(H2) | 2 (H2) | |||||
AgNWs | −1.75 (Ag/AgCl) | 140 (CO) | 70 (CO) | 2 M KOH | CO, H2, HCOO− | 92 |
25 (H2) | 10 (H2) | |||||
25 (HCOO–) | 10 (HCOO−) | |||||
CuNWs | −0.7 | −10 | 65 (H2) | 0.1 M KHCO3 | H2, CO | 57 |
8 (CO) | ||||||
17 (HCOO–) | ||||||
CuAgNWs | −0.7 | −10 | 46 (H2) | 0.1 M KHCO3 | H2, CO, HCOO− | 57 |
14 (CO) | ||||||
24 (HCOO−) | ||||||
OD-CuNWs | −1.1 | −0.85 (CH3CH2OH) | 7.3 (CH3CH2OH) | 0.1 M KHCO3 | CH3CH2OH, CH4, C2H4 | 93 |
−1.73 (CH4) | 20 (CH4) | |||||
−2.35 (C2H4) | 20.1 (C2H4) | |||||
Cu(Ag-20)20 NWs | −1.1 | −4.1 (CH3CH2OH) | 16.5 (CH3CH2OH) | 0.1 M KHCO3 | CH3CH2OH, CH4, C2H4 | 93 |
−2.39 (CH4) | 10 (CH4) | |||||
−3.76 (C2H4) | 14.9 (C2H4) | |||||
CuAuNWs (Au on Cu) | −1.1 | // | 45 (CO) | 0.1 M NaHCO3, 0.5 M NaClO4 | CO, H2, HCOO− | 60 |
5 (HCOO−) | ||||||
50 (H2) | ||||||
CuAuNWs (Cu on Au) | −1.1 | // | 55 (CO) | 0.1 M NaHCO3, 0.5 M NaClO4 | CO, H2, HCOO− | 60 |
5 (HCOO) | ||||||
40 (H2) | ||||||
CuAgNWs (Cu on Ag) | −1.1 | /// | 45 (CO) | 0.1 M NaHCO3, 0.5 M NaClO4 | CO, H2, HCOO− | 60 |
10 (HCOO) | ||||||
45 (H2) | ||||||
CuAgNWs (Ag on Cu) | −1.1 | // | 55 (CO) | 0.1 M NaHCO3, 0.5 M NaClO4 | CO, H2, HCOO− | 60 |
10 (HCOO) | ||||||
35 (H2) | ||||||
CuAuNWs | −1.25 (Ag/AgCl) | −3.8 | 89 (CO) | 0.5 M KHCO3 | CO | 94 |
Cu NWs-Bi NSs | −0.86 | −10 | 87 (HCOO−) | 0.1 M KHCO3 | HCOO− | 95 |
CuSn | −0.9 | 30 | 78.6 | 0.1 M KHCO3 | HCOO− | 61 |
The density of surface defects in terms of grain-boundaries has been also exploited to enhance the catalytic performance of CuNWs. In 2020, Goddard III, Huang and coworkers reported the electrochemical post-treatment of chemically synthesized CuNWs, enabling impressive selectivity towards C2 products by suppressing the C1 pathway.35 In particular, the authors demonstrated that the application of a very large reductive potential (−1.05 V) in the same electrolyte used for the electrochemical CO2RR governs the formation of a highly stepped surface structure with an increased density of catalytic active sites, resulting in an FE for C2H4 greater than 70% and exceptional stability for more than 200 h.
Recently, Xia and coworkers proposed an alternative approach to increase the surface roughness of CuNWs based on a synergistic chemical oxidation with O2 or H2O2. Even if with different efficiencies for these two oxidizing agents, an increased selectivity toward ethylene was observed.50 The use of a post-synthetic electrochemical treatment based on a sequence of potentiostatic pulse at different potentials to remove the capping agent has also shown to be beneficial to increase the conversion of CO2 to CO with an FE of 100% at E = −1.0 V.54
Although a variety of post-synthesis treatments have been recently implemented for CuNWs, three main aspects still need to be improved in this field for the implementation of the practical and robust electrocatalytic production of added-value products from CO2, as follows: (i) the competition between the CO2RR and HER in the highly active sites, which refers to the strong affinity of these active sites to water or electrolytes; (ii) the low CO2RR selectivity among added-value products (e.g., CO vs. HCOOH); and (iii) the long-term stability of CuNWs. In particular, the spontaneous oxidation of Cu NWs is still a major problem to be tackled given it results in the attenuation of the electrode capacitance.
Recently, some of these issues have been overcome by the insertion of proper heteroatoms in the Cu nanostructure. For example, Chen and coworkers recently highlighted a remarkable decrease in overpotential toward methane production as a direct consequence of optimized amounts of Ag interdiffused in the pristine CuNW.55 Generally, CuAg alloy NWs impart larger selectivity towards the formation of hydrocarbons and oxygenated derivatives with respect to pure CuNWs, which is attributed to the ability of Ag atoms to suppress the competitive HER.56 A promising result in this field was reported by Choi and coworkers, who achieved impressive tuneable selectivity from C2H4 to CH4 with a maximum of 72% CH4 yield at −1.17 V. The authors introduced the concept of “intimate atomic CuAg interface”, as schematically shown in Fig. 3, which was realized by means of galvanic replacement of Cu with Ag.57
Fig. 3 (a) Starting CuNWs. (b) Galvanic replacement on the surface. (c) Surface activation through in situ formation of CuAg assemblies during the electrochemical CO2RR. Reproduced with permission from ref. 57. Copyright 2021, Springer. |
This approach enables the creation of localized CuAg alloy, then overcoming the loss of the peculiar Cu ability to form C2 and C3 hydrocarbons and alcohols, which is often observed after alloy formation. Importantly, the proposed procedure can potentially be implemented by exploiting multi-metal compositions with a limited mixing degree with Cu.57
Alternatively, high selectivity toward ethanol production was recently demonstrated by exploiting an electrochemical approach, which was suitable for the production of Au-doped CuNWs.58 In particular, a potentiostatic-pulse electrodeposition procedure was used to produce CuxAuy nanowire arrays starting from a solution of Cu and Au salt, over an Au foil using an aluminium oxide mask. Interestingly, the Cu/Au ratio in the final alloy was optimized by controlling the deposition potential value and the so-obtained catalysts ensured the selective production of ethanol from CO2 with an FE of 48% at E as low as −0.5 to −0.7 V RHE. Recently, CuNWs decorated with AuNPs were grown by homo-nucleation, enabling good selectivity towards multi-carbon products. The best-performing alloy, containing only 0.7% Au, exhibited an FE for C2+ species of 65.3% and a larger current density (12.1 mA cm−2 at −1.25 V) than pure CuNWs.59
The electrodeposition of different metals has also been explored to grow bimetallic catalysts in a segmented configuration, allowing to drive different CO2 reduction product distributions as a function of the relative position of the two metals.60 Recently, the synergy between Cu activity and Sn selectivity has been also proposed for the electrochemical production of formate. Wang and coworkers61 designed, synthesized, and tested a bimetallic copper-tin based core–shell alloy@oxide nanostructure, where the CuSn core ensured efficient electrical contact with the active sites, whereas the catalytic activity and selectivity towards formate were guaranteed by the external layer of SnO2 doped with amorphous Cu. The selectivity was demonstrated to be affected by the thickness of the external shell, resulting in the generation of formate when it was thick enough (1.8 nm), whereas for thinner layers (0.8 nm), the main product was CO.
The doping of CuNWs with halides has been also tested, where iodide showed increased selectivity toward C2H6. The FE observed was 24%, a substantial increase compared to the 4% observed with the undoped CuNW. The increased C2H6 production was accompanied by a concomitant decrease in C2H4. These experimental results were corroborated by DFT calculation, showing that the presence of iodide in the Cu structure strengthened the absorption of C2H4 and accelerated its hydrogenation.62 Interestingly, the use of antimony has been exploited to obtain good selectivity for the formation of CO, as in the case of the electrodeposition of Cu2Sb on a CuNW array.63
Moreover, in the case of CuNWs, the efficiency of the electrical contact between the catalysis sites and the support is known to affect the overall current density and chemical transformation rate of the process. In this framework, a very simple experimental approach based on mixing NWs with carbon powder and Nafion was exploited to support AgNWs with a diameter of 200–400 nm on a glassy carbon electrode, showing a superior catalytic performance to that of NWs with a similar diameter.68 Alternatively, the core–shell NW configuration has emerged as an effective solution to boost the catalyst/support coupling, in particular in the vertical array geometry. Li and coworkers reported the largest specific CO2RR activity (413 μA cm−2 at −0.6 V) to date and specific electrocatalytic activity toward CO production (current density 5.27 mA cm−2 at −0.6 V), which were directly correlated with the use of a silver@silver chloride core−shell nanowire array formed by the nanoimprinting technique.69 The exceptional activity and good selectivity were ascribed to the presence of Cl as subsurface atoms in the metal Ag lattice, contributing to the suppressed HER and increased activity.
Heteroatom doping or alloying represents a valuable opportunity toward the discovery of new catalytic materials displaying enhanced activity, including nanostructured Ag-based catalysts.70–72 Moreover, alloying represents an effective approach for increasing the wire resistance to poisoning processes as in the case of alloyed PdAgNWs, where Pd effectively works in term of selectivity toward the formation of formate from electrochemical CO2RR with an overpotential that is nearly zero, while it also reduces the reaction intermediates interaction due to its lower work function, thus overall increasing the catalyst lifetime. However, as a drawback, Pd suffers from rapid deactivation due to CO poisoning.73
Although the use of noble metals as catalysts has limited interest for large-scale application, they still represent proof-of-concept approaches that can pave the way for near future perspective. This is the case of AgAu core–shell NWs, which showed nearly 100% CO2-to-CO electroreduction at −1.2 V as a result of the mixing of Au and Ag in a 0.5:1 ratio to form Ag@Au0.5 alloy NWs88 (Fig. 4).
Interesting kinetic studies were also carried out to shed light on the nature of the electrochemical CO2RR rate-determining step. In particular, electrochemical impedance spectroscopy analysis (EIS) and Tafel plot analysis showed the lowest charge transfer resistance (Rct) and smaller slope for the Ag@Au0.5 alloy composition among others, highlighting how the latter parameter can be potentially exploited to tune the heterogeneous ET rate.
Ligands and surfactants are not always detrimental to the catalytic activity, but it has been showed that they can drive the transformation of CO2 by tailoring the physical and chemical environment of NWs,74 thereby tuning the interactions between the metal and the reaction intermediates.75 The use of an organic layer to impart hydrophobic character to CuNWs has been reported to be an effective strategy to increase the CO2 concentration near the Cu active sites and to inhibit the HER as a result of the decreased water affinity. Polytetrafluoroethylene (PTFE) was used as a surface modifier to allow the increased diffusion of CO2 to the active layer. The so-obtained modified NWs showed good selectivity toward CO formation with an FE of 71% at −0.4 V and a formic acid selectivity at −0.6 V characterized by an FE of 68%.76 A similar effect was also obtained using a Nafion layer over CuONWs, resulting in higher selectivity toward CO, which increased from 8.72% to 43.15% at −1.3 V with suppression of the HER.77 Interestingly, the hydrophobic effect was also invoked to explain the results obtained after the functionalization of the surface of a Cu dendritic structure by a monolayer of 1-octanethiol, which enabled the observation of the strong deactivation of the HER from 71% to 10% FE and an effective increase in the generation of C2H4 and ethanol, achieving an FE of 56% and 17%, respectively, at −1.5 V. This achievement was attributed to the formation of a triple solid/liquid/gas phase boundary, a type of “lotus effect”, favouring the interaction of CO2 with the Cu surface.78
Polydopamine polymer has also been exploited to functionalize the surface of Cu, resulting in a 2.3-times increase in the CH4 generation respect to the bare CuNWs as well as resulting in enhanced stability, most probably due the synergistic effect of the phenolic group in the polymer backbone, which could stabilize the activated CO by H-bonding and the amino groups that capture and transfer protons to it, thus overall favouring the formation of CH4.79 Recently, Agapie and coworkers showed that the incorporation of polyamine on the flat or dendritic Cu surface results in an increase in the selectivity toward ethylene,80,81 while the use of N-substituted pyridinium additives enables the production of ethanol.82 Interestingly, theoretical calculations predict a path toward the use of amine-based ligands to stabilize useful intermediates for the formation of C2 oxygenated products.83
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