The overconsumption of fossil fuels is a cause of increased CO2 emission in the atmosphere, which presents numerous environmental problems such as increasing sea levels and environmental degradation. Considering that the consumption of fossil fuels remains necessary at present, it is worth looking into the recycling of the emitted CO2 by reducing the latter to useful organics or liquid fuels, which can then be used as alternative clean energy resources [1-3]. In recent years, photochemical [4, 5] and electrochemical methods [6, 7] have been primarily examined toward the reduction of CO2. The electrochemical method is the most promising approach owing to its convenient large-scale application capability and simple tuning possible at room temperature. Various electrode materials have extensively been investigated to obtain different reduction products such as carbon monoxide, formic acid, methane, and methanol [6-8]. Metal electrodes are readily available and can provide satisfactory current density in aqueous media.
Specifically, extensive studies have been conducted on Cu electrodes [9, 10] because Cu has the unique ability to catalyze the formation of hydrocarbons [7, 8, 11]. Efforts have been devoted to alloying Cu with other different metals [12, 13] and modifying the Cu electrode surface [14] to improve the catalytic performance of Cu. Kanan et al. [15] examined the modification of Cu electrode by annealing Cu foil in air and electrochemically reducing the resulting Cu2O layers. The modified Cu required a lower overpotential than polycrystalline Cu toward catalyzing the reduction of CO2 owing to the exposed crystal facets on the Cu electrode after annealing and electroreduction. Thus, modifying the surface of electrodes with certain metals is an efficient method to promote the activity toward CO2 reduction. For instance,Zhao et al. [16] modified Co3O4 nanotubes with Cu nanoparticles. Modification with the Cu nanoparticles influenced the adsorption of intermediate products, resulting in high selectivity toward the formation of formic acid. Moreover, the yield and selectivity toward the formation of formic acid are the highest to date among other previously reported results. In another study,Rudnev et al. [17] modified single crystal platinum with copper and reported that the resulting Cu/Pt (110) electrode is currently the most active among all electrodes examined to date. Although some studies have focused on the modification on polycrystalline Cu, the modification of oxide-derived Cu with transition metals has not been investigated to date.
In this work, an oxide-derived Cu electrode was modified with Ni,Zn, or Au for application in CO2 reduction and detailed insights into the effect of modification of these transition metals on Cu electrode were presented.
Copper foil (0.025 mm thickness, 99.999% metals basis,Alfa Aesar),Na2CO3 (≥99.999%,Sigma-Aldrich),ZnSO4·7H2O (99.995%,Aladdin),NiCl2·6H2O (analytical reagent grade,Sinopharm Chemical Reagent Co.,Ltd.),HAuCl4·4H2O (analytical reagent grade,Sinopharm Chemical Reagent Co.,Ltd.), and KCl (guaranteed reagent grade,Xilong Scientific Co.,Ltd.) were used in the present study.
The electrochemical experiments were conducted on a PAR-263A potentiostat (EG&G)—a three-electrode system was used for the experiments. Copper foil was used as the working electrode. Platinum plate served as the counter electrode. All data presented in this work are relative to the saturated calomel electrode (SCE).
The electrolysis experiments were performed in a glass H-cell. Naphthol membrane was used to separate the working and counter electrode compartments to prevent oxidation of the reduced CO2 products. The volume of the cathode chamber was 5.5 mL.
The liquid-phase products were quantified using solvent-suppressed 1D 1H NMR spectroscopy (500 MHz,Avance Ⅲ). For the NMR analysis, a 500-μL electrolyte sample was mixed with 100 μL of 14.1 mmol/L dimethyl sulfoxide in D2O as an external standard. The charge of the liquid products was calculated from the NMR data, and the Faraday efficiency was obtained by dividing the charge by the total reduction charge.
The oxide-derived Cu electrode was prepared using the method by Kanan et al. [15]. After cleaning the Cu foil (1 cm ×1 cm) in phosphoric acid, the foil was annealed in air at 300 ℃ for 5 h. The resulting copper oxide electrode was then electrochemically reduced at −0.9 V for 1 h in 0.1 mol/L NaHCO3 obtained by blowing CO2 in Na2CO3 solution. The reduction of the copper oxide layers was complete when the reduction current was nearly zero.
Modification of the prepared oxide-derived Cu electrode was performed by potentiostatic deposition. To achieve efficient deposition, the latter was conducted at potentials more negative than the thermodynamic potentials. Specifically, the deposition potentials of Ni,Zn, and Au on the oxide-derived Cu electrode were set at −0.9,−1.2, and −0.5 V in 1 mmol/L NiSO4, 1 mmol/L ZnSO4, and 1 mmol/L HAuCl4, respectively. The deposition charges were 0.29, 0.28, and 0.29 C for Ni,Zn, and Au, respectively. The deposition charge was optimized accordingly. For example, modification of the oxide-derived Cu electrode with Ni was performed at 0.10, 0.29, and 0.50 C Ni, and the Faraday efficiencies of the reduction products on the different electrodes were compared. The 0.29 C Ni-modified electrode showed the highest Faraday efficiency toward the formation of formic acid. Hence, 0.29 C was chosen as the deposition charge for Ni. It should be pointed out that an accurate deposition charge cannot be determined because hydrogen evolution simultaneously occurs on the electrode during modification.
The microstructure of the electrode raw material and unmodified and modified electrodes was characterized by scanning electron microscopy (SEM; Hitachi-S4800).
For the electrolysis experiments, 5 mL of 0.1 mol/L NaHCO3 was introduced in the cathode chamber of the H-cell and CO2 was continuously blown throughout the experiment to ensure the saturation of CO2 in solution. The reduction of CO2 was performed under constant potential at −1.2,−1.3,−1.4,−1.5, and −1.6 V. Electrolysis lasted for 2 h to enrich the reduction products. To normalize the current density, the double-layer capacitances were measured to determine the active surface areas of the electrodes.
Fig. 1(a),(b) shows the SEM images of the annealed Cu and annealed Cu after reduction (oxide-derived Cu), respectively. The annealed copper foil had a rough surface; however, the surface of the oxide-derived Cu was rougher. This could be attributed to the formation of smaller crystal domains upon reduction. The oxide-derived Cu feature more exposed (100) and (110) sites that can bind strongly with the intermediate product COOHads and realize a low overpotential [18]. In a study by Kanan et al. [19], grain boundaries were considered as the reason for high catalytic CO2 reduction activity. Fig. 1(c) shows the changes in the reduction current upon annealed Cu (copper oxide) layers as a function of time. The reduction current decreased to nearly zero after 1 h, indicating that the reduction of the copper oxide layers was complete. Comparison of the SEM images in Fig. 1(d)-(f) and Fig. 1(b) revealed that modification with Ni,Zn, or Au minimally changed the morphology of the oxide-derived Cu; the morphology of the modified oxide-derived Cu was rough and not well defined.
As linear sweep voltammetry (LSV) experiments can be easily performed and allow complete measurement of the reduction current during CO2 reduction in a wide potential region,LSV of CO2 reduction on the different electrodes was performed, and the results are shown in Fig. 2. CO2 reduction occurred at potentials lower than −0.9 V by comparing the curves recorded in CO2-saturated 0.1 mol/L NaHCO3 solution and in N2-saturated solution. The electrodes modified with Zn and Au showed higher current densities than the oxide-derived Cu electrode, whereas the electrode modified with Ni showed a lower current density than the Cu electrode. It should be noted that the currents obtained from both hydrogen evolution and CO2 reduction contribute to the total voltammetric current. The catalytic performance toward CO2 reduction on the different electrodes can be quantitatively evaluated by determining the Faraday efficiency of the formation of the different products detected by NMR and gas chromatography.
The liquid-phase products of CO2 reduction at constant potential were analyzed by NMR spectroscopy. Fig. 3 shows the Faraday efficiency of the formation of formic acid in the potential range of −1.2 to −1.6 V, and Table 1 lists the Faraday efficiency of the formation of ethanol and n-propanol. On oxide-derived Cu, at potentials of −1.2 and −1.3 V, formic acid was the only liquid-phase product detected, and the corresponding Faraday efficiencies were 5.6% and 15.0%. At more negative potentials (−1.4 to −1.6 V), the Faraday efficiency of the formation of formic acid generally increased with increasing potentials, and small amounts of ethanol and n-propanol were detected.
Ni modification of the oxide-derived Cu electrode increased the Faraday efficiency of the formation of formic acid and n-propanol. The alcohol products were detected at applied reduction potentials ranging from −1.4 to −1.6 V. At −1.5 V, the Faraday efficiency of the formation of formic acid was 30.0%, and those of ethanol and n-propanol were 1.6% and 2.7%, respectively. These values were higher than the corresponding values obtained on the unmodified oxide-derived Cu electrode.
To understand the rationales for the high Faraday efficiency obtained for the Ni-modified electrode, the gas-phase products of CO2 reduction on the oxide-derived Cu and Ni-modified oxide-derived Cu electrodes were analyzed by online gas chromatography. As shown in Table 2,Ni modification significantly increased the yield of CO. Ni has a smaller atomic radius (r = 0.1246 nm) than Cu (r = 0.1278 nm). Hence, modification of Cu with Ni is expected to instigate lattice contraction when compared with pure Cu. Such a geometric strain will result in a downshift of the d-band center, which decreases the binding energy of CO [13]. As a result, the Ni-modified Cu will yield more low-degree reduced products (CO and HCOOH) than pure Cu. Previously,Todoroki and coworkers [14] have also reported that monolayer and sub-monolayer Ni on the Cu(111) surface increase the yield of CO. As for the increase of multi-carbon alcohols, the addition of Ni may promote coupling of C-C bonds.
Zn modification of the oxide-derived Cu electrode decreased the Faraday efficiency of the formation of formic acid in the potential range studied. In the potential range of −1.4 to −1.6 V, small amounts of alcohols, including ethanol and n-propanol, were detected, and the Faraday efficiencies of the formation of the alcohols were slightly higher than those obtained on the unmodified oxide-derived Cu electrode. These results indicate that the introduction of Zn facilitates the hydrogenation of intermediate products slightly.
Also,Au modification of the oxide-derived Cu electrode decreased the Faraday efficiency of the formation of both formic acid and alcohols in the potential range studied. At −1.5 V, the Faraday efficiencies for the formation of formic acid and ethanol were only 20.5% and 0.2%, respectively. As previously reported [7], the main reduction product on the Au-modified electrode was CO owing to its weak bond with CO. Once CO2 is reduced to CO,CO easily desorbs from the surface; therefore, further reduction is difficult [20].
The effect of modification of Ni,Zn, and Au of oxide-derived Cu electrode on CO2 reduction was investigated. Formic acid was obtained as the main liquid product on all electrodes. The Ni-modified electrode showed the highest Faraday efficiency toward the formation of formic acid and n-propanol among all the electrodes studied.