Since the Industrial Revolution, excessive carbon dioxide (CO
2) emissions have emerged as a significant concern due to their potential to exacerbate global warming, contribute to sea level rise, and harm ecosystems [
1]. The conversion of CO
2 into high-value-added products through methods, such as electrocatalysis, photocatalysis, and thermal catalysis, represents an effective approach to utilize CO
2 resources and advance towards achieving carbon neutrality [
2-
4]. Electrocatalysis distinguishes itself among the aforementioned methods for its inherent simplicity, operability, and the ability to harness electricity generated from renewable resources [
4,
5]. However, the electrocatalytic reduction of CO
2 encounters significant thermodynamic barriers and slow reaction kinetics, especially during the conversion of the stable linear CO
2 molecule into the *CO
2− radical anion [
5]. Thus, the advancement of efficient and durable electrocatalysts with high current density and superior selectivity for desired production is essential for enhancing the kinetics of the CO
2 electroreduction.
Currently, numerous researchers are actively exploring the applications of non-precious transition metal-based electrocatalysts in the field of the CO
2 electroreduction, due to their abundant reserves and competitive catalytic performance [
2,
6-
8]. As illustrated in Table S1 (Supporting information), various classes of transition metal compounds have been explored for the CO
2 electroreduction, including metal nitrides, sulfides, phosphides, and antimonides. These electrocatalysts have demonstrated good catalytic performance for the CO
2 electroreduction, with certain systems achieving remarkable Faradaic efficiencies exceeding 90% for target products under optimized conditions. Despite these advances, metal borides remain relatively underexplored for the CO
2 electroreduction compared to other transition metal compounds. Recently, some researchers have discovered that incorporating trace B (< 10 wt%) into metal structures as B-doped catalysts could result in a redistribution of electron states in metal electrocatalysts [
9-
14]. This change could alter the adsorption of reaction intermediates, thereby impacting the catalytic performance in the electrocatalytic reduction of CO
2 [
15]. For example, introducing B atoms (2.3 wt%) into bismuth (Bi) could alter its local electronic structure, thereby enhancing the catalytic activity for CO
2 electroreduction and improving the selectivity for HCOOH over a wide potential range [
16]. The intercalation of B atoms (1.26 wt%) could also adjust the average oxidation state of copper (Cu), control *CO adsorption and dimerization, and then promote the generation of C
2 products [
17]. Moreover, a B-doped (6.3 at%) palladium catalyst (Pd-B/C) was more effective in boosting the formation of HCOOH compared to Pd/C [
18]. These results indicated that the introduction of trace B element in metal structures could affect the activity and selectivity of electrocatalytic reduction of CO
2. Therefore, we speculate that transition metal borides with a precisely defined structure, higher B content and larger CO
2 adsorption capacity [
19,
20] hold great potential to serve as cost-effective and high-efficiency candidates for the electrocatalytic reduction of CO
2.
Notably, transition metal borides exhibit diverse composition, structural, and electronic characteristics, primarily including metal-rich borides (M
xB,
x > 1), monoborides (MB), metal diborides (MB
2), and boron-rich borides (MB
x,
x > 2) [
21]. Among these borides, the well-known hexagonal AlB
2-type (
P6/mmm) metal borides with high electrical conductivity and low electrical resistivity have attracted significant attention from researchers [
22]. This kind of borides is characterized by close-packed transition metal sheets and graphene-like B layers, and can be synthesized with a variety of transition metals [
23]. The presence of graphene-like B layers played an important role in enhancing electronic conductivity and providing more active sites [
24]. It is worth noting that the choice of transition metals and the interaction between B and transition metals can have a profound effect on the physical and chemical properties of transition metal diborides, particularly in terms of their electrocatalytic performance [
25]. Moreover, Li
et al. theoretically demonstrated that monolayer two-dimensional transition-metal diborides exhibited a remarkable catalytic activity in selectively converting CO
2 to CH
4 [
26]. Additionally, hard/superhard transition metal diborides obtained through the high pressure-high temperature (HPHT) are integral bulks, which can be directly utilized as self-supporting electrodes for electrocatalytic reduction of CO
2 [
27]. In comparison to traditional powder electrocatalysts, these self-supporting electrodes can not only prevent the aggregation of electrocatalyst or the concealment of active sites caused by binder addition [
28], but also eliminate the interface impedance between the conductive substrate and electrocatalyst. This facilitates efficient electron and proton transfer [
29], which will ultimately enhance the catalytic performance for the electrocatalytic reduction of CO
2. The aforementioned facts motivate us to further explore the catalytic performance of various AlB
2-type metal borides self-supporting electrodes for the electrocatalytic reduction of CO
2.
In this study, the AlB
2-type metal diborides (TM = Ti, Zr, Hf, V, Nb, Ta, Cr, Mn, Mo) were fabricated using the HPHT method (
Fig. 1a). The detailed temperature, pressure, and duration parameters for preparing different metal diborides are provided in Table S2 (Supporting information). The X-ray diffraction (XRD) patterns of different samples in
Fig. 1b confirm the successful synthesis of the hexagonal AlB
2-type metal diborides. Meanwhile, it can also be seen that these transition metal diborides synthesized by the HPHT method exhibit high crystallinity and purity. As depicted in
Fig. 1c, the Rietveld refinement of XRD pattern reveals that the ZrB
2 sample corresponds to a hexagonal unit cell with the space group
P6/mmm (No. 191) [
30]. The lattice parameters for the ZrB
2 sample are
a =
b = 3.16067(3) and
c = 3.52094(6) (Table S3 in Supporting information), showing excellent agreement with values previously documented in the literature.
Fig. 1d shows the comparison of average distance for adjacent metal-B and B-B atoms in different metal diborides. Although the average distances of metal-B and B-B may change with the variation of metal atoms, these metal diborides adapts the typical AlB
2-type structure characterized by graphene-like B layers sandwiched between transition metal layers (Fig. S1 in Supporting information). To further investigate the electronic structure of the ZrB
2 sample, the electronic characteristic was examined using electron localization function (ELF) and density of states (DOS). The ELF analysis (
Fig. 1e) reveals that there are ionic Zr-B and covalent B-B bonds in the ZrB
2 sample. Meanwhile, DOS value is not zero at Fermi energy level for the ZrB
2 sample (
Fig. 1f), indicating the intrinsic metallic behavior of the ZrB
2 sample. In addition, as confirmed by the DOS result (
Fig. 1f), the metallic property of the ZrB
2 sample mainly originates from d electrons of Zr layers, which can enhance its catalytic activity.
The morphologies of various metal diborides were also measured by scanning electron microscopy (SEM). In Fig. S2 (Supporting information), it can be observed that the surfaces of the obtained bulk metal diborides exhibit a rough and irregular texture, resulting from the abrasion of diamond griding disk. Meanwhile, high-resolution SEM images (Fig. S3 in Supporting information) reveal that different metal diborides were all composed of tightly packed, irregular nanoblocks. To further explore the morphology and structure of metal diborides, we conducted transmission electron microscopy (TEM) and high-resolution TEM (HRTEM) tests using the ZrB
2 sample as an example. Combining high-resolution SEM (Fig. S3b) and TEM images (
Fig. 2a), it can be observed that the ZrB
2 sample possesses a densely packed nano-block structure with grain size around 0.3–1.0 µm. In the HRTEM image (
Fig. 2b) of the ZrB
2 sample, the interplanar spacings of 0.272 nm and 0.333 nm can be attributed to the (100) and (001) planes of ZrB
2 [
31], respectively. The selected area electron diffraction (SAED) image (
Fig. 2c) of the ZrB
2 sample corresponds to the (101) and (100) planes of the hexagonal ZrB
2 phase [
32]. These findings are in agreement with the XRD results (
Fig. 1b). The energy dispersive X-ray spectroscopy (EDS) mapping (
Fig. 2d) of the ZrB
2 sample reveals a uniform distribution of the elements Zr (green) and B (red). A small amount of oxygen (O) elements is also observed on the surface of the ZrB
2 sample, which may be attributed to surface oxidation when exposed to air. To further investigate the chemical states of the elements in the ZrB
2 sample, X-ray photoelectron spectroscopy (XPS) spectra were analyzed, with the results shown in
Figs. 2e and
f, and Fig. S4 (Supporting information). The high-resolution XPS spectrum of Zr 3d (
Fig. 2e) consists of four peaks. The binding energies at 178.7 eV (Zr 3d
5/2) and 181.2 eV (Zr 3d
3/2) correspond to Zr-B bonds in ZrB
2, while the other two peaks located at 183.0 eV (Zr 3d
5/2) and 185.5 eV (Zr 3d
3/2) are attributed to Zr-O bonds of ZrO
2 [
31,
33,
34]. The B 1s XPS spectrum (
Fig. 2f) can be resolved into two peaks. The peak at approximately 187.5 eV is assigned to B-Zr bonds in ZrB
2, while the peak at 187.9 eV belongs to B-B bonds [
31,
33,
35]. In the O 1s spectrum (Fig. S4), the peak with a binding energy of 531.8 eV corresponds to O-Zr bonds in ZrO
2 [
31,
34], which may come from the surface oxidation of the ZrB
2 sample in air, consistent with the EDS mapping result (
Fig. 2d). Moreover, XPS spectra of other metal diborides are presented in Figs. S5-S12 (Supporting information), respectively. The above results indicate highly quality AlB
2-type metal diborides bulks can be synthesized using the HPHT method, accompanied by slight surface oxidation when exposed to air. This distinctive structure confers special physical and chemical properties upon them, potentially enhancing their effectiveness in facilitating electrocatalytic reactions [
36].
To assess the catalytic performance of as-synthesized metal diborides for the electrocatalytic reduction of CO
2, a series of electrochemical tests were conducted in a H-type cell employing a 1 mol/L [Bmim]PF
6-containing acetonitrile ([Bmim]PF
6(1M)-MeCN) solution as the electrolyte. In this study, the metal diborides, including TiB
2, ZrB
2, HfB
2, VB
2, NbB
2, TaB
2, CrB
2, MnB
2, and MoB
2, formed integral bulk materials, which were directly utilized as self-supporting electrodes for the electrocatalytic reduction of CO
2. The controlled potential electrolysis was initially carried out over different metal diborides at −2.2 V
vs. Ag/Ag
+ in CO
2-saturated [Bmim]PF
6(1M)-MeCN electrolytes. The products were detected by gas chromatography (GC) and nuclear magnetic resonance (NMR) spectroscopy. Upon analysis, it was found that the main gaseous products on these metal diborides were CO and H
2, with no liquid products being generated (
Fig. 3a). At −2.2 V
vs. Ag/Ag
+, the ZrB
2 electrode exhibited a CO Faradaic efficiency of 92.2%, significantly outperforming other metal diborides. Meanwhile, the current densities of different electrodes were normalized according to their geometric surface areas. In
Fig. 3a, the ZrB
2 electrode achieved a total current density of 51.5 mA/cm
2, which was 3.4, 3.4, 2.5, 2.1, 4.4, 4.7, 1.8, and 3.9 times higher than those of TiB
2, HfB
2, VB
2, NbB
2, TaB
2, CrB
2, MnB
2, and MoB
2 electrodes, respectively. These results suggest that the type of metal elements in the AlB
2-type metal diborides has a significant impact on the electrochemical reduction of CO
2 to CO. Meanwhile, linear sweep voltammetry (LSV) curves of the ZrB
2 electrode were recorded in Ar- or CO
2-saturated electrolytes (Fig. S13 in Supporting information), which indicated that the ZrB
2 electrode exhibits the ability to catalyze CO
2 reduction. In addition, to confirm the carbon source of CO product on the ZrB
2 electrode, the controlled potential electrolysis experiment was conducted under the same conditions, except that the CO
2 atmosphere was replaced with the Ar atmosphere. From Fig. S14 (Supporting information), it can be observed that no CO was detected under the Ar atmosphere, indicating that CO primarily originated from the reduction of CO
2. In a more comprehensive investigation, the relationship between the current density (or CO Faradaic efficiency) and the applied potential was analyzed for each metal diboride over a potential range from −2.0 V to −2.5 V
vs. Ag/Ag
+ (
Fig. 3b, Figs. S15 and S16 in Supporting information). When the applied potential was shifted negatively, the current densities over various metal diborides exhibited increasing trends (
Fig. 3b and Fig. S15), and the Faradaic efficiencies of CO on different metal diborides followed volcano plots (
Fig. 3b and Fig. S16). Impressively, the ZrB
2 electrode demonstrated an outstanding CO Faradaic efficiency of 92.2% at a potential of −2.2 V
vs. Ag/Ag
+, accompanied by a current density of 51.5 mA/cm
2 (
Fig. 3b). As the applied potential decreased to values less than −2.2 V
vs. Ag/Ag
+, the CO Faradaic efficiencies on the ZrB
2 electrode correspondingly diminished. As shown in Figs. S15 and S16, only the MnB
2 electrode achieved the maximum CO Faradaic efficiency (74.7%) at −2.2 V
vs. Ag/Ag
+, with corresponding current density of 34.9 mA/cm
2. The maximum CO selectivity at the surfaces of HfB
2 (72.0%), VB
2 (61.2%), NbB
2 (51.9%), and CrB
2 (67.0%) electrodes was observed at −2.3 V
vs. Ag/Ag
+, with corresponding current densities of 49.5, 27.9, 43.5, and 27.7 mA/cm
2, respectively. Meanwhile, the highest CO Faradaic efficiencies on TiB
2, TaB
2, and MoB
2 electrodes were 72.6%, 84.8%, and 82.4% at −2.4 V
vs. Ag/Ag
+, respectively. Although all of these metal diborides had the ability to electrocatalytically convert CO
2 into CO, the ZrB
2 electrode can efficiently facilitate this conversion and achieve the highest CO Faradaic efficiency (92.2%) at a relatively lower applied potential (−2.2 V
vs. Ag/Ag
+) compared to other metal diborides, indicating that the ZrB
2 electrode was more favorable for the electrocatalytic reduction of CO
2 to CO.
To further investigate the practicality of the ZrB
2 electrode, we conducted long-term stability testing in [Bmim]PF
6(1M)-MeCN electrolytes at a potential of −2.2 V
vs. Ag/Ag
+. Considering the volatilization of MeCN and the accumulation of carbonaceous compounds on the ZrB
2 electrode surface during the electrolysis experiment, the electrolyte was changed and the electrode surface was polished by diamond griding disk every 5–7 h. It is evident from
Fig. 3c that the current density and CO Faradaic efficiency remained relatively stable over the 61-h electrolysis period. Combining the SEM image and XPS spectra of the used ZrB
2 electrode (Fig. S17 in Supporting information), we discovered the good stability of the ZrB
2 electrode in effectively catalyzing the electroreduction of CO
2 to CO over prolonged operational periods. Despite the relatively stable current density maintained over the 61-h electrolysis period, we observed minor fluctuations in the current density for the electrocatalytic reduction of CO
2 with the electrolysis time. These fluctuations might be linked to factors such as the replacement of the electrolyte and the polishing of the electrode surface. Furthermore, slight variations in the charge-transfer resistance (
Rct) of the ZrB
2 electrode before and after the CO
2 electrolysis, as revealed by electrochemical impedance spectroscopy (EIS) measurements, could also contribute to changes in the current density [
37]. As shown in Fig. S18 (Supporting information), the ZrB
2 electrode demonstrated relatively low
Rct values both before and after CO
2 electrolysis. This suggested that the ZrB
2 electrode possessed favorable electronic transfer kinetics, thereby facilitating the electrocatalytic reduction of CO
2. Moreover, a slight decrease in the
Rct values of the ZrB
2 electrode was observed from 3.2 Ω pre-electrolysis to 2.2 Ω post-electrolysis conditions, indicating a minor reduction in
Rct values that could influence the electrocatalytic performance.
To better demonstrate the advantages of the self-supporting ZrB
2 electrode, we prepared a comparative ZrB
2 powder as a control sample. The ZrB
2 powder was drop-casted onto carbon paper to fabricate a conventional electrode, designated as the p-ZrB
2 electrode. In Fig. S19a (Supporting information), the current density and CO Faradaic efficiency of the p-ZrB
2 electrode were lower than those of the self-supporting ZrB
2 electrode across the entire potential range, primarily due to the adverse effects of the Nafion binder required for its preparation. The binder might not only induce aggregation of ZrB
2 particles but also block active sites, thereby impairing the electrocatalytic performance of the CO
2 reduction. Moreover, the p-ZrB
2 electrode demonstrated limited stability (Fig. S19b in Supporting information), maintaining the CO Faradaic efficiency and current density for only 3 h, as the crushed ZrB
2 sample with relatively large particles tended to detach from the electrode surface during the electrolysis. Further EIS measurements (Fig. S19c in Supporting information) revealed that the superior performance of the self-supporting ZrB
2 electrode might correlate with its lower
Rct value, which facilitated faster electron transfer rates and consequently enhanced the CO
2 reduction process. To the best of our knowledge, the stability and current density for the efficient electrocatalytic reduction CO
2 to CO observed on the ZrB
2 electrode surpasses most recently reported state-of-the-art B-containing electrocatalysts (
Fig. 3d and Table S4 in Supporting information) [
9-
13], which is beneficial for the industrial application and development of CO
2 electroreduction. Meanwhile, the performance of Zr-containing electrocatalysts for the electrocatalytic reduction of CO
2 is also shown in Table S5 (Supporting information). It can be observed that the primary product of these Zr-containing electrocatalysts for this reaction was mainly CO, with the exception of the bimetallic Cu-Zr electrocatalyst (ZrO
2/Cu-Cu
2O) [
38], whose main product was ethylene (C
2H
4). Compared to Zr-containing electrocatalysts that produced CO, the ZrB
2 electrode exhibits superior electrocatalytic performance. In addition, the ZrB
2 electrode displayed better stability compared to the transition metal compounds reported in the literature (Table S1).
It is widely recognized that the composition of the electrolyte plays a significant role in regulating the catalytic activity and product distribution of the electrocatalytic reduction of CO
2. In this study, we first evaluated the catalytic performance of the ZrB
2 electrode in an aqueous solution with potassium bicarbonate (KHCO
3, 1 mol/L) as supporting electrolyte and a non-aqueous electrolyte, specifically an MeCN solution with a supporting electrolyte of tetrabutylammonium hexafluorophosphate (TBAPF
6(1M)-MeCN). In 1 mol/L KHCO
3 aqueous electrolyte, the ZrB
2 electrode exhibited almost no catalytic activity towards CO
2 reduction, with the main product being H
2. It can be seen in
Fig. 4a that the Faradaic efficiency of H
2 over the ZrB
2 electrode was approximately 100.0% at all applied potential. In contrast, the highest CO Faradaic efficiency for the ZrB
2 electrode was 64.1% at −2.5 V
vs. Ag/Ag
+ in TBAPF
6(1M)-MeCN electrolytes, with a current density of 11.7 mA/cm
2 (
Fig. 4b). The high catalytic activity and selectivity of CO observed in the TBAPF
6(1M)-MeCN electrolyte compared to 1 mol/L KHCO
3 electrolyte suggest that the non-aqueous solution containing TBAPF
6 contributes to enhancing the catalytic performance of the ZrB
2 electrode. Based on this, we endeavored to utilize the ZrB
2 electrode in non-aqueous electrolytes to investigate its electrocatalytic performance for CO
2 reduction. In non-aqueous electrolytes, ionic liquids are commonly used as a supporting electrolyte for the electrocatalytic reduction of CO
2, especially those including imidazole cations. These ionic liquids can regulate the adsorption of CO
2 and its intermediates, thereby changing the catalytic activity of the electrode and achieving a co-catalytic effect [
39,
40]. Thus, the catalytic activity of the ZrB
2 electrode was further tested in MeCN solutions consisting of imidazole ionic liquids, including [Bmim]PF
6, 1‑butyl‑3-methylimidazolium perchlorate ([Bmim]ClO
4), 1‑butyl‑3-methylimidazolium acetate ([Bmim]OAc), 1‑butyl‑3-methylimidazolium nitrate ([Bmim]NO
3), and 1-ethyl-3-methylimidazolium hexafluorophosphate ([Emim]PF
6) (
Fig. 4c). The LSV curves in Fig. S20 (Supporting information) show that the ZrB
2 electrode exhibited a higher catalytic activity for CO
2 electroreduction in the [Bmim]PF
6(1M)-MeCN electrolyte compared to electrolytes containing other ionic liquids. In
Fig. 4c, the current densities and CO Faradaic efficiencies in [Bmim]PF
6(1M)-MeCN and [Emim]PF
6(1M)-MeCN electrolytes at −2.2 V
vs. Ag/Ag
+ were higher than those in TBAPF
6(1M)-MeCN electrolyte, indicating that ionic liquids with imidazole cations in the electrolytes could promote the generation of CO. In the [Emim]PF
6(1M)-MeCN electrolyte, the CO Faradaic efficiency (88.7%) and total current density (39.2 mA/cm
2) were notably lower than those in the [Bmim]PF
6(1M)-MeCN electrolyte. This discrepancy may be attributed to the cation variation in the ionic liquids, influencing the solubility of CO
2 and thus modulating the catalytic performance of the electrocatalytic reduction of CO
2 [
41-
43]. Furthermore, substituting the anions in the [Bmim]PF
6 with ClO
4−, OAc
−, and NO
3− resulted in decreased reaction kinetics and CO Faradaic efficiency on the ZrB
2 electrode. This result could be a consequence of these anions altering the properties of the electric double layer near the surface of the ZrB
2 electrode, thereby decreasing the rate of CO generation [
44]. Meanwhile, the strong association between the PF
6− anion and the CO
2 molecule can improve the solubility of CO
2. Based on the above results, it can be concluded that the supporting electrolyte [Bmim]PF
6 was beneficial for the electrocatalytic reduction of CO
2. The perfect combination of an MeCN solution with a supporting electrolyte of [Bmim]PF
6 and the ZrB
2 electrode may promote CO
2 adsorption, which is crucial for effective CO
2 electroreduction.
Fig. 4d also displays the impact of varying concentrations of [Bmim]PF
6 in the electrolyte on the electrocatalytic activity for the CO
2 electroreduction reaction using the ZrB
2 electrode at −2.2 V
vs. Ag/Ag
+. In the pure acetonitrile electrolyte, only trace amounts of CO were detected with negligible current density. This was due to the inherently low ionic conductivity of acetonitrile as a non-aqueous solvent, which severely limited charge transport and impeded the kinetics of the electrocatalytic reduction of CO
2. As [Bmim]PF
6 concentration increased (< 1 mol/L), both current density and CO Faradaic efficiency showed progressive enhancement, attributable to improved solution conductivity through ionic dissociation ([Bmim]
+ and [PF
6]
−) and facilitated charge transfer processes. However, exceeding 1 mol/L of [Bmim]PF
6 in the electrolyte led to declining performance metrics, primarily due to increased solution viscosity and intensified ion-pair ([Bmim]
+ and [PF
6]
−) interactions that collectively impeded mass transport and charge transfer kinetics. These observations established the optimal concentration of [Bmim]PF
6 was 1 mol/L, effectively enhancing the current density and CO Faradaic efficiency of the electrocatalytic CO
2 reduction.
In order to delve deeper into the potential reaction pathway for the electrocatalytic reduction of CO
2 to CO,
in-situ attenuated total reflection surface-enhanced infrared reflection spectroscopy (ATR-SEIRS) was utilized to identify the reaction intermediates on the ZrB
2 electrode (
Fig. 4e). The spectra were obtained within the potential range of −1.8 V to −2.2 V
vs. Ag/Ag
+, using the measurement at open circuit potential (OCP) as the reference. It is noticeable that no vibration peak is observable in the spectra of the ZrB
2 electrode at OCP. In the potential range of −1.8 V to −2.2 V
vs. Ag/Ag
+, newly emerged peaks at ~1710 cm
−1 could be assigned to the C=O stretching of the *COOH intermediate [
45-
49] during the electrocatalytic reduction of CO
2. Meanwhile, the peaks observed at ~2090 cm
−1 corresponded to *CO species, with their weak intensities possibly resulting from the rapid consumption of *CO for the formation of CO [
50]. Moreover, the prominent characteristic peaks at ~2345 cm
−1 are attributed to the adsorbed CO
2 on the surface of the ZrB
2 electrode. As the applied potential decreased, the intensity of these peaks gradually strengthened, indicating an increase in the consumption of the adsorbed CO
2 [
51]. Based on the above results, potential reaction pathway for the electrocatalytic reduction of CO
2 to CO on the ZrB
2 electrode can be speculated as follows: (1)
* + CO
2 →
*CO
2; (2)
*CO
2 + H
+ + e
− →
*COOH; (3)
*COOH + H
+ + e
− →
*CO; (4)
*CO →
* + CO, where
* represents the adsorption site on the surface of the ZrB
2 electrode.
DFT calculations were also carried out to clarify the intrinsic activity for the electrocatalytic performance in CO
2 reduction on the ZrB
2 surface. The B-terminated ZrB
2 (001) and Zr-terminated ZrB
2 (001) were utilized as model electrocatalysts to explore the active sites of the ZrB
2 electrode for the electroreduction of CO
2 (Figs. S21 and S22 in Supporting information). In Fig. S23 (Supporting information), we found that the desorption of *CO is an endergonic process on both the B-terminated ZrB
2 (001) and Zr-terminated ZrB
2 (001) surfaces. Compared to the B-terminated ZrB
2 (001) model (1.84 eV), the Zr-terminated ZrB
2 (001) model exhibits a lower energy barrier for *CO desorption (0.76 eV) suggesting that metal edge sites of the ZrB
2 (001) surface can enhance *CO desorption, thereby promoting the formation of CO. To further validate the role of metal edge sites in the ZrB
2 electrode, the energy barriers for *CO desorption on the ZrB
2 (101) and ZrB
2 (100) surfaces, which can be observed in the XRD and TEM results (
Figs. 1b,
2b and
2c), were also investigated. The results in
Fig. 4f further demonstrate that the Zr-terminated ZrB
2 surface can facilitate *CO desorption compared to the B-terminated ZrB
2 surface, indicating that Zr sites in the ZrB
2 electrode are the primary active sites for the electrocatalytic reduction of CO
2 to CO. Moreover, the thermodynamic limiting potentials for the electrocatalytic reduction of CO
2 (
UL(CO
2)) and HER (
UL(H
2)) on the Zr-terminated ZrB
2 (001) are shown in Fig. S24a (Supporting information). The difference (Δ
UL) between
UL(CO
2) and
UL(H
2) is a positive value, which means a higher selectivity of the electrocatalytic reduction of CO
2 [
52]. This is also consistent with experimental findings (
Fig. 3b). These results indicate that the metal sites on the ZrB
2 (001) surface can lower the desorption energy of *CO intermediates, suppress the HER, and ultimately enhance the activity and selectivity for the electrocatalytic reduction of CO
2 to CO.
In conclusion, we have successfully developed a range of bulk metal diborides through the HPHT method, utilizing them as self-supporting electrodes for the electrocatalytic reduction of CO2 in ionic liquid-based electrolytes. The as-obtained ZrB2 electrode demonstrated outstanding electrocatalytic performance in the conversion of CO2 to CO, achieving an impressive Faradaic efficiency for CO of up to 92.2% at −2.2 V vs. Ag/Ag+. More importantly, the ZrB2 electrode also exhibited extraordinary stability, lasting up to ~60 h. Mechanistic investigations corroborated that metal sites on the ZrB2 (001) surface played multiple roles of facilitating the desorption of *CO intermediates, inhibiting the HER, thereby accelerating the formation of the CO product. The superior electrocatalytic performance of AlB2-type metal borides positions them as highly promising candidates for CO2 conversion applications, thereby likely to spur the progression and exploration of other metal borides in the field of CO2 electroreduction.