1 Introduction
Nitrogen is an important component of the basic units of protein, enzyme, nucleic acid, and so on [
1–
3]. Although nitrogen accounts for about 78% of air, because of its strong ties, electronegativity and ionization characteristics, such natural resource cannot be used directly by most of the organisms, so a sustainable development route to obtain fixed nitrogen compounds like ammonia is necessary to serve human society from development of agricultural fertilizer to safety of energy storage [
4,
5]. In the industrial field, a large scale of ammonia synthesis is achieved by Haber–Bosch process. This process needs to burn a large number of fossil fuels to supply heat energy and emits a large amount of carbon dioxide, which intensifies the greenhouse effect of the earth [
6–
9]. Therefore, it is urgent to develop a new route of ammonia synthesis under mild conditions for energy conservation and environmental protection [
10–
13]. Electrocatalytic nitrogen reduction can theoretically be carried out at room temperature and atmospheric pressure, and the raw materials (water and nitrogen) are widely sourced in nature, which brings an opportunity to achieve the green synthesis of ammonia under mild conditions [
14–
16]. However, due to the difficulty of activation and fracture of N≡N triple bond and the low solubility of nitrogen, the electro-reduction of nitrogen is very difficult to be carried out in thermodynamics and kinetics [
17–
20]. Moreover, the existence of hydrogen evolution competition reaction will consume part of electrons and further lead to lower efficiency and selectivity of electrocatalytic nitrogen reduction reaction (NRR). Therefore, how to improve the selectivity of electrocatalytic NRR and then improve the efficiency of ammonia synthesis is a major challenge for the electrochemical synthesis of ammonia at room temperature and atmospheric pressure [
21–
23].
Generally, the catalyst is the key factor for the efficient electrocatalytic NRR under ambient conditions. Heterojunction and defect engineering located at heterogeneous structure interfaces are often considered active sites that promote charge separation and electron transfer during reactions. Noble-metal catalysts (Au, Pd, Rh and Ru) [
24–
27] demonstrate favorable catalytic activities on NRR, but limited resources and high cost hinder large-scale industri-alization. Nowadays, metal oxides are receiving increasing attention as promising alternative NRR catalysts due to their availability and respectable catalytic activities. Metal oxide interface plays an important role in improving catalytic activity due to the strong interface interaction. It can improve the stability of active sites for molecular activation [
28]. It has been verified in carbon dioxide reduction [
29,
30], methanol oxidation [
31,
32], and ammonia synthesis [
33]. Meanwhile, oxygen atoms on the surface of oxide catalysts are dug and squeezed by various physical and chemical methods to forming OVs with a positive charge, so as the electrons captured by the OVs can be injected into the anti-bonding orbit of N
2, which weakens the N≡N triple bond, reduces the reaction energy barrier and restrains the hydrogen evolution reaction. Therefore, the performance of NRR can be improved by the injection of OVs [
34–
36]. It is a good strategy to design a composite material with heterojunction interface effect and vacancy effect. The valence states of TiO
2 transition elements are +4. With the change of external conditions, they are easy to form low valence state, such as Ti
3+, thus exposing OVs [
37,
38]. In recent years, TiO
2, as the most common semiconductor material, has been widely used in energy-related research. TiO
2 [
39–
45] has been reported that it has a good performance in electrocatalytic nitrogen fixation, however, due to the weakness of its conductivity and ability to transmit electric charge, it needs to be doped or modified to reverse these disadvantages. On the other hand, the atomic number of Bi in the periodic table of elements is 83, Bi-related semiconductor materials express the advantages of good conductivity, low price and in-nocuity. Due to the higher adsorption free energy base between Bi and H
2, Bi is a material with low activity of hydrogen evolution reaction. Bi 6p band and N 2p orbit of interaction between N
2 selective adsorption on the surface could help for N≡N dissociation, so Bi or Bi-based material should be material has superior performance in electrocatalysis nitrogen fixation [
46,
47]. As a Bi-based semiconductor material, BiVO
4 can easily form defective oxygen vacancies on the surface, and its low-coordination V atoms are spin-polarized, which helps the activation and cleavage of N
2 molecules.
Therefore, we synthesized a BiVO
4/TNT heterojunction composite with oxygen vacancy and applied it for N
2 fixation. Firstly, a two-step electrochemical method is used to synthesize TiO
2 nanotubes on Ti foil. Then BiVO
4 is loaded on the TiO
2 nanotubes by hydrothermal method. TiO
2 nanotubes provide more reaction attachment sits concentrated on OVs, while BiVO
4 [
48,
49] optimizes the conductivity of composite and promotes electron transport. so that the catalytic performance of the composite is expected to be improved. BiVO
4 is supported on the surface of TNT to form a heterojunction with a synergistic effect between these two components [
33], which retains the respective properties.
In this paper, we use electrochemical oxidation method to synthesize TiO2 nanotubes with a very uniform tubular structure. Through the hydrothermal method, BiVO4 is loaded on TiO2 nanotubes, and the composite as electrode has relatively high efficiency and stable electrocatalytic nitrogen fixation performance. The electrochemical test shows that BiVO4/TNT have higher ammonia yield of 8.54 µg·h−1·cm−2 and higher Faraday efficiency (FE) of 7.70% in –0.8 V vs. RHE in 0.1 M Na2SO4 solution.
2 Experiment
2.1 TiO2 nanotube preparation
2.5 cm ×1.5 cm titanium foil was cleaned by acetone, ethanol and water separately. Then the Ti foil was dried with nitrogen and further anodized in the solution of 98 mL glycol, 0.33 g NH4F and 2 mL deionized water for the first time. The graphite plate was used as the opposite electrode. The reaction was under 60 V for 4 hours. Then the Ti foil was took out and washed by water and ethanol, and further dried in the air. The TiO2 film can be removed by ultrasonic method. The remaining Ti foil was anodized for the second time, under 50 V. After oxidized in the electrolyte for 1.5 h, high-quality TiO2 nanotubes were obtained on the Ti foil substrate (called TNT).
2.2 BiVO4/TNT preparation
Firstly, 0.03 M BiNO3·5H2O was dissolved in 30 mL 1 M nitric acid solution (solution 1), 0.05 M NH4VO3 was dissolved in 30 mL 1 M NaOH solution (solution 2). Then solution 2 was added into solution 1 drop by drop; secondly, TNT was placed on the bottom of 100 mL Teflon-lined stainless-steel autoclave, and the obtained mixed solution was transformed to the autoclave. The reaction conducted at 180◦C for 24 h. After cooling down to room temperature, the product was washed with ethanol and water, and then dried to obtain BiVO4/TNT. The scheme of synthesis procedure is shown in Fig. 1.
3 Characterization
X-ray diffraction (XRD) patterns of the prepared TNT and BiVO4/TNT are shown in Fig. 2(a). For the XRD of TNT, the main peak angles at 25.28, 48.05, 53.89 and 55.06 respectively correspond to (101), (200), (105) and (211) crystal faces of TiO2 (JCPDS Card No.21- 1272), while the main peak angles at 35.09, 38.42 and 40.17 respectively correspond to (100), (002) and (101) of Ti (JCPDS Card No.44-1294). Compared with pure TNT, BiVO4/TNT has two smaller peaks at diffraction angles of 18.67 and 28.82, which correspond to (110) and (−121) of BiVO4 (JCPDS Card No.14-0688). It indirectly proves that BiVO4 was loaded on TNT successfully. The morphologies and structures of the obtained BiVO4 and BiVO4/TNT were characterized by TEM and SEM Figs. 2(b) and (c) are the BiVO4 TEM and HRTEM images. From Fig. 2(b), it can be seen that the pure BiVO4 has a block structure with a length between 1– 2 µm. Figure 2(c) shows that the two different lattices spacing of BiVO4 are 0.26 nm and 0.31 nm, respectively, which correspond to its crystal planes of (200) and (– 121). Figures 3(a) and (b) show the SEM images of TNT. Figure 3(a) indicates that the TNT has a very uniform tubular structure with small holes which their diameters are about 100 nm. Figure 3(b) is the cross-section view of TNT, which confirms that the length of nanotubes is around 5 µm. Figure 3(c) indicates flake-like BiVO 4 loaded on TNT surface while Fig. 3(d) reveals the topography of the joint of BiVO4 and TNT, and further formed a connection structure.
In order to investigate the elemental constitutes and oxidation states of the composite, X-ray photoelectron spectroscopy (XPS) was applied to analyze the BiVO4/TNT sample. Figure 4(a) shows the full XPS peaks of BiVO4/TNT, including the elements of Bi, V, O and Ti. Figure 4(b) spreads the diffraction peak of Ti 2p, with the peak positions of 458.4 eV and 465.2 eV. Figure 4(c) shows the diffraction peak of Bi 4f, with the peak positions of 158.6 eV and 164.0 eV. Figure 4(d) reveals the diffraction peak of V 2p, with the peak positions of 516.6 eV and 524.1 eV. Figure S1 shows the XPS of TNT, including the elements of O and Ti. The O 1s peaks of BiVO4/TNT and TNT are shown in Figs. 5(a) and (b), where 529.6 eV represents lattice oxygen and 531.2 eV stands for oxygen vacancies. After normalized the O 1s peaks, it can be seen from Fig. 5(c) that BiVO4/TNT has more oxygen vacancies than the pure TNT, thus meaning that the composite can provide more active sites for the reaction.
4 Electrochemical performance test
The electrocatalytic properties of NRR were studied systematically in 0.10 M Na2SO4 by the aqueous solution of air tight H-cell. The anode chamber and cathode chamber containing 30 mL electrolyte solution were separated by Nafion 117 membrane. Then, BiVO4/TNT was used as the working electrode of electrocatalytic NRR. Nitrogen gas (99.999%) was firstly bubbled into the cathode chamber for 30 min (50 mL·min−1) Then, the bubbling rate was changed into a constant flow rate of 20 mL·min−1 during the whole electrolysis process, as shown in Fig. S2. During the whole measurement process, magnetic stirring maintained 400 rpm/min in the cathode chamber. Two glass vials containing 5 mL 0.05 M H2SO4 were used to connect with the cathode chamber to trap the escaped ammonia and prevent the contamination from the air, respectively.
The potential dependence of electrocatalytic NRR activity of the BiVO4/TNT was investigated firstly. As shown in Fig. 6(a), the linear sweep voltammograms (LSV) curves of the catalyst in 0.10 M Na2SO4 electrolyte Ar-saturated or N2-saturated 0.10 M Na2SO4 electrolyte are measured successively with the same working electrode. Under the condition of Ar and N2 saturation, the cathode current begins to appear at about−0.6 V vs. RHE, while the higher current density can be clearly seen in the N2 saturated electrolyte, indicating the additional contribution of NRR and the BiVO4/TNT possesses catalytic activity for the NRR. According to the polarization curve and deflection potential, the suitable potential window range of electrocatalytic NRR is−0.6 V to−1.0 V vs. RHE. After electrolysis for 2 hours at a specific potential of−0.6 V to−1.0 V vs. RHE, the generated NH3 was quantitatively determined by indophenol blue method.
Figure 6(b) shows the i–t curves of electrode decorated BiVO4/TNT at different applied potentials, the steady current density in NRR test explains that the catalyst has good chemical stability. The output of ammonia was studied by UV-Vis absorption spectrum of the electrolyte for 2 hours with indophenol blue indicator method. Figure 6(c) shows the UV absorption curve under different potentials, and the highest absorption intensity, which means the highest ammonia generation rate, was obtained under – 0.8 V vs. RHE. Furthermore, Fig. 6(d) shows the NH 3 yields and FEs of BiVO4/TNT under different potentials in N2-saturated solution. According to the UV absorption peak at 655 nm, the ammonia production rate under different applied potentials was calculated by comparing the measured ammonia standard curve (Figs. S1 and S2). The BiVO4/TNT composite has the highest ammonia production rate of 8.54 µg·h−1·cm−2 and higher FE (7.70%) under –0.8 V vs. RHE. It is worth noting that, with a more negative potential applied, the NH3 yield and FE were significantly reduced (–0.9 V vs. RHE). The reason is estimated that the effective adsorption sites of nitrogen are hindered by more protons. BiVO4/TNT has good selectivity in the electrocatalytic synthesis of ammonia. It can be proven according to Fig. S3 where is almost no hydrazine formation.
In order to verify that the source of ammonia is nitrogen rather than other possible nitrogen-containing substances, we conducted a series of control experiments to detect the ammonia yields, including air potential measurement (open circuit potential, OCP) under nitrogen flow, TNT measurement under nitrogen flow and BiVO4/TNT measurement under argon at –0.8 V vs. RHE. According to the UV absorption results, as shown in Fig. 7(a), there are almost no obvious peaks under OCP and Ar conditions. The production of ammonia indirectly proves that the source of nitrogen is nitrogen gas. On the other hand, the peak value of electrocatalytic nitrogen fixation of TNT is significantly lower than that of BiVO4/TNT, which further implies that the electrocatalytic nitrogen fixation performance of BiVO4/TNT is better than that of TNT. In Fig. 7(b), it is obvious that the ammonia yield of BiVO4/TNT is higher than that of pure TNT. In order to evaluate the stability of the catalyst, we repeated NRR tests six times under –0.8 V vs. RHE, as shown in Fig. 7(c). It can be seen that the ammonia production rate and FE are almost unchanged after 6 times tests. The ammonia yield is always around 8.5 µg·h−1·cm−2 and the FE is around 8%. For the i–t curve during the tests [Fig. 7(d)], the current densities were almost in a constant straight line, and the cycle current was almost unchanged. Notably, Fig. 7(e) indicates that the i–t curve nearly kept the same current within 12 h reaction, which further high-lighted the stability of the BiVO4/TNT catalyst. In addition, in Fig. 7(f), the N2-TPD curves show that the un-doped TNT and BiVO4/TNT displays two obvious different chemisorption peaks within the range of 100–700◦C, which could be due to the different N2 adsorption strength on the surface of the catalysts. The chemisorption peaks of BiVO4/TNT at 417◦C are higher than that of TNT (396◦C), which indicates that BiVO4/TNT heterostructure can effectively improve the chemisorption of N2 and subsequently makes the NRR performance.
In order to initially detect the catalyst’s activity of NRR, we also measured the LSV curves of TNT and BiVO
4/TNT in N
2-saturated electrolyte with a rotation rate of 600 rpm and a scanning rate of 5.0 mV·s
−1, as shown in Fig. 8(a). It can be seen that the current value of BiVO
4/TNT is higher than that of TNT at the same potential, which visibly confirms that the catalytic activity of BiVO
4/TNT is higher than the pure TNT. Figure 8(b) shows the impedance diagram of TNT and BiVO
4/TNT. Accordingly, a smaller impedance radius of BiVO
4/TNT means the smaller resistance value of BiVO
4/TNT than that of pure TNT, further confirming that the composite offers better performance for the electron transfer from the electrode to the decorated catalyst surface or interface. Figures 8(c) and (d) show the CV plots of BiVO
4/TNT and TNT at different scanning speeds from 10 mV/s to 50 mV/s, and the scanning area of BiVO
4/TNT is larger with the increasing of scanning rate. Figure 8(e) shows Tafel slopes of BiVO
4/TNT and TNT, in which BiVO
4/TNT presents a slope of 12.61 mF·cm
−2, being slightly higher than that of TNT (7.51 mF·cm
−2), which further supports that BiVO
4/TNT composite is more suitable for NRR. Based on the above analysis and the steps of nitrogen reduction summarized by predecessors [
50], a possible NRR mechanism of BiVO
4/TNT has been proposed in Fig. 9: (i) TNT, due to its porous structure, can strongly combine with BiVO
4, to form BiVO
4/TNT heterojunction; (ii) oxygen vacancies in BiVO
4/TNT promote N
2 adsorption and reduction when protons have been co-adsorbed; and (iii) continuous adsorption of H protons from the electrolyte can attack and destroy the N≡N bond, resulting the final formation of ammonia. Clearly, porous TNT serves as the substrate to host BiVO
4 and active site to provide H-sources for NRR over the interface, and BiVO
4 can fix N
2 and boost its reduction.
To study the reasons promoting the nitrogen fixation on the interface of BiVO4/TNT from the view of electronic structure, a first-principles calculation is carried out (the detailed calculation settings are introduced in supporting information). The relaxed interface structure (heterojunction) is shown in Fig. 10(a) and the charge distribution of heterojunction is shown in Fig. 10(b) in order to provide a straightforward observation of the electronic structure.
To make a detailed analysis on the electronic structure of BiVO4/TiO2 interface, the Bader analysis is adopted to calculate the charge (or “captured” electrons) of each atom. It is found that, for the same element, the charge of each atom in BiVO4/TiO2 heterojunction distribute on a wide range rather than varying slightly along with a certain value. To make this clear, the charge of atoms in single phase and heterojunction are plotted in the same histogram. Considering that both BiVO4 and TiO2 contain element O, two histograms of O charge are plotted. The histograms are shown in Fig. 11. It is notable that, although all the atoms in involved cells are counted, the different size between cells results in different number of counted atoms in histogram, which, however, does not influence our analysis since only the tendency of charge transfer is concerned.
According to Figs. 11(a) and (b), it can be deduced that the charge of O in TiO2 does not change much after becoming a heterojunction, but there is an obvious electron loss for O atoms in BiVO4. In contrast, as shown in Figs. 11(c)–(e), the metal elements Ti, Bi and V obtain some electrons after forming heterojunctions. Considering that the structures of BiVO4 and TiO2 are incoherent, there are massive defects along with their interface in heterojunction, generating many high-energy-electrons (active electrons). This is critical for catalysis activity, because the nitrogen fixation mechanism of metal atoms containing the process injecting the electrons into antibond of nitrogen. Since the metal atoms obtained additional active electrons when forming heterojunction, it is not surprised that the catalysis property of heterojunction is better than that of pure TiO2. Furthermore, the defected interface leads to the variation of local atom’s electronic properties, and some atoms with electronic properties benefiting catalysis become active sites. These phenomena will be further enhanced by OVs along with the interface, and OVs themselves act as active sites.
5 Conclusion
In this paper, we developed a facile method to synthesize a BiVO4/TNT catalyst which has a heterojunction interface with rich oxygen vacancies. Bismuth vanadate composite on TNT surface could form more oxygen vacancies and heterojunction structure between them, which not only provide a place for nitrogen adsorption, but also improve electron transfer ability and NRR catalytic activity, thus improving electrocatalytic nitrogen fixation performance. The synergistic effect of BiVO4 and TNT can obviously decrease the protons transition distance and the over-potential of the nitrogen fixation reaction. The BiVO4/TNT has a higher ammonia yield of 8.54 µg·h−1·cm−2 and higher FE of 7.70% at –0.8 V vs. RHE in 0.1 M Na2SO4 solution. This work could stimulate the rational designing of composite catalysts with heterojunction structure and rich oxygen vacancies.