Chang
Liu
a,
Yang
Yang
*a,
Xinyu
Li
a,
Jinfeng
Wang
a,
Xu
Jing
*a and
Chunying
Duan
ab
aSchool of Chemistry, Dalian University of Technology, 116024, China. E-mail: yangyang@dlut.edu.cn; xjing@dlut.edu.cn
bState Key Laboratory of Coordination Chemistry, Nanjing University, Nanjing, 210093, China
First published on 2nd June 2025
Electrocatalytic reduction of nitrite to ammonium (NO2RR) presents a promising approach for removing harmful NO2− and efficiently synthesizing ammonium but still faces difficulties, due to the complex six-electron transfer reaction, the formation of various by-products and competition from the hydrogen evolution reaction (HER). Herein, we constructed a metal–organic tetrahedral cage H1 (FeII4L6) with a large inner cavity and Fe metal centers surrounded by hydrazide groups that act as hydrogen bond acceptor sites. This enables the cage to efficiently recognise nitrite and thermodynamically activate it under electrocatalytic conditions for its efficient reduction to ammonium. The kinetic experiments demonstrated that the catalytic process followed the Michaelis–Menten mechanism, which further verified the key role of host–guest interactions in the mimetic activation of nitrite and the enzyme-like catalytic behavior.
Nitrogen, as a core element of Earth's living system, plays an irreplaceable role in maintaining ecological balance and the progress of human civilisation.12 Ammonium salts are high-value chemical raw materials widely used in the production of nitrogen-rich fertilizers and play a crucial role in various chemical reactions and industrial applications.13 Nitrite (NO2−) emissions from industrial production are a major source of water pollution and pose a significant threat to the environment.14 Electrocatalytic reduction of nitrite to ammonium (NO2RR) presents a promising approach for removing harmful NO2− and efficiently synthesizing ammonium.15,16 However, the NO2RR is a complex six-electron transfer process that involves the generation of multiple intermediates, often accompanied by by-products such as NO, N2O and N2H4.17–19 Additionally, the hydrogen evolution reaction (HER) competes with the NO2RR, which reduces the efficiency of the target reaction. This competition not only diminishes the catalyst's selectivity for the nitrite reduction reaction but also may lead to hydrogen gas as a by-product, further lowering overall catalytic efficiency.20–22 According to previous studies, MOCs, due to host–guest interaction properties, can efficiently regulate electron and proton transfer processes, recognize substrates through inclusion, and specifically activate certain substrates.23–25 Therefore, we speculate that metal–organic cages may exhibit unique catalytic advantages in the nitrite reduction reaction, enabling a highly efficient nitrite reduction process.
Herein, we have designed an Fe-based tetrahedral cage H1 (FeII4L6), formed through the self-assembly of iron(II) ions and organic ligands L containing hydrazide groups. The tetrahedral cage has a large inner space and amide groups evenly distributed around the metal site can act as hydrogen bond acceptors with the substrate. We hypothesize that the hydrogen-bond acceptor amide groups in the internal cavity of H1 can interact with nitrite to facilitate its activation. By introducing metal–organic domain-limited systems into the electrocatalytic reduction of nitrite to ammonium (NO2RR), host–guest interactions facilitate the rapid transfer of electrons and protons from the active sites to the substrates (Scheme 1). This strategy may provide new ideas for electrocatalytic reduction of nitrite to ammonium.
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| Scheme 1 The tetrahedral cage can selectively recognize nitrite and thermodynamically activate it, enabling efficient electrocatalytic reduction of nitrite to ammonium. | ||
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1), 0.1 M LiCl, 0.1 M NaNO2, and 0.1 mM H1. Before adding the 0.1 mM H1 catalyst, the cell was purged with argon gas for 20 minutes. After 6 hours of reaction, the yield of the target NH4+ was determined by UV-visible spectroscopy.
. CCDC 2429704.† The data were collected and reduced using APEX4 programs. The structure was solved using ShelXT and refined by full-matrix least-squares in ShelXL. Disordered anions and solvent molecules could not be modeled and were handled using the SQUEEZE routine in PLATON.26–28 The SQUEEZE process accounted for 8 OTF− anions, one diethyl ether molecule, approximately 8.5 DMF molecules, and 26.5 water molecules. The validity of the squeezed content was further supported by TGA. Although the data resolution and completeness are suboptimal, the connectivity and geometry of the core structure remain unambiguous.
The single crystal structural analysis revealed the formation of an FeII4L6 tetrahedral cage and H1 crystallized in the P
space group. The six ligands acted as the edges of the tetrahedral cage and each iron ion was coordinated to three different 2,2-bipyridine units in a mer position with three delocalized NN chelators, showing the robust geometry and high stability of H1. The adjacent Fe ions were separated by an Fe⋯Fe distance of about 22.4 Å. The cage was equipped with an internal cavity with a volume of about 1298.3 Å3, and a triangular window with a height of about 20.3 Å (Fig. 1b), indicating the ability of H1 for substrate encapsulation. The hydrazide groups embellished on the tetrahedral edges were supposed to offer the hydrogen bonding sites around the tetrahedral cage, which would benefit the interactions in the host–guest combination, enabling fast electron and proton transfer from the active sites to substrates.29
The 1H NMR spectrum showed a single set of ligand signals, evidencing the high symmetry of the H1 molecule. The complex exclusively contains low-spin iron(II) centres, as confirmed by sharp diamagnetic 1H NMR signals and its characteristic dark purple colour.30 The diffusion-ordered NMR spectrum (DOSY) showed that all resonances corresponded to a single species, with a diffusion coefficient of 5.01 × 10−11 m2 s−1 (Fig. 2a).
The ESI-MS spectrum of H1 (1.0 mM) in CH3CN solution exhibited an intense peak at m/z = 422.8595, corresponding to the [FeII4L6]8+ species, which proved the stability of H1 in solution and the presence of divalent iron ions in H1 (Fig. 2b). These results collectively verified the successful formation of the target cage structure with high purity.
The cyclic voltammogram (CV) of H1 in DMSO solution displayed quasi-reversible FeI/Fe0, FeII/FeI and FeIII/FeII couples at −1.46 V, −0.44 V and 0.27 V (vs. Ag/AgCl), respectively.31 Upon the addition of Et3N·HCl to the H1 solution, cyclic voltammograms showed new catalytic waves at approximately −1.16 V (vs. Ag/AgCl). The intensity of these waves increased linearly with increasing concentration of Et3N·HCl, indicating that the H1 hydrogen evolution reaction (HER) occurs at approximately −1.16 V (vs. Ag/AgCl) (Fig. S18 and S19, ESI†).
The cyclic voltammograms (CVs) showed the reduction potential of NO2− at near −1.4 V (vs. Ag/AgCl) (Fig. S16, ESI†). However, the addition of NO2− into the H1 solution at increasing concentrations caused new catalytic waves at approximately −1.3 V (vs. Ag/AgCl) besides the reduction potential of the cage itself. Notably, the catalytic wave exhibited a shift from −1.3 V (vs. Ag/AgCl) to near −1.1 V (vs. Ag/AgCl) as the NO2− concentration increased (Fig. 3d). This anode shifted reduction potential of the encapsulated NO2− compared with the free NO2− suggested that H1 could activate NO2− in a thermodynamic way and expand the interval between NO2− reduction and proton reduction, which may play a key role in the further selective electrocatalytic reduction of NO2−.23,32,33
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1) solution (Fig. S24 and S25, ESI†). Our catalytic performance was initially evaluated in a single-chamber electrochemical cell, where hydrophobic carbon paper served as the working electrode, an Ag/AgCl solid-state electrode was used as the reference electrode, and a graphite electrode with a diameter of 5.0 mm functioned as the counter electrode. Controlled potential electrolysis experiments were conducted using the H1 (0.1 mM) catalyst in a DMSO/MOPS (v/v = 2
:
1) solution containing 0.1 M LiCl as the electrolyte and 0.1 M NaNO2 as the guest molecules and carried out over 6 hours. The ammonium ion concentration was determined using a standard colorimetric method (Fig. S26 and S27, ESI†).36 Linear sweep voltammograms demonstrated a linear relationship between the current intensity of the reaction mixture and the NO2− concentration (Fig. 4b). The UV-vis absorption spectroscopy test on the electrolyte solution after the reaction and the XPS analysis of the hydrophobic carbon paper after the CPE indicated that the catalyst demonstrated excellent stability throughout the reaction process (Fig. S29 and S42, ESI†).
In order to fully analyse the products and by-products of the reaction process, we used a variety of analytical techniques. Gas chromatography (GC) and gas chromatography–mass spectrometry (GC–MS) were used to detect and analyse the gases produced during the reaction. The results showed that at an applied potential of −1.2 V, a small amount of hydrogen gas was generated (Fig. S33 and S34, ESI†). Immediately after electrolysis, all gases in the reaction chamber were purged into a sealed absorption system containing a diluted NaOH aqueous solution. The resulting solution was then analysed using ion chromatography (IC). The results showed no detectable formation of nitrogen oxide by-products (Fig. S31, ESI†). Furthermore, to probe for the potential formation of hydrazine (N2H4) as a side product, UV-vis spectroscopy was employed using the Watt and Christo method. The results indicated that no hydrazine was formed during the reaction (Fig. S32, ESI†). These findings confirm the high selectivity of the electrocatalytic reduction of nitrite by H1.
Under optimal conditions, the nitrite reduction reaction catalysed by H1 achieved a maximum faradaic efficiency of 35.1% and a TON of 856, and only NH4+ was detected as the reduction product, indicating its high selectivity. Moreover, the NH4+ yield reached 85.6%, with a production rate of 14.27 mM h−1 at an applied potential of −1.1 V (vs. Ag/AgCl). When the applied potential was increased from −0.9 V to −1.1 V (vs. Ag/AgCl), the NH4+ yield significantly increased from 56.3% to 85.6%, and the production rate increased from 9.43 mM h−1 to 14.27 mM h−1. Additionally, the TON value increased from 563 to 856, the faradaic efficiency slightly improved, and no hydrogen generation was detected. However, at −1.2 V (vs. Ag/AgCl), the NH4+ yield dropped to 70.5%, the conversion rate decreased to 11.75 mM h−1, and the TON decreased to 705, with only a trace amount of H2 observed (Fig. 4c and d). In addition, in the CPE experiment, the current remained stable, demonstrating that H1 remained stable in solution and maintained its catalytic performance over extended reaction periods without a decline in activity that could affect reaction efficiency.
To determine the source of nitrogen, isotope labeling experiments were conducted using Na15NO2 in the CPE experiment. In the 1H NMR spectrum of the treated reaction solution, two hydrogen signals were observed with a coupling constant of 75 Hz. In the 15N NMR spectrum, a clear signal was detected at 19.6 ppm. These isotope labeling experiments further confirmed that the nitrogen in the ammonium originates from nitrite (Fig. S35 and S36, ESI†).
Control experiments were performed under identical conditions. The mononuclear complex M1 was synthesized by reacting 2,2′-bipyridine with Fe(OTF)2. M1 closely resembles a vertex of tetrahedral cage H1, but M1 lacks the cavity microenvironment. The ESI-MS spectrum of M1 (1.0 mM) in CH3CN solution exhibited a prominent peak at m/z = 262.0872. Comparison with simulation based on natural isotopic abundance indicated that the peak corresponds to the [FeIIL′3]2+ species (Fig. S8, ESI†), demonstrating the physical phase purity and stability of M1. The coordination environments of the metal ions in M1 and H1 are identical. However, the FT-IR reflectance spectrum revealed no interaction between M1 and nitrite (Fig. S14, ESI†). The UV-vis spectroscopy titration experiments showed that no iso-absorption point was created between M1 and nitrite (Fig. S12, ESI†). The cyclic voltammograms showed that the addition of NO2− affected only the change in current, with no new catalytic waves produced (Fig. S22, ESI†). When M1 was used as a catalyst, the ammonium yield was found to be low, at only 14%. We deduce that the mononuclear compound M1, lacking a cavity-limited domain centre, cannot specifically recognize and activate nitrite, despite possessing a similar iron-reducing centre.
In contrast, no catalytic products were observed when Fe(OTF)2 and L were used as catalysts. It is likely that host–guest interactions within the inner cavity of the metal–organic tetrahedral cage H1 (primarily hydrogen bond acceptor sites and electrostatic interactions arising from the high cationic charge of H1) played a crucial role in the electrochemical catalytic conversion, rather than the simple FeII centres and amide group of L. Further comparative experiments also demonstrated that MOPS buffer and passage of argon gas were necessary for product detection (Table 1).
| Entry | Deviation from standard conditions | Yield (%) |
|---|---|---|
Standard conditions: H1 (0.1 mM) and NaNO2 (0.1 M) in DMSO/MOPS (v/v = 2 : 1) containing LiCl (0.1 M) for 6 h. Yields were determined using the standard colorimetric method. N.D. = not detected. |
||
| 1 | None | 85.6% |
| 2 | Under air | N.D. |
| 3 | No MOPS | N.D. |
| 4 | No stirring | 42% |
| 5 | Fe(OTF)2 | N.D. |
| 6 | L | N.D. |
| 7 | M1 instead of H1 | 14% |
When the concentration of NO2− was fixed and the concentration of H1 varied between 0.02 and 0.1 mM, the initial reaction rate increased with H1 concentration from 0.158 mM h−1 to 0.283 mM h−1, showing a first-order linear relationship (Fig. 5b).37 Kinetic studies of the reduction of NO2− to ammonium by H1 revealed that the catalytic process follows a primary reaction pathway. To further validate the catalytic process of NO2− reduction by the H1 electrocatalytic system as a mimicked enzyme catalysis, the reaction kinetics were studied under different applied potential conditions by varying the substrate concentration. The double reciprocal fitting of the initial reaction rate and the corresponding substrate concentration showed a linear relationship (Fig. 5c). Lineweaver–Burk analysis shows that under different voltages, the initial reaction rate exhibits saturation behaviour with respect to NO2− concentration.38 The fitting results align with the Michaelis–Menten mechanism in enzyme-catalysed reactions. The nearly identical Km (ca. 4.1 mM) across different applied potentials, along with the linear relationship between Kcat and applied potentials, supported the Michaelis–Menten mechanism.39 Therefore, we suggested that host–guest activation interactions, primarily hydrogen bonding and electrostatic interactions between the hydrogen-bonded acceptors and nitrite in the internal cavity of the tetrahedral cage H1, played a crucial role in thermodynamically activating and facilitating its efficient electrocatalytic reduction to ammonium (Fig. 5a).
Crystallographic data for H1 have been deposited at the CCDC under 2429704† and can be obtained from https://www.ccde.cam.ac.uk/structures.
Footnote |
| † Electronic supplementary information (ESI) available. CCDC 2429704. For ESI and crystallographic data in CIF or other electronic format see DOI: https://doi.org/10.1039/d5dt00766f |
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