RESEARCH ARTICLE

Electrocatalytic reduction of NO to NH3 in ionic liquids by P-doped TiO2 nanotubes

  • Shangcong Zhang 1,2 ,
  • Qian Liu 3 ,
  • Xinyue Tang 4 ,
  • Zhiming Zhou 4 ,
  • Tieyan Fan 4 ,
  • Yingmin You , 1,2 ,
  • Qingcheng Zhang , 4 ,
  • Shusheng Zhang 5 ,
  • Jun Luo 6 ,
  • Xijun Liu , 7
Expand
  • 1. College of Electrical and Electronic Engineering, Wenzhou University, Wenzhou 325035, China
  • 2. Low Voltage Apparatus Technology Research Centre of Zhejiang, Wenzhou University, Wenzhou 325035, China
  • 3. Institute for Advanced Study, Chengdu University, Chengdu 610106, China
  • 4. College of Chemistry and Materials Engineering, Wenzhou University, Wenzhou 325035, China
  • 5. College of Chemistry, Zhengzhou University, Zhengzhou 450000, China
  • 6. Tianjin Key Lab for Photoelectric Materials & Devices, School of Materials Science and Engineering, Tianjin University of Technology, Tianjin 300384, China
  • 7. State Key Laboratory of Featured Metal Materials and Life-cycle Safety for Compesite Structures, School of Resource, Environments and Materials, Guangxi University, Nanning 530004, China
yymfd@163.com
zhangqc@wzu.edu.cn
xjliu@tjut.edu.cn

Received date: 16 Sep 2022

Accepted date: 16 Oct 2022

Published date: 15 Jun 2023

Copyright

2023 Higher Education Press

Abstract

Designing advanced and cost-effective electrocatalytic system for nitric oxide (NO) reduction reaction (NORR) is vital for sustainable NH3 production and NO removal, yet it is a challenging task. Herein, it is shown that phosphorus (P)-doped titania (TiO2) nanotubes can be adopted as highly efficient catalyst for NORR. The catalyst demonstrates impressive performance in ionic liquid (IL)-based electrolyte with a remarkable high Faradaic efficiency of 89% and NH3 yield rate of 425 μg·h−1·mgcat.−1, being close to the best-reported results. Noteworthy, the obtained performance metrics are significantly larger than those for N2 reduction reaction. It also shows good durability with negligible activity decay even after 10 cycles. Theoretical simulations reveal that the introduction of P dopants tunes the electronic structure of Ti active sites, thereby enhancing the NO adsorption and facilitating the desorption of *NH3. Moreover, the utilization of IL further suppresses the competitive hydrogen evolution reaction. This study highlights the advantage of the catalyst−electrolyte engineering strategy for producing NH3 at a high efficiency and rate.

Cite this article

Shangcong Zhang , Qian Liu , Xinyue Tang , Zhiming Zhou , Tieyan Fan , Yingmin You , Qingcheng Zhang , Shusheng Zhang , Jun Luo , Xijun Liu . Electrocatalytic reduction of NO to NH3 in ionic liquids by P-doped TiO2 nanotubes[J]. Frontiers of Chemical Science and Engineering, 2023 , 17(6) : 726 -734 . DOI: 10.1007/s11705-022-2274-8

1 Introduction

Ammonia (NH3) is one of the most highly important artificial chemicals used in the industry that can act as an essential precursor for nitrogen fertilizers, medicine production, dyes, and so on. In contrast, nitric oxide (NO) is a primary air pollutant of great concern as it is directly related to many diseases and malfunctions [15]. In general, the fixation of molecular nitrogen (N2) to NH3 is a key step for the natural N2 cycle [610]. However, the strong and nonpolar N≡N bond makes the N2 molecule extremely stable and inert [11,12]. Accordingly, the industrial Haber−Bosch process requires a large amount of energy input and involves the emission of greenhouse gases as well [13,14]. In contrast, electrosynthesis powered by renewable electricity represents a promising approach for producing NH3 under ambient conditions and thus attracts significant research attention, in particular, for N2 reduction reaction (NRR) [1517]. However, the reported NH3 yield rate and Faradaic efficiency (FE) are obviously far away from the industrial requirements [18]. Therefore, development of more efficient electrocatalytic system toward NH3 production is highly desirable and demands systematic explorations.
Recently, some advances have been achieved in electrochemical denitration (that is, NO reduction reaction (NORR)) [11,12,19]; and metal [11], alloy [20], and sulfide [21] have been reported as potential NORR-active materials. Theoretically, NO exhibits lower cleavage energy and better solubility compared to N2, which is expected to be beneficial for more efficient electrosynthesis of NH3. For example, Peng et al. [12] used single niobium (Nb) atoms as superior NORR electrocatalyst under ambient conditions. Sun and coworkers [21] confirmed that MoS2 nanosheets could display a high NH3 yield rate of 281.1 μg·h−1·mgcat.−1 in acidic media. Noteworthy, the selective catalytic reduction technology has been widely adopted for NO abatement, which consumes massive NH3 and H2 [11,12]. In this case, NORR offers an appealing strategy for NO removal. Although the related improvements have been made, desirable NORR performance while largely suppressing competitive hydrogen evolution reaction (HER, in particular, at more negative potentials) has still not been achieved. In this regard, heteroatom doping has been regarded as an effective strategy to optimize electrochemical performance [6,2224]. Besides, electrolytes can also significantly affect the interfacial properties, and directly impact catalyst selectivity and overall activity [25,26]. Keeping these considerations in mind, herein it is inferred that the combination of catalyst-doping and electrolyte-optimization may be a feasible strategy to promote NORR.
In this study, phosphorus (P)-doped titania (TiO2) nanotubes (P-TNTs) were synthesized via a two-step approach. Further, it was found that these nanotubes exhibited a notably high NO-to-NH3 conversion with a maximum FENH3 of 89% and a corresponding yield rate of 425 μg·h−1·mgcat.−1 in an ionic liquid (IL)-containing electrolyte. Moreover, these nanotubes also exhibited impressive NORR durability over 10 cycles. The obtained performance metrics were found to be comparable to the best-reported results (see details in Table S1 (cf. Electronic Supplementary Material, ESM)). Density functional theory (DFT) was further used to verify that the introduction of P dopants could activate NO molecule and simultaneously accelerated the desorption of *NH3. Moreover, the usage of hydrophobic IL was able to effectively suppress the competitive HER. Accordingly, the catalyst-electrolyte engineering offers a novel strategy for the development of high-performance NORR catalysts as well as for other electrochemical reactions.

2 Experimental

2.1 Synthesis and characterizations

Preparation of P-TNTs and TNTs. Preparation was carried out following the literature method [27], briefly, TiO2 powder (3 g) was added to NaOH solution (50 mL, 10 mol∙L–1) in a polytetrafluoroethylene (PTFE, Teflon) beaker under vigorous stirring. The solution was placed in a PTFE-lined autoclave and heated for 22 h at a controlled temperature in the range 120−160 °C. The white, powdery TNTs were thoroughly washed with water until the washing solution achieved pH 7. The obtained TNTs were heat treated at 400 °C for 2 h in a crucible in the presence of NaH2PO2. The reference sample (TNTs) was prepared via an identical synthesis route but without NaH2PO2 addition. Notably, all the chemicals were of analytical grade and were purchased from Sigma-Aldrich. The NaOH solution used in this study was prepared using ultrapure water (18.2 MΩ) from Millipore purification system. Further, inductively coupled plasma spectrometry measurements excluded the presence of possible metal ions (e.g., Fe2+, Cu2+, Ni2+, Zn2+) in P-TNTs and TNTs.
The morphology of the prepared samples was characterized by scanning electron microscopy (SEM, Quanta FEG 250) and transmission electron microscopy (TEM, Talos F200X). The crystalline structures were analyzed by X-ray diffraction (XRD, Rigaku D/max 2500) with Cu Kα radiation (λ = 0.154598 nm). X-ray photoelectron spectroscopy (XPS, ESCALAB 250Xi, Thermo Scientific) was acquired with a monochromatic Al Kα radiation source.

2.2 NORR tests

All electrochemical properties were evaluated at ambient temperature and pressure in a gas-tight H-type cell separated by an anion exchange membrane (Nafion 211) with 1-butyl-1-methypyrrolidinium tris(pentafluoroethyl)trifluorophosphate ([C4mpyr][eFAP], 50 mL, 0.1 mol∙L–1) solution. The Nafion membrane was pretreated according to the procedure reported in our previous study. A catalyst ink with concentration of 0.1 mg·mL−1 was loaded onto a carbon paper. The as-prepared electrodes, graphite rod, and saturated calomel electrode were used as working electrode, counter electrode, and reference electrode, respectively. In this study, all potentials were calibrated against the reversible hydrogen electrode (RHE) scale. For NORR, chronoamperometric analysis test was conducted in NO (99.99% purity) saturated IL-containing electrolyte (i.e., [C4mpyr][eFAP]/H2O with a mass ratio of 97:3) and the electrolyte was purged with Ar for 30 min before the test. The NO gas flow rate was set to be 20 sccm.

3 Results and discussion

The synthesis procedure and morphology characterizations of the samples are presented in Fig.1. Fig.1(a) (refer to the Experimental section for more details) depicts that TNTs (Figs. S1 and S2, cf. ESM) were first prepared by a modified hydrothermal process reported by Kasuga et al. [27]. Then, the obtained suspension was washed in acidic solution to remove impurities. Finally, the P dopant was introduced into the TiO2 lattice by pyrolysis at high temperature with the addition of NaH2PO4 [28]. The SEM and TEM images were used to analyze these nanotubes. The results indicate that P-TNTs show a typical tube-like structure with a wall thickness in the range of 2–6 nm (Fig.1(b, c)). Noteworthy, no obvious morphology change could be observed during the phosphorization.
Fig.1 Synthesis and structural characterizations for P-TNTs: (a) synthetic depiction illustrating preparation of P-TNTs sample, (b) typical SEM images, and (c) TEM images of P-TNTs, (d) high-resolution TEM (HRTEM) image of P-TNTs, and (e) high-angle annular dark-field scanning TEM (HAADF-STEM) image and elemental mapping of Ti, O, and P in P-TNTs.

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Fig.1(d) exhibits the results of HRTEM characterization, showing the lattice fringes of P-TNTs with a d-spacing of 0.352 nm, which correspond to the (101) crystal plane of anatase TiO2. Additional HAADF-STEM and the corresponding EDX mapping images of P-TNTs indicate the P element is uniformly distributed throughout the TNTs (Fig.1(e)).
The crystallographic structure of P-TNTs was characterized by XRD analysis (Fig.2). Fig.2(a) demonstrates that all the characteristic peaks of P-TNTs match well with anatase phase TiO2 (JCPDS No. 21-1272). Moreover, no obvious peaks from other phases or impurities are observed. The surface compositions and electronic structures of P-TNTs were further characterized by XPS measurements. Figure S3 (cf. ESM) reveals that XPS survey spectrum confirms the existence of Ti, O, and P elements in these nanotubes. High-resolution P 2p XPS spectrum shows two peaks located at 134.3 and 133.4 eV, which can be assigned to P 2p1/2 and P 2p3/2 (corresponding to P–O–Ti), respectively (Fig.2(b)) [28,29], confirming the successful doping of P in TNTs to form P-TNTs. Moreover, the P content in P-TNTs is 1.65 wt %, measured by ammonium molybdate spectrophotometry, which is close to that estimated from XPS measurement (1.58 wt %).
Fig.2 Fine structure of P-TNTs: (a) XRD pattern of P-TNTs, (b) and (c) high-resolution XPS spectra for P 2p and Ti 2p, and (d) Raman spectrum.

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The XPS spectrum at Ti 2p region (Fig.2(c)) shows two peaks at 464.5 and 458.8 eV corresponding to Ti4+ oxidation state of P-TNTs. Besides, the comparison of Ti 2p XPS spectra shows a negative shift after the P doping (Fig. S4, cf. ESM)), which can be explained from the larger charges on P (1.89) compared to that on Ti (1.34) [30], thus the charges get accumulated around the P atom and the Ti atom exhibits lower binding energy. Furthermore, the negative shift of binding energy also indicates the feasibility of the electron transfer between the P dopants and TiO2 [31]. In the O 1s XPS spectrum (Fig. S5, cf. ESM)), three peaks at 530.3, 531.6, and 532.5 eV are indexed to Ti–O, P–O–Ti, and O–P, respectively [32]. Raman spectrum shown in Fig.2(d) was further acquired, which shows peaks of anatase TiO2 at 157, 267, 451, and 670 cm−1. All these above-mentioned results support the successful doping of P into the TiO2 lattice. Moreover, the projected density of states (PDOS) for TNTs and P-TNTs confirm the appearance of new states originating from the 3p orbitals of P atom (Fig. S6, cf. ESM). The simulated results obtained in this study and reported in previous studies indicate that P doping can effectively reduce the band gap of TiO2 [29,33], and is significantly beneficial for faster charge transfer during the electrolysis.
Next, the NORR performances of P-TNTs and TNTs were evaluated and compared in a typical H-cell with three-electrode system in NO-saturated [C4mpyr][eFAP] (3 wt % water) solution (Fig.3). The generated NH3 was quantified by indophenol blue spectrophotometric method and carefully calibrated (Fig. S7, cf. ESM). Herein, all reported potentials were obtained versus the RHE. Figure S8 (cf. ESM) displays that the polarization curve of P-TNTs shows an increased current density compared with the polarization curve recorded under Ar-saturated electrolyte, indicating that P-TNTs sample is active toward NORR. Moreover, P-TNTs deliver larger current densities compared with TNTs (Fig.3(a)), manifesting the beneficial role of P dopant in the TiO2 lattice. Notably, prior to NORR, the current density is less than 1 mA·cm−2 in the potential range from 0.1 to ‒0.8 V vs RHE. Further, the NORR activity of the two samples under different working potentials was investigated herein. Fig.3(b) illustrates that the highest FENH3 on TNTs is only 42% at ‒0.7 V vs RHE, while P-TNTs show two times higher FENH3 of 89% at ‒0.8 V vs RHE (Fig.3(c)). In contrast, the obtained maximal NH3 yield rate on P-TNTs is found to be 425 μg·h−1·mgcat.−1, significantly larger than that of TNTs (Fig.3(b,c)). To verify the reliability of our spectrophotometric method, the FENH3 and yield rate of P-TNTs were further examined by 1H nuclear magnetic resonance (1H NMR) and IC measurements (Fig.3(d)), both of which give results very close to those quantified by indophenol blue method.
Fig.3 NORR performance of P-TNTs in an IL-containing electrolyte: (a) Polarization curves of TNTs and P-TNTs in NO-saturated electrolyte, supported on carbon paper, (b, c) FENH3 and yield rate at different applied potentials for TNTs and P-TNTs, respectively, (d) FENH3 and yield rate of P-TNTs at −0.8 V vs RHE detected by three independent quantification methods, (e) FENH3 and yield rate of P-TNTs during 10 consecutive recycling electrolysis. Error bars depicted in (b–d) represent the standard deviation of three independent samples.

Full size|PPT slide

Surprisingly, the achieved FENH3 values for P-TNTs at more negative potentials still remain above 76% (Fig.3(c)). This is mainly due to the utilization of IL-containing electrolyte that can effectively suppress the side reaction of HER [26], as confirmed by the NORR performance evaluated in aqueous solution (Fig. S9, cf. ESM). As expected, the FENH3 and yield rate values from aqueous electrolyte are all significantly lower than those from no-aqueous one. Remarkably, the obtained performance metrics of P-TNTs are comparable to the recently best-reported NORR results and outperform most of NRR catalysts (Table S1).
In order to prove the production of NH3 from NORR process catalyzed by P-TNTs, additional control experiments were performed. Figure S10 (cf. ESM) exhibits that no NH3 was detected on P-TNTs when NO was replaced with Ar. 1H NMR spectrum also confirms this result (Fig. S11, cf. ESM). The two control experiments also excluded the possible nitrogen contaminate from the used [C4mpyr][eFAP]. Besides, no NH3 could be observed when NO was electrolyzed by P-TNTs at open circuit (Fig. S10). These results collectively confirm that the produced NH3 was derived from the NORR electrolysis on P-TNTs.
To explore the stability of P-TNTs, cycling test at ‒0.8 V vs RHE was conducted (Fig.3(e)). Clearly, no obvious fluctuations in FENH3 and corresponding yield rate could be found after 10 consecutive cycles, indicating the excellent electrochemical stability of P-TNTs. The stable NORR activity was also manifested by chronoamperometry measurements, where acceptable current density and yield rate changes were observed after the 30-h electrolysis (Fig. S12, cf. ESM). Additional XRD pattern and TEM image confirm the structural and morphological stability of P-TNTs (Figs. S13 and S14, cf. ESM).
Strikingly, the above-mentioned enhanced NORR activity of P-TNTs could be ascribed to the introduction of P dopants and unique tube-like structure, which were found to be beneficial for the exposure of more catalytically active sites and faster mass and charge transfer (Fig.4). To verify this perspective, the double-layer capacitance (Cdl) of P-TNTs and TNTs was measured in this study. Fig.4(a) demonstrates that P-TNTs sample exhibits a larger Cdl value (31.7 mF·cm−2) than the counterpart (24.6 mF·cm−2), confirming that the P-doping resulted in an increased number of active sites for NORR [34,35]. Electrochemical impedance spectroscopy (EIS) measurements were performed, and the results presented in Fig.4(b) manifest that P-TNTs sample possesses a smaller interfacial charge-transfer resistance (17.5 Ω) compared with TNTs (25.8 Ω), indicating a faster mass and charge transfer kinetics [36,37].
Fig.4 Experiments and theoretical simulations: (a) charging current density differences plotted against scan rates and (b) EIS spectra. The inset shows the equivalent circuit. (c) Calculated PDOS of P-TNTs and the adsorbed NO, corrected with Fermi level, and (d) calculated free energy diagrams of NORR.

Full size|PPT slide

To reveal mechanistic insight into the intrinsic activity of P-TNTs, DFT calculations were carried out in this study. It is generally suggested that the HER competes with NORR [11], which usually induces a poor selectivity for NH3 production. Herein, the free energy profiles of hydrogen adsorption on the two catalysts were first calculated. The results indicate that P-TNTs sample shows a bit larger free-energy change for *H adsorption (∆GH* = –0.39 eV) than that of TNTs (∆GH* = –0.42 eV). This result confirms that HER on P-TNTs is reinforced, to some degree (Fig. S15, cf. ESM). However, noteworthy, the usage of hydrophobic [C4mpyr][eFAP] could largely inhibit the competitive HER [3841], as confirmed by the above-mentioned results (Fig.3 and S7).
Figure S16 (cf. ESM) presents the differential charge density analysis, revealing that P-TNTs exhibited a substantial charge exchange with *NO, thereby activating adsorbed NO molecule by weakening the N–O bond (change from 1.163 Å to 1.311 Å). Besides, the PDOS for P-TNTs shown in Fig.4(c) confirm the strong overlap of Ti 3d and P 2p valence orbitals with N 2p orbital, indicating that P-TNTs could effectively activate the NO molecule [4244], which is in accordance with the analyses shown in Fig. S16.
Next, the free energy profiles of NORR catalyzed by P-TNTs and TNTs were obtained, as displayed in Fig.4(d). The results indicate that the initial hydrogenation of P-TNTs was more energetically favorable, thus confirming a smaller energy barrier of 0.72 eV compared to TNTs (0.77 eV). Notably, the subsequent hydrogenation steps indicate downhill reaction processes. The largest reaction barrier occurs at the final desorption of *NH3, as depicted in Fig.4(d), where P-TNTs shows an energy barrier of 1.16 eV, obviously lower than that of TNTs (1.29 eV), indicating that P dopant can indeed significantly facilitate the NO-to-NH3 conversion [4550]. Overall, the strong affinity of NO molecule and decreased free-energy barriers induced by P doping synergistically optimize the NORR reaction paths.

4 Conclusions

In this study, P-doped TiO2 nanotubes were successfully prepared for NH3 production in IL-based electrolyte. The maximum FENH3 and yield rate could reach 89% (–0.8 V vs RHE) and 425 μg·h−1·mgcat.−1 (–0.9 V vs RHE), respectively, both of which are comparable to the best-reported NORR electrocatalysts and outperform most of the NRR results. The remarkable improvement of NORR performance is ascribed to (1) the optimized electronic structure of TiO2 induced by P doping, thereby activating NO molecule and reducing the energy barrier for the desorption of *NH3, and (2) the employment of IL that efficiently suppresses the competitive HER. Therefore, this study offers a promising exploration for the development of high-performance electrocatalytic system for NH3 synthesis by catalyst-electrolyte engineering strategy.

Acknowledgements

This work was financially supported by the National Natural Science Foundation of China (Grant Nos. 22075211, 21601136, and 21905246) and the Key Projects of Zhejiang Natural Science Foundation (Grant No. LZ20E010001).

Electronic Supplementary Material

Supplementary material is available in the online version of this article at https://dx.doi.org/10.1007/s11705-022-2274-8 and is accessible for authorized users.
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