DOI:
10.1039/D2MA00279E
(Review Article)
Mater. Adv., 2022,
3, 5207-5233
Electrochemical ammonia synthesis: fundamental practices and recent developments in transition metal boride, carbide and nitride-class of catalysts
Received
11th March 2022
, Accepted 2nd May 2022
First published on 6th May 2022
Abstract
Ammonia, a value-added chemical, major fertilizer and future transportation fuel, is conventionally and synthetically produced by the energy intensive Haber–Bosch process. For the conversion of nitrogen to ammonia, more energy efficient and environmentally friendly approach is required which can be fulfilled by the electrochemical nitrogen reduction reaction (NRR). Because of its sluggish kinetics and poor selectivity, the progress of NH3 production is far beyond the industrial periphery. So, to meet the current energy demands, here we have summarized the bottlenecks of the NRR and have discussed briefly how to overcome these issues in terms of competitive HER, N2 solubility in the electrolyte, and material specificity. Among the various categories of catalysts explored for NRR, we are here interested in transition metal borides (Mbenes), carbides (TMCs) and nitrides (TMNs) because of their respective benefits in selective N2 adsorption and its subsequent reduction. We have widely covered the DFT studies concerning these catalysts and their experimental implementations towards NRR. Along with that, we believe that this review with detailed fundamentals of N2 reduction will act as a tutorial for new-comers in this field. Finally, with the focus on the current challenges in this field, potential opportunities and future prospective have been provided.
Ashmita Biswas
| Ashmita Biswas received her bachelor's degree with Chemistry Honours from the University of Calcutta in the year 2017. She has completed her master's degree from Indian Institute of Engineering Science and Technology, Shibpur, India (2017–2019). She is currently pursuing her PhD under the supervision of Dr Ramendra Sundar Dey at Institute of Nano Science and Technology, Mohali, India and Indian Institute of Science Education and Research, Mohali, India. She has published five research papers in peer-reviewed journals and provisionally filed one patent. Her research interest includes the development of noble-metal-free catalysts applicable for electrocatalytic reduction reactions in the field of sustainable energy. |
Sakshi Bhardwaj
| Sakshi Bhardwaj is currently a PhD candidate under the supervision of Dr Ramendra Sudar Dey in Institute of Nanoscience Science and Technology (INST), Mohali, India and Indian Institute of Science Education and Research, Mohali, India. She received her master's degree in chemistry from Guru Nanak Dev University, India, in 2018. Her current research focuses on the engineering of defect sites of carbonaceous nanomaterials for electrocatalytic applications. |
Tribani Boruah
| Tribani Boruah is currently pursuing her PhD from the Institute of Nano Science and Technology (INST), Mohali, India, under the supervision of Dr Ramendra Sundar Dey. She received her BSc degree in chemistry from Dibrugarh University, Assam, India, in 2016 and completed her masters from University of Delhi, New Delhi, India, in Organic Chemistry in the year 2019. Her current research interest includes the synthesis of non-precious metal-based Air electrode for rechargeable metal air batteries. |
Ramendra Sundar Dey
| Ramendra Sundar Dey is a Scientist at Institute of Nano Science and Technology, Mohali, India. Prior, he was a Hans Christian Ørsted postdoc fellow at Technical University of Denmark (DTU), Denmark. He received his PhD in chemistry in 2013 from Indian Institute of Technology (IIT) Kharagpur, India. He is involved in research in the field of electrochemistry of nanomaterials. His research interests focus on the architecture and engineering of nanomaterials for advanced energy storage technology and non-novel metal nanomaterials for electrocatalysis and hybrid energy technology. He has been honored with a number of prestigious national and international recognitions, like INSPIRE Faculty Award for 2015, Journal of Materials Chemistry A Emerging Investigator under the theme highlighting 2019's rising stars of materials by RSC. Recently he has been awarded as the Associate of Indian Academy of Science, Bengaluru, and member of the Indian National Young Academy of Sciences (INYAS). |
1. Introduction
Ammonia (NH3) is an important industrial chemical, useful fertilizer as well as a next generation renewable energy source for fuel cell technology.1 But its synthesis uses up to 3 to 5% of the world's natural gas. Therefore, a lot of research is being done all over the world for the electrocatalytic NH3 synthesis by nitrogen reduction reaction (NRR) under ambient conditions, which is a promising alternative to the famous century-old Haber–Bosch process.2 The major obstacles to this electrochemical process are the solubility issue of N2 in the electrolyte medium, competitive hydrogen evolution reaction (HER) occurring at the same voltage window as that of NRR, selectivity of most of the metals towards H2 adsorption than N2 and the sluggish counter-oxidation reaction at the anode.3 These are indeed major concerns as these factors directly affect the yield, production rate and faradaic efficiency (F.E.) of NH3 synthesis. A detrimental NRR kinetics makes way for the facile HER process.4,5 Moreover, a false positive NH3 production is often encountered if there is any nitrogenous source other than the feeding gas.6 Thus, several precautionary measures are a must to adopt during the NRR process. This approach had been initiated in the late 1960s; however, the field has started its development recently. With an attempt to gain industrial scale NH3 production, several new avenues got opened in the process of catalyst designing and electrolyte improvisation. While some researchers started working on membranes to capture protons and help easy diffusion of N2, so that there is less interference of H+ ions and restricted HER, others were more interested in investigating the reaction mechanisms being followed during NRR. Thus, this field has enormously widened with enough room for further exploration and development.7
Ren et al. have clearly demonstrated that about 90% of the research works on NRR are concerned with catalyst designing.4 The catalyst should be such that either it should be selective to N2 adsorption rather than protons or it should be engineered to have HER suppression ability by blocking the HER active sites. Considering the latter, several approaches have been adopted by researchers which include defect engineering, interface engineering, phase specific material designing and induced strained effects to gain dominance of NRR over HER.8–14 However, it is desirable to have a simpler catalyst system but with efficacy to meet the current demands for high NH3 production with improved current density and faradaic efficiency (F.E.) because a rather complicated system would only add to the constraints of NRR.
Transition metal borides, carbides and nitrides have drawn immense attention in this field for their advantages over other classes of catalysts. Transition metal borides take the advantages of dual active edges (from the metal end as well as the boride end).15 It is known that transition metals have σ-donation and π-back donation interactions with the adsorbed N2.16 However, it is noteworthy to mention that, borides can have energy as well as symmetry matched 2p orbital overlap with N2, which favours N2 adsorption on the B-active edges.17 In the case of transition metal carbides, owing to the bonding interactions of 2s and 2p orbitals of the C atoms with the d orbital of the transition metals, their electronic structures resemble those of noble metals near the Fermi edge.18 This reinforces the intrinsic electronic properties of these catalysts and helps to promote electron transfer from the catalyst surface to the reactants during NRR, enabling better charge transfer rates and NRR kinetics. Different from these two classes, the transition metal nitrides have inherent N-atoms, which act as the commencer of the NRR process on these catalysts.19 Basically, the competition of NRR with HER arises because of the competition between proton and N2 adsorption selectivity on the catalyst surface. But in this case, because of the special mars-van Krevelen mechanism, NRR dominates over HER.20 Considering all these key points, in this review firstly we have briefed the fundamentals of NRR followed by all the important experimental conditions like electrolytes favouring N2 solubility in the medium, pH of the medium, proton and electron accessibility limiting HER kinetics and the choice of metals favouring NRR. Further, we have elaborated the gradual progress of the transition metal borides, carbides and nitrides for NRR and also reviewed the limitations and scopes with these classes of catalysts. Fig. 1 demonstrates the scope of this review. We believe that, this review will be helpful enough for the newcomers in this field to design transition metal borides, carbides and nitrides preferably for NRR with high yield, production rate and faradaic efficiency for NH3 synthesis.
|
| Fig. 1 A systematic summary of electrochemical nitrogen reduction reaction. | |
2. Fundamental basis of NRR
2.1 Thermodynamics of NRR
Dinitrogen (N2) molecules are extremely inert owing to the high bond dissociation energy (941 kJ mol−1) of the triple bond, which accounts for just a portion of their inertness. The greater triple bond energy (962 kJ mol−1) in acetylene (C2H2), although C2H2 is significantly highly reactive than N2, is an obvious cause for the reactivity discrepancy. The first H-atom addition to N2 is endothermic (+37.6 kJ mol−1), while the reaction with C2H2 is exothermic (−171 kJ mol−1). Apparently direct protonation is generally allowed for C2H2, but not for N2.21 N2 has a low electron affinity (1.9 eV) and a high ionization potential (15.8 eV). The wide energy gap (10.82 eV) between the highest occupied (HOMO) and the lowest vacant molecular orbitals (LUMO) of N2 discourages electron transport reactions.22,23
The thermodynamic limitations imposed by the reaction intermediates explain the key bottlenecks in the reduction reaction of N2 to NH3. The electrocatalytic reduction of N2 to NH3 has similar equilibrium potentials to that of the contending HER. Among aqueous electrolytes, H2 is the primary NRR side product. Regardless, the NRR involves numerous proton–electron transfer pathways with intermediates. Although the redox potentials for the production of the N2H intermediate are quite negative, this indicates that the initial H-atom addition is extremely challenging. When applied to multistep catalytic processes comprising various intermediates, the thermodynamic methodology has highlighted significant shortcomings. The relative adsorption energy levels of several NRR intermediates could be scaled up in terms of Gibbs' energy requirement for each step.24 It is challenging to find an ideal catalyst with all reaction stages being thermodynamically neutral or favorable. There are no independent binding energies for the NH2 or N2H intermediate in NRR, resulting in a minimal overpotential of 0.4 V.25 Fortunately, subsequent theoretical calculations have revealed potential innovative ways to decrease overpotential which may be employed to break or avoid the scaling relations of NRR.
2.2 Different mechanistic approaches
In nature, plants can reduce nitrogen through numerous proton and electron transfer processes, which are catalyzed by iron-molybdenum nitrogenase enzymes under environmental conditions.26–28 The nitrogenase enzymes having Fe–Fe, Fe–Mo and Fe–V active moieties are believed to go through the reduction process by the enzymatic pathway where N2 undergoes side-on adsorption on the catalyst surface followed by alternative hydrogenation of each of the N atoms. This results in the release of two NH3 molecules subsequently. Nevertheless, analyzing and understanding the nitrogen fixation mechanism continues to be a difficult endeavor in the living organisms. After more than 150 years of research, F. Haber was able to effectively develop an artificial nitrogen-fixing industrial process29 in order to meet the demands of the manufacturing sector. Eqn (1) describes how an ammonium-containing combination of nitrogen and hydrogen is utilized to create ammonia under extreme conditions of high temperature and pressure while engaging a catalyst: | | (1) |
In contrast to the HER and ORR, where the reaction pathway has been well known using metal (Pt) model catalytic systems, the NRR lacks an appropriate catalyst to examine the mechanism, as standard noble metal catalysts, which work well in the HER and ORR, do not operate well in the NRR. The NRR reaction mechanism is still not clear, although the three main reaction mechanisms currently acknowledged are the dissociative mechanism, the associative pathway (alternating and distal), and the enzymatic pathway.29,30 In the dissociative mechanism, the N–N bond is broken first and then the two N atoms are adsorbed on to the catalyst, indicating the catalytic hydrogenation reaction, which is most prevalent in the Haber–Bosch technique because the kinetic parameters can provide enough power to impede the NN bond which is illustrated in Fig. 1.26 The hydrogenation reaction is initiated before the breakdown of the N–N bond in the associative pathway.31 Almost all the catalysts lean towards the associative mechanism of ammonia synthesis, which is further categorized into alternating and distal pathways. The alternating pathway is the same as the enzymatic pathway except for the fact that here, N2 undergoes end-on adsorption on the catalyst surface. This end-on adsorption is possible when the catalysts have free unsaturated sites (axially) for N2 adsorption. For the distal pathway, the farthest N atom is first protonated and released as NH3, followed by the protonation of the next N ad-atom. Au/TiO232 B-induced O vacant MnO233 and the S-vacant amorphous MoS3 catalyst34 follow the distal associative pathway, while the N-vacant polymeric carbon nitride35 follows an alternating associative pathway, where the two N-atoms alternately hydrogenate even before the N–N bond breaks, resulting in the release of one NH3 molecule followed by another ammonia molecule. The different mechanistic approaches adopted for NRR are elaborated in Fig. 2a–d.
|
| Fig. 2 Different mechanistic approaches of NRR. (a) Associative alternating pathway; (b) associative distal pathway; (c) dissociative pathway; (d) enzymatic pathway; (e) Mars–van Krevelen pathway and (f) surface hydrogenation driven NRR. Reproduced with permission from Ling et al.,41 Copyright 2019, American Chemical Society. | |
A special class of the N2 reduction mechanism is the Mars-van Krevelen pathway (Fig. 2e), which is mostly prevalent for transition metal nitrides.36 In this case, the N atom of the active element takes part in the NH3 synthesis besides the N2 gas purged into the electrochemical system. Although W2N3 is known to follow this pathway, upon creating N vacancies in W2N3, the reaction deviates to the distal associative pathway.37 A recent report suggests that, even O-vacant V2O5 and CeO2 are interpreted within the Mars–van Krevelen mechanism for ammonia synthesis.38 While the class of anion vacancy inherited transition metal based electrocatalysts follow the associative pathway, a class of boron doped carbon nitride compounds tend to follow the enzymatic pathway at the cost of a low energy barrier.39,40
Recently, another interesting mechanistic approach has been highlighted by Ling et al., where they have focused on the weak N2 binding on the surface of noble-metal catalysts. They suggested a surface hydrogenation triggered NRR (Fig. 2f) on these noble metal surfaces where the first step was the adsorption of H+. Thereafter, under a relatively high coverage of *H, N2 got activated and reduced into *N2H2 by surface *H. Subsequently, the produced *N2H2 reduced into NH3 spontaneously. In this case, the reduction of H+ is the potential-determining step, while the activation and reduction of N2 into *N2H2 is the rate-determining step as shown in the figure.41
2.3 Activity descriptors for NRR
When it comes to electrocatalytic NRR, the production of NH3 and the faradaic efficiency (FE) are the two most important factors to take into consideration. The yield of any chemical substance is the most important consideration. In the case of NRR, the NH3 yield rate reflects the amount of ammonia produced per unit mass/area of catalyst loading with unit time, and it is intended to monitor the effectiveness of electrocatalysts. While conducting experimental investigations, this yield can be determined in μg h−1 mgcat−1 by using the chronoamperometry quantitative study, which is represented by eqn (2), where C is the measured NH3 concentration (μg mL−1), V is the volume of the electrolyte in the cathodic compartment, t is the electrolysis time, and mgcat is the mass of the catalyst loaded on the cathode surface. | | (2) |
Another measurement of the selectivity of an electrochemical process for NH3 production in comparison to competing reactions such as HER is the fraction of faradaic current used for nitrogen reduction in relation to the total current passed through the circuit. The following equation (eqn (3)) can be used to calculate the FE, where n is the number of electrons required for producing one NH3 molecule (n = 3), F is the Faraday constant (F = 96485 C mol−1), C is the measured NH3 concentration (μg mL−1), V is the volume of the electrolyte in the cathode compartment (mL), M is the relative molar mass of NH3 (M = 17 g mol−1), and Q is the total charge passed through the electrodes (C). | | (3) |
The surface-area-normalized production rate of NH3 (mol s−1 cm−2) was calculated by eqn (4) as below: | | (4) |
where AECSA represents the electrochemically active surface area of the active material.
The mass-normalized production rate of NH3 (mmol h−1 gcat−1) was calculated as below (eqn (5)):
| | (5) |
where
n is the number of electrons required for producing one NH
3 molecule (
n = 3),
F is the Faraday constant (
F = 96 485.33),
M is the relative molecular mass of NH
3 (
M = 17.03), and
Q is the overall charge that passes
via the electrodes.
Likewise, another important parameter is the turn-over frequency (TOF) of the electrocatalyst, which is a measure of the instantaneous efficiency of a catalyst, calculated as the derivative of the number of turnovers of the catalytic cycle with respect to the time per active site of the catalyst. It is given by the following equation:42
| | (6) |
where TOF is the turnover frequency (in h
−1),
rN is the ammonia-producing rate (in mmol g
−1 h
−1),
NA is the Avogadro constant (6.023 × 10
23 mol
−1) and
Nsas is the number of surface sites (in g
−1).
3. Rate determining factors for NRR
3.1 N2 solubility in the electrolyte
The most vital factor that is responsible for the low yield and production rate of NH3 is the poor solubility of N2 in the aqueous medium. Recently, Choi et al. have concluded that the catalysts that deliver low yield and production rate of NH3 fail to be convincing enough to actually reduce the dinitrogen in the medium.43 It is reasonable to consider that if the concentration of N2 in the medium at the vicinity of the catalyst surface is not sufficient, then the yield of NH3 cannot be high, however efficient the catalyst be. Of course, the N2 adsorption efficiency of the catalyst will play a role besides N2 solubility in the medium.
Ionic liquids are the most efficient in this respect to solvate N2 gases in the medium. Gomes and co-workers worked with room temperature ionic liquid 1-butyl-3-methylimidazolium tetrafluoroborate, [bmim][BF4],44 and calculated the solubility of N2 in terms of mole fractions of solute and Henry's law constant given by eqn (7) and (8).
| | (7) |
where
nliq2 is the amount of solute dissolved in the ionic liquid and
nliq1 is the total amount of ionic liquid.
| | (8) |
where
KH is Henry's law constant,
f2 is the fugacity of the solute and
ϕ2 is the fugacity coefficient of the solute calculated in the usual way,
p and
T are the pressure and temperature of gaseous solute present in the gas bulb and
peq and
Teq are the equilibrium pressure and temperature respectively.
This study showed that this ionic liquid electrolyte was able to solvate N2 with x2 = 6.076 and KH = 1646 at room temperature. [bmim][BF4] and 1-butyl-3-methylimidazolium hexafluorophosphate [bmim][PF6]45 are widely used for this solubility study. The same group further worked on 1-alkyl-3-methylimidazolium (Cnmim, n = 2, 4, 6) tris(pentafluoroethyl)-trifluorophosphate ionic liquids (eFAP) and confirmed that the improved solubility of gases is due to the interaction of the solute (N2) with the polar part of the ionic liquids as proved by the enthalpies of solvation and the site–site solute–solvent radial distribution functions using molecular simulation.46 They further extended their finding to arrive at a point that ionic liquids with partial fluorination on the cation were found to increase CO2 and nitrogen mole fraction solubility up to 50% compared to their hydrogenated counterparts.47 Basically, perfluorinated organic liquids have a backbone of strong C–F bonds that cause a loss in molecular flexibility and a decrease in polarity, which in turn help to solvate the gas molecules facilely.48 While Gomes et al. explored the anionic effect and showed a 30% increase in N2 solubility from [C8mim][NTf2] ([NTf2] is the bis(trifluoromethanesulfonyl)imide ion) to [C8mim][BETI] ([BETI] is the bis(pentafluoroethanesulfonyl)imide), Noble et al. examined the influence of the imidazolium cation and found that the N2 solubility decreased by approximately 36% due to the polar nature of the nitrile group.49 To implement this strategy into the field of NRR, MacFarlane and group worked on [C4mpyr][eFAP] and [P6,6,6,14][eFAP] ionic liquids for NRR,50 having a N2 solubility of 0.20 mg g−1 and 0.28 mg g−1 respectively. The current density and yield were found to be more with the [C4mpyr][eFAP] IL due to its lower viscosity, which supports higher mass transport while the F.E. was better for [P6,6,6,14][eFAP] (60%). From theoretical calculations it was derived that N2 was likely to interact with the F-atoms and greater the charge delocalization over the anionic and cationic part of the ionic liquids, better will be the interaction of the F-ends with N2 and higher will be the N2 solubility. Keeping this issue in mind, they further synthesized a series of phosphonium-based ILs with highly fluorinated anions, which displayed high N2 solubility and all were found to be promising towards NRR.51 This is a wide research field on its own and there is much scope to implement these ionic liquids in NRR in a better optimized way so that along with high F.E., the yield and production rate of NH3 could be simultaneously improved.
3.2 Restriction of HER toward improved F.E. for NRR
Most of the times, the performance of the catalysts towards NRR is receded by an alarming issue which is the competitive hydrogen evolution process (HER).52 The multiphase proton-coupled-electron process (NRR) not only involves a number of intermediates that are difficult to trace but also requires six electrons and six protons to completely get reduced to ammonia. This is unlike the case of HER, which involves a much faster kinetics with only two electrons and two protons.53 Again, from thermodynamics point of view, the dissociation of the NN bond is an energy intensive process. Therefore, although NRR and HER have the same working window, NRR suffers from a huge overpotential while HER becomes predominant. It is noteworthy that, at a low negative potential window, NRR becomes operative but with a lower current density. With the increase in the negative applied potential, the current density increases significantly, but the faradaic efficiency for NRR is drastically hampered by the rapid H2 evolution.1,54–56 Thus, with respect to the medium, accessible electrons and protons and material choice, it is crucial to maintain a proper balance so that either the working potential window for NRR could be increased or the achievable current could be more at a low negative potential. A detailed discussion regarding the above-mentioned points is provided below.
3.2.1 Influence of pH of electrolyte.
For NRR, the pH of the electrolyte has an important role to play as it is directly linked to the concentration of the proton donor participating in the reduction process which consequently is related to the selectivity of NRR (Fig. 3a).55 Usually, aqueous electrolytes include acidic electrolytes such as 0.1 M HCl and 0.05 M H2SO4, neutral electrolytes such as 0.1 M phosphate buffer solution (PBS), 0.5 M LiClO4 and 0.1 M Na2SO4, and alkaline electrolytes such as 0.1 M NaOH and 0.1 M KOH.6,57–59
|
| Fig. 3 Schematic representation of HER suppression. (a) Effect of pH on dominant NRR over HER. (b) Limiting proton source in the medium, restricting HER. The image of the ionic liquid has been reproduced with permission from Zhou et al.,50 Copyright 2017, Royal Society of Chemistry. (c) Hydrophobic coating over the material to prevent HER. (d) Surface/semi-metal or surface/semi-conductor heterostructure inhibiting HER kinetics. | |
Centi et al. studied the effect of pH of electrolytes on ammonia selectivity using Fe2O3-CNTs under different pH of 0.6 (0.25 M KHSO4), 7 (0.25 M K2SO4), 9.4 (0.5 M KHCO3), and 13.7 (0.5 M KOH).60 It was found that with the rise in the pH value the NRR FE increased and the maximum FE was obtained in the case of 0.5 M KOH (0.164%) which was almost two times more than that for 0.25 M KHSO4 (0.075%). Likewise, for Mo2C nanodots anchored on carbon cloth in a proton rich electrolyte (pH = 2), a low FE of 1.6% was obtained as compared to that in a proton suppressed electrolyte with FE = 7.8% (pH = 3).61 In addition to this, Wu et al. revealed in their study that the nanoporous N-doped carbon catalyst showed better selectivity for NRR in the case of 0.1 M KOH than in 0.1 M HCl.62 These studies conclude that high pH electrolytes with less proton availability lead to superior NRR selectivity due to the sluggish HER process.
The neutral PBS electrolyte with limited proton availability may be favourable in hindering the H2 generation. Recently, Feng et al. demonstrated that the Pd/C catalyst in the neutral PBS electrolyte was more selective towards NRR than in acidic or basic media due to restricted HER.63 Also in the case of the Fe/Fe3O4 catalyst the same trend is followed.64 Additionally, the pH of the medium determines whether H2O (basic medium) or H3O+ (acidic medium) would act as proton donor during NRR (Fig. 3a). The Volmer step in the HER mechanism involves a high energy barrier for water dissociation in neutral and basic pH which is not the case in acidic medium.65 Therefore, the HER process in alkaline and neutral electrolytes is more sluggish than in acidic electrolytes because of the restricted Volmer step. It is also to be noted that the pH of the electrolyte and selectivity towards NRR may be limited due to the cell configuration and catalyst.66 Still there is a need to explore the effect of pH of the electrolyte and the local pH gradient around the catalyst for deep understanding of NRR selectivity.
3.2.2 Control over electron and proton accessibility.
As already mentioned above, the kinetics of NRR is limited due to the faster HER kinetics. Nørskov and co-workers have confirmed that while HER is dependent on the proton and electron concentration by first-order, NRR is independent of the same as shown in eqn (1) and (2).67 Naturally, if the electron and proton accessibility could be limited either from the medium or from the material respectively, NRR could be facilitated over HER. | | (9) |
| | (10) |
3.2.2.1 Control over proton accessibility from medium.
One of the vital components of any electrocatalytic process is the working electrolyte, which provides the platform for the reactions to occur. Generally, aqueous electrolytes are used for an ambient NRR process. However, in the case of acids like HCl, H2SO4, HClO4 and H3PO4, the proton sufficiency cannot be controlled in the medium and that is why it is more favourable to use the corresponding salts. The presence of alkali metal cations like Li+, Na+ and K+ favours the NRR process owing to their tendency to form solvation shells, and hence steric effects. Several groups have investigated the role of cations in reinforcing the NRR kinetics68.42 It has been found both theoretically and experimentally that, the smaller is the size of the cations, such as in the case of Li+, the affinity to form a hydration shell is maximum, which thereby increases the transfer barrier for the H2O molecules close to the catalyst surface restricting the water splitting process. After a systematic investigation, Rondinone and co-workers confirmed that Li+ in the medium outperformed Na+ and K+ with respect to NRR F.E. at different applied potentials like −0.8 V, −1.0 V and −1.2 V (vs. RHE) over an N-doped carbon nanospike (CNS) catalyst.69 They also showed that the F.E. dropped remarkably as the size of the alkali metal ion increased from Li+ to Na+ to K+. Not only the size of the cation, the concentration of the cation was also found to play a role in NRR F.E. – Yan et al. found that with the increase in the cation (K+) concentration in the electrolyte from 0.2 to 1.0 mol L−1, higher degree of the solvation layer over the surface of a bismuth nanocrystal (BiNC) catalyst could be achieved, which significantly retarded the migration of the protons in the electrical double layer (EDL). This led to an increase in the current density and thus F.E. for the NRR from 9.8 to 67%.42 This trend and activity of alkali metal cations were irrespective of the catalysts and besides suppressing HER, K+ was also able to promote N2 adsorption on the catalyst surface.70
Besides this, another approach to limit the proton access in aqueous electrolytes is by using an optimum concentration of methanol/2-propanol in water.71,72 While Kim et al. showed that 2-propanol/water (9:1 v/v) brought about effective NRR than the all-aqueous electrolyte, Ren et al. showed that, at 0.16% water volumetric content in the water–methanol medium, the availability and dissociation process of water got substantially restricted, accompanied by an expanded electrochemical window and inhibited HER. In this work by Ren et al., at −1.2 V vs. Ag/AgCl, the methanol-enabled electrolyte recorded a high NRR F.E. of 75.9 ± 4.1% and an ammonia yield rate of 262.5 ± 7.3 μg h−1 mgcat−1 (FeOOH/CNTs), ∼8-fold enhancement than that obtained in a 0.1 M KOH aqueous electrolyte. The reason is that, at an optimum methanol content, methanol is able to initiate intermolecular H-bonding with the water molecules, which in turn makes it difficult to dissociate the O–H bond of water molecules (suppressed Volmer step of HER). They also showed that, methanol could surpass other organic electrolytes like ethanol, propanol, butanol and dimethyl sulfoxide with water. Tsuneto et al. tried to completely ignore water molecules yet achieve remarkable NH3 formation efficiency by incorporating Li+ (0.2 M LiClO4) into the organic electrolyte (tetrahydrofuran/ethanol (99:1 v/v)) on some metal electrodes. Lithium was found to act as a mediator to produce ammonia with a higher current efficiency (48.7%) when the electrolysis was conducted under a high pressure of N2 (50 atm).73 Contrary to this, ionic liquid (IL) electrolytes serve as a special candidate in solvating N2 and achieving high F.E. for NRR up to 60%.50,74,75 The control one could have in terms of electrolyte medium to limit the proton accessibility is schematically shown in Fig. 3b.
3.2.2.2 Control over proton migration at the material–medium interface.
From a material perspective, in order to prevent the H2O migration on the material surface, several researchers have sought the help of hydrophobic coatings over the active sites.58 The use of alkanethiols over the catalysts like MoS2 or Cu served as a hydrophobic layer inhibiting HER and promoting different electrolytic processes like NRR and CO2 reduction.76 Besides this, hydrophobic coatings around Au surfaces were also proved to have a benign effect on the energy efficiency of NRR.77 Similarly, Ling et al. used a zeolitic imidazolate framework (ZIF) coating on the surface of a Ag–Au catalyst to suppress the HER activity of the catalyst with a 4-fold improvement for the NRR F.E.78 As the ZIF layer is porous, to further prevent H2O diffusion through the pores, they coated the ZIF with an oleylamine layer, which further inhibited the HER process.79 Likewise, Wang and co-workers designed highly dispersed Au nanoparticles (active species) coated with a porous poly(tetrafluoroethylene) (PTFE) framework (hydrophobic layer).80 The PTFE modified surface of the Au catalyst enabled N2 diffusion to have sufficient N2 molecules at the surface of Au nanoparticles for their subsequent reduction. Owing to the hindered H2 evolution, the catalyst presented a considerably increased NRR F.E. in contrast to the original Au nanoparticles. More recently, Liu et al. reported a three-layered unique catalyst where the active interlayer of vacancy-rich ReSe2 was sandwiched between two layers of hydrophobic carbon fibres.81 In all these cases, the hydrophobic coating efficiently lowered the coverage of H2O molecules on the surface of the active site to impede the HER kinetics, rendering superior NRR selectivity (Fig. 3c).
3.2.2.3 Control over electron accessibility by catalyst engineering.
As already mentioned above, HER is dependent on the available electrons, while NRR and its corresponding NH3 production efficiency are not affected by this. Keeping this issue in mind, upon limiting the electron sufficiency from the material surface, HER could be sufficiently suppressed (Fig. 3d) as shown by Qiao et al. They adopted an interface engineering strategy on 2D mosaic Bi nanosheets that featured a relatively large charge-transfer resistance of ∼300 Ω, indicating a restricted electron transfer rate. As a result, HER was retarded delivering a high NRR F.E. of 10.46% at −0.8 V (vs. RHE).82 Similarly, Sn-based catalysts were explored by Biswas et al. where they experimentally as well as theoretically demonstrated a suppressed HER on the Sn site of SnS2 at the NPG@SnS2 interface, promoting selective NRR with 49.3% F.E.83,84 Röpke et al. fabricated their catalyst surface with conductive polyaniline (PAN) where they tuned the thickness of the PAN coating and thus controlled the electron accessibility and hence the kinetics of the NRR process.85 Additionally, PAN could also accelerate the adsorption of N2 molecules and their intermediates.86 Similarly, other conductive polymers like polyimide and polypyrrole could also be used to drive forward NRR by slowing down the transfer rate of the electron flux from the catalyst surface to the adsorbed reactants.4
3.2.3 Material specificity.
During NRR in aqueous medium, a parasitic reaction HER can go sideways. This is because H atoms get easily adsorbed on the catalyst surfaces in contrast to N2 molecules leading to evolution of H2 eventually, lowering the selectivity of NRR.87,88 So, the catalysts must be designed with the strategy of suppressing HER by decreasing the probability of adsorption of H atoms. Norskov et al. did a theoretical study to calculate the free energy of adsorption and reduction of N and H atoms on the surfaces of extensive metals in acidic medium.89 It was observed that transition metals (Fe, Mo, W, Rh) showed high activity for NRR but they also had a tendency to adsorb H atoms (Fig. 4a). There are a few early transition metals (Sc, Ti, Zr, Y) that exhibited stronger binding of N atoms than H atoms. Following this, these metals and their corresponding complexes like TiO2 nanosheets on Ti foil,90 Ti3C2Tx MXene nanosheets,91 Y2O3 nanosheets, ZrO2 nanoparticles,92etc. were obtained as they are electrochemically active for NRR. Although Sc-, Y-, Zr-, and Ti-based electrocatalysts have less binding ability for H atoms, their intrinsic NRR activity (FE ≤ 5%) is poor. Therefore, huge efforts are being made to improve their intrinsic NRR activity. Recent studies on single atom catalysts (SACs) are getting wide attention due to maximum atom-utilization and unsaturated coordination configuration in NRR due to suppression of HER (Fig. 4b and c).93,94
|
| Fig. 4 (a) Volcano plot for the NRR on metal surfaces with specific mechanistic assumptions. A shaded area in the plot represents the overlaid volcano diagram for the HER counterpart. Reproduced with permission from ref. 189, Copyright 2012, Royal Society of Chemistry. (b) NRR over HER selectivity plot at pH 0, 4, and 14; volcano plot of HER. Experimental exchange currents of HER versus MH bond strengths (heat of adsorption of H2 gas) for different metals (M), where the data are taken from Trasatti (1972). (c) Overview of selectivity of metals for NRR over HER from DFT as well as experimental point of view. Reproduced with permission from ref. 190, Copyright 2020, Elsevier B. V. | |
4. Transition metal borides (TMBs)
Transition metal borides or simply MBenes are an emerging class of catalysts, still in infancy in the field of NRR. Owing to the strong M–B and B–B covalent bonds, these catalysts offer high chemical and thermal durability and provide a high active surface area as compared to metal nitrides and carbides. As the composition of metal borides can vary over a wide range, they can act as metals/semiconductors/insulators in terms of electrical conductivity as per the requirement.95–97 Several computational studies have been done for different groups of MBenes to shed light on the choice of T.M with best NRR performance and to deduce an estimation regarding the NRR mechanism being followed (Fig. 5a and b). The TMBs used for NRR have been summarized in Table 1. A study by Li et al. showed that among the T.M (Sc, Ti, V, Cr, Mo and W) boride monolayers, VB, CrB, and MoB with the onset potentials of −0.396, −0.277, and −0.403 V, respectively, were screened out to be more effective for NRR (Fig. 5c). The VB monolayer was ascertained to follow the alternating pathway with the end-on configuration while CrB and MoB were more compatible to follow the mixed I pathway with the end-on and side-on configurations respectively (Fig. 5d and e).98 However, there is no particularity in terms of mechanism for different MBenes as shown in Fig. 5f and g. In addition to CrB and MoB, Guo et al. also suggested that WB, Mo2B, V3B4 and a few mixed metal borides like CrMnB2 and CrFeB2 act as a HER suppressant and have intrinsic basal plane activity for NRR with limiting potentials ranging from −0.22 to −0.82 V.99 Zhao's group also included TiB in the preference list for NRR, which was later experimentally proved by Luo and co-authors using a sputtered TiB2 film to enable superb electrochemical N2 reduction.100 It is noteworthy to mention that Ma and co-workers worked on ternary metal borides like molybdenum aluminum boride (MoAlB) single crystals experimentally, which afforded an NH3 yield of 9.2 μg h−1 cm−2 mg−1cat. and a faradaic efficiency of 30.1% at a low overpotential of −0.05 V versus RHE in alkaline solutions. The 3p/2p bands of Al/B were considered to interact with the N-orbitals and with the synergism of Mo, this catalyst successfully suppressed HER on its surface to give a reasonably fair faradaic efficiency for NRR.101
|
| Fig. 5 (a) All MBenes for which both experimental and theoretical studies have been proposed are listed in the periodic table of elements. The stable structural prototypes of MBenes are indicated in different colors. (b) Top and side views of calculation models for different MBene structural prototypes that were built. Reproduced with permission from Long et al.,191 Copyright 2021, American Chemical Society. (c) Computed free energy of adsorption of H2O and N2 on different Mbenes. Reproduced with permission from Guo et al.,192 Copyright 2020, Wiley-VCH Verlag GmbH. (d) Adsorption energy of end-on and side-on binding configurations of N2 on the Mbene surfaces. (e) Adsorption energies of N2 and NH3 on the surfaces of MBenes considered. (f) NRR volcano plot of MBenes with a descriptor of ΔG*N via the distal path, (g) NRR volcano plot of MBenes with a descriptor of ΔG*N via the alternating path; the data points that stand near the top of the volcano plot are highlighted. The arrows to the left represent strong adsorption of *N, and the arrows to the right mean weak adsorption of *N. Reproduced with permission from Long et al.,191 Copyright 2021, American Chemical Society. | |
Table 1 A brief summary of transition metal borides used for NRR
Catalyst |
Electrolyte |
F.E. (%) |
NH3 yield rate |
Potential (vs. RHE) |
Ref. |
MoAlB SCs |
0.1 M KOH |
30.1 |
9.2 μg h−1 cm−2 mgcat−1 |
−0.05 V |
101
|
a-FeB2 PNSs |
0.5 M LiClO4 |
16.7 |
39.8 μg h−1 mgcat−1 |
−0.2 V, −0.3 V |
104
|
TiB2 |
0.1 M HCl |
11.37 |
1.75 × 10−10 mol s−1 cm−2 |
−0.3 V |
100
|
The beauty with this material is that one can have precise control over the choice of metal to involve the metal site as well as the boride counterpart in the activity during NRR. The interaction between boron and nitrogen is a well-known concept and has been illustrated in Fig. 1a. The strong coupling between the 2p orbitals of boron and nitrogen makes boron a favorable site for N2 adsorption17 (Fig. 6a–c). In the work by Cheng et al.,102 they have theoretically computed that the boron site for TaB is the active center for NRR, while the Fe site for FeB is more likely to carry out N2 reduction, but have a tendency to undergo H2 poisoning, affecting NRR kinetics. It is however considered that the B site is more active towards NRR than the metal sites for most of the M-benes.103 With respect to metal diborides, Yang et al. explored the electrocatalytic activity of FeB2, RuB2 and OsB2 for the N2 reduction reaction (NRR) by first principles calculations and found that these M-benes with surface B atoms as the active sites exhibited superior activity (with low onset potentials in the range of −0.03 to −0.26 V) for the NRR than those with metal active sites. Being a newly emerging field, there is a lot of controversy concerning the active sites of this material. For example, in contrast to the work by Yang et al., Chu et al. for the first time experimentally demonstrated the synthesis and NRR with amorphous FeB2 porous nanosheets and with the help of theoretical studies confirmed the active site to be Fe (Fig. 6d) and further revealed that amorphization lifted up the d-band center of the metal centre in FeB2 to boost d-2π* coupling between the active Fe site and the *N2H intermediate, resulting in enhanced *N2H stabilization and reduced reaction barrier. This resulted in an NH3 yield of 39.8 μg h−1 mg−1 (−0.3 V) and a faradaic efficiency of 16.7% (−0.2 V), significantly outperforming their crystalline counterpart, as can be seen from their NRR performance (Fig. 6e and f) and the full free energy reaction pathway (distal pathway in Fig. 6g). They also showed that, for the amorphous FeB2, the desorption of the first NH3 is the rate determining step.104 Another theoretical report by Wang et al. followed this trend for Mo2B2, where Mo was identified as the active site and its 4d-orbital electrons were particularly held responsible for the NRR process on the material surface. The good electrical conductivity of the material initiated faster NRR charge-transfer kinetics.105 The potential determining step being *NH2 + H+ + e− → *NH3, this catalyst followed the alternating pathway for NRR at the cost of a low energy barrier. However, an elaborate study by Li et al. on Fe-based borides suggested that, Fe and B can synergistically act as active sites for NRR. Not only that, M–M and B–B interactions can optimize the catalyst performance towards NRR mostly from the bulk than single atom sites. Thus, mass loading plays a very important role in tuning the activity of M-benes, with higher mass loading resulting in more improved performance. They also demonstrated that different phases of the catalysts exhibit different NRR mechanism pathways like the most favorable NRR paths for FeB and FeB2 are the alternating and dissociative paths, respectively.106 Mostly, for the M-benes where B serves as the active site, over a series of transition metals, mostly the enzymatic and consecutive reaction mechanisms are followed, while with the metal active sites, alternating, distal and enzymatic pathways are more preferred to achieve NRR overpotential (ηNRR) < 1 as shown in Fig. 1b.
|
| Fig. 6 (a) Simplified schematic of N2 bonding to TMs. (b) Electronic configuration of the pure B atom and B atom with sp3 hybridization. (c) N2 binding motifs to the B atom on the substrate. Reproduced with permission from ref. 193, Copyright 2018, American Chemical Society. (d) Optimized structures of c-FeB2 and a-FeB2 after N2 adsorption. Comparison of (e) NH3 yields and (f) FEs of c-FeB2 and a-FeB2 PNSs at various potentials. (g) Free energy diagrams of NRR reaction pathways on c-FeB2 and a-FeB2 at U = 0.3 V and pH = 7. Reproduced with permission from ref. 104, Copyright 2021, Elsevier B. V. | |
Unlike the MXenes where surface oxidation is a major concern to block the active sites, once oxidized, these MBenes can catalyze NRR via the self-activating process, reducing O*/OH* into H2O* under reaction conditions, and favoring the N2 electroreduction. As a result, the exceptional activity and selectivity, high active area (≈ 1019 m−2) and antioxidation nature render these MBenes pH-universal catalysts for NH3 production without introducing any dopants and defects. However, vacancy engineering is also explored in the M-bene materials. Both cationic and anionic vacancies are rendered by Li's group and Chen's group respectively and assembled with single atom crystals to bring about more efficiency in the NRR performance by the combined advantages of SACs and M-benes with defects. Re and Os implanted into Mo vacancies of Mo2B2O2 nanosheets (Fig. 7a–c) were found to possess remarkable catalytic activity with relatively low barrier values of the potential-determining step (PDS) of 0.29 and 0.32 eV, which are lower than that of the single Ru atom decorated on Mo2CO2 (0.46 eV).107 Chen's group predicted that Ti single atom doped B-vacant VB2 (Ti@VB2) having a limiting potential of −0.61 V for NRR is the most effective among all the other single atom doped 2D-TMBs with a B vacancy.108
|
| Fig. 7 (a) Top and side views of the structure of SA-doped Mo2B2O2, where red, purple, green, and white balls represent O, Mo, B, and doped SA, respectively. The charge density difference of N2 adsorption geometries in the O vacancy of SA-doped Mo2B2O2: (b) Mo site and (c) SA site. (b) Reactivity screening of Mo2B2O2–SA systems for NRR, according to the linear distribution with regard to the free energy changes of the first and the last hydrogenation steps (ΔG(N2–NNH) and ΔG(NH2–NH3)), with Mo2B2O2–Mo (the pure Mo2B2O2 with O vacancy) as the boundary line. (c) Calculated potential vs. SHE for HER (U*H) and NRR (U*NNH) for selectivity screening. The dashed line represents U*H = U*NNH. Reproduced with permission from ref. 107, Copyright 2020, American Chemical Society. | |
However, there is no parity in the mechanistic performance of the different M-benes. It is absolutely dependent on the metal being used and the phase of the boride being formed. It is however easy to simulate metal as well as mixed-metal borides but for practical experimentation, it is very crucial to maintain appropriate conditions in order to obtain the phase-specific M-benes. Like for example, CoB and Co2B are the most widely synthesized M-benes, applied for different energy applications other than NRR.109 But the synthesis strategy used there may not work accurately for other metal borides, requiring different experimental conditions. Thus, it is indeed important to optimize the conditions and properly characterize the material before going deep into the electrochemical performance for NRR. However, there is enough room for exploration of this category of catalysts as only three to four experimental reports are available on NRR with FeB2, MoAlB, TiB2 and Ti@VB2.
5. Transition metal carbides (TMCs)
Transition metal carbides (TMCs) have been shown to be effective catalysts for the NRR, in addition to transition metal oxides (TMOs) and transition metal nitrides (TMNs).110–115 According to recent studies,116 adsorption capacity for N2 is greatly influenced by elemental electronic properties, since only atoms that have partially filled d-orbitals with correct symmetry can synergistically acquire electrons from N2 and donate back to N2. Notably, the p-back-donation method has the capability of effectively weakening N–N bonds while concurrently strengthening metal–N bonds.117 To activate the N–N bond, it is necessary to fabricate electron-donating electrocatalysts that include an abundance of catalytic activation sites. In accordance with the well-known d-orbital hypothesis,118 transition metal carbides (TMCs) display an electronically favorable architecture and adsorption119 exhibiting intrinsic noble-metal-like behavior because of the dense d-orbitals of the transition metal, which allows for much more p-back donation possibilities for the adsorbates.120 The capacity to donate electrons to the N2 p* antibonding orbitals and cleave the N–N bonds is further enhanced by creating anion vacancies with localized electrons. Moreover, vacant d-orbitals of transition metal carbides have excellent adsorption capacity.121 The sp-hybridized state of the transition metal, which exists in the carbides, is delocalized on the surface, where it will interact with the d-state of the transition metal as well as the s-state of carbon. To effectively activate the N–N triple bond with NRR catalytic activity, a highly occupied orbital affords more possibilities for reverse donation to the p orbital of N2.
Moreover, the two-dimensional transition metal carbides are a novel class of 2D materials that have sparked current interest.122 Metal carbide research began in 2011 with the discovery of the first Ti3C2 compound, which has grown to a family of over 30 members.123 In the report by Sang et al.,124 the authors have grown a TiC single layer on a Ti3C2 substrate to introduce a 2D Ti5C4 material in the field of electrocatalysis. But the prospect of 2D transition metal oxides/nitrides/carbides as possible electrocatalysts toward NRR has only been briefly considered from a theoretical standpoint.
It is believed that Mo carbides (MoC) would be useful for a wide range of electrochemical energy conversion applications, including NRR, because of their comparable d-band electrical density to that of metal Pt.125,126 The transition metal molybdenum (Mo) has been explored for converting N2 gas to NH3. In accordance with DFT calculations, the bond strength of nitrogen (N2) trapped on the Mo domains is too strong to allow the formation of ammonia (NH3) upon the Mo active sites.127 Bonding with nonmetals including carbon atoms with high electronegativity might reduce the Mo and N2 interaction, improving N2 fixing efficiency. Consequently, molybdenum carbides were studied as photocatalytic materials for N2 fixation. Furthermore, the MoC architecture has been utilized as an electrocatalyst for N2 reduction with a lower NRR (0.54 V),128 while, with a 0.3 V potential at its (1 1 1) plane, cubic MoC has been reported as a noble NRR electrocatalyst, proving the MoC material's utility for NRR.128 Additionally, a composite made of oxygen-containing molybdenum carbides embedded in nitrogen-doped carbon layers was created by Qu et al. using dopamine and molybdate as precursors.129 A synergistic combination among O–MoC and N-doped carbon shells resulted in high catalytic activity (NH3 production rate: 22.5 g mg hcat−1), selectivity (95%) (HCl solution: 0.5 m Li2SO4), and stability (95%) (HCl solution: 0.1 m Li2SO4). Interestingly, DFT simulations by Matanovic et al.128 investigated cubic MoC as an electrode material for NH3 production. However, on all MoC surfaces except MoC(111), H-atoms competed with N-atoms. It is possible that HER will be inhibited at low potentials on MoC(111), but this is not the case on any other surfaces. This is owing to the wider stability area of N ad-atoms relative to that of H ad-atoms. As a result of the presence of carbon vacancies, the hydrogen development and build-up of H ad-atoms can be reduced, indicating that the metal-to-carbon ratio can be increased while maintaining the same attraction for N ad-atoms as in MoC. By exposing to high hydrogen evolution conditions, Wang et al.130 developed Mo4C nanodots embedded in carbon nanosheets (Mo2C/C) that served as a better NRR catalyst. Considering ambient circumstances, the as-prepared Mo2C/C demonstrated outstanding catalytic activity with high NH3 production (11.3 mg h−1 Mo2C) and FE (7.8%). Further, their comparative test reduced the influence of hydrogen evolution to get the precise NRR activity of Mo2C/C. The FE increased about 5-fold in the proton-suppressed condition compared to the NRR findings in the proton-enriched condition. Nevertheless, under a proton-suppressed state, the NH3 production rate of Mo2C/C was reduced significantly. Excessive HER suppression may increase NRR selectivity but reduce NRR activity. Thus a suitable proton donor is required. Mo2C also exhibits more activity in HER than in NRR due to the presence of uncontrolled and diverse flaws, edges, and a mixture of distinct crystal facets that are present. A new 2D a-Mo2C material with a strongly oriented (200) facet of the a-Mo2C phase was proven by Sun and Li131 as an NRR catalyst. Due to the Mo2C's single crystal facet, this catalyst attained a phenomenal FE of 40.2%.
The electrocatalytic performance of Mo2C nanodots embedded in ultra-thin carbon nanosheets (Mo2C/C) was reported by Wang et al. to be remarkable for NRR.130 Inside a 0.5 M Li2SO4 solution, NH3 yield was 11.3 mg h−1 (pH = 2). The NRR technique utilizes Mo2C nanodots as active center sites, as indicated by DFT and electronic state density calculations. The results showed that severe HER inhibition did not promote NRR activity, showing that Mo2C/C may execute NRR under HER circumstances. Mo2C nanorods were produced and deposited on glassy carbon electrodes for electrochemical NRR. Mo2C/GCE had good catalytic activity, yielding 95.1 mg NH3 per mgcat and 8.13% faradaic efficiency (0.1 M HCl at 0.3 V (vs. RHE)). A highly active surface, the (121) facet, of the Mo2C nanorods successfully absorbed and activated N2 as a result of its high surface activity. Besides Mo2C, the researchers discovered cobweb-like MoC6,132 Cr3C2 nanoparticles,133 and additional N2 fixation catalysts.
However, TMC-based catalysts have limited NRR activity because their HER-active edges favor H-ad atoms over N-ad atoms. To address this issue, structural or component adjustments are required to improve NRR. To achieve effective NRR catalysis under high hydrogen evolution conditions, researchers synthesized molybdenum carbide nanodots embedded in ultrathin carbon nanosheets (Mo2C/C). This unique inlaid arrangement reduces hydrogen overflow on the catalyst surface, allowing for increased N2 diffusion. Using density functional theory, Li et al. discovered that the surface of molybdenum carbide may be terminated by hydrogen through the Volmer process.127 Due to its moderate HER overpotential, huge DGmax (1.4 eV), and kinetic barrier (20.0 eV), H-covered Mo2C was not an effective NRR catalyst. Consequently, molybdenum carbide has been reported hardly for NRR. In 2018, Cheng et al. examined the electrocatalytic activity of Mo2C nanodots incorporated in carbon nanosheets (Fig. 8a).130 They had a high NH3 yield (11.3 mg h−1 mgcat−1) and faradaic efficiency (7.8%). To achieve actual NRR activity, the authors applied a hydrophobic carbon cloth instead of a hydrophilic one, and increased the pH from 2 to 3. When compared to the findings obtained under proton-rich circumstances, the faradaic efficiency obtained under proton-suppressed conditions was approximately five times higher (Fig. 8b), but the NH3 yield was much lower (Fig. 8c), showing that an optimal proton donor is required for NRR to produce a large NH3 yield. The extremely active surface of Mo2C nanodots allows them to absorb and activate nitrogen (Fig. 8d). Also, the Mo2C nanodots were equally enclosed in carbon nanosheets, reducing hydrogen coverage on the catalyst surface and increasing N2 diffusion. On the other hand, Fang et al.134 created Mo2C nanodot coated 3D ultrathin macroporous carbon (Mo2C@3DUM-C). Mo2C@3DUM-C showed increased electron and mass transmission due to its three-dimensional ultra-thin macroporous carbon framework. At 0.20 V, Mo2C@3DUM-C demonstrated 9.5% NRR efficiency and 30.4 mg per h per mgcat NH3 yield. Mo2C@3DUM-C also had high catalytic stability for NRR due to its geometrical and electrochemical stability. In another study, Qu et al. effectively synthesized oxygen-doped MoC nanoparticles encapsulated in N-doped carbon shells with adjustable core–shell nanomaterials (OeMoC@NC-T) for NRR135 (Fig. 8e). OeMoC produced 22.5 mg per h per mgcat NH3 and had a faradaic efficiency of 25.1%. On the basis of reaction energies (vs. conventional hydrogen electrode), V3C2 and Nb3C2 were identified to be the most promising options. From a kinetic perspective, V3C2 had lower activation energy barriers (0.64 eV) than Nb3C2, and its reaction profile was smoother with lower energy barriers for additional hydrogenation phases.136 On the other hand, DFT calculations revealed that the central Ti atoms displayed the maximum adsorption of N2 (1.344 eV) as compared to certain other sites such as O, C, and lateral Ti atoms. Thus, Ti3C2 supported by stainless steel mesh (SSM) obtained a maximum faradaic efficiency of 4.62% (0.1 V versus RHE) and an NH3 yield rate of 4.72 μg h−1 cm−2.137
|
| Fig. 8 (a) Schematic representation of the synthetic route for molten salt Mo2C/C nanosheets. (b) Faradaic efficiency, (c) yield rate and (d) NRR mechanistic pathway of Mo2C/C in proton-suppressed and enriched environments. Reproduced with permission,130 Copyright 2018, Wiley-VCH Verlag GmbH. (e) Schematic illustration of the fabrication procedure of OeMoC@NC-T. Reproduced with permission,135 Copyright 2019, American Chemical Society. | |
Using an ultrasonic reduction method, Liu et al. created an accordion-like morphology of Au nanoparticle-anchored Ti3C2. At 0.2 V, Au/Ti3C2 produced 30.6 mg per (h mg) of NH3 and had a Faraday efficiency of 18.34%.138 The authors established that the high energy of N2 adsorption on the interface among high-valence-state gold clusters and Ti3C2 represented the driving force for the breaking of triple N–N bonds, and that the overall activation energy threshold could be decreased by efficiently stabilizing N2* species while destabilizing NH2NH2* species via an alternate channel instead of the conventional one. As a consequence of the synergistic effect, 1T-MoS2/Ti3C2 composites demonstrated excellent stability, excellent durability, and remarkable NRR activity, with a faradaic efficiency of 5.26% and a nitrogen production rate of 36.28 mg h−1 mgcat−1 at 0.35 V vs. RHE.139
5.1 MXenes and MXene derivative catalysts
MXenes have emerged as one of the foremost intensively explored novel materials. They possess excellent potential as active catalysts for catalytic conversion including environmental remediation, due to their remarkable layered architecture, relatively high surface area, ample active sites, and superior chemical inertness. MXenes are intriguing catalysts for N2 absorption as well as reduction, as their effectiveness has indeed been formerly forecast.140,141 Recent developments illustrate MXenes or their derivatives in adsorbing, stimulating, and reducing nitrogen (N2) to ammonia (NH3) via electrocatalytic as well as photoelectrochemical nitrogen reduction reaction (NRR). Despite the conventional Haber–Bosch approach, which directly implements fossil fuels with highly energetic techniques, the electrochemical NRR is regarded as appropriate as well as environmentally acceptable for NH3 production. Nevertheless, the NH3 productivity and efficacy of NRR adopting MXene-based catalysts continue to be relatively insufficient to achieve real world applications. Consequently, a basic understanding of NRR pathways with their considerable limitations should be addressed for prospective advancements.
In this regard, several experimental investigations with comprehensive findings suggest that MXenes could function competitively with the reference Pt-, Co-, or Pd-based catalysts in converting N2 to NH3. Furthermore, one most significant benefit of MXenes as a catalyst is that certain chemicals included within seem to be earth-abundant. Owing to their affordability, the catalysis cost can indeed be severely decreased without affecting the effectiveness. Throughout NH3 electrosynthesis, Ti3C2/FeOOH displayed an excellent FE of approximately 5.78% at an exceptionally low potential, closer to that of Pt.142 Ti3C2Tx nanosheets besides binding with dimethyl sulfoxide (DMSO) as well acquired better electrochemical behavior for nitrogen reduction, showing an NH3 production of 20.4 mg h−1 mgcat.−1 with a FE of 9.3% in acid buffer.143 Various forms of MXenes might be effectively utilized for the catalysts for the electrochemical NRR, e.g. V3C2 and Nb3C2, leading to maximal overpotentials of approximately 0.64 and 0.90 eV, respectively, and hence diverse MXene nanocomposites have also been published.144 Significant modification techniques including improvement of MXenes via considerably improved synthesis with appropriate material compositions are being developed to enhance their applicability for N2 catalyst purposes.
However, the NRR does have a slow kinetic response and therefore is inadequately generated. The emerging 2D MXene category is considered to be more competitive in aqueous medium, suppressing HER while promoting NRR. MXenes could be synthesized into much more efficient catalysts as well as coupled with other catalytic substances to produce hybrid materials. MXenes could be fabricated into thin films as 2D materials, strengthening their feasibility for implementation in devices. Conversely, the minimum quantity of material utilization and the minimal infrastructure are anticipated to be cost-effective in terms of hydrogen generation and its production rate. A similar approach can be adopted for NRR catalysts employing MXenes. Additionally, thin-film MXenes could be embedded into the reactors thereby potentially leading to low-cost NH3 production. But it is still too early to draw such a definitive inference since in the attempt to reasonably develop the optimum MXene catalyst for NRR with practical implications, numerous tasks must be addressed. Table 2 summarizes the research paradigm carried out for N2 reduction to NH3 adopting various metal-carbides as well as MXene-based catalysts and its derivatives as an electrocatalyst.
Table 2 Summary of metal carbides, MXenes and MXene derivatives for NRR
Catalyst |
Electrolyte |
FE (%) |
NH3 yield |
Potential vs. RHE (V) |
Ref. |
α-Mo2C |
0.1 M Na2SO4 |
40.2 |
3.36 μg h−1 cm−2 |
−0.55 |
174
|
Mo2C@3DUM-C |
0.1 M HCl |
9.5 |
30.4 μg h−1 mgcat−1 |
−0.2 |
134
|
1T-MoS2/Ti3C2 |
0.1 M HCl |
5.26 |
36.28 μg h−1 mgcat−1 |
−0.35 |
139
|
Au/Ti3C2 |
0.1 M HCl |
18.34 |
30.6 μg h−1 mgcat−1 |
−0.2 |
138
|
Mo2C/C |
0.5 M Li2SO4 |
7.8 |
11.3 μg h−1 mgcat−1 |
−0.3 |
130
|
Cr3C2@CNFs |
0.1M HCl |
8.6 |
23.9 μg h−1 mgcat−1 |
−0.3 |
133
|
Mo3Fe3C |
0.1 M Li2SO4 |
27 |
72.5 mmol h−1 gcat−1 |
−0.05 |
101
|
Mo2C/NC |
0.1 M Na2SO4 |
12.3 |
70.6 μmol h−1g cat−1 |
−0.2 |
175
|
1T-MoS2@Ti3C2 |
0.1 M HCl |
10.94 |
30.33 μg h−1 mgcat−1 |
−0.3 |
176
|
Surface-engineered Ti3C2 |
0.1 M KOH |
7.01 (20 °C) |
1.71 μg h−1 cm−2 |
−0.2 |
177
|
9.03 (60 °C) |
12.46 μg h−1 cm−2 |
−0.2 |
Ti3C2Tx (T ¼ F, OH) MXene nanosheets |
0.1 M HCl |
9.3 |
20.4 μg h−1 mgcat−1 |
−0.4 |
178
|
Fluorine-free Ti3C2Tx (T ¼ O, OH) |
0.1 M HCl |
9.1 |
36.9 μg h−1 mgcat−1 |
−0.3 |
179
|
TiO2/Ti3C2Tx |
0.1 M HCl |
8.42 |
26.32 μg h−1 mgcat−1 |
−0.6 |
180
|
Oxygen-vacancy-rich TiO2/Ti3C2Tx |
0.1 M HCl |
16.07 |
32.17 μg h−1 mgcat−1 |
−0.45, −0.55 |
181
|
Ti3C2 MXene nanoribbons |
0.5 M KOH |
3.1 |
14.76 μg h−1 mgcat−1 |
−0.5 |
182
|
Hydroxyl-rich Ti3C2Tx QDs |
0.1 M HCl |
13.30 |
62.94 μg h−1 mgcat−1 |
−0.5 |
183
|
V2CTx MXene |
0.1 M Na2SO4 |
4 |
12.6 μg h−1 mgcat−1 |
−0.7 |
184
|
Cu/Ti3C2Tx MXene |
0.1 M KOH |
7.31 |
3.04 mmol h−1 cm−2 |
−0.5 |
185
|
NeS-doped Ti3C2Tx |
0.05 M H2SO4 |
6.6 |
34.23 μg h−1 mgcat−1 |
−0.55 |
186
|
Ni nanoparticles/V4C3Tx MXene |
0.1 M KOH |
14.86 |
21.29 μg h−1 mgcat−1 |
−0.55 |
187
|
6. Transition metal nitrides (TMNs)
For overall development of NRR, along with noble metals like Au, Pd, Rh, Ru, etc., various advanced transition metal electrocatalysts such as transition TMNs, TMCs,130,145 TMOs146,147 and TMBs148,149 have attracted the attention in recent years. Among these, TMNs are of great importance due to their high conductivity, modulable electronic structures, good stability and cost efficiency. As explained above, for NRR, different types of mechanisms can be followed depending upon the system. TMNs follow the heterogeneous Mars-van Krevelen (MvK) mechanism, which makes these materials more promising as in this mechanism, the aforementioned two main challenges in NRR are overcome: (1) elimination of high energy required to break the triple bond of the N2 molecule and (2) suppression of the parasitic HER.150,151 Basically, in this mechanism, the N on the catalyst layer is electrochemically reduced to ammonia under ambient conditions and the so formed vacancies are replenished with gaseous nitrogen that regenerates the catalyst (Fig. 1e). Furthermore, the adsorption of gaseous N2 onto the nitride catalyst is highly facilitated as the N-vacancy decorated on the nitride surface has high surface energy that solves the problem of low solubility of N2 in water.36,152,153
Skulason et al. provided deep insights into catalysts especially into TMNs (FeN, CoN, NiN, RuN, RhN, PdN, OsN, IrN, CrN, VN, NbN, CrN) which are active and selective for NRR to ammonia following the MvK mechanism by theoretical investigations. The onset potential for NH3 formation was calculated by DFT calculations via conventional AM, DM, and combination of these two mechanisms (AM-DM) and compared with the MvK mechanism to determine the lowest onset potential on the clean surface of TMNs.154 Since adsorption of N2 is an endothermic process, therefore, MvK is always favoured on TMNs. Out of the various TMNs, rocksalt VN and ZrN are found to be the most promising candidates due to the requirement of low bias for ammonia production and HER suppression. DFT presented that at the onset potential, the so formed N-vacancies get easily repaired with gaseous nitrogen injected to the system and are not poisoned by oxygen or hydrogen from the aqueous electrolyte.155,156
Zhang et al. presented a computational study of molybdenum nitride (MoN2) nanosheets as an electrocatalyst for NH3 synthesis using DFT.157 Pure MoN2 itself is not found to be an ideal catalyst but Fe-doping in MoN2 can reduce the ΔGmax for the rate determining step (RDS) and the so formed Fe-doped MoN2 can act as a promising catalyst for electrochemical conversion of NH3 from water and air. Therefore, the untreated MoN2 can be used as an excellent starting material for designing advanced NRR electrocatalysts.
Sun et al. demonstrated the non-noble metal electrocatalyst Mo2N nanorods for the first time as an efficient electrocatalyst to convert N2 to NH3 under ambient conditions in 0.1 M HCl and achieved a high FE of 4.5% and a NH3 yield of 78.4 mg h−1 mgcat−1 at −0.3 V vs. RHE, which is substantially higher than that of a MoO2 precursor.158 The DFT calculations revealed that after nitrogenation of MoO2, the free energy barrier (ΔGH*) of the potential determining step of NRR decreases dramatically. The same group further synthesised the MoN nanosheet array on the carbon cloth (MoN NA/CC) as an efficient catalyst for NRR with a high NH3 yield of 3.01 × 10−10 mol s−1 cm−2 and a FE of 1.15% at −0.3 V vs. RHE in 0.1 M HCl.159 DFT calculations revealed that MoN NA/CC follow the MvK mechanism for NRR. Further, Wang et al. for the first time modified the MoN electrocatalyst with cation vacancies by fabricating MoN nanocrystals with sufficient Mo vacancies in a N-doped hierarchical porous carbon framework (MV-MoN@NC) because engineering cation vacancy in the TMNs is an effective strategy to improve the electrochemical NRR response.160 The formation of defects within the sample was proved by X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS) studies. MV-MoN@NC in comparison with non-defective samples MoN, NC, and MoN@NC exhibited best catalytic activity with 76.9 μg h−1 mg−1 cat. ammonia yield and 6.9% FE at −0.2 V vs. RHE with stability up to 48 h. The cation vacancy decorated MV-MoN@NC has shown a much superior NH3 production rate to that of reported electrocatalysts with anion vacancies. The occurrence of NRR via MvK was confirmed by the NMR technique which gave the qualitative analysis of the 15N isotopic experiment by weakening of triplet coupling of 14NH4+ in the NMR spectra when 15N is used as a feed gas. The improvement in the NRR activity was confirmed by computational and experimental results, which revealed that Mo vacancies in the MoN surface regulate the electronic structure of MoN and reduce the barrier height from 1.40 to 0.61 eV for the potential-determining step (PDS). Further, local density of states (LDOS) revealed that Mo vacancies created strong hybridisation between molecular orbitals and Mo d orbitals, which led to the easy release of NH3 molecules as the strength between N and Mo atoms got decreased. This work provides a new pathway of synthesizing electrocatalysts with cation defects in nitrides to catalyze N2 reduction. Shanmugam et al. recently prepared an efficient and cost-effective electrocatalyst: cubic molybdenum nitride (γ-Mo2N) nanoparticles by an in situ nitridation method on two-dimensional hexagonal boron nitride (h-BN) sheets.161 The interfacial engineering of the Mo2N-BN bridge is found to be selective for N2 reduction. This way of controlling the defects to design the electronic structure of the catalyst can be an effective way for selective NRR.
Vacancy creation within the catalyst has great impact on enhancing the intrinsic activity of electrocatalysts because there occurs alteration in the electronic structure, adsorption–desorption energies of the intermediates and surface charge-transfer properties. For example, oxygen vacancies162 and nitrogen vacancies121 improved the adsorption and activation of N2 molecules for subsequent reaction steps. In the case of TMN-based NRR electrocatalysts following the MvK mechanism, N-vacancies have an important role to play. In the MvK mechanism, N-vacancies are created by the release of NH3 molecules and are replenished with the feed of N2. There occurs cycling between the empty and filled states. Qiao et al. prepared a 2D layered W2N3 nanosheet having N-vacancies.37 These N-vacancies were characterized by a series of ex situ synchrotron-based EXFAS measurements and were found to be active for NRR with a NH3 production rate of 11.66 ± 0.98 μg h−1 mgcat−1 and a FE of 11.67 ± 0.93% at −0.2 V vs. RHE. Further DFT calculations also suggested that N-vacancies on W2N3 facilitate N2 adsorption and also lower the thermodynamic limiting potential for NRR.
Qu et al. developed a VN nanowire array on carbon cloth (VN/CC) via nitridation of the V2O5 nanowire array precursor and achieved a high NH3 yield (2.48 × 10−10 mol−1 s−1 cm−2) and a FE of 3.58% at −0.3 V vs. RHE in 0.1 M HCl.163 This work along with providing us an efficient catalyst material for NRR in acidic media also opens up a new avenue for TMNs in NRR.
For mechanistic studies of MvK in NRR, Yan et al. performed quantitative isotope-exchange experiments to determine the density of active sites in the initial and steady state in NRR catalysts (Fig. 9a).36 In 14N/15N-exchange experiments, the initial active sites were identified by the amount of 14NH3 formed with 15N as a feed. Then, in the steady state the number of active sites could be determined by subjecting the used catalyst for the second round with 14N as a feed. Therefore, only 15N sites will participate in 15NH3 production (Fig. 9b and c). Using this approach, the intrinsic activity and quantitative analysis can be achieved. This study opens up a new way for deep understanding of active sites on TMNs for NRR.
|
| Fig. 9 (a) Schematic illustration representing the isotopic exchange experiments on V14NO to determine the density of active sites of the initial and steady-state in the NRR. (b) Isotopic composition of active surface N sites as a function of time in the NRR. (c) Amounts of 14NH4+ and 15NH4+ produced during the isotopic exchange experiments at various time points during NRR. Reproduced with permission from ref. 36, Copyright 2019, Wiley-VCH Verlag GmbH. | |
Du's group in a recent study did a critical assessment of the electrocatalytic activity of vanadium(III) nitride, niobium(III) nitride, and Nb4N5 for NRR.158 According to the previous theoretical studies, vanadium and niobium nitrides are expected to be catalytically active toward NRR but this study argued that ammonia is produced in nitride catalysts from lattice N but in a non-catalytic process. So, the present study emphasizes the need of reliable testing and analysis techniques for the right assessment of catalytic properties of the materials.
Within the defect engineering, heteroatom dopants are important participants as they can modulate the surface electronic structure and can reduce the overpotential for the electrocatalytic process to fasten up the NRR process.164 For non-metal heteroatom doping in pristine catalysts, S, O, B and P are selected. However, in the case of TMNs oxygen doping has shown positive effects on NRR.162,165 Yang's group presented that partially oxidised VN (VN0.7O0.45) is an active and stable electrocatalyst for NRR that follows the MvK mechanism as confirmed by 15N2 experiment.166
To study the evolution of the catalyst during the reaction, operando X-ray absorption near edge spectroscopic (XANES) analysis was conducted (Fig. 10a–c). As shown in the figure the position of the corresponding white lines remains the same with time indicating no detectable leaching of V during NRR. The interesting point is that during NRR there occurs conversion of VN0.7O0.45 to VN which is responsible for deactivation of the catalyst. The conversion rate increases as the potential becomes more negative (Fig. 10d). It is confirmed by the decrease in the intensity of the pre-edge peak. This result was also supported by DFT investigations, that only the N2 atoms adjacent to surface O are responsible for catalytic activity (Fig. 10e). This work opens up the area for providing more experimental evidence that will verify the hypothesis and the theoretical work.
|
| Fig. 10 Operando K-edge XANES spectra of VN at different potentials of (a) 0.1 V and (c) 0.2 V versus RHE as a function of time. The inset in (c) shows the corresponding pre-edge peak. (b) The left and right panels show the pre-edge and the white line the peaks at 0.1 V vs. RHE as a function of time, respectively. (d) Time-dependent pre-edge area at different potentials. (e) Proposed reaction mechanism for NRR on the surface of VN0.7O0.45via the MvK and catalyst deactivation mechanism. Reproduced with permission from ref. 166, Copyright 2018, American Chemical Society. | |
Another study demonstrating that the performance of TMNs for NRR can be enhanced by partial oxidation was done by Shao et al.162 Partially oxidized chromium nitride (chromium oxynitride: CrO0.66N0.56) nanoparticles were synthesized and their NRR activities were evaluated in a proton exchange membrane electrolyzer (PEMEL) system under ambient conditions. Their NRR activity was found to be better than that of pure Cr2O3 and CrN. This finding confirmed the hypothesis that metal oxynitride-based catalysts can act as promising candidates for NRR.
Zhang et al. presented a report with O doping in commercial titanium nitride (TiN) with active phase titanium oxynitride (TiOxNy) obtained by plasma etching (PE) of ball-milled TiN.165 The as-synthesized catalyst TiN-PE with high TiOxNy active species delivered a NH3 yield rate of 3.32 × 10−10 mol s−1 cm−2 and a FF of 9.1% at −0.6 V vs. RHE in 0.1 M Na2SO4 solution which is significantly higher than that achieved for pristine commercial TiN and ball-milled TiN-BM samples. This study gives proof of the benefits of doping for improved catalysis.
Recently, single-atom catalysts (SACs) have gained much attention in the field of catalysis due to their unique electronic structure, uniform distribution of SACs in the substrate and their maximized utilization.57,167 Many SACs such as Mo,168 Fe,169 Sc,170 Y,170 Ru,171etc. with enhanced NRR activity have been reported. These reported SACs are available in powdered form, so polymer binder is used to attach the catalyst to the current collector that reduces the overall activity of the catalyst. In a recent report, Gao and Zhang developed a 3D-self standing integrated electrode with single Bi atom incorporated hollow titanium nitride (TiN) nanorods encapsulated in a nitrogen-doped carbon layer (NC) supported on carbon cloth (NC/Bi SAs/TiN/CC) for electrocatalytic NRR. The 3D porous structure ensured the maximum exposure of active sites along with efficient mass transfer that improves the catalyst activity. The combined effect of the NC matrix and TiN nanorods prevents the aggregation of Bi SACs and also facilitates the charge transport in NRR. On the other hand, the cooperative effect between Bi SAs and TiN simultaneously promotes the hydrogenation of N2 and eases the desorption of NH3. Therefore, NC/Bi SAs/TiN/CC attained a superior FE of 24.60% at −0.5 V vs. RHE and a high NH3 yield rate of 76.15 μg mgcat−1 h−1. This study enforces to work in future on 3D self-supported SACs by rational designing of the structure and electronic configuration for improved catalysis. The TMNs used for NRR have been summarized in Table 3.
Table 3 A brief summary of TMNs used for NRR
Catalyst |
Electrolyte |
FE (%) |
NH3 yield rate |
Potential |
Ref. |
MoN NA/CC |
0.1 M HCl |
1.15 |
3.01 × 10−10 mol s−1 cm−2 |
−0.3 V vs. RHE |
159
|
W2N3 |
0.1 M KOH |
11.67 ± 0.93 |
11.66 ± 0.98 μg h−1 mgcat−1 |
−0.2 V vs. RHE |
37
|
NC/Bi SAs/TiN/CC |
0.1 M Na2SO4 |
24.60 @ −0.5 V vs. RHE |
76.15 μg mgcat−1 h−1 @ −0.8 V RHE |
— |
188
|
Mo2N nanorods |
0.1 M HCl |
4.5 |
78.4 μg h−1 mg cat−1 |
−0.3 V vs. RHE |
158
|
VN/CC |
0.1 M HCl |
3.58 |
2.48 × 10−10 mol−1 s−1 cm−2 |
−0.3 V vs. RHE |
163
|
VN |
0.05 M H2SO4 |
6.0 |
3.3 × 10−10 mol s−1 cm−2 |
−0.1 V vs. RHE |
166
|
TiN-PE |
0.1 M Na2SO4 |
9.1% |
3.32 × 10−10 mol s−1 cm−2 |
−0.6 V vs. RHE |
165
|
MV-MoN@NC |
0.1 M HCl |
6.9% |
76.9 μg h−1 mgcat−1 @ −0.2 V vs. RHE |
— |
160
|
CrO0.66N0.56 |
|
6.9% @ 1.8 V |
8.9 × 10−11 mol s−1 cm−2 @ 2.0 V |
— |
162
|
7. Conclusion and future perspective
In this work, we have systematically investigated the fundamental practices of the nitrogen reduction process. The kinetics of NRR is governed by a number of factors, which include nitrogen solubility in electrolytes, competitive HER and choice of materials that facilitate NRR over HER. Here for the first time, we have provided a detailed understanding of the solubility of N2 in different ionic liquid electrolytes, being worked upon to date, which can be further implemented experimentally during NRR. Thereafter, all the factors including choice of electrolyte medium, control of pH and material engineering have been generalized that provide a brief overview of which factors should be kept in mind while performing NRR so that HER could be substantially suppressed. Finally, we have highlighted three categories of catalysts like transition metal borides, carbides and nitrides and discussed their importance in NRR, developments over the ages as well as scopes that could be extended further. These materials could be improvised in a better way considering all the factors and choice of metals highlighted in the review in order to achieve significant NRR in terms of yield, production rate and faradaic efficiency.
• Being an emerging field, there is extensive room for exploration in terms of experimentation in the case of TMBs. The theoretically predicted structures of the TMBs and the presumed conditions of material performance do not often hold true and conventional during their experimental counterpart and naturally discrepancies arise to establish the actual active structure and its mechanistic role in NRR. This would be easier if experiments and theory go hand in hand at this infancy of the TMBs in the field of NRR.
• Recently, mixed metal borides are coming into limelight due to the electronic configuration and orbital overlap between the mixed metals and obviously the synergistic role played by the metals and the boron centre benefitting NRR. Only one experimental report provides information about mixed metal borides, so there is still a lot of opportunity to tune the choice of metals preferably, which would favour the NRR kinetics.
• Since there are still single reports for several metal borides for NRR, more experimental works and optimizations are desired to verify the reproducibility of the reaction conditions for various metals.
• To leverage high-performance, TMC electrocatalysts are also viable in the upcoming years, the respective major topic areas necessitate a broad focus. Presently, several unique concepts for scalable and reliable fabrication of effectively tailored TMCs need to be suggested for addressing functional electrocatalysts. Integrating numerous modification techniques, notably nanosizing, hybridization, or heteroatom doping, with a convenient fabrication technique throughout one phase or less phases is anticipated.
• Theoretical results might reveal valuable insight regarding the energy transmission pathway of chemical intermediates, which might encourage the development of the desired TMC architecture at the atomic level.
• For further improvement in TMNs as NRR catalysts, the synthesis methods should be understood deeply. Djire et al.172,173 synthesized Ti2NTx and Ti4N3Tx nitride MXenes and presented their usage in storage and HER. So, nitride MXenes would be an interesting topic to work on their material characterization, MvK mechanism and performance evaluation in NRR.
• In situ high-edge experimental tools are required to gain deeper insight into the mechanistic pathways followed by all the categories of catalysts for NRR.
Recently there has been growing interest for the interdisciplinary compounds like TM-boro-carbides and boro-nitrides because of the superconductivity and synergistic effect of the material constituents towards NRR.
Conflicts of interest
There are no conflicts to declare.
Acknowledgements
A. B., S. B. and T. B. thank the Institute of Nano Science and Technology, Mohali, for providing the fellowship. This work was financially supported by the DST SERB (CRG/2020/005683) funding agency.
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Footnote |
† These authors contributed equally. |
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