Recent advances in 2D structured materials with defect-exploiting design strategies for electrocatalysis of nitrate to ammonia
Abstract
Ammonia has been used in a wide variety of applications, and with the recent interest in hydrogen energy as a green energy source, it is emerging as a cost-effective, high-density hydrogen carrier due to its three hydrogen atoms. Currently, ammonia is produced by the Haber-Bosch method at high temperatures and pressure, which is energy-intensive and emits large amounts of carbon dioxide. As a viable alternative, the electrochemical conversion of nitrate to ammonia has emerged as an efficient and eco-friendly synthesis method. To encourage further exploration in this field, this review offers insights into utilizing two-dimensional materials as electrochemical catalysts, focusing on designs that exploit defects for nitrate reduction to ammonia.
Keywords
INTRODUCTION
As the world transitions to a renewable energy and hydrogen (H2) economy to achieve a carbon-neutral society, ammonia is gaining traction as a hydrogen carrier[1,2] and carbon-free fuel[3,4] for hard-to-decarbonize sectors such as power generation[5,6] and transportation[7,8]. Unlike hydrogen, which liquefies at around -253 °C, ammonia liquefies at -34 °C, making it easy to store and transport [Table 1][9,10]. Globally, about 180 million tons of ammonia are produced yearly[11], of which 80% is used as a fertilizer for agriculture, and the remaining 20% is used in explosives, pharmaceuticals, and more[12]. Ammonia is produced under high temperature and pressure conditions (350-550 °C, 150-250 bar) via the Haber-Bosch process, which is an energy-intensive procedure that requires 1%-2% of the total energy produced by humans on the earth[13] [Figure 1A]. In addition, the amount of methane consumed in the production process is about 3.5 times higher, and more than 400 million tons of CO2 is emitted annually to produce ammonia, which can cause environmental problems[14].
Comparison of liquid hydrogen and liquid ammonia
Properties | Unit | Liquid hydrogen | Liquid ammonia | Ref. |
Density | kg/m3 | 70.6 | 682 | [13] |
Transported temperature, pressure | °C, bar | -253, 1.2 bar | -33, 1 bar | [13] |
The gravimetric energy density (LHV) | MJ/kg | 120 | 18.6 | [14] |
Volumetric energy density (LHV) | MJ/L | 8.49 | 12.7 | [14] |
Gravimetric hydrogen content | wt% | 100 | 17.8 | [14] |
Volumetric hydrogen content | kg H2/m3 | 70.8 | 121 | [14] |
Explosive limit in air | vol% | 18.3-59 | 16-25 | - |
Storage method | Liquefaction | Liquefaction | - |
Electrochemical ammonia production has been proposed as an alternative to the Haber-Bosch process and is gaining traction due to several advantages [Figure 1B]. First, it is energy efficient, as ammonia can be produced under ambient conditions, as opposed to the high temperature and pressure conditions of the Haber-Bosch method[15]; Second, it is environmentally friendly as it can be combined with renewable energy sources (solar, tidal, and wind) with low carbon emissions[16]; Third, it uses nitrogen and water as reactants, eliminating the use of fossil fuels as a source of H2, with the required protons (H+) generated on-site through the oxidation of water[17]. Finally, the process has advantages such as flexible reaction control[18], scalability, and on-demand on-site NH3 production[19]. Electrochemical ammonia synthesis is mainly based on nitrogen reduction reactions (NRR)[20,21], and although many preliminary results have been obtained, the low efficiency has limited its commercialization[22]. To overcome this limitation, electrochemical ammonia synthesis using the ionic states of nitrogen oxides has recently been investigated[23-27].
From the nitrogen cycle, nitrogen oxides are stable forms under normal aerobic conditions[28]; however, as the accumulation of nitrogen oxides increases due to industrial activities, it causes health problems such as liver damage[29] and blue baby[30]. To restore the nitrogen cycle, the World Health Organization (WHO) stated that the maximum tolerable concentration of NO3- in water and wastewater is 50 mg/L[31]. For the removal of nitrogen oxides, physical removal methods are still used, such as reverse osmosis[32] or ion exchange[33]; however, these costs are high, about $1-2 million per year per city (based on a population of 500,000 in the US)[34].
Recently, nitrate reduction reaction (NitRR), also known as NO3RR, has been studied due to its ability to synthesize ammonia and remove pollutants simultaneously[35,36]. In addition, following advantages over nitrogen, the solubility of NO2- or NO3- is about 40,000 times that of N2 gas, and the dissociation of N-O (204 kJ/mol) compared to N≡N (945 kJ/mol) is much easier, making NitRR more economical than NRR[37,38]. As a result, the total conversion and energy efficiency of NitRR is much higher than NRR, and its performance can be further improved by strategic catalyst design. NitRR mechanisms involve nine protons, eight electrons, and reaction pathways depending on the reaction conditions[39]. Due to their complex pathways, NitRR to ammonia has a variety of by-products, such as N2, NO, and NO2-, which increases the difficulty of analyzing the mechanism[40]. Various papers have revealed the mechanism, selectivity, and activity of NitRR. In previous studies, the rate-determining step (RDS) of NitRR is generally known to be NO3- to NO2- on transition metal (TM) surfaces and under acidic conditions[41]. The RDS can be seen in Figure 2. To increase the efficiency of the overall NitRR, it is necessary to develop a catalyst that facilitates the adsorption/desorption of NO3-. The metal-based catalysts, such as Pt[42], Pd[43], Ag[44], Sn[45], and Cu-based catalysts[46-48], are considered universal selections in the electrocatalytic process to lower the NitRR overpotential due to their high activity and appropriate adsorption energy of nitrate[49]. These are verified theoretically by the online differential electrochemical mass spectrometry (DEMS) and density functional theory (DFT) calculation[43,46,48].
Over the past decade, there has been increasing interest in atomistic, low-cost two-dimensional (2D) nanosheet materials with unique physicochemical properties, such as high specific surface area, desirable morphology with myriad binding sites, and excellent reaction rates due to fast ion diffusion pathways[50]. In particular, 2D nanosheets are promising materials for catalysis due to their high surface efficiency[51], which can be exposed to active sites. Many studies have been conducted on layered double hydroxides (LDH)[52,53], chalcogenides[54,55], MXenes[56,57], metal-organic frameworks (MOFs)[58,59], etc.[60-62]. These 2D materials have found applications as catalysts or substrates, leveraging their intrinsic properties such as conductivity and activity for NitRR. Certain 2D materials, such as graphene, show limited electrocatalytic properties for NitRR; however, they have high conductivity, rendering them more suitable as substrates than active materials. This enhances conductivity and creates a synergy effect when used with functional materials.
To synthesize efficient electrocatalysts, porosity engineering is critical in carrying abundant active sites and shortened channels through meso-/macropores for mass/charge transport[63]. Also, the oxygen vacancy (OV)[64,65] in oxides is used as a powerful strategy to regulate the crystalline structure, electronic structure, and surface properties. In addition, doping heteroatoms efficiently modifies the electron structure of electrocatalysts to decrease the value of GH*∆ of the electrocatalysts and to improve electrochemical activity[66]. It can make synergistic effects to boost mass transfer on 2D nanosheets and increase active sites through the multiscale defect. Moreover, the adjustment of interlayer spacing can not only tune the atomic distance and electron interaction but also manipulate the electronic structure of host materials, promising higher electrical conductivity[54]. Therefore, design strategies for electrocatalysts make it very possible to modulate the binding strength of intermediates, such as NO2-, and the competitive hydrogen evolution reaction (HER) process in NitRR.
In this review, we provide an overview of 2D materials as electrochemical catalysts and report the latest results of applying defects, such as doping, OVs, and topological defects, to enhance their activity as electrocatalysts in the electrochemical synthesis of ammonia. We also present our views on future research directions for ultrathin 2D materials to encourage further active research.
2D STRUCTURE ELECTROCATALYSTS: DEFECT ENGINEERING
Layered double hydroxides
The earth-abundant TM catalysts have been focused on overcoming the disadvantages of noble metal catalysts. However, the TMs quickly foam M-H bonds, leading to low Faradaic efficiency (FE) and poor selectivity of NH3[67,68]. High HER performance makes NitRR performance soft because HER is a competitive reaction with NitRR. Moreover, another problem exists in that NO3- has an innately lower binding affinity with TMs in the aqueous solution because of strong hydrogen bonding and its symmetrical resonant structure[47]. Recently, TM-based LDHs (TM LDHs, [M1-x2+M´x3+(OH)2]x+(An-)x/n·mH2O), sometimes called Hydrotalcite-like compounds (HTLCs), have been focused on NitRR fields. The TM LDH consists of divalent (M2+: e.g., Ni2+, Mg2+, or Zn2+) and trivalent (M´3+, e.g., Mn3+, Fe3+, and Al3+) metal cations with interlayer exchangeable inorganic or organic anions (An-: e.g., NO3-, SO42-, CO32-, and Cl-)[69]. TM LDH catalysts have many advantages, such as large surface area, active site, low cost, easily tunable electric structure, and chemical composition[70]. The various synthesis methods of TM LDHs have been researched because of their unique 2D structure. The exfoliation method belongs to the top-down method and is usually used to make 2D materials, including TM LDH nanosheets. Other top-down synthesis methods have been studied, such as plasma etching and liquid exfoliation. Otherwise, bottom-up methods also have attention owing to their relatively simple process. Microemulsion, Coprecipitation, and hydrothermal processes were representative bottom-up methods to synthesize TM LDH nanosheets[71-73]. TM LDH catalysts could be easily synthesized through a one-step or two-step hydrothermal process[70].
TM LDH catalysts can easily apply reforming methods to improve performance due to their intrinsic 2D structure. Distortion is a frequently used method in 2D materials, leading to a distorted surface, which can cause more exposure of the edge site to enhance electrocatalytic performance. OVs are one of the representative defect engineering methods used to improve the electrochemical properties in the TM LDH catalysts by boosting the charge transfer/separation and optimizing the reaction kinetics. These vacancies also make TM LDH catalysts higher electrical conductivity and increase adsorption for oxygen-based intermediates[74]. Recently, the hybrid TM LDH-based catalysts for NitRR, including two kinds of metal, have been studied in most research. These mixed TM LDH catalysts show good reactive performance due to synergistic effects. Du et al. efficiently synthesized the CoFe LDH catalysts with the hydrothermal method in Figure 3A, and the catalyst performed excellent FE, NH3 selectivity, high activity, and durability in alkaline conditions[52]. The DFT calculations indicated that CoFe LDH has a downhill reaction step
Figure 3. (A) Schematic image of the synthesis process for CoFe LDH and its cell composition for NitRR. (B) Reaction-free energies for *NO3, *NO2, and *NH3 on the Fe LH, Co LH, and CoFe LDH surfaces. (C) FE and NH3 selectivity of CoFe LDH according to potential. (D) The consecutive recycling test of CoFe LDH at -0.45 V (vs. RHE). (A-D) Figures are reprinted with permission from Ref.[52]. Copyright 2022 Elsevier[52]. (E) Comparison of NH3 yield rate and FE of Ni3Fe-CO3 LDH with reference materials. (F) The recycling test of Ni3Fe-CO3 LDH/Cu foam electrode at -0.2 V (vs. RHE). (G) NH3 yield rate and FE using multi-metallic TM LDH/Cu foam electrodes. (E-G) figures are reprinted with permission from Ref.[53]. Copyright 2023 The Royal Society of Chemistry[53]. (H) XRD patterns of Cu/Co/Al-HTLCs. (I) The transformation of NO3 and total nitrogen (TN) on Cu/Co/Al-HTLCs according to time at -0.74 V (vs. RHE). (H and I) Figures are reprinted with permission from Ref.[75]. Copyright 2020 MDPI[75].
Chalcogenides
The low-cost TM chalcogenide materials have been considered to replace the high-cost precious metal catalysts. A TM chalcogenide is a chemical compound of at least one TM cation and at least one more chalcogen anion (S, Se, and Te). Among the TM chalcogenides, TM dichalcogenides (TMDs), such as metal disulfides (MS2) and diselenides (MSe2), with M4+ (Mo4+, Ti4+, and V4+) have been widely used in various electrochemical applications due to the unique physicochemical and structural features[76]. TMDs have unique layered structures, and one of them, TiS2, was investigated as a cathode material for secondary batteries because of its layered structure that can be intercalated by lithium in the 1970s[77]. In addition to these structure features, TMDs can be easily doped with various TMs to tune the electric structure and chemical composition[78].
More recently, to improve the electrocatalytic performance, various nanostructures of TMDs have been studied. Partially, 2D TMDs exhibit the potential for NitRR owing to their large active area and tunable electronic structure. These 2D TMDs can be categorized into trigonal prismatic (hexagonal, H), octahedral (tetragonal, T), and distorted phase (T´)[79]. Various defect engineering is also studied, and sulfur vacancies (SVs) are one of the representatives in the field of TMD catalysts[80].
Doping single metal atoms into 2D materials is considered one of the effective strategies to enhance the electrochemical performance of a catalyst[81,82]. Such strategies can significantly improve the electrochemical NitRR performance of a catalyst by incorporating metal dopants into 2D materials. Li et al. investigated the iron single atomic catalyst (SAC) supported on 2D MoS2 (Fe-MoS2) nanosheets for NitRR [Figure 4A][54]. Additionally, Cu-, Ni-, and Co-MoS2 nanosheets were also studied to compare with Fe-MoS2 catalysts, and Fe-MoS2 has higher electrochemical performance than that of other catalysts [Figure 4B and C]. DFT studies show that Fe-MoS2 presents the deoxidation of the *NO to *N intermediate, decreasing the energy barrier of the reaction pathway to synthesize ammonia. Ding et al. also studied Fe-MoS2 catalysts through DFT calculations for NitRR[83]. Since Fe on the MoS2 improves the activating NitRR and suppressing HER, Fe-MoS2 achieved a high FE of 90% and a yield rate of 9.75 mg h-1 cm-2 for NH3 production at -0.85 V
Figure 4. (A) TEM image of Fe-MoS2 nanosheets on the carbon support. (B) FEs for NH3 on Cu-MoS2, Ni-MoS2, Co-MoS2, and Fe-MoS2 nanosheets at different potentials. (C) Reaction Gibbs free energies of intermediates on M-MoS2 nanosheets. (A-C) figures are reprinted with permission from Ref.[54]. Copyright 2021 Wiley-VCH GmbH[54]. (D) Potential dependent NH3 yield rate and FE of
Transition metal oxides
In the electrocatalytic field, low-cost TM oxide (TMO) catalysts have attracted attention for commercialization by replacing precious metal catalysts. TMO catalysts have many advantages, such as ease of synthesis, thermal and chemical stability, low cost, and high earth abundance to be used as catalysts[84]. However, these catalysts cannot be directly used for NitRR because TMOs have some disadvantages when used as catalysts because of their low electronic conductivity, relatively low active site, and low selectivity[85]. Optimization strategies, such as nanostructure and defect engineering, have been considered to overcome these challenges and improve electrocatalytic performance. Nanostructure engineering is a process method for making catalysts have nanoscale structures, including nanoparticles and 2D structures. These structures increase the higher active area, narrow the band gap, and promote electronic conductivity[86]. Synthesizing 2D TMOs through the top-down method has challenges, leading to multiple attempts to explore the bottom-up method. For instance, Sun et al. and Sun et al. synthesize ultrafine 2D nanosheets of TMOs[87,88]. Huang et al. demonstrated the fabrication of graphene-like TMO nanosheets by utilizing graphene oxide (GO) as a 2D template, wherein metal precursors were deposited on the GO surface and then calcined[89]. Various TMs could synthesize 2D TMOs using either a 2D template or surfactant molecules. Defect engineering, such as OVs, is commonly used to improve NitRR performance with changes in electronic structure and surface properties. Standard modification methods, such as hydrogen heat treatment, thermal annealing, wet chemical reduction, and electroreduction, can quickly generate OVs in TMOs[65].
Wang et al. studied Cu/CuOx in-plane heterostructured nanosheet arrays with OVs (Cu/CuOx/CF) for NitRR [Figure 5A][60]. This 2D nanosheet structure has rich exposing active sites and high mass/charge transfer. Moreover, OVs and in-plane heterojunctions tune electronic structures and improve adsorption capabilities and properties. The test results show that Cu/CuOx/CF achieves higher electrocatalytic performance, FE of 93.58%, and an NH3 production of 0.23 mmol h-1 cm-2 at -1.3 V (vs. saturated calomel electrode, SCE) than that of CuOx/CF, Cu/CF, and Cu Foam [Figure 5B and C]. For five cycles, the retention of the yield rate and FE of Cu/CuOx/CF was maintained at a high level in Figure 5D. Zhao et al. studied the modulation of multi-scale defects, such as OVs and nanoholes, on the Co3O4 catalyst for NitRR[61]. The defective Co3O4/Co with an interlaced nanosheet was synthesized through electrodeposition and calcination. The OVs improved the adsorption of NO3- and increased active sites. The rich nanoholes displayed in Figure 5E may make additional channels for convenient mass transfer. As shown in Figure 5F, the adsorption energy of NO3- on Co3O4-2Ov is lower than others at -1.81 eV. In addition, the energy barrier of HER on Co3O4-2Ov is the highest value of 1.15 eV [Figure 5G]. These results show that the OVs could enhance NO3- adsorption and suppress HER. Figure 5H shows that Co3O4/Co-I has a higher yield rate of 4.43 mg h-1 cm-2 and FE of 88.7% than that of Cu3O4/Co-h in 0.1 M Na2SO4 with 1 mg mL-1 of KNO3 solution. Co3O4/Co exhibits a high performance in a flow electrolyzer system, with a yield rate of
Figure 5. (A) Schematic image of the synthesis process for Cu/CuOx/CF. (B) NH3 yield rates and FEs of Cu/CuOx/CF at different potentials. (C) NH3 yield rates and FEs of Cu/CuOx/CF, CuOx/CF, Cu/CF, and CF. (D) The Cu/CuOx/CF recycling test was at -1.3 V
Metal-organic frameworks
MOFs are new crystalline porous materials that can be formed by coupling metal ions/clusters with organic ligands[86]. They have been widely used in batteries[90], supercapacitors[91], catalysis[92], etc.[93,94] due to their advantages such as high specific surface area[95], tunable pore size, and high porosity[96]. The 2D nanosheets of MOFs have recently emerged as a promising material that makes them valuable in widespread electrocatalytic fields due to their atomic-level thickness, abundant active sites, and large surface area. Additionally, 2D MOF/COF nanosheet synthesis methods can be divided into top-down and bottom-up[97]. In the former, bulk crystals are synthesized first and then split into multi-layer or even single-layer nanosheets. The latter involves directly synthesizing 2D nanosheets by controlling the growth of bulk crystals in a specific direction. Bulk crystals connected between layers by hydrogen bonds or van der Waals forces are successfully exfoliated using ultrasound, mechanical force, etc. Due to the electrocatalytic reactions being related to the surface properties of the materials, 2D MOF materials provide an opportunity to construct an efficient electrode with the advantages of flexible surface and active sites for electrocatalysis. In addition, the crystal structure of 2D MOF nanosheets provides highly exposed surface area and active sites at the atomic level. These consequences significantly shorten the diffusion lengths of the products and reactants to improve the performance of an electrocatalyst and have shown excellent performance in many fields. However, some traditional MOFs still suffer from low conductivity and stability.
Lv et al. reported 2D-In MOFs as an electrocatalyst with a uniformly dispersed single-atom site and enzyme mimic system for efficient NitRR[98]. The 2D-In MOFs were synthesized through a wet chemical method, and they showed a high ammonia yield rate of 278.8 μg h-1 cm-2 at -0.7 V (vs. RHE) and pH 2 with an optimal FE of 92%. These high performances are due to their stable microenvironment space and reversible ligand dissociation, as shown in Figure 6A. Figure 6B shows the solid-state cyclic voltammograms of 2D-In MOFs, showing two peaks of 0.22 and 0.55 V (vs. FC/FC+). Both peaks are attributed to redox-active tetrathiafulvalene (TTF) ligand and quasi-reversible electron transfer process. The reversible ligand dissociation at various potentials and pH is studied by in situ Raman spectroscopy in Figure 6C and D. The two peaks of 363 and 505 cm-1 correspond to the In(III), and after the applied negative potential, two weak peaks of 438 and 806 cm-1 appeared, which are due to In(II) and NO3- adsorption at pH 1~3, respectively. On the other hand, apparent differences in peaks are not found in Figure 6D, which means the ligand dissociation mechanism does not work at the high pH. Lastly, the DFT method verifies the ligands’ dynamic dissociation catalytic mechanism theoretically [Figure 6E].
Figure 6. (A) Schematic illustration of the multifunction motifs assembled in 2D-In-MOF and their functional characteristics and dynamic ligand dissociation mechanism. (B) Solid-state cyclic voltammograms of 2D-In-MOF conducted in 0.1 M LiBF4 in CH3CN electrolyte. (C) Ex situ and in situ Raman spectra of 2D-In-MOF before (black) and after (red) electrocatalysis in H2SO4 (pH = 1) with 0.5 g L-1 KNO3 and (D) in 50 mM H2SO4 (pH = 5) with 0.5 g L-1 KNO3. (E) Free energy diagram of electrochemical conversion of NO3- to NH3 for 2D-In-MOF and the optimized geometric structures of intermediates corresponding to the N-end pathway (pH = 2/3). (A-E) Figures are reprinted with permission from Ref.[98]. Copyright 2022 American Chemical Society[98]. (F) HR-TEM image of Cu1Co1HHTP, (G) The electrocatalytic activities of various CuxCoyHHTP catalysts at -0.6 V (vs. RHE). (H) d-orbit PDOS of Cu site in Cu1Co1HHTP and CuHHTP slabs. (I) Free energy diagrams of the NitRR process on Cu1Co1HHTP and CuHHTP slabs. (F-J) Figures are reprinted with permission from Ref.[99]. Copyright 2023 Elsevier[99].
Liu et al. reported bimetallic conductive copper-cobalt hexahydroxytriphenylene MOF (CuxCoyHHTP), which has a synergy effect between different single-metal sites and shows a great yield rate and a FE of
Fang et al. reported 2D-Fe cyano NSs (nanosheets) as multi-functional electrocatalysts that have abundant Fe0 active sites for NitRR and oxygen evolution reaction (OER) via topotactic conversion and electro-reduction [Figure 7A][100]. As shown in Figure 7B, Fe cyano NSs have a large active surface area, which is 1.54 times the Fe-cyano bulk and super hydrophilic properties from electrical double-layer capacitance (EDLC) and contact angle data. These properties are due to 2D engineering and hydrophilic functional groups and are favorable for electrode contact with electrolytes and NO3- adsorption. In addition, the X-ray Photoelectron Spectroscopy (XPS) data shows the generation of Fe0 in Fe cyano NSs after the electro-reduction process, and the Fe0 sites are verified as active sites for NitRR by poisoning Fe sites using potassium thiocyanide (KSCN) [Figure 7C and D]. DFT simulation shows negative ΔG of NO3- adsorption on Fe0 sites that supports the suppression of HER and NitRR selectivity. In the electrochemical NitRR test, the Fe cyano NSs exhibit a high ammonia yield rate of 42.1 mg h-1 mgcat.-1 and an FE of over 90% at -0.5 V (vs. RHE) [Figure 7E]. Furthermore, Fe cyano NS-based material as a multifunctional catalyst showed excellent durability without degradation of cell voltage at 60 mA cm-2 for an electrolyzer of OER and NitRR [Figure 7F]. Therefore, recent research on 2D-MOFs as electrocatalysts has progressed due to their high surface area and shortened diffusion lengths. In particular, 2D-MOFs, which have uniformly dispersed single atom sites and doped single heteroatom sites, show a synergistic effect on electrochemical activity and can improve conductivity and stability with reversible reactions.
Figure 7. (A) Synthesis of ultra-large Fe-cyano NSs via directional freezing. (B) EDLC of blank CFP electrode, Fe-cyano bulk, and NS electrocatalysts. Inset of (B) CAs of (i) blank CFP electrode, (ii) Fe-cyano bulk, and (iii) NS electrocatalysts. (C) Poisoning experiment on Fe-cyano-R NSs. (D) H2O and NO3- adsorption on Fe0. (E) Ammonia yield rate and Faradaic efficiency (FE) at various potentials on Fe-cyano NSs. (F) Stability of electrolyzer. Reprinted with permission from Ref.[100]. Copyright 2022 American Chemical Society[100].
MXenes
MXenes are generally defined as 2D TM carbides or nitrides, with Ti3C2Tx synthesized from the Mn+1AXn (MAX) phase of Ti3AlC2 first reported in 2011[101]. The thickness of MXenes is typically in the 1 nm range and depends on the n value (Mn+1XnTx) of the MXenes[102]. MXenes are primarily synthesized by selectively etching the A layer from the precursor MAX phase, which is a precursor of MXenes and is typically a series of ternary layer compounds, where M is a TM, A is an element of group IIIA or IVA in the periodic table, and X is carbon or nitrogen [Figure 8A][103]. Because the M-X covalent bonds and M-A metal bonds on MAX are powerful, for breaking the M-A bonds, potent etching agents such as hydrofluoric acid (HF) and lithium fluoride-hydrochloric acid mixtures (LiF-HCl) are required. As a result, the surface of MXenes is terminated with abundant functional groups such as -OH and -O, which vary in type and amount depending on the etching route [Figure 8B][104]. Various stoichiometries of MXenes have been studied, such as monometallic MXenes, bimetallic MXenes, and multi-metal MXenes [Figure 8C][105].
Figure 8. (A) A schematic representation of MAX structures from n = 1 to n = 4 and their etched MXene structures. Reprinted with permission from Ref.[103]. Copyright 2021 Wiley-VCH)[103]. (B) A schematic of different surface functional groups depending on the etching route. Reprinted with permission from Ref.[104]. Copyright 2018 Wiley-VCH[104]. (C) Schematic depicting different MXene stoichiometries. Reprinted with permission from Ref.[105]. Copyright 2023 Wiley-VCH[105].
Due to their numerous properties, including unique mechanical properties[106], metallic conductivity[107], in-plane anisotropic structure[108], and tunable band gap[109], MXenes have been arising as multipurpose 2D materials for promising applications[110-112]. Compared to other 2D materials, they have abundant terminal functional groups[113], enabling reversible redox reactions[114]. Unlike other 2D materials, they do not require processing to increase the exposure and density of active sites. In general, MXene basal planes are considered catalytically inactive[115]. However, these can become active by tuning their terminal groups.
Cai et al. reported that surface hydroxyl on oxygen-functionalized Ti3C2 MXene (Of-TiMX) plays a vital role in the NitRR process[115]. The Of-TiMX was synthesized via three steps of etching, exfoliation, and calcination to make an oxygen group on the surface of TiMX [Figure 9A]. The Of-TiMX shows not only selective NitRR but also a high FE and an ammonia yield rate of 90.4% and 0.99 mg h-1 cm-2 at -1.7 V (vs. SCE), which indicates HER is effectively suppressed on its surface [Figure 9B].
Figure 9. (A) Schematic illustration of synthesizing the Of-TiMX for NitRR. (B) FEs of ammonia and nitrite of Of-TiMX at different potentials. (C) Pourbaix diagrams for Of-TiMX at pH 7. (D) Free-energy diagrams for NitRR on the surface of full OH-terminated Of-TiMX at U = 0.0 V and U = -1.2 V (vs. SHE). Reprinted with permission from Ref.[115]. Copyright 2023 Elsevier[115].
From the surface Pourbaix diagram, the trend of the amount of surface hydroxyl grows as the potential increases [Figure 9C]. This trend is related to the experimental results that the Of-TiMX has the highest NitRR performance at -1.7 V (vs. SCE) because the hydroxyl groups allow interfacial H-bonding with NO3- and other intermediates for NH3 production. In addition, the free energy diagram for NitRR on the hydroxyl-covered surface of Of-TiMX suggests the NitRR pathway to synthesize ammonia and support high optimized potential and selectivity [Figure 9D]. Hence, recent research on MXenes and advances in computational science have been extensive. Significantly, the surface modification of MXenes, which have abundant and tuneable functional groups on their surface, is determined to improve electrocatalytic activity and selectivity with a high ammonia yield rate.
Graphene-based materials
To reduce the use of precious metals, carbon nanomaterials are commonly used in electrocatalytic applications due to their high electrical conductivity, low cost, and chemical stability[117]. Graphene, one of the carbon nanomaterials, has mainly been utilized as a catalyst or support to improve the electrocatalytic performance of the NitRR owing to its 2D structure. However, when used alone, graphene has relatively poor electrocatalytic properties, such as low activity and selectivity. Various engineering approaches have been investigated to overcome these problems, including a combination of TMs and defect engineering.
Graphene has been widely used as a support for single-atom catalysts (SACs) due to its suitability as an excellent structural support. SACs are dispersed or coordinated atomically on the surface of 2D materials such as graphene, and surface defects are often utilized as their active sites. These catalysts have many advantages, including high stability, activity, selectivity, efficient active sites, and drastic cost reduction. Additionally, they allow for the tuning of the selectivity and activity of electrocatalytic reactions[118]. To synthesize the SACs, lots of synthesis methods, such as wet-chemical, MOF-derived, atomic layer deposition (ALD), co-precipitation, and impregnation, have been investigated[119].
Wu et al. synthesized Fe SAC anchored on graphene through pyrolysis and etching, as shown in
Figure 10. (A) Schematic image of the synthesis process for Fe SAC. (B) NH3 partial current density and yield rate of Fe SAC, FeNP/NC, NC. (C) NH3 FE of Fe SAC at different potentials. (D) Calculated minimum energy pathway on Fe SAC for NitRR. (E) Calculated accessible energy pathway at U = 0 and -0.3 V (vs. RHE). (A-E) Figures are reprinted with permission from Ref.[62]. Copyright 2021 Springer Nature Limited[62]. (F) The metal atoms and substrates considered for constructing the DACs on N-graphenes. (G) Calculated free energy of NitRR on Cu2/N3-6 and the involved intermediates. (H) Potential-dependent NH3 yield rate and FE of Cu2/N3-6. (F-H) Figures are reprinted with permission from Ref.[121]. Copyright 2023 Elsevier[121]. (I) HR-TEM image of ox-LIG. (J) NH3 FE and (K) ox-LIG, LIG, and rGO yield rates at different potentials. (I-K) Figures are reprinted with permission from Ref.[122]. Copyright 2023 Wiley-VCH GmbH[122].
Beyond the study of SACs, dual-atom catalysts (DACs) have been investigated because of their unique structure. Their structure could suppress HER on their surface and increase the selectivity of NitRR due to an ensemble effect[120]. Zhao et al. calculated the DFT of DACs embedded in N-graphene for NitRR and demonstrated the results with subsequent experiments[121]. The geometric structure of DACs is determined by the d-band type of the constituent metals [Figure 10F and G]. The DFT indicated the synergistic effects of two active sites improve the activation of catalysts, which is related to intrinsic d-band centers of active sites. Then, it is revealed that Cu2@N3-6 catalysts have high electrocatalytic performance for NitRR in DFT results, and Cu2@N3-6 achieved a high FE of 97.4% and yield rate of 18.2 mg h-1 cm-2 at -0.8 V (vs. RHE) in the experiment [Figure 10H].
Defect engineering can increase the electrochemical activity of the graphene for the NitRR due to the change in electronic structures. Huang et al. show a skyscraping FE of nearly 100% with amorphous graphene for NitRR[122]. The amorphous graphene was synthesized via laser induction, which resulted in numerous defects, disordered pentagons, hexagons, and heptagons in graphene, and Figure 10I shows these defects in graphene. These defects increase the selectivity of the graphene for NitRR. The amorphous graphene has high electrocatalytic performances, which are FE of about 100% and NH3 production of
CONCLUSIONS AND PERSPECTIVES
Electrochemical synthesis of green ammonia has been focused on as an alternative way to the energy-intensive Harber-Bosch process due to its advantages, such as zero-carbon emission, scalability, and production under ambient conditions. However, commercialization of NitRR undergoes inevitable drawbacks, such as low selectivity of ammonia and high cost of electrocatalysts, due to immature technology and competitive HER. To increase the electrochemical performance of the NitRR, the design strategies of electrocatalysts have been studied over the past decade. Furthermore, 2D structured materials have been investigated as promising candidates for efficient electrocatalysts due to their advantages, such as a particular surface area with an abundant active site, ease of modification, and low cost. In addition, various defect engineering, such as oxygen defect, doping, and topological defects, have been considered to improve the electrocatalytic performance because these defects in 2D electrocatalysts not only increase the mass/charge transport, active site, and electrical conductivity but can also tune the electronic structure.
This review summarized the recent advances and development of 2D catalysts with defect engineering for NitRR. While some 2D materials are employed as catalysts for NitRR, certain drawbacks become apparent. For example, TMOs exhibit low conductivity, and graphene demonstrates low activity. However, defects emerge as a solution, addressing these intrinsic issues by enhancing catalyst conductivity and activity. Unexplored 2D materials, such as TaS2, MoTe2, and defect-rich CNTs, remain untapped for converting from nitrate to ammonia. Additionally, various defect engineering techniques, such as N-P or N-S co-doping and topological defects, await NitRR exploration. Consequently, the remaining candidates can potentially increase ammonia yield and FE.
Recent studies demonstrated the high electrocatalytic performance of NitRR, as shown in Table 2. Understanding the NitRR mechanism on the catalyst is essential to improve electrocatalytic performance. In previous studies, the NitRR mechanism of defects-containing 2D catalysts has also been investigated by the DFT method. However, most DFT calculations have focused on point defects, such as vacancies and doping. There are still unresolved issues related to NitRR regarding complex 2D and 3D defects, such as grain boundaries (GBs), twins, distortion, voids, and cracks. In realistic situations, catalysts have numerous GBs, and the unsaturated coordination of GB atoms can enhance catalytic activity. DFT calculations can utilize two GB bulk models built based on the coincidence site lattice (CSL) theory to address this. Moreover, appropriate conditions are also necessary for understanding the precise properties of each type of defect.
Comparison of different 2D-structured materials as electrocatalysts for NitRR
Category | Electrocatalysts | Synthesis method | Substrate | Electrolyte | NH3 yield rate | FE (%) | Selectivity (%) | Ref. |
Layered double hydroxide (LDH) | CoFe LDH | Hydrothermal | Ni foam | 1 M KOH + 1,400 ppm KNO3 | @-0.45 V | 97.68 | 98.93 | [52] |
Ni3Fe-CO3 LDH | Co-precipitation | Cu foam | 1 M KOH + 5 mM KNO3 | 1.261 mg h-1 cm-2 @-0.2 V (vs. RHE) | 96.80 | 95.80 | [53] | |
Chalcogenide | Fe-MoS2 | Hydrothermal | Carbon cloth | 0.1 M Na2SO4 + 0.1 M NaOH + 0.1 M NaNO3 | @-0.5 V | 98 | [54] | |
Fe-MoS2 | Hydrothermal | Carbon cloth | 1 M LiCl + 0.25 M LiNO3 | 9.75 mg h-1 cm-2 @-0.85 V | 90 | [83] | ||
Cu-SnS2-x | Solvothermal | Carbon cloth | 0.1 M KOH + 0.1 M KNO3 | @-0.7 V | 93.80 | [55] | ||
B-MoS2 | Hydrothermal | Carbon cloth | 0.5 M Na2SO4 + 0.1 M NaNO3 | 10.8 mg h-1 cm-2 @-0.7 V | 92.30 | [123] | ||
Transition-metal oxide (TMO) | Co3O4/Co-l | Electrodeposition & calcination | Co foam | 1.000 ppm NO3- + 0.1 M Na2SO4 | 4.43 mg h-1 cm-2 @-0.8 V | 88.70 | 83.30 | [61] |
Cu/CuOx/CF | Oxidation treatment | Cu foam | 0.5 M K2SO4 + 200 mg L-1 NO3- | @-1.3 V (vs. SCE) | 93.58 | 95.00 | [60] | |
CuO NWAs@Fe3O4 | Hydrolysis & pyrolysis | Cu foam | 1 M KOH + 1,400 ppm NO3- | @-0.27 V | 99.46 | 88.68 | [124] | |
Metal-organic framework (MOF) | Ni-MOF | Solvothermal | Ni foam | 70 mg·L-1 NaNO3, 0.1 M Na2SO4 | 110.13 ug h-1 cm-2 @-1.4 V | 96.40 | 80 | [58] |
cMOF(CuxCoyHHTP) | Hydrothermal | Carbon cloth | 0.5 M Na2SO4 + 0.1 M NaNO3 | @-0.6 V | 96.40 | [99] | ||
Fe-cyano NSs | Sol-gel | Carbon fiber paper | 0.1 M KNO3 + 1 M KOH | @-0.5 V (vs. RHE) | 90.20 | [100] | ||
In-MOF In8 | Solvothermal | Carbon paper | 5 mM H2SO4 + 15 g·L-1 KNO3 | 256.9 μg h-1 mgcat.-1 @-0.7 V (vs. RHE) | 90.10 | 99.30 | [98] | |
MXene | Ti3C2 | Etching & ultrasonication | Carbon paper | 0.5 M K2SO4 + 200 ppm KNO3 | 0.99 mg h-1 cm-2 @-1.7 V (vs. SCE) | 90 | [115] | |
BP/Nb2C | Self-assembly | Carbon cloth | 0.1 M K2SO4 + 0.05 M KNO3 | @-0.6 V (vs. RHE) | 90.4 @-0.5 V vs. RHE | [125] | ||
Bi2O3/MXene | Solvothermal | Carbon paper | 1,000 ppm NO3- + 0.5 M Na2SO4 | 7.00 mg h-1 cm-2 @-1.8 V (vs. SCE) | 91.10 | [126] | ||
Fe1Cu2@MXene | Wet-chemical | Carbon cloth | 100 mg L-1 KNO3 + 0.1 M Na2SO4 | 1.2 mg h-1 cm-2 @-0.95 V (vs. RHE) | 52 | 99.60 | [127] | |
FeNPs@MXene | Wet-chemical | Carbon cloth | 100 mg L-1 NO3 + 0.5 M Na2SO4 | ~0.8 mg h-1 cm-2 @-0.95 V (vs. RHE) | 20.00 | 76.80 | [128] | |
CuCl_BEF | Wet-chemical | Carbon cloth | 100 mg L-1 NO3 + 0.5 M Na2SO4 | 1.82 mg h-1 cm-2 @-1.0 V (vs. RHE) | 44.70 | 98.60 | [129] | |
Mo2C NSs | Carbonization | Carbon paper | 1 M NaOH + 0.1 M NaNO3 | 25.2 mg h-1 mgcat.-1 @-0.4 V (vs. RHE) | 81.4 @-0.3 V vs. RHE | [130] | ||
Graphene-basedmaterial | Fe SAC | Wet-chemical | Glassy carbon | 0.1 M K2SO4 + 0.5 M KNO3 | @-0.85 V (vs. RHE) | 75 @-0.66 V vs. RHE | 69 | [62] |
Cu2@N3-6 | Pyrolysis method | Carbon cloth | 0.5 M Na2SO4 + 0.1 M NaNO3 | 18.2 mg h-1 cm-2 @-0.8 V (vs. RHE) | 97.40 | [121] | ||
ox-LIG | Laser induction | Cellulose paper/Au layer | 1 M NaNO3 | 2,859 μg h-1 cm-2 @-0.93 V (vs. RHE) | 96.40 | > 70 | [122] |
Understanding fluid dynamics within the flow electrolyzer is a critical concern in the scale-up process. These considerations become particularly vital as cell designs progress from H-type cells to flow cells for NitRR. Understanding NitRR in the flow state is paramount. Various approaches can be employed to achieve a comprehensive understanding of NitRR in a flow state, including computational simulations such as computational fluid dynamics (CFD) and molecular dynamics (MD). Additionally, in situ characterization techniques, such as in situ Fourier-transform infrared spectroscopy (FT-IR), in situ Raman spectroscopy, in situ X-ray absorption spectroscopy (XAS), in situ scanning electrochemical microscopy (SECM), and online DEMS, need further exploration to accurately decipher the conversion of NO3- to NH3 accurately and to gain insights into the kinetics of the reaction. These in situ measurements will provide clues to suppress the production of by-products such as H2, N2, and NO2-. Although some challenges remain, progress is highly expected through continuous research. This review will help bridge the gap between theory and experiment to understand 2D materials and defect engineering for NitRR.
DECLARATIONS
Author’s contributions
Conceptualization, investigation, visualization, validation, writing - original draft, writing - review & editing: Choi J, Im S, Kim JK, Sim U
Investigation, visualization, writing - review & editing: Choi J
Validation, writing - review & editing: Surendran S
Writing - review & editing: Moon DJ, Kim JY
Availability of data and materials
Not applicable.
Financial support and sponsorship
This work was supported by the Korea Institute of Energy Technology Evaluation and Planning (KETEP) grant funded by the Korean government (MOTIE) (No. RS-2023-00242227 (Clean Hydrogen and Ammonia Innovation Research Center) and No. 20224000000320). This work was supported from the National Research Foundation of Korea (NRF) grant funded by the Korean government (MSIT) (No. 2022R1A2C1012419). This work was supported by the New & Renewable Energy Core Technology Program of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) granted financial resource from the Ministry of Trade, Industry & Energy, Republic of Korea (No. 20213030040590). This research was supported by Nano·Material Technology Development Program through the National Research Foundation of Korea (NRF) funded by Ministry of Science and ICT (2020M3H4A3106313). Additionally, this work was backed by the KENTECH Research Grant funded by the Korea Institute of Energy Technology, Republic of Korea (KRG2022-01-016). This research also benefited from the "Regional Innovation Strategy (RIS)" through the National Research Foundation of Korea (NRF), funded by the Ministry of Education (MOE) (2021RIS-002).
Conflicts of interest
All authors declared that there are no conflicts of interest.
Ethical approval and consent to participate
Not applicable.
Consent for publication
Not applicable.
Copyright
© The Author(s) 2024.
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How to Cite
Choi, J.; Im, S.; Choi, J.; Surendran, S.; Moon, D. J.; Kim, J. Y.; Kim, J. K.; Sim, U. Recent advances in 2D structured materials with defect-exploiting design strategies for electrocatalysis of nitrate to ammonia. Energy Mater. 2024, 4, 400020. http://dx.doi.org/10.20517/energymater.2023.67
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