Colloidal Nanocrystal-Based Electrocatalysts for Combating Environmental Problems and Energy Crisis

The serious threat that human beings face in near future will be shortage of fossil fuel reserves and abrupt changes in global climate. To prepare for these serious concerns, raised due to climate change and shortage of fuels, conversion of excessive atmospheric CO2 into valuable chemicals and fuels and production of hydrogen from water splitting is seen most promising solutions to combat the rising CO2 levels and energy crises. Amoung the various techniques that have been employed electrocatalytic conversion of CO2 into fuels and hydrogen production from water has gained tremendous interest. Hydrogen is a zero carbon-emitting fuel, can be an alternative to traditional fossil fuels. Therefore, researchers working in these areas are constantly trying to find new electrocatalysts that can be applied on a real scale to deal with environmental issues. Recently, colloidal nanocrystals (C-NCs)-based electrocatalysts have gained tremendous attention due to their superior catalytic selectivity/activity and durability compared to existing bulk electrodes. In this chapter, the authors discuss the colloidal synthesis of NCs and the effect of their physiochemical properties such as shape, size and chemical composition on the electrocatalytic performance and durability towards electrocatalytic H2 evolution reaction (EH2ER) and electrocatalytic CO2 reduction reactions (ECO2RR). The last portion of this chapter presents a brief perspective of the challenges ahead.


Introduction
A clean environment and sustained energy resources are essential for future generations. With growing concerns for both dwindling traditional fossil fuels and global warming, there is an urgent need to develop renewable and environmentally benign alternatives to address these issues of mankind [1][2][3]. Currently, humans are mainly dependent on fossil fuels and thus extract carbon from the geosphere and put it into the atmosphere where it causes global warming. There are two methods that can be helpful in preventing and reducing carbon emissions. The first and convenient way to stop carbon emissions is to move towards zero carbon-emitting resources. In view of this, hydrogen (H 2 ) produced by photo/electrocatalytic water splitting has shown great potential to become the fuel of the future. The merits have been attributed to its high energy density and it produces only one by-product of water upon combustion [4]. Thus H 2 , which is a zero carbon-emitting fuel, can be a promising solution to the mitigation of climate change. The second method is to capture carbon from the atmosphere and then store it back into the geosphere. However, the geosphere sequestration of CO 2 has no financial benefits. In contrast, chemical transformation of excess accumulated CO 2 from air into valuable industrial products, such as fuels (methanol, ethanol), hydrocarbon (methane, ethylene) and chemicals (formic acid, acetic acid), is an effective way to solve both global warming and energy crises [5,6]. Furthermore, it has economic significance from an industrial point of view. However, carbon-di-oxide reduction (CO 2 R) is a highly cumbersome and non-specific process. So far, several approaches, such as biochemical, chemical, thermal, photochemical and electrochemical catalysts have been explored to achieve aspirated activity and selectivity in this region [7][8][9]. Nonetheless, unlike other catalytic system electrocatalysts have gained tremendous attention due to its easy operation at ambient temperature and pressure. In addition, the selectivity of the product can be obtained by just adjusting reaction conditions, such as redox potential, electrode, and electrolyte, pH temperature and so on. The main advantage of using electrocatalysts is that they can be powered by renewable energy sources that emit zero carbon. For all these reasons, many research activities have shifted to the areas of EH 2 ER and ECO 2 RR (Figure 1) [10].
Over the years of time metal, metal oxide, metal sulphide have shown great promise in ECO 2 RR and EH 2 ER using electrocatalysis phenomenon. These electrocatalysts are being considered as a promising system that would be able to operate on a real scale without polluting environment. Whereas, there are still many limitations that are associated with electrocatalysts, such as high cost, poor product selectivity, high overpotential and low stability [11]. Colloidal Nanocrystal (C-NC) based electrocatalysts have become indispensable to overcome these limitations to certain extent owing to their larger surface to volume ratio, precise shape, long-term durability, and the plethora of configurations [12,13]. These factors are important in influencing their efficiency, selectivity, and durability for EH 2 ER and ECO 2 RR. For example, variation in the size and/or shape causes alteration in reactivity at Colloidal Nanocrystal-Based Electrocatalysts for Combating Environmental Problems… DOI: http://dx.doi.org /10.5772/intechopen.95338 different locations (edges/corners/faces) of the C-NC due to changes in a specific atomic-arrangement of active centers and crystal surface energy. The impact of these features will be discussed in detail as this chapter unfolds.
The purpose of this chapter is to elaborate on recent research developments and challenges in the field of heterogeneous C-NCs-based electrocatalysts for ECO 2 RR and EH 2 ER. In the first part of this chapter, colloidal synthesis of nanocrystals will be discussed. The second part of this chapter will address the structural aspects, such as size, shape, and composition, are important in tuning the catalytic efficiency, selectivity, and durability of NC-based catalysts for ECO 2 RR. Here a brief introduction of effect of ligand functionalization and effect of MOF/NCs hybrid system on ECO 2 RR activity will be also discussed. In the third part of this chapter, the role of C-NCs-based catalysts on EH 2 ER, its activity and stability is given. Moreover, the detailed mechanism of EH 2 ER is also discussed in this part. Finally, Authors have given extractive commentary that sheds light on the future perspective of ECO 2 RR and EH 2 ER in conclusion.

Colloidal synthesis of NCs
The C-NC is an inorganic material with a size of 1-100 nm and surface covering of protecting capping agents like polymer and surfactants molecules. Generally, the inorganic part exhibits characteristic features, such as optical, electrical, magnetic, and catalytic, that can be tuned by changing their physicochemical parameters, while surface capping guarantees the stabilization of these structures and paves the way for synthesizing more complex structures [14,15]. The physical parameters like morphology and chemical composition of C-NCs can be easily adapted by varying their reaction parameters like monomer concentration forming inorganic core of NCs and judicious choice of capping substances for surface covering. Over the last two-three decades, researchers have gained good control over synthesis of highquality and cost-effective NCs with uniform morphology and chemical constituents using colloidal synthesis [16][17][18][19]. The C-NC S approach has not only enhanced efficiency, selectivity of NCs, but also improved their service life. So far, researchers have found many commercial applications of C-NCs in various fields ranging from life sciences to the material world. One of the striking applications of C-NCs is in the field of biological imaging of cells, where quantum dots are used owing to their excellent fluorescent properties and also they do not photo-chemically bleach out like organic dyes [20]. Recently, quantum dots are being used commercially in LED displays also known as QLED-displays [21]. In addition, C-NCs-based photo/ electro-catalysts for ECO 2 RR and EH 2 ER are being developed to solve the energy crisis and global warming. However, their uses at economical scale in this area is still facing challenges. Deep insights of C-NCs synthesis and the effect of C-NCs physiochemical parameters on their electrocalytic properties need to be investigated for their successful applications at the economical level.
In general, C-NCs can be synthesized in both water and organic solvents. However, synthesizing a broad spectrum of NCs requires different reaction conditions that are much more feasible to achieve in organic solvents compared to water that is mainly used in the synthesis of noble metal C-NCs [14]. Therefore, in this section, authors will focus on organic phase C-NCs synthesis. Generally, C-NCs synthesis requires three major elements: 1) precursor molecules or building blocks forming inorganic core of NCs, 2) capping agents, and 3) organic solvents. Capping agents sometime act as solvent. The process of nanocrystal formation starts with transformation of precursor molecules into unstable and reactive species or monomers that usually occurs at quite high temperature. Thereafter, these monomers lead to formation of C-NCs whose growth is mainly influenced by capping agents. The crystallization of C-NCs can be best understood using widely accepted LaMer mechanism as depicted in Figure 2 [22][23][24][25]. Based on this mechanism, NCs development considered to have three major steps. In the first phase, the precursor molecules are converted to the reactive species, or monomer, and then eventually reach to a supersaturated phase (I), where no particle or second phase is still visible. In the next step, reactive species concentrate to the critical limit of supersaturation (phase II), at which a thermodynamically feasible state (Cmin) is developed for nucleation, followed by monomers to form initial seed for nucleation. In the second phase, the supersaturation again drops at some point due to instant nucleation, reducing the monomer concentration below Cmin that triggers the third phase (III) of the mechanism, that is, the growth of NCs. In this phase, because of monomer concentrations remain below C min , therefore, NCs grow without forming further nuclei until they attain an equilibrium state. During the growth phase of C-NCs, capping agents also play an important role in determining the final morphology of NCs. First and foremost, the capping agent should have a tendency to adsorb on the surface of the growing NCs.
Secondly, capping agents are required to bind in such a way that it can desorb and adsorb on the surface of growing NCs during growth process, making growing NCs surface accessible for reactive monomers, yet surface covering of capping agents, overall, stabilize NCs [14,26].

Size control in C-NCs synthesis
During NC synthesis, control over size uniformity is a prominent feature of contemporary synthetic methods. The LaMer mechanism discussed earlier not only explains the formation of NCs, but is also an approach to synthesize C-NCs with narrow size distributions. The essential element of LaMer approach to synthesize uniform-sized C-NCs is to divide crystallization into two disparate events; nucleation and growth. As discussed previously, the nucleation occurs for short periods of time, also known as burst nucleation, triggering a different growth phase where all nuclei then grow at the same rate without generating extra nuclei. The formation of extra nuclei during the growth phase can cause differences in the size of C-NCs because the newly formed nuclei will lag behind the previously growing NCs in growth kinetics. The The LaMer mechanism based formation of active monomers, burst nucleation, and subsequent slow growth of colloidal nanocrystals. Adapted from [23].
Colloidal Nanocrystal-Based Electrocatalysts for Combating Environmental Problems… DOI: http://dx.doi.org /10.5772/intechopen.95338 several methods utilize LaMer mechanism to grow uniform size C-NCs [24,27]. The first example is seed-mediated growth method where reaction medium is introduced pre-developed nuclei at low monomer concentration to inhibit secondary nucleation. Therefore, these pre-developed nuclei further grow up to the desired size of C-NCs without creating extra nuclei. However, in order to obtain narrow size distribution of NCs, it is still required to control growth phase as well. The second example is hot injection method where the reaction medium at high temperature is rapidly supplemented with the precursor or reducing reagents to create a state of supersaturation that triggers subsequent burst nucleation. The next example is the heating up method where reaction medium pre-treated with precursor, and capping agents is heated at high temperature to induce the LaMer crystallization. Due to the simplicity of this method it is often used to synthesize C-NCs at large scale [28][29][30].

Shape control in C-NCs synthesis
Unlike the bulk materials, the physiochemical properties of C-NCs are also strongly dependent on their shape. In this chapter, authors will further discuss how the shape of C-NCs can be adapted to improve the service life, selectivity and efficiency of electrocatalysts. Generally, C-NCs shapes can be tuned by means of both thermodynamic and kinetic controls. In C-NCs synthesis, capping agents are used, primarily, to obtain the desired shape using their specific binding nature on the surface of the growing NCs [31]. If the surface adsorption of capping agents causes the decrement in surface energy of any specific facet, then the obtain shape will be favored by thermodynamically. Whereas, if capping agents serves an obstruction between growing NCs and diffusing monomers then the resulting shape of C-NCs will be governed by kinetic factors [32,33]. Thermodynamically, the growing NCs attain it most likely shape by reducing its total surface free energy. For example, during the formation of fcc NC, the capping agents first selectively adheres to the (100) plans, which in turn, decreases their surface free energy [32]. These selective adsorptions onto the (100) plans causes transformation of cuboctahedron into cubic structure due the subsequent growth of higher energy facets. Whereas, in the kinetic regime, capping agents selectively adhere to some specific facets to lower their growth rate compare to others, resulting in various NCs shapes. Simultaneously, capping agents inhibit the diffusion of pre-deposited atoms over the NCs surface. In the real situation, however, the final shape of C-NCs is governed by the comparable kinetics of diffusion and deposition of monomers to growing NCs [32].

Mechanistic insight of ECO 2 RR
Thermodynamically, CO 2 is a quite stable molecule (bond dissociation enthalpy of C=O is ~750 KJ mol −1 ), so high energy is required for its activation. Moreover, the highest oxidation state of CO 2 , causes problems for its selective reduction [34]. A catalyst in this regard is an alternative that offers reactive sites for its selective and rapid transformations. In this chapter, the authors are focusing specially on NC-based electrocatalyst for ECO 2 RR. Generally, ECO 2 RR involves several proton/ electron transfers processes that take place at the cathode (catalyst). This process is considered to have three major stages. First, CO 2 is absorbed on the catalytic surface and its binding strength depends on the structure and composition of the NC as well as the nature of the electrolyte. Once it is absorbed, an electron is transferred to the CO 2 molecule that produces surface bound CO 2 −. Intermediate as depicted in Figure 3. This step is known as a rate-limiting step because it requires large reconstitution energy to convert linear CO 2 into twisted form, that is, CO 2 .− . For this reason, it requires extra potential (overpotential of −1.91 V) for electrochemical CO 2 conversion, even if it is thermodynamically feasible. After the formation of CO 2 . − its reactivity on the catalytic surface determines resulting product in ECO 2 RR. In principle, an optimal binding of the intermediate on the surface of the electrode is required for the rapid electron transfer process, thereby, increasing the selectivity and kinetics of the conversion. The reason for this is, a very strong affinity with intermediates will poison the surface of the electrode, while weak interaction will disrupt the electron transfer process. Sn, In and Pb, for example, represent week interaction with CO 2 − . intermediate, therefore, further reduction leads to production of HCOO − as resulting product [35]. In comparison, CO 2 − . on the surface of Ag, Au and Zn is reduced to COOH * which can be further reduced into CO * [35]. However, CO * has week affinity towards these metal ions, and thus, gaseous CO is generated. Interestingly, Cu, which has been extensively studied by Hori et al., shows optimal binding with CO * and uniquely reduces CO 2 in many products including alcohol and hydrocarbons [35]. Whereas, metals, such as Pt and Ni, have a strong affinity for CO*, which prevents further reduction, and for this reason, these metals favor EH 2 ER over ECO 2 RR [35]. Therefore, optimal interaction between metal-based electrodes and surface bound intermediates has a significant importance in product selection and/or reaction rate.
Furthermore, it was realized that surface properties of electrocatalyst, such as, surface area, roughness, composition, and morphological design have profound influence on efficiency, selectivity and durability of electrodes in electrochemical reactions [37][38]. It is a general understanding that the higher surface area provides good economy of the active center on the surface relative to the bulk, and thus, accelerates CO 2 reduction. Similarly, Cu shows optimal coordination with CO, however, changes in surface structure, such as roughness, may deviate from their normal behavior. For example, Jiang et al. showed that the high population of under-coordinated sites on the rough surface of the Cu leads to the formation of oxygen-containing compounds and hydrocarbons compared to CO due to enhanced interaction with CO* intermediates [38]. However, it is still challenging to adjust the optimal binding energy for intermediates to increase selectivity/reactivity towards ECO 2 RR, because of the large number of intermediates and many possible intricate pathways involved. Until now, many bulk metal-based electrodes have been investigated from both a material and structural point of view; however, Reaction pathways leading to the formation of formate, CO, and C-H products are highlighted. Adapted from [36]. Abbreviation: RDS, rate-determining step.
Colloidal Nanocrystal-Based Electrocatalysts for Combating Environmental Problems… DOI: http://dx.doi.org/10.5772/intechopen.95338 they are still facing many hurdles, such as: 1) high overpotential of the existing electrodes, 2) obtaining a mixture of products due to poor product selection of the catalyst, 3) deactivation of metal-based electrodes in short periods, 4) high cost of metal-based electrodes such as Ag, Au, Pt etc. discourages their use economically, 5) slow kinetics, or low activity. Beside there is always a competitive reaction EH 2 ER to the ECO 2 RR based on the thermodynamics. Rapid electron transfer in first step of electrochemical CO 2 reduction may be an effective strategy to suppress EH 2 ER, which, in turn, accelerates ECO 2 RR. In Table 1, the authors have summarized electrochemical Eqs. (1-16) of CO 2 R in some valuable products such as CH 4 , CH 3 OH, HCOOH, etc., with their respective equilibrium potentials in aqueous medium (pH 6.8) at 1 atm. and 25°C with respect to standard hydrogen electrode (SHE) [39,40]. The equilibrium potential of the ECO 2 RR, as provided, corresponds to the equilibrium potential of the EH 2 ER.

C-NCs-based heterogonous catalyst for ECO 2 RR
Recent studies have shown that nanometer-sized (1-100 nm) electrocatalyst is not only capable of reducing overpotential, but also shows an improvement in current density for CO 2 conversion. Regardless of the metal, the electronic structure of the catalysts at nanoscale is a key player in determining their efficiency, selectivity and durability for ECO 2 RR. Several electronic factors have been determined, such as finite size effects, and the location of the d band center that can tune the binding strength of intermediates, such as CO * , CHO * , etc., on the nanoparticle   Table 1.
Thermodynamic electrochemical half-cell equations of CO2R products, along with their relative standard redox potential (vs SHE in volt), or E(V) at pH 6.8 [39,40].
In addition, the geometric effect is an important factor that is crucial in stabilizing the specific intermediate during the reduction process, which leads to an increase in selectivity [44,45]. When using C-NC-based electrocatalysts, electronic and geometric factors can be adapted to increase selectivity, stability and activity using several approaches, such as size adjustment, shape modification, compositional control, surface functionalization and reaction conditions. As discussed earlier, the nucleation and growth process can be optimized by changing the reaction conditions (thermodynamic and kinetic of the reaction) to achieve the desired C-NCs with well-defined composition, and morphology. Therefore, C-NCs-based catalytic systems have been found to be highly promising to lead the catalytic field that can achieve higher selectivity and efficiency than existing systems. Here, our focus will be mainly on to understand how properties like size, shape, morphology, composition and surface functionalization of nanocrystal affect efficiency and durability of C-NCs-based electrocatalysts for ECO 2 RR.

Effect of C-NCs size on ECO 2 RR
The size is an important factor for C-NC-based electrocatalysis because different size of C-NCs show different activity/selectivity towards ECO 2 RR. Several studies have shown that alteration in size at nanoscale can affect both atomic distributions at various reaction sites (plans, edges, corners) and electronic structure of NCs, changing their catalytic characteristics. Therefore, the search for the optimal size C-NC showing the best efficiency, selectivity and durability requires contemporary research in this area. So far, to explore the effect of size towards ECO 2 RR, different sizes of electrocatalysts have been evaluated, however, our focus here is towards C-NC-based electrocatalysts. Colloidal synthesis of NCs is an excellent approach to study different sizes of NCs while keeping other factors such as shape and composition stable. Loiudice et al. synthesized spherical and cubical Cu C-NCs in the size range of 7.5-27 nm and 24-63 nm respectively for ECO 2 RR [46]. Their study has revealed unprecedented correlation between size of NCs and their electrochemical activity as well as selectivity for ECO 2 RR. The activity of Cu C-NCs increases as size of NCs within same morphology decreases, however, this does not hold while comparing cubical NCs with spherical. For example, the 44 nm cube has higher current density than 27 nm sphere. To understand this phenomenon, the propensity of Cu (100) facet towards ethylene production can provide a better understanding. Based on previous findings, it is widely accepted that the Cu (100) plane is selective for the electrochemical reduction of CO 2 in ethylene. Additionally, edges in ethylene production are thought to be responsible for the absorption and stabilization of an important intermediate (i.e., COOH *) as well as inhibiting EH 2 ER. In this study, the X-ray diffraction pattern has shown a higher contribution of the Cu (100) plane in the nanocube than in the nanosphere and Cu foil. Interestingly, among all Cu C-NCs, a size of 44 nm exhibited highest selectivity with 50% FE for ethylene and overall 80% for ECO 2 RR over EH 2 ER. This can be ascribed to changes in atomic configuration at different sites of C-NC due to differences in size. As nanocube move from smaller to larger sizes, the number of atoms at the edges and corners decreases, however, the number of atoms at the plane site increases. As a result, it came close to the morphology of a single crystal, where all the atoms of the surface are populated on the (100) plane. And, as previously stated edges also play an important role in electrochemical reduction of CO 2 into C 2 products. Therefore, an optimal balance between ratio of edge to plane site in 44 nm Cu C-NC, suggesting not only its unique selectivity for C 2 H 4, but also an overall activity towards ECO 2 RR.
Similarly, Zhu et al. investigated the non-monotonic size-dependent selectivity of Au C-NCs for CO 2 reduction into CO [47]. Among Au C-NCs of size 4, 6, 8, 10 nm synthesized, the 8 nm exhibited a highest selectivity for CO production with FE of ~90% at −0.67 V vs. RHE as shown in Figure 4(c). Based on the DFT calculations, the group concludes that dominance of edge sites at 8 nm C-NC facilitates selective CO 2 reduction in hydrocarbons, whereas depletion of corner sites inhibits EH 2 ER. They have further reported the unique selectivity of Au 13 C-NC towards EH 2 ER. Although Au 13 facilitates the formation of COOH* intermediate as compared to Au (211) and Au (111) facet, a stronger binding with CO* intermediate would lead to its lower tendency to produce CO 2 reduction products.
Additionally, as shown in Figure 4(f), the free energy of formation (ΔGfor mation ) of H* intermediates on Au 13 is lower than ΔGfor mation of COOH*, suggesting the generation of H 2 at low overpotentials. Furthermore, this study is found to correspond to a size dependence study on the small size (2-15 nm) Cu C-NCs for ECO 2 RR. For particle sizes at 5-15 nm, significantly higher activity and selectivity were found for H 2 and CO than for hydrocarbons. Moreover, particles smaller than 5 nm in size showed an exponential increase in the formation of H 2 and CO relative to hydrocarbons. This unique property of small C-NCs is due to an increase in under coordinated catalytic sites, which, in turn, strongly stabilize and bind with H * and CO * intermediates. Strong adsorption of H* and CO* intermediates is suggested to prevent subsequent hydrogenation of CO into hydrocarbons, so the increase in H 2 and CO production occurs at small (<5 nm) NCs.

Effect of C-NCs shape on ECO 2 RR
The shape of the C-NC plays an important role in determining the selectivity/ activity of the electrocatalysts. Several findings have shown that the shapedependent C-NC activity/selectivity towards ECO 2 RR is typically associated with the presence of specific crystal plane. For example, Suen et al. have revealed that cubic Cu C-NC (C-Cu) with mainly (100) facet shows enhanced selectivity towards C 2 products while octahedron Cu C-NC (O-Cu) with predominantly (111) facets shows selectivity for C 1 products in ECO 2 RR [48].
Besides, Zhou et al. have illustrated the correlation between different shapes of C-NCs and their corresponding crystal planes using a stereographic triangle as depicted in Figure 5(a) [49]. The lower index surfaces, namely, the (100) (110)   cube, octahedral, and rhombic dodecahedral, respectively. These low index surfaces are said to be less energetic, that is, catalytically less active. However, the plains lying on three sidelines of triangle and one which is residing inside the triangle are known as high index surfaces, that is, catalytically more active and stable. The high index planes (310), (311), (331), and (321) are correlated with tetrahedron, trapezohedron, trisoctahedron, and hexoctahedron, respectively, as illustrated in Figure 5(b). The high energy of these polyhedron is attributed to predominance of atomic steps, islands and kinks on their surface. For example, a concave rhombic dodecahedron Au C-NC enclosed with multiple high index planes showed excellent activity and selectivity towards CO formation [50]. In addition, this particular structure of Au C-NC was found durable for longer period of time. Summing up, low coordinating high index planes with CN less than 7 exhibits high catalytic activity, selectivity, stability whereas low index planes with higher CN greater than 6 exhibits lower catalytic activity and stability.
Lattice strain has evolved as another factor that have a significant influence on electrocatalytic properties of C-NCs towards ECO 2 RR. It was studied that strain generates a distortion in lattice, which, in turn, alters d-band center of metallic C-NCs. The altered d-band center either facilitates or lowers the adsorption of intermediates, as a result of that changing catalytic properties. Typically, upshifting of the d-band center facilitates adsorption of reaction intermediates on the surface of C-NCs. This is because, as the d band center approaches the Fermi level, which is the highest occupied state, the antibonding orbitals move over it, causing them to empty. This, as a result, strengthens the binding strength of the reaction intermediate on the catalytic surface and, therefore, enhances the reaction kinetics [51] In general, lattice strain in C-NCs can be induced by shaping C-NC in various morphologies, which leads to the inward displacement of atoms at high-energy locations, such as corners and edges, while the outward displacement of atoms on planes to gain overall crystal stability. These compression and expansion in the atomic arrangement in the NC S induce aeolotropic strain gradients that may improve the catalytic efficiency/selectivity of C-NCs [45]. Octahedral and Icosahedron C-NC of Pd with similar sizes were examined by huang et al. to investigate the effect of strain on ECO 2 RR. They observed that icosahedral/C C-NC shows higher FE (91% with −0.81 V vs. RHE) for CO production than octahedral/C C-NC in ECO 2 RR. The molecular simulations and DFT calculations showed that surface strain in icosahedral C-NC enhanced catalytic selectivity due to shifting in d-band center, which, in turn, facilitates absorption of a key intermediate (COOH * )  [49] with permission from the Royal Society of Chemistry.

Effect of C-NCs composition on ECO 2 RR
The variation in composition of metal C-NCs is another intriguing factor that plays an important role in tuning electrocatalytic efficiency/selectivity towards ECO 2 RR. Among other effects of composition, the synergistic effect where the mutual synergy between both electronic and geometric effects determines the activity/selectivity of C-NCs towards ECO 2 RR is well known. The electronic effect can be understood by the concept of shifting in d-band center due to alteration in composition. In addition to the electronic effect, the geometrical effect also makes a significant contribution, where the particular atomic arrangement in the active center can modify the binding strength of the reaction intermediate, thereby improving the electrocatalytic efficiency/selectivity towards ECO 2 RR [44]. Therefore, to understand the synergistic chemistry between geometric and electronic effects in this section, the electrocatalytic efficiency, selectivity and durability of bimetallic C-NCs and doped C-NCs electrocatalysts towards ECO 2 RR will be discussed.

Bimetallic C-NCs
Until now, several bimetallic NCs have been investigated for ECO 2 RR. For example, Kortlever et al. have found an optimal composition of a novel Pd 70 Pt 30 /C electrocatalyst highly active and selective towards HCOOH production. Moreover, this has a remarkably lower onset potential close to 0 V vs. RHE, making it best catalyst till the date [53]. However, usage of noble high-cost metals discourages its application on economical scale. Incorporation of non-noble metals such as Cu, Ni, Fe, etc., in bimetallic system could serve a better alternative to address high cost and stability of electrocatalyst. Kim et al. synthesized different composition of NCs including Au, AuCu, AuCu 3 , Au 3 Cu, and Cu, which were assembled in a monolayer on glassy carbon while keeping precise control over morphology (Size, Shape etc.) [44]. When considering electronic effect solely, pristine Au NC should have shown higher activity due to its optimal binding with COOH and CO intermediates. Interestingly, they have observed higher activity for Au 3 Cu bimetallic C-NC than expected one. Therefore, electronic effect mere does not explain volcanic acti vity correlation for C-NCs. The geometric effect that works synergistically along with electronic effect ensure further stabilization of intermediates, thus, explaining optimal activity of Au 3 Cu bimetallic C-NC towards electrochemical CO 2 reduction, among others. Previous studies have shown excellent properties of In based metal catalysts for selective CO 2 conversion into HCOOH. However, these metal catalysts suffer from limited current density and poor stability.
Kown et al. synthesized In 2 O 3 -ZnO C-NCs that showed excellent selectivity towards formation of HCOOH [54]. The XRD pattern showed that pre reduction of these C-NCs during electrolysis leads to the formation of In-Zn bimetallic C-NCs. Among all Zn 1-x In x NCs, In 0.05 Zn 0.95 offered remarkable selectivity for HCOOH production at FE of 95% (−1.2 V vs. RHE) as well as with higher current density. The higher catalytic activity was seen in both Zn 1-x In x O and Zn 1-x In x with decreasing value of x. The XPS data has revealed predominance of O vacancies in bimetallic systems at lower x, which, in turn, decreases thickness of oxide layers in Zn 1-x In x . Consequently, conductivity of Zn 1-x In x C-NCs increases at lower x, therefore, facilitates rapid electron transfer processes in ECO 2 RR. Thus, highest catalytic activity of Zn 0.95 In 0.05 C-NC is attributed to its remarkable conductivity. DFT calculations revealed that tight binding of OCHO* on pristine In, which impedes HCOOH production, has weakened by introduction of Zn in bimetallic C-NC. Therefore, mutual synergies of In with Zn in bimetallic system enhanced its catalytic selectivity in CDRR as compared to In [54]. Guo et al. have shown compositional effect in Cu 3 Pt C-NCs is responsible for improved activity and selectivity for CH 4 [55]. It was observed that increasing Cu contents in bimetallic NC leads to desorption of more CO * intermediates that subsequently gets protonated into CH 4 . Moreover, Pt which shows higher affinity for H + has significantly accelerated protonation of CO * . However, higher Cu content beyond ratio of Cu and Pt (3:1) raised CO * poisoning, and thus, declining in CH 4 production [55].

Dopped C-NCs
In doped C-NCs, extrinsic or intrinsic introduction of impurities can cause a change in the electronic structure in a way that can enhance catalytic efficiency/ selectivity and durability. For example, the incorporation of impurities can provide additional electrons (n-type) or additional vacancies (p-type), thereby, increasing the conductivity of the catalyst that would otherwise be poor in conductivity. Therefore, the increased conductivity may accelerate the electron transfer process in the ECO 2 RR. Although many advances have been made in the field of doped C-NCs, some studies conducted in ECO 2 RR. Recently, a group led by Kim et al. reported an unprecedented selectivity of vanadium ( 23 V) doped In 2 O 3 C-NCs towards CH 3 OH formation in addition to HCOOH and CO, previously not known with pristine In and In 2 O 3 [56]. This can be understood using the commonly suggested scheme for producing CH 3 OH shown in the

C-NCs/metal organic framework hybrid
In the past years, molecular organic frameworks (MOFs) have received significant attention in the field of catalysis, including ECO 2 RR, where they have been used primarily to provide solid support for molecular catalysts [57,58]. The combination of MOF with C-NCs creates a class of hybrid materials that have demonstrated great potential to become future class of electrocatalysts with improved efficiency/selectivity and durability. Concerning this, a deep understanding of the material design and working principle of these novel hybrid systems is indispensable prior to implementing them practically. Recently, Guntern et al. investigated catalytic selectivity and durability of Ag C-NCs/Al PMOF hybrid system for electrochemical CO 2 reduction [59]. Based on UV visible and XPS data, it was concluded that electron transfer from MOF to Ag C-NC in this hybrid system increases electron density at Ag C-NC, thereby, facilitates electron transfer to CO 2 .− intermediate. As in result, selectivity of Ag C-NCs/Al PMOF towards CO increases than pristine Ag C-NCs while decreases for H 2 ER. Additionally, a small contribution of transport events due to diffusion of reactants and products within pores of MOF adds in the selectivity of NC/MOF hybrid towards CO. Besides, NC/MOF hybrid system showed better stability compared to bare Ag C-NCs at lower potential [59].

Ligand functionalized C-NCs
Capping agents such as, organic ligands, surfactants or polymers are engendering factors of surface anchoring molecules that are crucial in synthesis of C-NCs based catalysts with well-defined shape, uniform size distribution and different composition. After synthesis, these capping agents can significantly alter C-NCs catalytic efficiency in both positive and negative way by staying absorbed on their surface. For example, Wang et al. reported that catalytic activity of Ag NCs modified with capping agents increased by 53-fold compared to pristine Ag NCs towards ECO 2 RR [60]. In Several studies it has been shown that presence of surface molecule can affect active site of NC in numerous ways: 1) by perturbing electronic structure of active sites 2) by introducing steric hindrance that impedes diffusion of absorbates reaching at active center 3) by blocking selective facets of C-NCs, which, in turn, could enhance selectivity and activity. Moreover, chiral ligands can be used to produce stereoselective products. Therefore, surface functionalized NCs has opened a new window in the field of electrocatalytic reactions where unprecedented control over efficiency/selectivity can be achieved by ligand design [61,62]. However, researchers still have a limited understanding of how these anchoring ligands affect the local electronic environment of NC and how the backbone of anchoring ligands regulates reactivity between NC and surrounding reactants, or reaction intermediates.
Pankhurst et al. have tuned ECO 2 RR selectivity of Ag C-NCs using different imidazolium ligands [63]. Here they were able to introduce different organic component by varying tail and anchoring groups on imidazole motif. When performed ECO 2 RR, the ligand bearing NO 2 anchoring group with octyl tail-found highly selective towards CO with FE of 92%. It was concluded that interaction between cationic imidazolium group with CO 2 increases population of this reactant over the catalytic surface. Furthermore, an optimal chain length of ligand tail-group increased hydrophobicity of surface, and thus, increases selectivity and efficiency for ECO 2 RR by inhibiting EH 2 ER. However, electronic changes induced by ligand anchoring-group did not improve significantly properties of electrocatalyst. The next example of ligand surface functionalization for ECO 2 RR discusses N-heterocyclic-carbine functionalized Au C-NCs (Au C-NC-Cb) from group led by Cho et al. The significant downfield shifting in 13C NMR peaks of NHC reveals strong electron donation from ligand to metal, making Au C-NCs surface electron-rich. As in result, it facilitates the electron transfer process to CO 2 , and thus, enhances efficiency of Au C-NC-Cb relative to bare Au C-NCs [64].

C-NCs-based heterogeneous catalyst for EH 2 ER
The concept of using electric current to control various chemical reactions achieved much attention, since the time when humankind invented first power resources. Splitting of water to produce hydrogen and oxygen gas started much earlier, but now it has started at large scale in industrial process and seems to play a crucial role in combating the future energy crisis. The increasing demand for energy day by day and the shortage of fossil fuels have encouraged scientists to develop a renewable and clean source of energy.
Hydrogen is considered a clean source of energy because by-product of H 2 combustion is H 2 O and the starting material to obtain H 2 is water, therefore, an efficient and clean source to supplant the depleting fossil fuels [65][66][67].
Moreover, H 2 produces highest energy on combustion of per unit mass relative to any other fuels, thus, leading to become a fuel of future. The H 2 can be produced by electrochemical water splitting reaction which is an endothermic process with a potential of ΔE° = 1.23 V and ΔG° = 237.2 kJ mol −1 . Water splitting generates both hydrogen and oxygen. For the process of electrochemical water splitting the reactions that occur at anode are called as oxygen evolution reaction (O 2 ER) and the reactions which occurs at cathode are called as H 2 evolution reaction (H 2 ER) [68]. Electrocatalysis is actually an attempt to elucidate and predict observable phenomena like overall activity of the reactions that occur on the surface of electrode by the interactions of electrode/electrolyte interface. Development of an efficient electrocatalyst is important to minimize the energy losses during the electrocatalytic splitting of water to produce hydrogen and oxygen gas. Figure 6 shows a diagrammatic representation of evolution of hydrogen (Depicted to the left-side of Figure 6) and oxygen (depicted to the right side of Figure 6) gas on the surface of glassy carbon electrode (GCE) after deposition of catalyst on its surface.
The reactions which are central to hydrogen energy are two types. These are hydrogen evolution (2H + + 2e − → H 2 ) and hydrogen oxidation (H 2 → 2H + + 2e − ) reactions. The research of oxidizing and evolving hydrogen was started in 1960 but it gained importance in 1970 and 1990 when the shortage of oil was realized [69]. The most success in this regard was achieved when precious metals like platinum (Pt) were used. Metal NPs on the surface of carbon also showed great success in H 2 ER and hydrogen oxidation reaction (H 2 OR).
In the world of EH 2 ER electrochemistry, recent merge of computational quantum chemistry and nanotechnology have shown great progress in explaining fundamentals and basics of EH 2 ER with much emphasize on its utility and storage [51,70,71]. Metallic Pt is considered as 'state of the art catalyst' and exhibits small Tafel slope values and extremely high exchange current density (j 0 ) [72][73][74]. However, because of high cost and less availability of Pt, a sustainable, cost effective, and stable catalyst needs to be developed. So, there have been efforts to synthesize the EH 2 ER active catalysts from the transition metals that are abundant in nature.

Mechanistic overview of EH 2 ER
EH 2 ER kinetics has a long history and have been explained in detail [69]. EH 2 ER (2H + +2e-→ H 2 ) is a process involving a series of electrochemical steps which takes place on the electrode surface and results in the evolution of hydrogen. There are two mechanisms in acidic and basic conditions accepted universally as shown in In the above reactions, H* indicates an adsorbed hydrogen atom that has been adsorbed chemically on the surface of electrode (M) at the active site. These reaction pathways are highly dependent on electronic and chemical properties of the electrode surface [76]. Tilak et al., explained that rate controlling steps (1, 2 and 3) is predicted by deducing Tafel slope values from EH 2 ER polarization curves [72]. The mechanism and rate determining step is studied by the Tafel slope. Tafel slope is an inherent and interesting property because it gives information about the potential difference required to increase or decrease the current density by 10-fold. Tafel slope is also useful to determine the effectiveness of a catalyst. In order to calculate the Tafel slope the linear portion of the Tafel plots is to be fitted in the Tafel equation (η = b log (j) + a, where η = overpotential, b = Tafel slope, and j = current density) [77,78]. Theoretical facts about Tafel slope have been derived from Butler-Volmer equation and it is proved for three limited cases. First, if the discharge reaction proceeds very quickly and H 2 is evolved by the rate determining combination reaction (Tafel step). The slope value is 29 mV dec-1 at 25°C (2.3RT/2F). Second, if the discharge reaction proceeds very quickly and H 2 is evolved by the rate determining desorption reaction (Heyrovsky step). The slope value for this step is 40 mV dec-1 at 25°C (4.6RT/3F). Third, if the discharge reaction proceeds very slowly and then the rate determining step will be Volmer step irrespective of the fact whether H 2 is evolved by the combination reaction or the desorption reaction. The Tafel slope is 116 mV dec -1 at 25°C (4.6RT/F). The detailed mechanism is shown in Figure 7. It is evident that reaction (1) represents chemical adsorption, whereas, reaction (2) and (3) exhibits H atoms desorption from the electrode surface, which are competing with each other. Sabatier and co-workers came with an idea (Sabatier principle) that a better catalyst should not only form a strong bond with absorbed H* and facilitates the proton electron transfer process, but also it should be weak enough in facial bond breaking to assure quick release of H 2 gas [79]. It is difficult to establish a quantitative relationship between energies of H* intermediate and rate of electrochemical reaction owing to absence of directly measured surfaceintermediate bonding energy values [80]. However from the perspective of physical chemistry, both for H* adsorption and H 2 evolution on the catalyst surface can be determined from the change in free energy of H* adsorption (∆GH*) using EH 2 ER free energy diagram [81]. According to Sabatier principle, under the condition ∆GH* = 0 will have maximum overall reaction rate (expressed in terms of EH 2 ER exchange current density, j0).

Metal-based C-NCs for EH 2 ER
An important correlation between ∆GH* and j0 have been proposed in the form of "volcano curve" for a wide variety of electrode surfaces as illustrated in Figure 8 [81,82]. Pt group of metals are the most efficient in the process and that's why are found at the top of the volcano curve, because they have small Tafel slope and quasi zero onset potential.
However, due to high cost of Pt, various research groups have been working on modifying Pt group metals such as engineering the NCs. Crystal plane (110) of Pt NCs has been proved good surface for EH 2 ER. Like Pt, Palladium (Pd) NCs have been showing great promise as it is in the same group and has almost same size and its lattice matches about 0.77% to Pt, good thing about Pd is that it is comparatively cheaper than Pt. Pd has one advantage that it can adsorb hydrogen from both electrolytes and the gas phase. Pd can be loaded on various supports to increase its activity as it alters surface area and electronic conductivity of the nanocrystals [84]. Huang et al. observed that Pd C-NCs deposited on carbon paper substrate has activity higher than Pt black electrode and it required very less catalyst loading that is 0.0106 mg cm −2 [85]. One thing to be noted about Pd is that it has higher activity in acidic medium than alkaline medium because of lower Pd-H binding energy and lower activation energy, acid (32.3 ± 0.7 kJ/mol) and base (38.9 ± 3.0 kJ/mol). Ruthenium (Ru) NCs are also being explored for EH 2 ER. As the Sabatier principle suggest that catalyst should not have much stronger binding to the hydrogen and should possess moderate binding capacity so desorption is easy, Ru-H follows this trend as it has ~65 kcal/mol energy for Ru-H bond and thus less activation barrier for desorption process [86]. Ru C-NCs are usually used with some support as they have durability problems because of aggregation. One such example where Joshi et al. used Ru C-NCs supported with Tungsten (W). DFT calculations suggest that Ru (0001) has high H 2 binding to surface energy but using W support, it could reduce the H 2 adsorption energy and changes the electronic environment thus making it similar to Pt (111) and increases its activity for EH 2 ER process [86]. Baek et al. revealed that Ru when deposited on graphene nanoplatelets (GnP) to form Ru@ GnP, its activity usually surpasses that of Pt/C in both acidic and alkaline medium. This happens because it is more stable, possess low Tafel slope (30 mV dec −1 in 0.5 M aq. H 2 SO4; and 28 mV dec −1 in 1.0 M aq. KOH) and also has comparatively low overpotential at 10 mA cm −2 (13 mV in 0.5 M aq. H 2 SO 4 ; 22 mV in 1.0 M aq. KOH) [87]. Not only Pt, Pd, Ru, metals like Iridium (Ir) are also explored for the EH 2 ER process and also earth abundant metals are used but they are prone to corrosion in the presence of alkaline and acidic medium. Thus, the other way is using non-noble metals for the process.
Non-Noble metals follow this trend for the catalytic activity Nickel (Ni) > Molybdenum (Mo) > Cobalt (Co) > W > Iron (Fe) > Copper (Cu) which is calculated using the voltammetric techniques [88]. Ni shows a very good catalytic activity when using in the hybrid form of Ni/NiO/CoSe 2 because this composite helps in less resistance to charge transfer. But this hybrid has poor stability as Ni does not work well in acidic medium [89]. Recent studies by Qiu et al. found that when Ni is used with graphene it forms Ni-C bonds which increases the stability as well as the activity of the catalyst and is the best one proved for the process using Ni [90]. Co when embedded with Nitrogen rich CNTs forms a very good catalyst that catalyzed at all pH ranges. The reason for this good activity at all pH ranges is the N-doped content and the structural defect caused by the caused by pyrolysis of the Co-NRCNTs at higher temperatures [91]. These Nitrogen rich Co based catalyst can also be dispersed over the nanofibers for improving the catalytic activity. These particular catalysts also showed good stability for various potential cycles of process [92]. Along with Co and Ni Other Non-Noble metals are also used for the EH 2 ER process including Fe, W, Mo but these all face the problem of their stability and there is still a lot to discover in this field.

Non-nobel metal-based C-NCs for EH 2 ER
To avoid using precious noble metals there have been a plethora of reports using non-noble metal-based C-NCs for EH 2 ER process. Some of them are transition Metal Oxides (TMOs), transition metal nitrides (TMNs), transition metal carbides (TMCs), transition metal borides (TMBs), transition metal phosphides (TMPs), transition metal dichalcogenides (TMDs). In this section the authors will discuss about the advancement in these types of NCs their advantage and disadvantages all. Although there are huge number of reports on transition metal-based compounds, but Mo and W display very good catalytic activity out of all of them. TMOs are easily available, stable, not harmful to the environment and obviously not precious like noble metals and thus is a good class of EH 2 ER catalysts. Out of all the TMOs, Mo (MoO 2 ) and W (WO 2 ) based EH 2 ER catalysts are best as they have high electrical conductivity as compared to other TMOs the credit goes to their monoclinic and distorted rutile crystal structure [93]. Compact MoO 2 faces have a problem of aggregation and thus various research groups tried to bring changes in the catalyst by decreasing the size of structure, forming hybrid composites, doping the MoO 2 or even introducing surface defects. One such example where Yu et al. encapsulated MoO 2 with phosphorous-doped porous carbon embedded on rGO to form MoO 2 @PC-rGO which has a small tafel slope (41 mV dec-1 ) and less over potential (ƞ 10 = 64 mV). Here electronic coupling between MoO 2 and rGO along with the porous carbon layer helps in getting rid of the problem of aggregation and improves its efficiency as a EH 2 ER catalyst [94]. The other important metal oxide for EH 2 ER is WO 2 . Reports have revealed when WO 2 have vacancies of oxygen, it provides large number of active sites and thus augmented the EH 2 ER process as compared to the compact WO 2 counterpart. One such example where Shen et al. encapsulated WO x with Carbon on a Carbon support to form WO x @C/C which has EH 2 ER activity comparable to Pt metal with ultra-low overpotential (ƞ 60 = 36 mV) and very small tafel slope (19 mV dec −1 ) which is because of the thick carbon shell helping in increase of charge transfer and also changes the Gibbs free energy values of H* for different adsorption sites [95].
TMNs are also other class of noble metal-compound based NCs for EH 2 ER. The importance lies in the fact that they possess more contraction of the d bands and density of state near Fermi level because of interaction of negatively charged N atom which expands the lattice and increases it efficiency as a catalyst to make it comparable to noble metals like Pt, Pd [96]. As discussed earlier, whenever NCs are encapsulated with carbon material they tend to avoid aggregation and improve the efficiency as a catalyst. encapsulated with N-doped carbon material to form MoN@NC which exhibited very low overpotential (ƞ 10 = 62 mV dec −1 ) and small tafel slope (54 mV) as depicted in Figure 9 (c) [97]. WN also possess same features as they exhibit less activity when used as it is but when encapsulated with carbon material its activity increases, one such example is using WN encapsulated with N doped graphene material (WN x NRPGC) which has high electrocatalytic activity because of the formed hetero-architecture [98]. Ni based TMNs have also been explored a lot as they possess high electrocatalytic activity.

Metal-alloy-based C-NCs for EH 2 ER
Whenever there is introduction of another element in the lattice of the metal synergistic effect comes into effect (intercalation of crystal planes, change in the metal-metal length to have strain and also formation of heteroatom bond to give ligand effect). This result in the change of electronic properties and morphology and hence in the electrocatalytic activity of the catalyst. To reduce loading of noble metals they are doped either with other comparatively cheap noble metal or sometimes with transition metal. The authors will discuss examples of both these types. Pt can be doped with Pd to form 1-D single crystalline material (thickness 3 nm) which increases the Pt utilization efficiency this was done by Liu et al. using solution phase method directed by surfactant [99]. Pt can also be doped with non-noble metals one such example is the use of Pt-Co alloy encapsulated on carbon material, thus possessing high activity as displayed by the small tafel slope of 20 mV dec −1 . This catalyst requires very less loading of Pt (ca. 5 wt %) and has activity comparable to Pt/C catalyst [100]. Using the same strategy Pd and Ru can also be doped with either noble metal or transition metals, some examples are Pd-Au catalyst, Pd-Co catalyst, Ru-Co and Ru-Ni [101][102][103][104].
Transition metal can be alloyed with transition metal itself and thus it can be a very good alternative for noble metal electrocatalysts because of the cost-effective nature of them. These alloys could either be binary alloys or ternary alloys, the authors will discuss examples from both binary and ternary alloys. Ni can form alloy with various other transition metal, but Ni-Mo binary alloy is considered best for the EH 2 ER. Zhang et al. worked on the synthesis of MoNi 4 supported over the MoO 2 cuboids over the Ni foam. This catalyst has the activity similar to Pt/C with zero onset potential and ƞ 10 = 15 mV and very low tafel slope of 30 mV dec −1 [105]. Ni binary alloys face the problem of corrosion which can be overcome by using the carbon support along with the Ni based alloy. Co also form binary alloys with Fe using N-doped carbon-based support. Also, Co can be alloyed with Mo forming good electrochemical catalyst for EH 2 ER such as Co 3 Mo having an overpotential of ƞ 10 = 68 mV and tafel slope of 61 mV dec −1 [106]. Ternary alloys in the recent times have gained popularity for EH 2 ER electrochemical catalysts as electronic and morphological features of catalyst can be tuned by variation in compositions of various metals and thus it can act as the good promising substitute for the noble-metal-based EH 2 ER catalyst. One such example is the use of small amount of Pt (4.6%) to the Fe-Co binary alloy to form the PtCoFe@CN electrocatalyst which demonstrated activity similar to that of commercial 20% Pt/C having an overpotential of ƞ 10 = 45 mV as depicted in Figure 10(b) [107].
Research is still going on to prepare the ternary alloys without using the noble metals in it and that will really be the landmark in this field as it will be a catalyst with cost-effective nature.

Conclusions
This chapter discuses a thorough study of recent acheivements by C-NCs-based elelctroctalysts for ECO 2 RR and EH 2 ER. In this chapter, the authors have tried to summarize role of C-NCs in ECO 2 RR and EH 2 ER and the scope of these two important electrocatalytic reaction in combating the energy crises for human kind in introduction part. The examples that are discussed in this chapter were taken from recent reports in literature. The first part of this chapter sheds light on colloidal synthesis of nanocystals. The second part of this chapter emphasizes on effect of shape, size and composition in determining the catalytic activity, selectivity and stability of C-NCs for ECO 2 RR. Here the effect of ligand functionalization and MOF/NCs hybrid system on ECO 2 RR activity is also illustrated. The third part of this chapter addreses the role of C-NCs-based electrocatalysts on EH 2 ER, its activity and stability. In this part, indepth study about mechanism of EH 2 ER is also discussed. Although a lot has been done in ECO 2 RR but ECO 2 RR still face a big challenge in selectivity, similarly in EH 2 ER a lot of research has been dedicated to find a substitute of state-of-art Pt/C catalyst which is very much expensive. However, researchers have been sucessful in discovering the costeffective electrocatalysts which are as good as Pt/C but they are still facing the stability issues.

Author Contributions
RN, AP (Abhay Prasad), AP*(Ashish Parihar) designed the study, reviewed the literature, wrote and edited the manuscript. MSA and RS provided the inputs while editing the manuscript. The complete review article was edited and finalized by RN, AP, and AP*.