Ceria-Based Materials in Hydrogenation and Reforming Reactions for CO2 Valorization

Introduction

For the first time since the Industrial Revolution the global CO₂ atmospheric concentration have reached the threshold of 400 parts per million, increasing the average world temperature by 1.5°C within the next two-three decades (US, EPA, 2016; IPCC report, 2017). This poses a threat upon the environment and a great challenge for today's society, that must combine the drive toward a continued economic growth and ever-increasing demand of energy and chemicals with the need to preserve the environment for future generations. Among the main strategies which have been considered to reduce or minimize CO₂ atmospheric emissions, one is its capture and storage (Araújo and de Medeiros, 2017). Carbon capture and storage (CCS) comprises separation of CO₂ from industrial sources, compression and transportation to a geologic site for storage, or to enhanced oil recovery. Taking into account that the potential sequestration capability and the industrial use of CO₂ are more than 150 times lower than its production, the CCS approach should be adopted only if we are able to develop technologies to convert efficiently CO₂ into chemicals or fuels, in an alternative strategy, identified as CCSU, CO₂ capture-storage-utilization (Cormos et al., 2018).

Therefore, in an envision of a free-carbon footprint circular economy, CO₂ should substitute fossil carbon as feedstock to produce fuels and chemicals, while solar, wind, and geothermal sources should be employed for the production of electricity and H₂ (Martens et al., 2017). Nowadays, there are many emerging technologies based on chemical catalysis, electrocatalysis, photocatalysis, and biocatalysis, but they are still not mature to make realistic the transition toward a mixed carbon-hydrogen economy (Kondratenko et al., 2013).

Since the fuel market is many times larger than the chemicals market, several efforts are directed to develop technologies to recycle back CO₂ emissions to a synthetic transportable fuel. In this field, the highest readiness have been achieved by the technologies based on catalytic processes such as the reverse water gas shift (CO₂+H₂↔CO+H₂O, RWGS), the methane dry reforming (CH₄+CO₂↔2CO+2H₂, MDR), the methanation of CO₂(CO₂+4H₂↔CH₄+2H₂O, CM), and CO₂ conversion to oxygenates (Götz et al., 2016).

The methane dry reforming reaction is an endothermic process that occurs at high temperature (>800°C). This implies that the catalysts employed (mainly Ni, Co and related alloys) can sinter and coke due to CH₄ cracking, moreover they can be deactivated by the presence of sulfurous compounds in the stream (Lavoie, 2014).

The direct hydrogenation of CO₂ to methane is instead an exothermic process, thus thermodynamically favored at low temperature. A low operating temperature poses kinetic constrains which require efficient catalysts to be overcome. Various metals of the group VIIIB in the periodic table have been tested as catalysts for this reaction. Ru resulted one of the most active and selective as well as highly resistant to oxidizing atmosphere, however its high price limits its industrial application (Su et al., 2016). Nickel has been proved to be a valid alternative, especially for its low cost. The main disadvantage in using Ni is its high tendency to oxidize in the operating atmosphere, to poison in presence of sulfur gases and to volatilize forming nickel carbonyls, which are very toxic (Rönsch et al., 2016).

The reverse water gas shift reaction (RWGS) is a slightly endothermic process promoted mainly by copper based and supported ceria catalysts. Its main advantage is the formation of CO, which can be used as building block in other processes such the Fisher-Tropsch and the methanol syntheses. The production of methanol through the RWGS resulted competitive against that obtained by a direct hydrogenation of CO₂, which is another possible reaction recently investigated to valorize CO_2. Also in this case, the main issues are due to the need of a highly selective catalyst resistant to sintering and to poisoning due to coke and sulfur deposition (Daza and Kuhn, 2016).

A common feature of the above mentioned reactions is the simultaneous occurrence of several equilibrium reactions that may limit the selectivity of the process considered. Moreover, they require a highly active catalyst since CO₂ is a very stable molecule. An important aspect in developing suitable catalysts to overcome the issues of these processes is the choice of an appropriate support. The support has a pivotal function in controlling the morphology and the oxidation state of the metal phase, its dispersion and, consequently, the activity and durability of the catalyst. Moreover, it can work as co-catalyst in the activation and dissociation of CO₂. Among different supports CeO₂ and mixed oxides based on ceria have proved to play a significant role in improving the catalytic performance for these processes.

The first catalytic application of ceria was as an oxygen storage component in automotive three-way catalysts but the use of ceria based oxides in catalysis is nowadays ubiquitous. Several articles give insight into the fundamentals of these materials and many recent reviews summarize their applications in catalysis (Trovarelli and Fornasiero, 2013; Montini et al., 2016; Xie S. et al., 2017; Devaiah et al., 2018). The superior catalytic capability of CeO₂ are straightly linked to the reversible redox pair Ce³⁺/C⁴⁺ and to its surface acid basic properties (Trovarelli, 1996). Moreover, when nanostructured, or in its doped form, this oxide is characterized by a large number of surface defects, primarily oxygen vacancies (Małecka, 2016; Trovarelli and Llorca, 2017). The presence of these defects on the surface often alters dramatically the adsorption and subsequent reactions of various adsorbates on the support and on metal particles. Moreover it may contribute to generate very reactive metal-support interfaces (Mullinsn, 2015; Rodriguez et al., 2017). Shape and size of the ceria nanocrystals can be designed and controlled by different strategies of preparation and treatments to boost redox properties and enhance catalytic activity (Wu et al., 2016; Trovarelli and Llorca, 2017; Ma et al., 2018). With this basis the review analyzes the role of ceria and ceria doped oxides in the reforming processes for the valorization of CO₂, highlighting advantages and disadvantages of their use. Emphasis is given to the peculiar role of ceria in the CO₂ reforming processes mechanisms, in the perspective of designing cost-effective formulations based on ceria oxides that can boost the entry into the market of these technologies.

CO₂ Methanation Reaction

CO₂ hydrogenation is in many cases the first step in the transformation of CO₂ into valuable chemicals (Wang et al., 2011; Kondratenko et al., 2013). The reaction can lead to a series of products ranging from CO (via the reverse water gas shift) to alcohols and hydrocarbons, thus being of potential interest for several practical applications. CO₂ hydrogenation to methane (1), known also as Sabatier reaction or CO₂ methanation, represents a significant example of the conversion of waste (the CO₂ emission) into energy (or energy carrier).

$\begin{array}{cc}{\text{CO}}_{\text{2}}{\text{+4H}}_{\text{2}}\leftrightarrow {\text{CH}}_{\text{4}}{\text{+2H}}_{\text{2}}\text{O}(\Delta {\text{H}}_{\text{298K}}=\text{-252}.\text{9}\text{KJ/mol})& (1)\end{array}$

Among other implications, this reaction is a key step of the so called “Power-to-Gas” technology which nowadays is receiving great attention due to its potentialities in the renewable energy scenario (Götz et al., 2016; Rönsch et al., 2016; Li W. H. et al., 2018c). This process would allow an almost carbon neutral cycle by using hydrogen from renewables. The reduction of CO₂ to methane proceeds via the transfer of eight electrons and presents strong kinetic limitations, thus requiring the presence of a suitable catalyst (Wei and Jinlong, 2011; Su et al., 2016). Catalysts for CO₂ methanation are comprised by supported noble or transition metals, and there is a general agreement in the literature on the fact that the reaction mechanism is strongly influenced by the nature of the support (Su et al., 2016; Frontera et al., 2017).

M-CeO₂ Catalysts

Ceria-based catalysts have been found to possess higher activity and selectivity to methane with respect to other oxides for the methanation of carbon dioxide (Das and Deo, 2012; Tada et al., 2012; Atzori et al., 2017; Diez-Ramirez et al., 2017; Dreyer et al., 2017; Fukuhara et al., 2017; Martin et al., 2017; Li M. et al., 2018). The investigation of CO₂ methanation on ceria-based materials dates back to the 90's, when firstly significant differences in this reaction between ceria and other supports were described (Trovarelli et al., 1991; de Leitenburg and Trovarelli, 1995). In particular, it was demonstrated that following a high temperature (500°C) reduction treatment the transient activity of a Rh/CeO₂ catalyst was much higher compared to rhodium deposited on other oxides. This behavior was attributed to the presence of oxygen vacancies on the surface of reduced ceria, that were filled by the water formed during reaction thus explaining the transient nature of the high activity recorded for Rh/CeO₂. Similarly, other noble metals supported on ceria showed a prominent transient behavior in CO₂ methanation (de Leitenburg et al., 1997).

More recent studies revealed that indeed oxygen vacancies and ceria reducibility play an important role for CO₂ hydrogenation to methane on metal-ceria systems, irrespective of the metal (Sharma et al., 2011, 2016; Tada et al., 2012; Upham et al., 2015; Wang et al., 2015; Wang F. et al., 2016; Zhou et al., 2016; Diez-Ramirez et al., 2017; Dreyer et al., 2017; Bian et al., in press). Wang et al. compared the activity of Ru supported on ceria nanocubes (NC), nanorods (NR), and nanopolyhedra exposing different facets for CO₂ methanation (Wang et al., 2015). Their results clearly demonstrate that the most active catalyst, i.e., Ru on CeO₂ nanocubes, is the one that shows the highest concentration of oxygen vacancies which serve as active sites for CO₂ activation. In a similar study carried out for Ni supported on ceria nanocubes and nanorods, instead, the highest activity was recorded over Ni/CeO₂-NR, which presented a higher number of Ce³⁺ sites (Bian et al., in press). The apparent contradiction is due to the fact that in the first study the most defective structure was that of ceria nanocubes, whereas in the second it was that of ceria nanorods. This is likely linked to the variability of the defective structure of ceria nanorods, for which growth direction of crystal planes, exposed facets, and presence of defects may depend on synthesis approach (Trovarelli and Llorca, 2017).

Mechanism of Reaction

The coupling of advanced characterization techniques with in situ and theoretical studies allowed to uncover the effect of CeO₂ redox properties: the reduced and basic ceria surface favors the adsorption of CO₂ and its decomposition, while the presence of oxygen vacancies catalyzes the formation and dissociation of reaction intermediates (Figure 1).

FIGURE 1

Figure 1. Proposed mechanism for CO₂ activation on ceria surface.

Regarding CO₂ adsorption/activation, it is reported that this happens to a significant extent only on reduced ceria or in presence of H₂, indicating that the presence/formation of a vacancy is a necessary prerequisite (Sharma et al., 2016). Beside the first CO₂ chemisorption step, the mechanisms proposed in the literature for the hydrogenation of carbon dioxide to methane on ceria-based systems, obtained from in situ or operando measurements, follow two major routes: the formate and/or the carbonate route. Wang et al. couple steady-state isotope transient kinetic analysis (SSITKA)-type in situ DRIFT infrared spectroscopy with operando XANES and Raman spectroscopy to observe the evolution of intermediates and surface species during CO₂ hydrogenation over Ru/CeO₂ nanocubes (Wang F. et al., 2016). According to their results recorded from 25 to 400°C, CO₂ converts to carboxylate species ${\text{CO}}_2^{\text{δ}-}$ by interacting with surface Ce³⁺ and this step is followed by the reaction of ${\text{CO}}_2^{\text{δ}-}$ with surface hydroxyls to produce formate (HCOO⁻) species. Formates dissociation to methanol then takes place at around 300°C with subsequent hydrogenation of methanol to methane. The presence of reduced ceria (Ce³⁺) is necessary to initiate the reaction, and based on the observation reported in this work it changes drastically the picture with respect to Ru on alumina support, on which CO₂ chemisorption gives rise to the formation of bicarbonates. In agreement with this work, the evolution of formates on Ru/CeO₂ and bicarbonates on Ru/Al₂O₃ has been observed also by Dreyer et al. (2017). A different situation is described by Sharma et al., who observe the formation of carbonate species on a Ru-substituted ceria catalyst by in situ DRIFT (Sharma et al., 2016). The discrepancy might be due to the fact that in this last example the metal is substituted in the ceria lattice, giving rise to a different configuration of the metal-ceria entity. Nevertheless, also in this case the authors postulate the need of a reduced ceria surface and/or the presence of oxygen vacancies to activate the CO₂. Also in the case of Ni-based catalysts there are some apparent contradictions. The carbonate route has been described for example by Zhou and coworkers for Ni/CeO₂ catalysts, prompted again by the formation of oxygen vacancies (Zhou et al., 2016). The formate route is proposed instead by Bian and coworkers, who recently studied the methanation activity of Ni supported on ceria nanorods (Bian et al., in press). They also link the evolution of formates to the presence of reduced Ce³⁺ sites. Other authors have observed the coexistence of the two reaction intermediates (formate and carbonate species) on Ni/CeO₂ and Rh/CeO₂ catalysts (Konishcheva et al., 2016; Martin et al., 2017), thus leading to the conclusion that both routes can take place, jointly or separately, likely depending on reaction conditions. A theoretical work by Lu and coworkers describes the occurrence of different paths for CO₂ reduction on ceria (111), demonstrating that indeed the nature of the surface (defective or stoichiometric) and of the reaction environment is crucial for the establishment of one or another reaction route (Lu et al., 2015). Despite the different mechanisms reported, there is a general agreement on the role of ceria which is always that of adsorbing and activating CO₂ via a redox mechanism involving Ce³⁺ and/or oxygen vacancies. A recent study by Li et al. on an Ir/CeO₂ catalyst sheds some light on another important element, i.e., the effect of ceria in tuning the chemical properties of the metal (Li et al., 2017), another issue that might explain the different mechanisms reported by different research groups for the same metal. In this work it is reported that the selectivity toward methane (or carbon monoxide) strongly depends upon Ir oxidation state, which in turn is determined by the capability of ceria to transfer oxygen atoms to Ir nanoparticles due to a strong metal support interaction. It is clear then that different preparation routes and/or different metal loadings can change the way ceria interacts with the metal itself, thus affecting the reaction mechanism.

Ceria as Promoter

Ceria has not been studied only as a support for methanation reaction but also as a dopant on other oxides, with the aim of improving the overall catalytic activity. The addition of CeO₂ has been shown to enhance the reducibility of the catalysts (Liu et al., 2012; Tada et al., 2014; Abate et al., 2016; Toemen et al., 2016), to increase metal dispersion (Bian et al., 2015; Nie et al., 2017), to improve catalyst stability (Liu et al., 2012; Toemen et al., 2016; Nie et al., 2017), and to promote CO₂ adsorption by modifying the basicity of the supports (Westermann et al., 2017). In particular, in the case of Ni-Al₂O₃ catalyst it was found that a little amount of CeO₂ (2–3 wt%) was enough to enhance not only the catalytic performances but also the stability during long time operation, while a further increase in ceria content resulted in a slight activity loss (Liu et al., 2012; Nie et al., 2017). Nevertheless, from a literature survey it is not straightforward to determine the optimum ceria loading for Ni-alumina catalysts, since a positive effect was reported also for much higher (60%) ceria content (Bian et al., 2015).

M-CeO₂-ZrO₂ Catalysts

When ceria is coupled with zirconia all the above mentioned aspects are emphasized, and where a comparison with pure ceria is reported the mixed oxide shows a better catalytic activity (Razzaq et al., 2013; Zhu et al., 2013). The enhanced performances of Ce-Zr based catalysts with respect to pure ceria can be ascribed to the higher number of defects, which are known to form upon addition of Zr⁴⁺ ions into the lattice of ceria, and the subsequent increase in oxygen mobility. Most of the papers dealing with ceria-zirconia as support or promoter for CO₂ methanation involve nickel (Aldana et al., 2013; Cai et al., 2013; Pan Q. et al., 2014; Nizio et al., 2016; Ashok et al., 2017; Le et al., 2017) or Ni-based bimetallic formulations (Ocampo et al., 2011; Razzaq et al., 2013; Zhu et al., 2013; Pastor-Pérez et al., 2018; Shang et al., 2018) as the active phase. In general, these studies highlight the high reducibility of ceria-zirconia based catalysts and their remarkable stability during time on stream operation, also when CeO₂-ZrO₂ is used as a dopant (Le et al., 2017). The former aspect is clearly due to the well-known redox properties and oxygen storage capacity (OSC) of Ce-Zr solid solutions, whereas the latter appears to be related to the interaction between the metal and the support which can avoid or limit particle sintering. A strong metal-support interaction has a positive effect on catalytic activity both in transient (i.e., during temperature ramping) and in steady state (isothermal) conditions, as shown by comparing the behavior of Ni-CeZr prepared by different methods giving rise to different degrees of interaction between Ni and ceria-zirconia (Aldana et al., 2013; Ashok et al., 2017). The higher methanation activity and stability during time-on-stream operation has been attributed to Ni species strongly interacting with the support and to the higher mobility of surface oxygen/hydroxyl species. When compared with other supports, ceria-zirconia is found indeed to improve metal-support interaction with beneficial effect on catalytic performance (Razzaq et al., 2013). Moreover, an opportune tailoring of the synthesis procedure, for example by incorporation of Ni ions into Ce-Zr lattice by impregnation or ammonia evaporation, can lead to samples with higher metal dispersion, oxygen vacancies and reduced ceria sites (Pan Q. S. et al., 2014; Ashok et al., 2017). Also the addition of another metal such as Ru (Shang et al., 2018) or Co (Zhu et al., 2013; Pastor-Pérez et al., 2018) can promote the activity and stability of Ni-CeZr formulations, in particular by stabilizing Ni dispersion, reducing carbon deposits and increasing the amount of basic sites.

Different aspects should be taken into account if looking for the optimum ceria-zirconia composition, which seems to depend upon several factors. For example the role of surface area is not univocal comparing various Ce/Zr molar or mass ratios, and this is likely due to different preparation methods, experimental conditions, Ni loading etc. For some authors the best results are actually obtained on samples with the highest surface area (Cai et al., 2013; Zhu et al., 2013), while in other studies this is not the case. The ratio between Ce and Zr has been found to influence the amount and distribution of Ni²⁺ and Ni⁰ species, the best composition being thus the one that guarantees the optimum of these active centers (Ocampo et al., 2011). Ce/Zr ratio has been reported to affect also metal dispersion and the amount and strength of basic sites (Nizio et al., 2016). Regarding the mechanism of CO₂ hydrogenation to methane on ceria-zirconia based catalysts, the carbonate/formate route seems confirmed by in situ DRIFT experiments, which also exclude the formation of CO as a reaction intermediate (Aldana et al., 2013; Pan Q. et al., 2014; Ashok et al., 2017).

Performances of the catalysts above discussed are summarized in Table 1.

TABLE 1

Table 1. Survey of CO₂ methanation ceria based catalysts considered in this review.

CO₂ Hydrogenation to Value Added Chemicals Other than Methane

The products of CO₂ hydrogenation different from methane are usually divided into three main groups, depending on the reaction pathway, i.e., methanol synthesis, reverse water gas shift (RWGS) and CO₂ Fischer-Tropsch (CO₂-FT), the latter two being intimately linked with each other (Porosoff et al., 2016). The fundamental properties of ceria and ceria-zirconia for CO₂ methanation play a crucial role also in these CO₂ hydrogenation reactions, for which the degree of CO₂ reduction by hydrogen, beside other factors such as temperature and H₂/CO₂ ratio, is generally controlled by the nature of the metal active phase. Pt/CeO₂ for example is highly selective toward CO with respect to methane as well as Cu/CeO₂, whereas Co and Ni-based catalysts are selective toward methane (Porosoff and Chen, 2013; Dai et al., 2017).

Methanol Synthesis

M-CeO₂ Catalysts

Metal-ceria interaction, and particularly metal-ceria interface, is found to be a key parameter for the hydrogenation of CO₂ to methanol (Rodriguez et al., 2015; Kattel et al., 2017). This reaction is widely investigated as methanol is a valuable raw material and an intermediate for the synthesis of other chemicals (Alvarez et al., 2017). Recent studies on inverse ceria-copper catalysts reveal the importance of the superficial interaction between the two components (Graciani et al., 2014; Senanayake et al., 2016; Rodriguez et al., 2017). Inverse oxide/metal configurations are regarded in general as more active than traditional metal/oxide systems and can provide stronger bonding at the interface due to perturbations of the electronic properties of the oxide. This is indeed the case of CeO_x/Cu(111), whose superior activity for methanol production is attributed to the abundance of Ce³⁺ sites that can stabilize ${\text{CO}}_2^{\text{δ}-}$ intermediates. The synergistic effect between the metal and CeO₂ has been reported also on conventional systems in which the metal is deposited onto the ceria surface, and again the enhanced activity for CO₂ hydrogenation has been attributed to the increased reduction of ceria promoted by metal-support interaction and the subsequent formation of oxygen vacancies (Tsubaki and Fujimoto, 2003; Choi et al., 2017; Vourros et al., 2017; Malik et al., 2018). The relevance of this interaction is nicely demonstrated by Vourros et al., who compares the activity of gold nanoparticles supported on different oxides. From this work it appears clearly that when Au is deposited on ceria the activity for CO₂ hydrogenation to methanol depends almost uniquely on the metal-support interplay, ceria being inert for the reaction as well as gold supported on alumina (Vourros et al., 2017). Also, in the earlier paper of Tsubaki and Fujimoto it is reported that depending on the degree of sample reduction (at low or high temperature), the hydrogenation of carbon dioxide is selective toward methane (T_red = 200–400°C) or methanol (T_red = 500–550°C) on Pd/CeO₂ catalyst. This is attributed to a weaker or stronger bonding of CO on catalyst surface, which in turn depends on the reciprocal arrangement of Pd and ceria, that leads to CH₄ (in the case of low temperature reduction) or to CH_xO intermediates (for high temperature reduction), respectively (Tsubaki and Fujimoto, 2003). The synergy between metal and support can be tailored also by choosing opportune ceria facets, as demonstrated by carrying out CO₂ hydrogenation on copper supported on ceria with different morphologies (Ouyang et al., 2017). In this case it was found that the best catalytic activity is given by Cu on ceria nanorods exposing the (100) and (110) faces, which guarantee the strongest Cu-CeO₂ interaction.

CeO₂ as Promoter

Ceria has been successfully applied also as a promoter to conventional Cu/Zn/Al and other oxide based catalysts for methanol synthesis from CO₂ and H₂ (Richard and Fan, 2018). In particular, it is reported that for Cu-based catalysts the addition of ceria can increase the number of basic sites and the dispersion of the supported metal (Gao et al., 2013; Zhan et al., 2014; Shi et al., 2018), and can change the electronic environment of copper promoting the metal-ceria interaction (Wang et al., 2002; Bonura et al., 2011; Ban et al., 2014).

Mechanism of Reaction

The mechanism of CO₂ hydrogenation to methanol described in the literature involves the formation of carboxylate species and CH_xO intermediates excluding a role of formates, due to their too high stability (Graciani et al., 2014; Rodriguez et al., 2015). Formates, which were instead the main intermediates for CO₂ methanation (see section CO₂ Methanation Reaction), are indeed observed also in this case but they are identified as spectators (Senanayake et al., 2016). This mechanism and relative observations are in agreement with the theoretical work by Kumari et al. who investigated CO₂ hydrogenation on CeO₂(110) surface and reported a tight bond of formate intermediates on ceria, thus making their participation in the reaction unlikely (Kumari et al., 2015). On the other side, a recent experimental paper by Malik et al. describe the formate route as the most probable and their results agree with the microkinetic analysis performed by Cheng and Lo again on CeO₂(110) surface (Cheng and Lo, 2016). It is not easy to understand the reasons of these apparent contradictory results. For example Cheng and Lo suggest that at moderately high H₂/CO₂ ratio the formate route is favorable, so one might argue that the value of 9 for H₂/CO₂ ratio used in the work by Graciani et al. is too high, or that the different catalyst configuration (inverse CeO₂/Cu catalyst for Graciani, conventional PdZn/CeO₂ for Malik) makes the difference. An interesting explanation, which could account in general for the discrepancies reported in the literature for CO₂ hydrogenation routes and intermediates formed on ceria surfaces, is that inferred from the theoretical work by Cheng et al. It is observed that depending on the type of vacancy (in site or split) the binding of CO₂ on ceria surface is different (Figure 2). This leads to different paths of CO₂ activation (Cheng et al., 2013). Whichever the explanation, theory and experiments agree in highlighting the role of the reduced ceria surface, similarly to what reported for CO₂ methanation, with oxygen vacancies responsible of charge redistribution and consequent CO₂ activation.

FIGURE 2

Figure 2. Two CO₂ adsorption configurations on reduced ceria (110) with in-plane (A) vacancy [Rv(InP)] and (B) split vacancy (Rp5). The surface oxygen nearest the vacancy is labeled as O_v. Both structural parameters and energies of adsorption are depicted (from Cheng et al., 2013, reproduced with permission of AIP Publishing).

Reverse Water Gas Shift Reaction

The reduction of CO₂ to CO by the reverse water gas shift (2) is another fundamental reaction for the production of valuable chemicals, for example as the first step of the Fischer-Tropsch synthesis (Wang et al., 2011; Centi et al., 2013; Daza and Kuhn, 2016; Yang et al., 2018).

$\begin{array}{cc}{\text{CO}}_{\text{2}}\text{+}{\text{H}}_{\text{2}}\leftrightarrow \text{CO}\text{+}{\text{H}}_{\text{2}}\text{O}(\Delta {\text{H}}_{\text{298K}}=\text{41}.\text{2}\text{KJ/mol})& (2)\end{array}$

From a thermodynamics point of view, the reverse water gas shift (RWGS) is an equilibrium limited endothermic reaction favored at high temperature. It is a very promising route for the valorization of CO₂ because of the technical feasibility and readiness of the process. Several authors investigated this reaction, but there are comparatively few studies specifically devoted to RWGS on ceria-based materials, whereas much more work involves it indirectly because it takes place to some extent in any process where CO₂ and H₂ are present in the reaction mixture (Wang et al., 2011). As a matter of fact though, many specific papers regarding the RWGS on ceria-based catalysts have been published very recently demonstrating the increasing interest toward this topic.

M-CeO₂ and CeO₂ Based Catalysts

Most of the materials investigated contain noble (Pt, Ru) or transition metals (Ni, Cu, Co, Fe) as the active phase, but also pure (Kovacevic et al., 2016; Liu Y. et al., 2016) or doped ceria (Lin et al., 2015) has been reported to be active for the RWGS. Moreover, the addition of CeO₂ as a dopant promotes the RWGS activity of other oxides such as Ga₂O₃ (Zhao et al., 2012) and In₂O₃ (Wang W. et al., 2016) and Zn-doped ceria (Lin et al., 2015). The activity has been ascribed to the abundance of vacancies which can favor the adsorption and the activation of CO₂. Nevertheless the work by Kovacevic et al. suggests that there are other factors that should be considered, as for example the lattice microstrain and/or the intrinsic reactivity of different ceria facets. Any correlation of catalytic activity with the number of oxygen vacancies nor with the sample reducibility has been observed (Kovacevic et al., 2016). An indication toward the structure sensitivity of the reverse water gas shift on ceria comes from the work by Lin et al. who investigate the reactivity of copper supported on ceria nanorods and nanospheres (Lin et al., 2018). The authors explain the higher activity of Cu/CeO₂ nanorods with an enhanced CO₂ dissociative adsorption on CeO₂(110) terminations which leads to the preferential formation of active bidentate carbonates and formates intermediates. In the paper by Kovacevic et al. the most reactive plane appears to be the (100) of ceria nanocubes [but they do not consider samples exposing (110) facets], so in this respect a more comprehensive study would be desirable in order to discriminate clearly the reactivity of different ceria planes for the RWGS reaction, in presence or in absence of a supported metal.

The metal-support interaction (Panaritis et al., 2018; Ronda-Lloret et al., 2018; Wang and Liu, 2018) as well as the effect of ceria in the dispersion of the active phase (Wang et al., 2013; Lu and Kawamoto, 2014; Wang L. et al., 2017; Sun et al., 2019) have a strong effect on the activity for the RWGS reaction. The role of ceria in dispersing the active phase seems particularly relevant in determining the selectivity toward CO. Different authors in fact report that large metal particles are in general selective toward methane, whereas highly dispersed nanoparticles favor the RWGS over methanation (Lu and Kawamoto, 2014; Wang L. et al., 2017; Aitbekova et al., 2018). The interesting paper by Aitbekova et al. nicely demonstrates how the selectivity toward CO with respect to methane can be tuned by a low temperature restructuring of the catalyst. In this case Ru/CeO₂, gives rise to single-site RuO_x species in strong interaction with ceria. The same effect is only partially observed for Ru/Al₂O₃ and Ru/TiO₂, indicating a key role of ceria in the re-dispersion of ruthenium. This aspect is very important and should be considered in future work in light of tuning the CO₂ hydrogenation selectivity of ceria-based catalysts. The selectivity is indeed a key issue: it depends on the reaction conditions and on the nature of the metal active phase, but it has been shown that also ceria surface plays a great role in this respect, being able to activate different reaction pathways for CO₂ leading to different products (Cheng et al., 2013; Lu et al., 2015).

Mechanism of Reaction

The proposed reaction mechanisms for the reverse water gas shift over ceria-based materials usually involve the adsorption and dissociation of CO₂ on defective ceria surface followed by the formation of surface carbonate and formate species (Goguet et al., 2004; Lin et al., 2018). Surface carbonates are indicated as reaction intermediates, whereas formates are supposed to be “minor intermediates” due to their stronger bond and slower exchange rate observed in transient isotopic experiments (Goguet et al., 2004; Jacobs and Davis, 2005). However, in the recent study by Lin et al. the reported rate of decomposition of bidentate carbonates and bidentate formates is similar (Lin et al., 2018). The redox step, i.e., the formation of surface oxygen vacancies on ceria by hydrogen in presence of a metal, is necessary to initiate the reaction (particularly to activate CO₂). This does not imply a redox mechanism for the RWGS (Wang L. C. et al., 2015; Chen et al., 2016), which is conversely supposed to follow an associative pathway (Goguet et al., 2006). All these studies, highlight that the reaction conditions adopted can affect significantly the mechanism and the reader should be aware of this when considering the number of possible pathways proposed in the literature.

Fischer-Tropsch Reaction

Ceria as Promoter

The direct hydrogenation of CO₂ to hydrocarbons, known also as CO₂-FT, has been addressed only recently as a way for carbon dioxide upgrading. An ideal catalyst for this process should be active for both RWGS and FT synthesis, thus making its design quite complicated (Porosoff et al., 2016; Guo et al., 2018; Li and van Veen, 2018). To overcome this issue, the approach is that of designing bifunctional catalysts that couple both RWGS and FT functionalities in a single material, and a few attempts have been made also with ceria-containing formulations (Dorner et al., 2011; Samanta et al., 2017; Xie C. et al., 2017). Dorner et al. observed that the addition of ceria to a Fe/Mn/K-alumina catalyst significantly improved performances for the hydrogenation of CO₂ to C₂-C₅ olefins, due to ceria promotion of the RWGS reaction. A similar approach has been described by Samanta et al. who added 5% Ce on a K/Fe-Al-O spinel observing an increase in selectivity for methane and light C₂-C₄ with respect to the undoped catalyst (Samanta et al., 2017). Xie et al. instead tested successfully a composite material constituted by a Pt/CeO₂ core (RWGS functionality) surrounded by a Co-mesoporous silica shell (FT functionality) (Xie C. et al., 2017).

M-CeO₂ Catalysts

Interestingly, also pure ceria has demonstrated some potentialities as a good support for direct CO₂-FT, depending on its morphology. On Fe/CeO₂ systems it has been reported in fact a correlation between catalytic activity and ceria morphology (Torrente-Murciano et al., 2016). The different reducibility of ceria nanoparticles, nanocubes and nanorods has been shown to change the degree of CO₂ conversion, as well as the selectivity toward higher hydrocarbons with respect to methane and the olefin to paraffin ratio obtained. This last effect is attributed to the capability of saturating the hydrocarbon chain, higher for the more reducible support (i.e., ceria nanorods) on which paraffin's production is favored. Also the strength of CO₂ bonding on ceria has been demonstrated to affect the selectivity of ceria-containing catalysts (Samanta et al., 2017).

Summary and Perspective for CO₂ Hydrogenation Catalysts Based on Ceria

Tables 2A,B summarize and provide details regarding the catalysts considered above.

TABLE 2A

Table 2A. Survey of Catalysts for CO₂ hydrogenation to methanol considered in this review.

TABLE 2B

Table 2B. Survey of Catalysts investigated for the reverse water gas shift reaction (rWGS) considered in this review.

To conclude, among the several studies regarding CO₂ hydrogenation over ceria-based catalysts two main general issues can be identified for future tailoring and improvement of these materials. The first one is mainly related to the interaction between CeO₂ and the supported metal, and different strategies can be found in both experimental and theoretical works to enhance the metal-ceria interplay. The second issue involves the tuning of ceria surface acid/base and redox properties, which have been found to influence strongly the pathway for CO₂ activation (Lu et al., 2015).

In this respect, an interesting and very recent approach is suggested by the work of Huang and coworkers who have demonstrated the possibility of creating series of solid frustrated Lewis pair (FLPs) sites on the surface of ceria (Zhang et al., 2017; Huang et al., 2018). FLPs are constituted by Lewis acids and bases which are sterically prevented from interacting with each other (thus called “frustrated”). The concept has been firstly proposed for homogeneous hydrogenation reactions (Stephan, 2009), and has been then successfully transferred to heterogeneous catalysts for CO₂ hydrogenation (Ghuman et al., 2015, 2016). Thanks to their unique configuration, these sites can dissociate hydrogen to produce a proton site in proximity to a hydride site that together constitute a very reactive environment for CO₂ activation. In the case of ceria, FLPs are generated by the abundance of surface defects which can be used to prevent the formation of classical adjunct Lewis acid-base couples as shown in Figure 3.

FIGURE 3

Figure 3. Schematic of solid FLPs on CeO₂(110) and CeO₂(100) constructed by surface oxygen vacancy regulation. White and red balls represent Ce and O atoms, respectively. Atoms labeled by blue circles represent the Lewis acid (Ce) or Lewis base (O) of solid FLPs. The position of oxygen vacancy is labeled by V_O in blue (Huang et al., 2018, Reprinted with permission from American Chemical Society).

This peculiar surface configuration of CeO₂ has already been proven to be very active for the hydrogenation of alkenes and alkynes (Zhang et al., 2017) and can represent a very promising step forward for the exploitation and improvement of ceria-based materials for the valorization of CO₂ through hydrogenation reactions.

CO₂ Reforming of Methane

Another process for the valorization of CO₂ is its use as oxidizing agent in the process of reforming of methane (methane dry reforming, MDR). This process involves the utilization of methane and carbon dioxide, which are greenhouse gases, to produce syngas (CO and H₂) as building block for the production of liquid fuels and chemicals (Lavoie, 2014). Since it consumes CO₂, MDR represents an highly efficient way to reduce the carbon footprint of the world's growing consumption of methane (associated with the exploitation of natural gas) in comparison to other reforming processes.

The overall reaction (Equation 3)

$\begin{array}{cc}{\text{CH}}_{\text{4}}\text{+}{\text{CO}}_{\text{2}}=\text{2CO}\text{+}{\text{2H}}_{\text{2}}(\Delta {\text{H}}_{\text{298K}}=\text{247kJ/mol})& (3)\end{array}$

is thermodynamically unfavorable since implies the activation of two very stable molecules and requires temperatures higher than 1,000°C to obtain significant conversion in stoichiometric conditions (Nikoo and Amin, 2011), while a CO₂/CH₄ ratio higher than 3 would be necessary to have good conversion at lower temperature (750°C) (Li et al., 2008; Nikoo and Amin, 2011).

Actually, the MDR is a complex process that implies several equilibria depending on the operating temperature and can lead to the formation of dimethylether, methanol, alkanes and alkenes and carbon as side products. In the range of 650–1,000°C the main side reaction is the RWGS (reaction a) (Lavoie, 2014) along with a series of reactions (reactions b-e) that in stoichiometric conditions lead expectedly to the formation of carbon.

a) CO₂ + H₂ ↔ CO + H₂O              (ΔH_298K = 41 kJ/mol)

b) CH₄ ↔C + 2H₂                            (ΔH_298K = 74.9 kJ/mol)

c) 2CO ↔CO₂ + C                           (ΔH_298K = −172 kJ/mol)

d) CO₂ + 2H₂ ↔ C + 2H₂O             (ΔH_298K = −90 kJ/mol)

e) CO + H₂↔C + H₂O                     (ΔH_298K = −131 kJ/mol)

Several transition metals (Ni, Ru, Rh, Pd, Ir, Pt, Co) supported on various supports have been investigated to catalyze the conversion of both CO₂ and CH₄ at intermediate temperatures (500–800°C), with Rh, Pt, and Ru (Pakhare and Spivey, 2014) showing high activity, thermal stability and a remarkable resistance to the carbon deposition. Despite the optimal properties of noble metals in this process, nickel would be the metal selected for an industrial development of the process because it is easily available, cheap and likewise active (Lavoie, 2014; Bian et al., 2017). However, nickel is prone to be deactivated by carbon deposits since it catalyzes the cracking process of methane while having a poor activity for the dissociation of CO₂; moreover it can easily sinter at the MRD operating temperature. Different approaches have been followed to tackle these challenges (Li and Gong, 2014) such as alloying/doping Ni with other metals (Cu, Co, Pt, Pd, Sn, Na, K, Ca), or confining/embedding it in well-defined environments (cavities, channels, core-shell) in appropriate supports (Bian et al., 2017). Ni has been dispersed on several supports like Al₂O₃, ZrO₂, TiO₂, MgO, MgAlO, SiO₂, and CeO₂, or Ce_xM_1−xO₂, (M = Zr, Pr, Gd) etc. (Usman et al., 2015).

Table 3 summarizes the most recent studies on dry reforming catalysts based on CeO₂ or on its parent oxides.

TABLE 3

Table 3. Survey of MDR Catalysts investigated from 2016–2018 organized according the use of CeO₂ as support, promoter or component of a solid solution.

CeO₂ as Catalyst

The activity of CeO₂ alone (BET SA: 23 m²/g) in the dry reforming process was investigated by Laosiripojana and Assbumrungrat (2005). Results were benchmarked with those of a typical Ni/Al₂O₃ catalyst._. Despite a relative low conversion (32% for CH₄ at 900°C) ceria proved to be a catalyst much more stable, showing a deactivation of 7% over time in comparison to that underwent by Ni/Al₂O₃ (96%). In this study, which is one of the few that has investigated the dry reforming activity of purer ceria (Otsuka et al., 1997), it is also pointed out that the main drawback of ceria is its basic nature that would favor the adsorption and hydrogenation of CO₂ at disadvantage of methane activation.

Ni-CeO₂ Catalysts

From Table 3 it is clear that in the dry reforming process ceria has been used as support or promoter; the metal component can be a noble metal but very often Ni, a Ni alloy or Co. Therefore, it is evident that CeO₂ has a crucial role in the development of durable nickel dry reforming catalysts operating at intermediate temperature. CeO₂ strongly interacts with Ni and recently experimental and DFT calculation demonstrated that the strong metal-support interaction between Ni and CeO₂ can activate and modify the electronic and chemical properties of the metal allowing the activation of methane even at room temperature (Liu Z. et al., 2016). Ambient-pressure X-ray Photoelectron Spectroscopy (XPS) analysis and Scanning Tunneling Microscopy, (STM) characterization of NiO supported on CeO₂(111) substrate revealed that when Ni atoms or small clusters are in tight contact with ceria the methane can be activated at room temperature and the dry reforming reaction become possible at a much lower temperature than that typically reported for conventional Ni based catalysts (427° C). In this case the active phase contained small particles of metallic Ni dispersed on partially reduced ceria, and the strong metal-support interaction caused large electronic perturbations responsible of a 80% lower activation barrier for the C-H bond with respect to that of Ni (111) surface (Figure 4).

FIGURE 4

Figure 4. Reaction energy profile for the CH₄ → CH₃ + H reaction on isolated Ni atoms and Ni₄ clusters on the CeO₂(111) (A) and Ce₂O₃(0001) surfaces (B), in comparison to Ni(111). The structures shown to the left and right of the reaction pathways correspond to the side views of the optimized molecularly adsorbed and dissociated states used in the search of the transition state structure. All energies are relative to CH₄ in the gas phase. Reproduced from Lustemberg et al. (2016), with permission of ACS publications.

Ni-CeO₂: Mechanism of Reaction

Ni and O atoms work in cooperative way to dissociate CH₄ molecules and once the first C-H bond of methane has been broken the sequential decomposition of the other CH_x intermediates into C is hypothesized to be very fast. C reacts with O present on the surface of catalyst and the resulting oxygen vacancies on the support enhance the ability of the system to adsorb and dissociate CO₂. Figure 5 shows a cartoon with the mechanism of reactions.

FIGURE 5

Figure 5. In presence of ceria the kinetics follows a Mars-van Krevelen mechanism, where active carbon is oxidized by CeO₂, while oxygen vacancies are replenished by O from CO₂ dissociation; the carbon fibers growth is hindered by CeO₂, which provides extra oxygen for their gasification. Adapted from Liang et al. (2018) with permission of ACS publications.

This type of mechanism, which involves separate steps for the activation of methane on the metal (the rate determining step) and for the activation of CO₂ on the support and at the interfacial sites, was suggested to be operative also in other ceria based systems (Bobin et al., 2013; Makri et al., 2015; Simonov et al., 2017).

In such systems the kinetics balance between the two steps was demonstrated to be an effective method to contrast the catalyst deactivation due to the growth of graphitic carbon filaments. Thanks to their oxygen exchange properties ceria based supports may easily provide extra oxygen incrementing the gasification rate of carbonaceous deposits.

Ni-CeO₂ Catalysts: Design Strategies

In order to facilitate the occurrence of a support- mediated redox bi-functional mechanism for MDR a winning strategy is to improve both the dispersion of Ni and the oxygen storage capability of the support by increasing the concentration and mobility of oxygen vacancies on its surface. Figure 6 summarizes some of the strategies described below.

FIGURE 6

Figure 6. Strategies to stabilize and activate Ni/CeO₂ catalysts.

Deng et al. demonstrated that this can be obtained by tuning simultaneously the compositions and the morphology of the support (Deng et al., 2016). An outstanding improvement in the catalytic performance and durability of Ni nanoparticles was observed when Ni was dispersed on a solid solution of Ce_xNi_1−xO_2−δ with a well-defined architecture.

In this system the presence of defects favors the reducibility and dispersion of Ni improving its dry-reforming activity, while the mesostructure in which Ni particles are confined works synergistically to boost the metal/support interaction. This study is a good example of the potentiality and versatility of fluorite-type ceria structure for engineering powerful MDR catalysts.

The importance of a confinement of Ni particles and of a redox bifunctional mechanism in enhancing the stability of Ni dry reforming catalysts has been also highlighted in the recent study of Das et al. (2018). In this case Ni particles are maintained well-dispersed by their encapsulation into a layer of SiO₂, with CeO₂ forming a sandwiched core-shell structure Ni-SiO₂@CeO₂. This configuration induces a change in the reaction mechanism from a mono functional pathway on the metal to a bifunctional route in which ceria has an active role in the activation of CO₂ and in the removal of coke. The interaction between the SiO₂ and CeO₂ layers is pivotal for an enhanced decoking action of cerium as it contributes to an increase in the number of defects (Ce³⁺, oxygen vacancies) and thus in a greater availability of mobile oxygen on the surface of the cerium layer. The importance of optimizing the nature of CeO₂/SiO₂ interface has been pointed out in other reports, and the strategies adoptable for the purpose can be different due to the versatility in manufacturing SiO₂ based nanostructured substrates (Taufiq-Yap et al., 2013; Zhao et al., 2016). It is interesting to observe that Zhao et al. obtained outstanding methane conversion of 90% at 750°C for a NiCe@m-SiO₂ yolk-shell configuration where a SiO₂ shell contains NiO/CeO₂ particles. The catalyst showed similar characteristics to those of the sandwiched configuration with well confined Ni particles and the presence of CeO₂/SiO₂ interfaces with a high oxygen mobility. We could assume that in both configurations there is a synergic action among the three components and the confinement of Ni has a key role in influencing the properties of the mutual interfaces.

Considering the several studies published on Ni-Ce systems, it is possible to conclude that the redox properties of CeO₂ has two mutually dependent beneficial effects. The easy reducibility of CeO₂ promotes the reduction of nickel phases through a spillover mechanism. Additionally, the oxygen vacancies created in the ceria lattice are able to stabilize the supported metal particles; this builds a synergic system where the oxygen exchange properties of CeO₂ are involved in a complex series of pathways to produce CO and H₂ and inhibiting coke formation.

Other M-CeO₂ Catalysts

A similar synergism has been shown also in Co-Ce and Pd-Ce dry reforming catalysts (Singha et al., 2017; Zhang et al., 2018). In these systems the metal-support interaction is even stronger activating the dry reforming of methane already at 520 and 350°C, respectively. In all these catalysts the formation of a specific metal-ceria interface has a key role in decreasing the oxygen vacancy formation energy by up to a few eVs and in changing the electronic state of metal clusters (Liu et al., 2017; Ruiz Puigdollers et al., 2017).

Taking into account the crucial role of interface sites in improving catalytic activity and stability of ceria supported catalysts, several approaches have been followed to maximize their number and optimize their configurations. The properties of the metal-ceria interfaces can be tuned through thermal and redox treatments and by selecting synthesis methods aimed at reducing the size of crystallites in both the support and the metal. Another factor to be considered is the choice of the appropriate metal loading (Djinović et al., 2015). As a rule of thumb to avoid sintering phenomena and to maximize dispersion the metal loading should be in the range of 3–10% and the temperature of catalysts calcination below 500°C (Aw et al., 2014).

Low temperatures of calcination limit the sintering process especially in the case of the use of Co, probably because of the low melting point of its precursor (Co₃O₄, m.p., 895°C). It was reported that Co/CeO₂ catalysts prepared via impregnation showed a 18% drop in the hydrogen yield if calcined at 600°C instead of 500°C (Abasaeed et al., 2015).

M-Nanostructured Ceria Catalysts

Recently a plasma treatment of CeO₂ powder before of and after its impregnation with Ni precursors has been adopted instead of a more conventional thermal treatment (Odedairo et al., 2013). The unusual treatment led to obtain (i) a clean metal–support interface, (ii) the exposure of specific surface crystallographic planes-[(111) and (100)]-for ceria, (iii) Ni clusters of 10–30 nm well-dispersed on the support surface. All these characteristics resulted in a more active and stable catalyst and would suggest that the use of nanostructured ceria support (cube, rods) may have a positive role in the dry reforming process. The study of Wang N. et al. (2016) confirms this hypothesis for Ni/CeO₂ catalysts. Nanostructured catalysts showed the following order of reactivity Ni/Ce-nanorods>Ni/Ce-nanoctas>Ni/Ce-nanocubes>Ni/Ce-nanoparticles when tested in methane dry reforming reaction in the range of 550–750°C. The higher activity and carbon resistance of catalysts supported over CeO₂ nanorods has been attributed to the incorporation of Ni into the ceria in a distinct configuration different from those of the other nanostructures. Ni resulted strongly anchored to the Ce-nanorods with a site geometry and coordination environment that favor the mobility of oxygen and the catalytic activity. Despite these encouraging results, the use of nanostructured ceria in MDR reaction would be limited to temperature up 700–750°C, because of their low thermal stability.

Redox and/or thermal pre-treatments can induce morphological and structural changes in the interface, strengthening the metal-support interaction or inducing inhibitory processes such as partial encapsulation of metal particles by means of the ceria support. A strong bonding between Ni and CeO₂ that inhibited Ni particle sintering was obtained via a pre-reduction of Ni/CeO₂ in H₂ in the temperature range of 500–700°C, while higher temperatures of reduction (≥600°C) induced decoration/encapsulation of Ni nanoparticles by a thin layer of reduced ceria support with partial coverage of Ni surface. This modification decreased catalytic activity of Ni, nevertheless it improved its resistance to coking (Li and van Veen, 2018).

Syntheses via co-precipitation or via sol gel generally result in more active and stable catalysts with respect to those obtained via impregnation, since these approaches permit to achieve a greater Ni-ceria interaction in the final system.

Ceria as Promoter

The method of synthesis and the ratio among the components become important when CeO₂ is used as promoter or modifier, as in Ni/CeO₂/Al₂O₃ catalysts. When added to Al₂O₃, CeO₂ has beneficial impact in the dispersion of Ni and in avoiding the formation of undesired Ni Aluminate phases. Moreover, it leads to an improvement in the durability of the catalyst generally proportional to the ceria concentration (Chen et al., 2013). With regard to the impact on the activity and selectivity, it is crucial to optimize the composition in order to maximize the surface area of the metal and the interfacial surface between CeO₂ and Ni (Damyanova et al., 2018).

The observation that ceria can change the properties of the supports and influence their interaction with NiO having a beneficial effect on the endurance of the catalysts has been reported for other systems based on MgO (Fang et al., 2018), ZrO₂, (Kumar et al., 2008), SiO₂, (Taufiq-Yap et al., 2013), and hydrotalcite (Debek et al., 2015). Despite the general improvement on the longevity, the effect of ceria addition on the activity and selectivity of these catalysts depends on the type of the support and can be also slightly negative. Considering the literature, it is clear that in multicomponent-catalysts the optimal composition is one in which the surface area of the metal, the basicity of the carrier oxide and the availability of surface oxygen vacancies are balanced to close the catalytic cycles involved in the dry reforming process.

M-Doped CeO₂ Catalysts

The same perspective of optimizing a winning composition for the process has driven the studies on supports based on ceria doped with zirconium or with rare earths elements (Gd, Sm, Pr) (Makri et al., 2015; Vasiliades et al., 2016; Wolfbeisser et al., 2016; Gurav et al., 2017; Wang F. et al., 2017).

The use of ceria-zirconia mixed oxide in the development of Ni catalysts generally leads to an improvement in the catalyst activity and selectivity; however the impact depends on the composition and on the synthesis methods, and about these aspects there is no always agreement in the literature. The controversial results sometimes reported for similar compositions are mainly related to the different approaches adopted for their synthesis. It was highlighted for example that the addition of surfactants, which are used to increase the mesoporosity and surface area of Ni/Ce_xZr_1−xO₂, can be beneficial or not, depending on the selected composition and on the type and amount of surfactant. A large amount of surfactant leads generally to an irreversible encapsulation of Ni during thermal/redox treatments (Wolfbeisser et al., 2016; Pappacena et al., 2018). Although the preparation method is an important way to develop the properties of these substrates, it should not be overlooked that the operating conditions, thermal and redox treatments often induce nanostructural and compositional changes in these oxides, which lead to materials with different surface properties and compositions from those expected. For example, Djinovic et al. demonstrated that the activity of NiCo catalysts supported by Ce_0.8Zr_0.2O₂ was changing over time showing a self-activation due to the completion of the Ni particle reduction and the recrystallization of the support from a cubic to a more polyhedral shape of crystallites (Djinović et al., 2014). Therefore, in order to identify the most promising support composition for the process, efforts must be directed primarily to the understanding and control of the surface transformations of these systems under operating conditions.

The performance improvement of these materials has been correlated with the enhancement of both their OSC and their thermal resistance induced by the doping. The high thermal resistance of ceria-rich ceria-zirconia solid solutions allows a limited growth of their crystallites during thermal treatments, that in turn hinders the aggregation of Ni particles favoring metal dispersion (Kambolis et al., 2010).

Very recently, by using transient isotopic studies, a Mars-van Krevelen mechanism has been proposed to correlate the redox behavior of ceria doped support with the ability to get rid of the carbon accumulated on the metal during the dry reforming reaction. In this mechanism the support provides a pool of surface and subsurface oxygen able to remove the carbon species formed both via methane cracking and via Boudouard reaction. It has also been noted that the coke resistance of Ni catalysts on these supports is not clearly correlated with their bulk OSC properties (Makri et al., 2015). It is instead more related to their surface reducibility and to the oxygen mobility to the Ni interfacial sites. According to the literature, the advantages in the durability of MRD Ni based catalysts supported on Ce-Zr oxides are associated to ceria molar contents higher than 50%, and they are normally attributed to the crystalline cubic structure characteristic of these cerium-rich compositions (Kumar et al., 2007, 2008; Zeng et al., 2013; Nahar and Dupont, 2014; Djinović et al., 2015; Muñoz et al., 2017).

Another aspect to be considered is that the insertion of zirconia into the ceria lattice affects its basic properties. CO₂-TPD studies on Ni/CeZr catalysts proved that the addition of zirconium increments the number of basic sites of medium and weak strength that are crucial to enhance the conversion of methane and to favor the adsorption/activation of CO₂ (Zeng et al., 2013; Pappacena et al., 2018). Conversely, the insertion of rare earth elements would increase the number of strong basic sites. The presence of these type of sites has been correlated with the accumulation of carbonates, that were proved to work as spectators in the ceria-zirconia solid solutions and as intermediates in rare earth doped ceria supports (Makri et al., 2015). However, the role of carbonates is still to be well elucidated in these materials. Taking into account that zirconium decreases the basicity of ceria, while rare-earth elements increase it, one can hypothesize that a correct balance between acidic and basic sites into this oxide can be achieved by a co-doping approach. Recently we have demonstrated that the co-doping of ceria with zirconium and neodymium enhanced the activity and selectivity of Ni catalysts in comparison to those singly doped (see Figure 7; Pappacena et al., 2018).

FIGURE 7

Figure 7. Methane dry reforming activity of Ni catalysts prepared by wet impregnation of supports of CeO₂, CeO₂ doped with Nd or Zr and of CeO₂ co-doped with Zr and Nd. (GHSW = 8,000 h⁻¹, CH₄/CO = 1.5). It was possible to obtain an improvement of ceria MDR activity only by co-doping, which affects both redox and acic-basic properties of support. Adapted from Pappacena et al. (2018), “Open Access” and licensed by the respective authors in accordance with the Creative Commons Attribution (CC-BY) license.

Bobrova et al. reported high performance for a Ni+Pt catalyst supported on a ceria zirconia composition co-doped with Pr and Sm (Bobrova et al., 2016). All these multicomponent systems gave H₂/CO ratio close to 1, thus suggesting that playing with the compositions of metal phase and/or of the support can be a valid strategy to limit the activity of ceria toward the Reverse Water Gas Shift reaction (RWGS, CO₂ + H₂↔CO + H₂O), which is the main issue to be addressed when ceria enters in the formulations of catalysts for the methane dry reforming process.

Conclusions

In the framework of the development of a carbon free footprint circular economy based on the valorization of CO₂ we have reviewed the role of ceria in the development of catalysts for processes of growing relevance such as the dry reforming of methane and CO₂ hydrogenation to CH₄, CO and methanol. The engineering of these catalysts formulations is aimed at improving the synergic interaction between the different components (metal, support, and promoters) in order to maximize yield and selectivity (see Scheme 1).

SCHEME 1

Scheme 1. Summary of concepts reviewed in this article.

We have shown that cerium dioxide and ceria-based materials can effectively contribute to enhance the catalytic activity through the following actions:

- by increasing the number of active sites and their activity

CeO₂ reducibility contributes to establish a strong metal-support interaction which promotes the mutual reducibility of the metal and the support through a spillover mechanism of H₂. The presence of surface defects (Ce³⁺ and oxygen vacancies) allows a good anchoring of metal particles on ceria support, thus leading to a higher metal dispersion. This results in a greater number of active sites (especially in case of non-noble transition metals such as Ni, Co, Cu), which for CO₂ reforming processes are mainly located at the metal-support interface.

- by enhancing the selectivity and durability of catalysts

Metal nanoparticles and a strong metal-support interaction are the basis of electronic perturbations at the metal surface and of spillover mechanisms that drive the selectivity of processes as well as the durability of the catalyst against inhibitory reactions, such as the formation of coke. Moreover, a strong metal-support interaction may inhibit sintering processes.

-by introducing different functionalities

The surface of nanostructured cerium oxide is characterized, in particular in reducing atmosphere, by the presence of oxygen vacancies V₀ and reduced cations Ce³⁺ that, in addition to being active sites for the activation of CO₂ in the processes, can act as acid-base pairs in the hydrogenation reactions.

-by offering versatility of approaches in designing and engineering appropriate interfaces

The morphological and structural characteristics as well as acidity, basicity, redox centers of ceria and ceria based oxide depends on the method of synthesis and on the extent of doping. Moreover, these supports are highly sensible to the type of environment. This expands the possibility of optimizing surface and interface properties of catalysts. However, more in-depth studies on the behavior and the evolving of these systems under reaction conditions are needed. A better understanding of structural and compositional changes, and of the corresponding redox properties undergone by systems under operating conditions would allow the creation of intelligent interfaces capable of exploiting the chemical-physical properties of cerium-based support for, in situ, functional rearrangements or rejuvenation processes.

Incidentally, this work summarizes the peculiar characteristics of Ni/CeO₂ and Ni/Ce_xZ_r1−xO₂ systems since these catalysts are among the most studied catalysts in methanation and in the methane dry reforming processes. Recent studies have demonstrated that these compositions are also active in the direct conversion of methane to alcohols (Okolie et al., 2017; Lustemberg et al., 2018). Even if further studies will be necessary to understand the catalytic behavior of Ni/Ce systems under working condition and to improve their stability, it is expected that these compositions will have a significant impact in the industrial development of catalytic processes for the valorization of both CO₂ and CH₄.

Author Contributions

MB wrote introduction, conclusions, and the paragraph on methane dry-reforming. SC wrote the paragraph on CO₂ hydrogenation. AT reviewed the whole manuscript.

Conflict of Interest Statement

The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

References

Abasaeed, A. E., Al-Fatesh, A. S., Naeem, M. A., Ibrahim, A. A., and Fakeeha, A. H. (2015). Catalytic performance of CeO₂ and ZrO₂ supported Co catalysts for hydrogen production via dry reforming of methane. Int. J. Hydrog. Energy 40, 6818–6826. doi: 10.1016/j.ijhydene.2015.03.152s

CrossRef Full Text | Google Scholar

Abate, S., Mebrahtu, C., Giglio, E., Deorsola, F., Bensaid, S., Perathoner, S., et al. (2016). Catalytic performance of γ-Al₂O₃-ZrO₂-TiO₂-CeO₂ composite oxide supported Ni-based catalysts for CO₂ methanation. Ind. Eng. Chem. Res. 55, 4451–4460. doi: 10.1021/acs.iecr.6b00134

CrossRef Full Text | Google Scholar

Aitbekova, A., Wu, L., Wrasman, C. J., Boubnov, A., Hoffman, A. S., Goodman, E. D., et al. (2018). Low temperature restructuring of CeO₂-supported Ru nanoparticles determines selectivity in CO₂ catalytic reduction. J. Am. Chem. Soc. 140, 13736–13745. doi: 10.1021/jacs.8b07615

PubMed Abstract | CrossRef Full Text | Google Scholar

Aldana, P. A. U., Ocampo, F., Kobl, K., Louis, B., Thibault-Starzyk, F., Daturi, M., et al. (2013). Catalytic CO₂ valorization into CH₄ on Ni-based ceria-zirconia. reaction mechanism by operando IR spectroscopy. Catal. Today 215, 201–207. doi: 10.1016/j.cattod.2013.02.019

CrossRef Full Text | Google Scholar

Alvarez, A., Bansode, A., Urakawa, A., Bavykina, A. V., Wezendonk, T. A., Makkee, M., et al. (2017). Challenges in the greener production of formates/formic acid, methanol, and DME by heterogeneously catalyzed CO₂ hydrogenation processes. Chem. Rev. 117, 9804–9838. doi: 10.1021/acs.chemrev.6b00816

PubMed Abstract | CrossRef Full Text | Google Scholar

Araújo, O. Q. F., and de Medeiros, J. L. (2017). Carbon capture and storage technologies: present scenario and drivers of innovation. Curr. Opin. Chem. Eng. 17, 22–34, doi: 10.1016/j.coche.2017.05.004

CrossRef Full Text | Google Scholar

Ashok, J., Ang, M. L., and Kawi, S. (2017). Enhanced activity of CO₂ methanation over Ni/CeO₂-ZrO₂ catalysts: influence of preparation methods. Catal. Today 281, 304–311. doi: 10.1016/j.cattod.2016.07.020

CrossRef Full Text | Google Scholar

Atzori, L., Cutrufello, M. G., Meloni, D., Cannas, C., Gazzoli, D., Monaci, R., et al. (2018). Highly active NiO-CeO₂ catalysts for synthetic natural gas production by CO₂ methanation. Catal. Today 299, 183–192. doi: 10.1016/j.cattod.2017.05.065

CrossRef Full Text | Google Scholar

Atzori, L., Cutrufello, M. G., Meloni, D., Monaci, R., Cannas, C., Gazzoli, D., et al. (2017). CO₂ methanation on hard-templated NiO-CeO₂ mixed oxides. Int. J. Hyd. Energy 42, 20689–20702. doi: 10.1016/j.ijhydene.2017.06.198

CrossRef Full Text | Google Scholar

Aw, M. S., Dražić, G., Djinović, P., and Pintar, A. (2016). Transition metal pairs on ceria-promoted, ordered mesoporous alumina as catalysts for the CO₂ reforming reaction of methane. Catal. Sci. Technol. 6, 3797–3805. doi: 10.1039/C5CY02082D

CrossRef Full Text | Google Scholar

Aw, M. S., Osojnik Crnivec, I. G., and Pintar, A. (2014). Toward enhanced conversion of model biogas mixtures: parametric tuning and mechanistic study for ceria-zirconia supported nickel-cobalt catalyst. Catal. Sci. Technol. 4, 1340–1349. doi: 10.1039/C3CY01079A

CrossRef Full Text | Google Scholar

Ban, H., Li, C., Asami, K., and Fujimoto, K. (2014). Influence of rare-earth elements (La, Ce, Nd and Pr) on the performance of Cu/Zn/Zr catalyst for CH₃OH synthesis from CO₂. Catal. Comm. 54, 50–54. doi: 10.1016/j.catcom.2014.05.014

CrossRef Full Text | Google Scholar

Bian, L., Zhang, L., Xia, R., and Li, Z. H. (2015). Enhanced low-temperature CO₂ methanation activity on plasma-prepared Ni-based catalyst. J. Nat. Gas Sci. Eng. 27, 1189–1194. doi: 10.1016/j.jngse.2015.09.066

CrossRef Full Text | Google Scholar

Bian, Z., Chan, Y. M., Yu, Y., and Kawi, S. (in press). Morphology dependence of catalytic properties of Ni/CeO₂ for CO₂ methanation: a kinetic mechanism study. Catal. Today. doi: 10.1016/j.cattod.2018.04.067

CrossRef Full Text | Google Scholar

Bian, Z., Das, S., Wai, H. M., Hongmanorom, P., and Kawi, S. (2017). A review on bimetallic nickel-based catalysts for CO₂ reforming of methane. Chem. Phys. Chem. 18, 3117–3134. doi: 10.1002/cphc.201700529

PubMed Abstract | CrossRef Full Text | Google Scholar

Bobin, A. S., Sadykov, V. A., Rogov, V. A., Mezentseva, N. V., Alikina, G. M., Sadovskaya, E. M., et al. (2013). Mechanism of CH₄ dry reforming on nanocrystalline doped ceria-zirconia with supported Pt, Ru, Ni, and Ni-Ru. Top. Catal. 56, 958–968. doi: 10.1007/s11244-013-0060-z

CrossRef Full Text | Google Scholar

Bobrova, L. N., Bobin, A. S., Mezentseva, N. V., Sadykov, V. A., Thybaut, J. W., and Marin, G. B. (2016). Kinetic assessment of dry reforming of methane on Pt+Ni containing composite of fluorite-like structure. Appl. Catal. B Environ. 182, 513–524. doi: 10.1016/j.apcatb.2015.09.049

CrossRef Full Text | Google Scholar

Bonura, G., Arena, F., Mezzatesta, G., Cannilla, C., Spadaro, L., and Frusteri, F. (2011). Role of the ceria promoter and carrier on the functionality of Cu-based catalysts in the CO₂-to-methanol hydrogenation reaction. Catal. Today 171, 251–256. doi: 10.1016/j.cattod.2011.04.038

CrossRef Full Text | Google Scholar

Cai, W., Zhong, Q., and Zhao, Y. X. (2013). Fractional-hydrolysis-driven formation of non-uniform dopant concentration catalyst nanoparticles of Ni/Ce_xZr_1−xO₂ and its catalysis in methanation of CO₂. Catal. Comm. 39, 30–34. doi: 10.1016/j.catcom.2013.04.025

CrossRef Full Text | Google Scholar

Centi, G., Quadrelli, E. A., and Perathoner, S. (2013). Catalysis for CO₂ conversion: a key technology for rapid introduction of renewable energy in the value chain of chemical industries. Energy Environ. Sci. 6, 1711–1731. doi: 10.1039/c3ee00056g

CrossRef Full Text | Google Scholar

Chen, W., Zhao, G., Xue, Q., Chen, L., and Lu, Y. (2013). High carbon-resistance Ni/CeAlO₃-Al₂O₃ catalyst for CH₄/CO₂ reforming. Appl. Catal.B Environ. 136–137, 260–268. doi: 10.1016/j.apcatb.2013.01.044

CrossRef Full Text | Google Scholar

Chen, X., Su, X., Liang, B., Yang, X., Ren, X., Duan, H., et al. (2016). Identification of relevant active sites and a mechanism study for reverse water gas shift reaction over Pt/CeO₂ catalysts. J. Energy Chem. 5, 1051–1057. doi: 10.1016/j.jechem.2016.11.011

CrossRef Full Text | Google Scholar

Cheng, Z., and Lo, C. S. (2016). Mechanistic and microkinetic analysis of CO₂ hydrogenation on ceria. Phys. Chem. Chem. Phys. 18, 7987–7996. doi: 10.1039/C5CP07469J

PubMed Abstract | CrossRef Full Text | Google Scholar

Cheng, Z., Sherman, B. J., and Lo, C. S. (2013). Carbon dioxide activation and dissociation on ceria (110): a density functional theory study. J. Chem. Phys. 138:014702. doi: 10.1063/1.4773248

PubMed Abstract | CrossRef Full Text | Google Scholar

Choi, E. J., Lee, Y. H., Lee, D. W., Moon, D. J., and Lee, K. Y. (2017). Hydrogenation of CO₂ to methanol over Pd-Cu/CeO₂ catalysts. Mol. Catal. 434, 146–153. doi: 10.1016/j.mcat.2017.02.005

CrossRef Full Text | Google Scholar

Cormos, A. M., Dinca, C., Petrescu, L., Chisalita, D. A., and Szima, S. (2018). Carbon capture and utilization technologies applied to energy conversion systems and other energy-intensive industrial applications. Fuel 211, 883–890. doi: 10.1016/j.fuel.2017.09.104

CrossRef Full Text | Google Scholar

Dai, B., Zhou, G., Ge, S., Xie, H., Jiao, Z., Zhang, G., et al. (2017). CO₂ reverse water-gas shift reaction on mesoporous M-CeO₂ catalysts. Can. J. Chem. Eng. 95, 634–642. doi: 10.1002/cjce.22730

CrossRef Full Text | Google Scholar

Damyanova, S., Pawelec, B., Palcheva, R., Karakirova, Y., Capel-Sanchez, M. C., Tyuliev, G., et al. (2018). Structure and surface properties of ceria-modified Ni-based catalysts for hydrogen production. Appl. Catal. B Environ. 225, 340–353. doi: 10.1016/j.apcatb.2017.12.002

CrossRef Full Text | Google Scholar

Das, S., Ashok, J., Bian, Z., Dewangan, N., Wai, M. H., Du, Y., et al. (2018). Silica–ceria sandwiched Ni core–shell catalyst for low temperature dry reforming of biogas: coke resistance and mechanistic insights. Appl. Catal. B Environ. 230, 220–236. doi: 10.1016/j.apcatb.2018.02.041

CrossRef Full Text | Google Scholar

Das, T., and Deo, G. (2012). Effects of metal loading and support for supported cobalt catalyst. Catal. Today 198, 116–124. doi: 10.1016/j.cattod.2012.04.028

CrossRef Full Text | Google Scholar

Daza, Y. A., and Kuhn, J. N. (2016). CO₂ conversion by reverse water gas shift catalysis: comparison of catalysts, mechanisms and their consequences for CO₂ conversion to liquid fuels. RSC Adv. 6, 49675–49691. doi: 10.1039/C6RA05414E

CrossRef Full Text | Google Scholar

de Leitenburg, C., and Trovarelli, A. (1995). Metal-support Interactions in Rh/CeO₂, Rh/TiO₂, and Rh/Nb₂O₅ catalysts as inferred from CO₂ methanation activity. J. Catal. 156, 171–174. doi: 10.1006/jcat.1995.1244

CrossRef Full Text | Google Scholar

de Leitenburg, C., Trovarelli, A., and Kaspar, J. (1997). A temperature-programmed and transient kinetic study of CO₂ activation and methanation over CeO₂ supported noble metals. J. Catal. 166, 98–107. doi: 10.1006/jcat.1997.1498

CrossRef Full Text | Google Scholar

Dȩbek, R., Motak, M., Galvez-Parruca, M. E., Grzybek, T., Da Costa, P., and Pieńkowski, L. (2017). Ceria promotion over Ni-containing hydrotalcite-derived catalysts for CO₂ methane reforming. E3S Web Confer. 14:02039. doi: 10.1051/e3sconf/20171402039

CrossRef Full Text | Google Scholar

Debek, R., Radlik, M., Motak, M., Galvez, M. E., Turek, W., Da Costa, P., et al. (2015). Ni-containing Ce-promoted hydrotalcite derived materials as catalysts for methane reforming with carbon dioxide at low temperature - On the effect of basicity. Catal. Today 257, 59–65. doi: 10.1016/j.cattod.2015.03.017

CrossRef Full Text | Google Scholar

Deng, J., Chu, W., Wang, B., Yang, W., and Zhao, X. S. (2016). Mesoporous Ni/Ce_1−xNi_xO_2−y heterostructure as an efficient catalyst for converting greenhouse gas to H₂ and syngas. Catal. Sci. Tech. 6, 851–862, doi: 10.1039/C5CY00893J

CrossRef Full Text | Google Scholar

Devaiah, D., Reddy, L. H., Park, S. E., and Reddy, B. M. (2018). Ceria-zirconia mixed oxides: synthetic methods and applications. Catal. Rev. Sci. Eng. 60, 177–277. doi: 10.1080/01614940.2017.1415058

CrossRef Full Text | Google Scholar

Diez-Ramirez, J., Sanchez, P., Kyriakou, V., Zafeiratos, S., Marnellos, G. E., Konsolakis, M., et al. (2017). Effect of support nature on the cobalt-catalyzed CO₂ hydrogenation. J. CO₂ Utiliz. 21, 562–571. doi: 10.1016/j.jcou.2017.08.019

CrossRef Full Text | Google Scholar

Djinović, P., Crnivec, I. G. O., Erjavec, B., and Pintar, A. (2014). Details behind the self-regeneration of supported NiCo/Ce_0.8Zr_0.2O₂ bimetallic catalyst in the CH₄-CO₂ reforming reaction. Chem. Cat. Chem. 6, 1652–1663. doi: 10.1002/cctc.201400059

CrossRef Full Text | Google Scholar

Djinović, P., Crnivec, I. G. O., and Pintar, A. (2015). Biogas to syngas conversion without carbonaceous deposits via the dry reforming reaction using transition metal catalysts. Catal. Today 253, 155–162. doi: 10.1016/j.cattod.2015.01.039

CrossRef Full Text | Google Scholar

Dorner, R. W., Hardy, D. R., Williams, F. W., and Willauer, H. D. (2011). C₂-${\text{C}}_5^{+}$ olefin production from CO₂ hydrogenation using ceria modified Fe/Mn/K catalysts. Catal. Comm. 15, 88–92. doi: 10.1016/j.catcom.2011.08.017

CrossRef Full Text | Google Scholar

Dreyer, J. A. H., Li, P., Zhang, L., Beh, G. K., Zhang, R., Sit, P. H. L., et al. (2017). Influence of the oxide support reducibility on the CO₂ methanation over Ru-based catalysts. Appl. Catal. B Environ. 219, 715–726. doi: 10.1016/j.apcatb.2017.08.011

CrossRef Full Text | Google Scholar

Elsayed, N. H., Roberts, N. R. M., Joseph, B., and Kuhn, J. N. (2016). Comparison of Pd-Ni-Mg/ceria-zirconia and Pt-Ni-Mg/ceria-zirconia catalysts for syngas production via low temperature reforming of model biogas. Top. Catal. 59, 138–146. doi: 10.1007/s11244-015-0513-7

CrossRef Full Text | Google Scholar

Fang, X., Zhang, J., Liu, J., Wang, C., Huang, Q., Xu, X., et al. (2018). Methane dry reforming over Ni/Mg-Al-O: on the significant promotional effects of rare earth Ce and Nd metal oxides, J. CO₂ Utiliz 25, 242–253. doi: 10.1016/j.jcou.2018.04.011

CrossRef Full Text | Google Scholar

Frontera, P., Macario, A., Ferraro, M., and Antonucci, P. (2017). Supported catalysts for CO₂ methanation: a review. Cataysts 7. 1–28. doi: 10.3390/catal7020059

CrossRef Full Text | Google Scholar

Fukuhara, C., Hayakawa, K., Suzuki, Y., Kawasaki, W., and Watanabe, R. (2017). A novel nickel-based structured catalyst for CO₂ methanation: a honeycomb-type Ni/CeO₂ catalyst to transform greenhouse gas into useful resources. Appl. Catal. A Gen. 532, 12–18. doi: 10.1016/j.apcata.2016.11.036

CrossRef Full Text | Google Scholar

Gao, P., Li, F., Zhao, N., Xiao, F., Wei, W., Zhong, L., et al. (2013). Influence of modifier (Mn, La, Ce, Zr and Y) on the performance of Cu/Zn/Al catalysts via hydrotalcite-like precursors for CO₂ hydrogenation to methanol. Appl. Catal. A Gen. 468, 442–452. doi: 10.1016/j.apcata.2013.09.026

CrossRef Full Text | Google Scholar

Ghuman, K. K., Hoch, L. B., Wood, T. E., Mims, C., Singh, C. V., and Ozin, G. A. (2016). Surface analogues of molecular frustrated lewis pairs in heterogeneous CO₂ hydrogenation catalysis. ACS Catal. 6, 5764–5770. doi: 10.1021/acscatal.6b01015

CrossRef Full Text | Google Scholar

Ghuman, K. K., Wood, T. E., Hoch, L. B., Mims, C. A., Ozin, G. A., and Singh, C. V. (2015). Illuminating CO₂ reduction on frustrated Lewis pair surfaces: investigating the role of surface hydroxides and oxygen vacancies on nanocrystalline In₂O_3−x(OH)_y. Phys. Chem. Chem. Phys. 17, 14623–14635. doi: 10.1039/C5CP02613J

CrossRef Full Text | Google Scholar

Goguet, A., Meunier, F. C., Tibiletti, D., Breen, J. P., and Burch, R. (2004). Spectrokinetic investigation of reverse water-gas-shift reaction intermediates over a Pt/CeO₂ catalyst. J. Phy. Chem. B 108, 20240–20246. doi: 10.1021/jp047242w

CrossRef Full Text | Google Scholar

Goguet, A., Shekhtman, S. O., Burch, R., Hardacre, C., Meunier, F. C., and Yablonsky, G. S. (2006). Pulse-response TAP studies of the reverse water-gas shift reaction over a Pt/CeO₂ catalyst. J. Catal. 237, 102–110. doi: 10.1016/j.jcat.2005.10.020

CrossRef Full Text | Google Scholar

Götz, M., Lefebreve, J., Mors, F., Koch, A. M., Graf, F., Bajohr, S., et al. (2016). Renewable power -to-gas: a technological and economic review. Ren. Energy 85, 1371–1390. doi: 10.1016/j.renene.2015.07.066

CrossRef Full Text | Google Scholar

Goula, M. A., Charisiou, N. D., Siakavelas, G., Tzounis, L., Tsiaoussis, I., Panagiotopoulou, P., et al. (2017). Syngas production via the biogas dry reforming reaction over Ni supported on zirconia modified with CeO₂ or La₂O₃ catalysts. Int. J. Hyd. Energy 42, 13724–13740. doi: 10.1016/j.ijhydene.2016.11.196

CrossRef Full Text | Google Scholar

Graciani, J., Mudiyanselage, K., Xu, F., Baber, A. E., Evans, J., Senanayake, S. D., et al. (2014). Highly active copper-ceria and copper-ceria-titania catalysts for methanol synthesis from CO₂. Science 345, 546–550. doi: 10.1126/science.1253057

CrossRef Full Text | Google Scholar

Guo, L., Sun, J., Ge, Q., and Tsubaki, N. (2018). Recent advances in direct catalytic hydrogenation of carbon dioxide to valuable C²⁺ hydrocarbons. J. Mat. Chem. A 6, 23244–23262. doi: 10.1039/C8TA05377D

CrossRef Full Text | Google Scholar

Gurav, H. R., Dama, S., Samuel, V., and Chilukuri, S. (2017). Influence of preparation method on activity and stability of Ni catalysts supported on Gd doped ceria in dry reforming of methane. J. CO₂ Utiliz. 20, 357–367. doi: 10.1016/j.jcou.2017.06.014

CrossRef Full Text | Google Scholar

Huang, Z. Q., Liu, L. P., Qi, S. T., Zhang, S., Qu, Y. Q., and Chang, C. R. (2018). Understanding all-solid frustrated-lewis-pair sites on CeO₂ from theoretical perspectives. ACS Catal. 8, 546–554. doi: 10.1021/acscatal.7b02732

CrossRef Full Text | Google Scholar

IPCC report (2017). IPCC report. Available online at: https://www.ipcc.ch/report/sr15/

PubMed Abstract

Jacobs, G., and Davis, B. H. (2005). Reverse water-gas shift reaction: steady state isotope switching study of the reverse water-gas shift reaction using in situ DRIFTS and a Pt/ceria catalyst. Appl. Catal. A Gen. 284, 31–38. doi: 10.1016/j.apcata.2005.01.013

CrossRef Full Text | Google Scholar

Kambolis, A., Matralis, H., Trovarelli, A., and Papadopoulou, C. H. (2010). Ni/CeO₂-ZrO₂ catalysts for the dry reforming of methane. Appl. Catal. A Gen. 377, 16–26. doi: 10.1016/j.apcata.2010.01.013

CrossRef Full Text | Google Scholar

Kattel, S., Liu, P., and Chen, J. G. (2017). Tuning Selectivity of CO₂ hydrogenation reactions at the Metal/Oxide Interface. J. Am. Chem. Soc. 139, 9739–9754. doi: 10.1021/jacs.7b05362

PubMed Abstract | CrossRef Full Text | Google Scholar

Kondratenko, E. V., Mul, G., Baltrusaitis, J., Larrazabal, G. O., and Perez-Ramirez, J. (2013). Status and perspectives of CO₂ conversion into fuels and chemicals by catalytic, photocatalytic and electrocatalytic processes. Energy. Environ. Sci. 6, 3112–3135. doi: 10.1039/c3ee41272e

CrossRef Full Text | Google Scholar

Konishcheva, M. V., Potemkin, D. I., Badmaev, S. D., Snytnikov, P. V., Paukshtis, E. A., Sobyanin, V. A., et al. (2016). On the mechanism of CO and CO₂ methanation over Ni/CeO₂ catalysts. Top. Catal. 59, 1424–1430. doi: 10.1007/s11244-016-0650-7

CrossRef Full Text | Google Scholar

Kovacevic, M., Mojet, B. L., Van Ommen, J. G., and Lefferts, L. (2016). Effects of morphology of cerium oxide catalysts for reverse water gas shift reaction. Catal. Lett. 146, 770–777. doi: 10.1007/s10562-016-1697-6

CrossRef Full Text | Google Scholar

Kumar, P., Sun, Y., and Idem, R. O. (2007). Nickel-based ceria, zirconia and ceria zirconia catalytic systems for low-temperature carbon dioxide reforming of methane. Energy Fuel 21, 3113–3123. doi: 10.1021/ef7002409

CrossRef Full Text | Google Scholar

Kumar, P., Sun, Y., and Idem, R. O. (2008). Comparative study of Ni based mixed oxide catalysts for carbon dioxide reforming of methane. Energy Fuel 22, 3575–3528. doi: 10.1021/ef800326q

CrossRef Full Text | Google Scholar

Kumari, N., Sinha, N., Haider, M. A., and Basu, S. (2015). CO₂ Reduction to methanol on CeO₂ (110) surface: a density functional theory study. Electrochim. Acta 177, 21–29. doi: 10.1016/j.electacta.2015.01.153

CrossRef Full Text | Google Scholar

Laosiripojana, N., and Assbumrungrat, S. (2005). Catalytic dry reforming of methane over high surface area ceria. Appl. Catal. B Environ. 60, 107–116. doi: 10.1016/j.apcatb.2005.03.001

CrossRef Full Text | Google Scholar

Lavoie, J. M. (2014). Review on dry reforming of methane, a potentially more environmentally-friendly approach to the increasing natural gas exploitation. Front. Chem. 2, 1–17. doi: 10.3389/fchem.2014.00081

PubMed Abstract | CrossRef Full Text | Google Scholar

Le, M. C., Le Van, K., Nguyen, T. H. T., and Nguyen, N. H. (2017). The impact of Ce-Zr addition on nickel dispersion and catalytic behavior for CO₂ methanation of Ni/AC catalyst at low temperature. J. Chem. 2017:4361056. doi: 10.1155/2017/4361056

CrossRef Full Text | Google Scholar

Li, M., Amari, H., and van Veen, A. C. (2018). Metal-oxide interaction enhanced CO₂ activation in methanation over ceria supported nickel nanocrystallites. Appl. Catal. B Environ. 239, 27–35. doi: 10.1016/j.apcatb.2018.07.074

CrossRef Full Text | Google Scholar

Li, M., and van Veen, A. C. (2018). Tuning the catalytic performance of Ni-catalysed dry reforming of methane and carbon deposition via Ni-CeO_2−x interaction. Appl. Catal. B Environ. 237, 641–648. doi: 10.1016/j.apcatb.2018.06.032

CrossRef Full Text | Google Scholar

Li, S., and Gong, J. (2014). Strategies for improving the performance and stability of Ni-based catalysts for reforming reactions. Chem. Soc. Rev. 43, 72245–77256. doi: 10.1039/C4CS00223G

PubMed Abstract | CrossRef Full Text | Google Scholar

Li, S. W., Xu, Y., Chen, Y. F., Li, W. Z., Lin, L. L., Li, M. Z., et al. (2017). Tuning the selectivity of catalytic carbon dioxide hydrogenation over iridium/cerium oxide catalysts with a strong metal-support interaction. Ang. Chem. Int. Ed. 56, 10761–10765. doi: 10.1002/anie.201705002

PubMed Abstract | CrossRef Full Text | Google Scholar

Li, W. H., Wang, H. Z., Jiang, X., Zhu, J., Liu, Z. M., Guo, X. W., et al. (2018). A short review of recent advances in CO₂ hydrogenation to hydrocarbons over heterogeneous catalysts. RSC Adv. 8, 7651–7669. doi: 10.1039/C7RA13546G

CrossRef Full Text | Google Scholar

Li, Y., Wang, Y., Zhang, X., and Mi, Z. (2008). Thermodynamic analysis of autothermal steam and CO₂ reforming of methane. Int. J. Hyd. Energy 33, 2507–2514. doi: 10.1016/j.ijhydene.2008.02.051

CrossRef Full Text | Google Scholar

Liang, T.-Y., Lin, C.-Y., Chou, F.-C., Wang, M., and Tsai, D. -H. (2018). Gas-phase synthesis of Ni–CeO_x hybrid nanoparticles and their synergistic catalysis for simultaneous reforming of methane and carbon dioxide to syngas. J. Phys. Chem. C 122, 11789–11798, doi: 10.1021/acs.jpcc.8b00665

CrossRef Full Text | Google Scholar

Lin, F., Delmelle, R., Vinodkumar, T., Reddy, B. M., Wokaun, A., and Alxneit, I. (2015). Correlation between the structural characteristics, oxygen storage capacities and catalytic activities of dual-phase Zn-modified ceria nanocrystals. Catal. Sci. Technol. 5, 3556–3567. doi: 10.1039/C5CY00351B

CrossRef Full Text | Google Scholar

Lin, L., Yao, S., Liu, Z., Zhang, F., Li, N., Vovchok, D., et al. (2018). In Situ characterization of Cu/CeO₂ nanocatalysts for CO₂ hydrogenation: morphological effects of nanostructured ceria on the catalytic activity. J. Phy. Chem. C 122, 12934–12943. doi: 10.1021/acs.jpcc.8b03596

CrossRef Full Text | Google Scholar

Liu, H., Da Costa, P., Hadj Taief, H. B., Benzina, M., and Gálvez, M. E. (2017). Ceria and zirconia modified natural clay based nickel catalysts for dry reforming of methane Int. J. Hyd. Energy 42, 23508–23516. doi: 10.1016/j.ijhydene.2017.01.075

CrossRef Full Text | Google Scholar

Liu, H. Z., Zou, X. J., Wang, X. G., Lu, X. G., and Ding, W. Z. (2012). Effect of CeO₂ addition on Ni/Al₂O₃ catalysts for methanation of carbon dioxide with hydrogen. J. Nat. Gas Chem. 21, 703–707. doi: 10.1016/S1003-9953(11)60422-2

CrossRef Full Text | Google Scholar

Liu, Y., Li, Z., Xu, H., and Han, Y. (2016). Reverse water-gas shift reaction over ceria nanocube synthesized by hydrothermal method. Catal. Comm. 76, 1–6. doi: 10.1016/j.catcom.2015.12.011

CrossRef Full Text | Google Scholar

Liu, Z., Grinter, D. C., Lustemberg, P. G., Nguyen-Phan, T.-D., Zhou, Y., Luo, S., et al. (2016). Dry reforming of methane on a highly-active Ni-CeO₂ catalyst: effects of metal-support interactions on C–H bond breaking. Angew. Chem. Int. Ed. 55, 7455–7459. doi: 10.1002/anie.201602489

PubMed Abstract | CrossRef Full Text | Google Scholar

Liu, Z., Lustemberg, P., Gutiérrez, R. A., Carey, J. J., Palomino, R. M., Vorokhta, M., et al. (2017). In Situ investigation of methane dry reforming on metal/ceria(111) surfaces: metal–support interactions and C–H bond activation at low temperature. Ang. Chem. Int. Ed. 56, 13041–13046. doi: 10.1002/anie.201707538

PubMed Abstract | CrossRef Full Text | Google Scholar

Lu, B. W., and Kawamoto, K. (2014). Preparation of mesoporous CeO₂ and monodispersed NiO particles in CeO₂, and enhanced selectivity of NiO/CeO₂ for reverse water gas shift reaction. Mat. Res. Bull. 3, 70–78. doi: 10.1016/j.materresbull.2014.01.043

CrossRef Full Text | Google Scholar

Lu, X. Q., Wang, W. L., Wei, S. X., Guo, C., Shao, Y., Zhang, M. M., et al. (2015). Initial reduction of CO₂ on perfect and O-defective CeO₂ (111) surfaces: towards CO or COOH? RSC Adv. 5, 97528–97535. doi: 10.1039/C5RA17825H

CrossRef Full Text | Google Scholar

Lustemberg, P. G., Palomino, R. M., Gutiérrez, R. A., Grinter, D. C., Vorokhta, M., Liu, Z., et al. (2018). Direct conversion of methane to methanol on Ni-Ceria surfaces: metal–support interactions and water-enabled catalytic conversion by site blocking. J. Am. Chem. Soc. 140, 7681–7687. doi: 10.1021/jacs.8b03809

PubMed Abstract | CrossRef Full Text | Google Scholar

Lustemberg, P. G., Ramirez, P. J., Liu, Z. Y., Gutierrez, R. A., Grinter, D. G., Carrasco, J., et al. (2016). Room-temperature activation of methane and dry-reforming with CO₂ on Ni-CeO₂(111) surfaces: effect of Ce³⁺ sites and metal–support interactions on C–H bond cleavage. ACS Catal. 6, 8184–8191. doi: 10.1021/acscatal.6b02360

CrossRef Full Text | Google Scholar

Ma, Y., Gao, W., Zhang, Z., Zhang, S., Zhimin, T., Yuxuan, L., et al. (2018). Regulating the surface of nanoceria and its applications in heterogeneous catalysis. Surf. Sci. Rep. 73, 1–36. doi: 10.1016/j.surfrep.2018.02.001

CrossRef Full Text | Google Scholar

Makri, M. M., Vasiliades, M. A., Petallidou, K. C., and Efstathiou, A. M. (2015). Effect of support composition on the origin and reactivity of carbon formed during dry reforming of methane over 5 wt% Ni/Ce_1−xM_xO_2−δ (M = Zr⁴⁺, Pr³⁺) catalysts. Catal. Today 259, 150–164. doi: 10.1016/j.cattod.2015.06.010

CrossRef Full Text | Google Scholar

Małecka, M. A. (2016). Ceria-based mixed oxides – beautiful structures. ChemistrySelect 1, 4246–4254. doi: 10.1002/slct.201600845

CrossRef Full Text | Google Scholar

Malik, A. S., Zaman, S. F., Al-Zahrani, A. A., Daous, M. A., Driss, H., and Petrov, L. A. (2018). Development of highly selective PdZn/CeO₂ and Ca-doped PdZn/CeO₂ catalysts for methanol synthesis from CO₂ hydrogenation. Appl. Catal. A Gen. 560, 42–53. doi: 10.1016/j.apcata.2018.04.036

CrossRef Full Text | Google Scholar

Martens, J. A., Bogaerts, A., Kimpe, N., Jacobs, P. A., Marin, G. B., Rabaey, K., et al. (2017). The chemical route to a carbon dioxide neutral world. Chem. Sus. Chem. 10, 1039–1055. doi: 10.1002/cssc.201601051

PubMed Abstract | CrossRef Full Text | Google Scholar

Martin, N. M., Velin, P., Skoglundh, M., Bauer, M., and Carlsson, P. A. (2017). Catalytic hydrogenation of CO₂ to methane over supported Pd, Rh and Ni catalysts. Catal. Sci. Technol. 7, 1086–1094. doi: 10.1039/C6CY02536F

CrossRef Full Text | Google Scholar

Montini, T., Melchionna, M., Monai, M., and Fornasiero, P. (2016). Fundamentals and catalytic applications of CeO₂-based materials. Chem. Rev. 116, 5987–6041. doi: 10.1021/acs.chemrev.5b00603

PubMed Abstract | CrossRef Full Text | Google Scholar

Mullinsn, D. R. (2015). The surface chemistry of cerium oxide. Surf. Sci. Rep. 70, 42–85. doi: 10.1016/j.surfrep.2014.12.001

CrossRef Full Text | Google Scholar

Muñoz, M. A., Calvino, J. J., Rodríguez-Izquierdo, J. M., Blanco, G., Arias, D. C., Pérez-Omil, J. A., et al. (2017). Highly stable ceria-zirconia-yttria supported Ni catalysts for syngas production by CO₂ reforming of methane. Appl. Surf. Sci. 426, 864–873. doi: 10.1016/j.apsusc.2017.07.210

CrossRef Full Text | Google Scholar

Nahar, G., and Dupont, V. (2014). Hydrogen production from simple alkanes and oxygenated hydrocarbons over ceria-zirconia supported catalysts: review. Ren. Sust. Energy 32, 777–796. doi: 10.1016/j.rser.2013.12.040

CrossRef Full Text | Google Scholar

Nie, W. X., Zou, X. J., Shang, X. F., Wang, X. G., Ding, W. Z., and Lu, X. G. (2017). CeO₂-assisted Ni nanocatalysts supported on mesoporous gamma-Al₂O₃ for the production of synthetic natural gas. Fuel 202, 135–143. doi: 10.1016/j.fuel.2017.04.026

CrossRef Full Text | Google Scholar

Nikoo, M. K., and Amin, N. A. S. (2011). Thermodynamic analysis of carbon dioxide reforming of methane in view of solid carbon formation. Fuel Proc. Technol. 92, 678–691. doi: 10.1016/j.fuproc.2010.11.027

CrossRef Full Text | Google Scholar

Nizio, M., Albarazi, A., Cavadias, S., Amouroux, J., Galvez, M. E., and Da Costa, P. (2016). Hybrid plasma-catalytic methanation of CO₂ at low temperature over ceria zirconia supported Ni catalysts. Int. J. Hyd. Energy 41, 11584–11592. doi: 10.1016/j.ijhydene.2016.02.020

CrossRef Full Text | Google Scholar

Ocampo, F., Louis, B., Kiwi-Minsker, L., and Roger, A.-C. (2011). Effect of Ce/Zr composition and noble metal promotion on nickel based Ce_xZr_1−xO₂ catalysts for carbon dioxide methanation. Appl. Catal. A Gen. 392, 36–44. doi: 10.1016/j.apcata.2010.10.025

CrossRef Full Text | Google Scholar

Odedairo, T., Chen, J., and Zhu, Z. (2013). Metal-support interface of a novel Ni-CeO₂ catalyst for dry reforming of methane. Catal. Commun. 31, 25–31. doi: 10.1016/j.catcom.2012.11.008

CrossRef Full Text | Google Scholar

Okolie, C., Belhseine, Y. F., Lyu, Y., Yung, M. M., Engelhard, M. H., Kovarik, L., et al. (2017). Conversion of methane to methanol and ethanol over nickel oxide on ceria–zirconia catalysts in a single reactor. Angew. Chem. Int. Ed. 56, 1–7. doi: 10.1002/anie.201704704

PubMed Abstract | CrossRef Full Text | Google Scholar

Otsuka, K., Sunada, E., Ushiyama, T., and Yamanaka, I. (1997). The production of synthesis gas by the redox of cerium oxide. Stud. Surf. Sci. Catal. 531–536. doi: 10.1016/S0167-2991(97)80386-2

CrossRef Full Text | Google Scholar

Ouyang, B., Tan, W. L., and Liu, B. (2017). Morphology effect of nanostructure ceria on the Cu/CeO₂ catalysts for synthesis of methanol from CO₂ hydrogenation. Catal. Commun. 95, 36–39. doi: 10.1016/j.catcom.2017.03.005

CrossRef Full Text | Google Scholar

Pakhare, D., and Spivey, J. (2014). A review of dry (CO₂) reforming of methane over noble metal catalysts. Chem. Soc. Rev. 43, 7813–7837. doi: 10.1039/C3CS60395D

PubMed Abstract | CrossRef Full Text | Google Scholar

Pan, Q., Peng, J., Sun, T., Wang, S., and Wang, S. (2014). Insight into the reaction route of CO₂ methanation: promotion effect of medium basic sites. Catal. Commun. 45, 74–78. doi: 10.1016/j.catcom.2013.10.034

CrossRef Full Text | Google Scholar

Pan, Q. S., Peng, J. X., Sun, T. J., Gao, D. N., Wang, S., and Wang, S. D. (2014). CO₂ methanation on Ni/Ce_0.5Zr_0.5O₂ catalysts for the production of synthetic natural gas. Fuel Proc. Technol. 123, 166–171. doi: 10.1016/j.fuproc.2014.01.004

CrossRef Full Text | Google Scholar

Panaritis, C., Edake, M., Couillard, M., Einakchi, R., and Baranova, E. A. (2018). Insight towards the role of ceria-based supports for reverse water gas shift reaction over RuFe nanoparticles. J. CO₂ Utiliz. 26, 350–358. doi: 10.1016/j.jcou.2018.05.024

CrossRef Full Text | Google Scholar

Pappacena, A., Razzaq, R., de Leitenburg, C., Boaro, M., and Trovarelli, A. (2018). The role of neodymium in the optimization of a Ni/CeO₂ and Ni/CeZrO₂ methane dry reforming catalyst. Inorganics 639, 2–15. doi: 10.3390/inorganics6020039

CrossRef Full Text | Google Scholar

Pastor-Pérez, L., Saché, E. L., Jones, C., Gu, S., Arellano-Garcia, H., and Reina, T. R. (2018). Synthetic natural gas production from CO₂ over Ni_−x/CeO₂-ZrO₂ (x = Fe, Co) catalysts: influence of promoters and space velocity. Catal. Tod. 317, 108–113. doi: 10.1016/j.cattod.2017.11.035

CrossRef Full Text | Google Scholar

Porosoff, M. D., and Chen, J. G. G. (2013). Trends in the catalytic reduction of CO₂ by hydrogen over supported monometallic and bimetallic catalysts. J. Catal. 301, 30–37. doi: 10.1016/j.jcat.2013.01.022

CrossRef Full Text | Google Scholar

Porosoff, M. D., Yan, B., and Chen, J. G. (2016). Catalytic reduction of CO₂ by H₂ for synthesis of CO, methanol and hydrocarbons: challenges and opportunities. Energy Environ. Sci. 9, 62–73. doi: 10.1039/C5EE02657A

CrossRef Full Text | Google Scholar

Razzaq, R., Zhu, H., Jiang, L., Muhammad, U., Li, C., and Zhang, S. (2013). Catalytic methanation of CO and CO₂ in coke oven gas over Ni–Co/ZrO₂-CeO₂. Ind. Eng. Chem. Res. 52, 2247–2256. doi: 10.1021/ie301399z

CrossRef Full Text | Google Scholar

Richard, A. R., and Fan, M. (2018). Rare earth elements: properties and applications to methanol synthesis catalysis via hydrogenation of carbon oxides. J. Rare Earths 36, 1127–1135. doi: 10.1016/j.jre.2018.02.012

CrossRef Full Text | Google Scholar

Rodriguez, J. A., Grinter, D. C., Liu, Z. Y., Palomino, R. M., and Senanayake, S. D. (2017). Ceria-based model catalysts: fundamental studies on the importance of the metal-ceria interface in CO oxidation, the water-gas shift, CO₂ hydrogenation, and methane and alcohol reforming. Chem. Soc. Rev. 46, 1824–1841. doi: 10.1039/C6CS00863A

PubMed Abstract | CrossRef Full Text | Google Scholar

Rodriguez, J. A., Liu, P., Stacchiola, D. J., Senanayake, S. D., White, M. G., and Chen, J. G.G. (2015). Hydrogenation of CO₂ to methanol: importance of metal-oxide and metal-carbide interfaces in the activation of CO₂. ACS Catal. 5, 6696–6706. doi: 10.1021/acscatal.5b01755

CrossRef Full Text | Google Scholar

Ronda-Lloret, M., Rico-Frances, S., Sepulveda-Escribano, A., and Ramos-Fernandez, E. V. (2018). CuO_x/CeO₂ catalyst derived from metal organic framework for reverse water-gas shift reaction. Appl. Catal. A Gen. 562, 28–36. doi: 10.1016/j.apcata.2018.05.024

CrossRef Full Text | Google Scholar

Rönsch, S., Schneider, J., Matthischke, S., Schlüter, M., Götz, M., Lefebvre, J., et al. (2016). Review on methanation – from fundamentals to current projects. Fuel 166, 276–296. doi: 10.1016/j.fuel.2015.10.111

CrossRef Full Text | Google Scholar

Ruiz Puigdollers, A., Schlexer, P., Tosoni, S., and Pacchioni, G. (2017). Increasing oxide reducibility: the role of metal/oxide interfaces in the formation of oxygen vacancies. ACS Catal. 7, 6493–6513. doi: 10.1021/acscatal.7b01913

CrossRef Full Text | Google Scholar

Samanta, A., Landau, M. V., Vidruk-Nehemya, R., and Herskowitz, M. (2017). CO₂ hydrogenation to higher hydrocarbons on K/Fe-Al-O spinel catalysts promoted with Si, Ti, Zr, Hf, Mn and Ce. Catal. Sci. Technol. 7, 4048–4063. doi: 10.1039/C7CY01118K

CrossRef Full Text | Google Scholar

Senanayake, S. D., Ramirez, P. J., Waluyo, I., Kundu, S., Mudiyanselage, K., Liu, Z. Y., et al. (2016). Hydrogenation of CO₂ to methanol on CeO_x/Cu(111) and ZnO/Cu(111) catalysts: role of the metal-oxide interface and importance of Ce³⁺ Sites. J. Phys. Chem. C 120, 1778–1784. doi: 10.1021/acs.jpcc.5b12012

CrossRef Full Text | Google Scholar

Shang, X. F., Deng, D. G., Wang, X. G., Xuan, W. D., Zou, X. J., Ding, W. Z., et al. (2018). Enhanced low-temperature activity for CO₂ methanation over Ru doped the Ni/Ce_xZr_(1−x)O₂ catalysts prepared by one-pot hydrolysis method. Int. J. Hyd. Energy 43, 7179–7189. doi: 10.1016/j.ijhydene.2018.02.059

CrossRef Full Text | Google Scholar

Sharma, S., Hu, Z. P., Zhang, P., McFarland, E. W., and Metiu, H. (2011). CO₂ methanation on Ru-doped ceria. J. Catal. 278, 297–309. doi: 10.1016/j.jcat.2010.12.015

CrossRef Full Text | Google Scholar

Sharma, S., Kumar, K. B. S., Chandnani, Y. M., Kumar, V. S. P., Gangwar, B. P., Singhal, A., et al. (2016). Mechanistic insights into CO₂ methanation over Ru-substituted CeO₂. J. Phys. Chem. C 120, 14101–14112. doi: 10.1021/acs.jpcc.6b03224

CrossRef Full Text | Google Scholar

Shi, Z., Tan, Q., and Wu, D. (2018). Ternary copper-cerium-zirconium mixed metal oxide catalyst for direct CO₂ hydrogenation to methanol. Mat. Chem. Phys. 219, 263–272. doi: 10.1016/j.matchemphys.2018.08.038

CrossRef Full Text | Google Scholar

Simonov, M. N., Rogov, V. A., Smirnova, M. Y., and Sadykov, V. A. (2017). Pulse microcalorimetry study of methane dry reforming reaction on Ni/Ceria-Zirconia catalyst Catalysts 7:268. doi: 10.3390/catal7090268

CrossRef Full Text | Google Scholar

Singha, R. K., Yadav, A., Shukla, A., Kumar, M., and Bal, R. (2017). Low temperature dry reforming of methane over Pd-CeO₂ nanocatalyst. Catal. Commun. 92, 19–22. doi: 10.1016/j.catcom.2016.12.019

CrossRef Full Text | Google Scholar

Stephan, D. W. (2009). Frustrated lewis pairs: a new strategy to small molecule activation and hydrogenation catalysis. Dalton Trans. 17, 3129–3136. doi: 10.1039/b819621d

CrossRef Full Text | Google Scholar

Stroud, T., Smith, T. J., Le Saché, E., Santos, J. L., Centeno, M. A., Arellano-Garcia, H., et al. (2018). Chemical CO₂ recycling via dry and bi reforming of methane using Ni-Sn/Al₂O₃ and Ni-Sn/CeO₂-Al₂O₃ catalysts. Appl. Catal. B Env. 224, 125–135. doi: 10.1016/j.apcatb.2017.10.047

CrossRef Full Text | Google Scholar

Su, X., Xu, J., Liang, B., Duan, H., Hou, B., and Huang, Y. (2016). Catalytic carbon dioxide hydrogenation to methane: a review of recent studies. J. Energy. Chem. 25, 553–565. doi: 10.1016/j.jechem.2016.03.009

CrossRef Full Text | Google Scholar

Sun, H., Wang, J., Zhao, J., Shen, B., Shi, J., Huang, J., et al. (2019). Dual functional catalytic materials of Ni over Ce-modified CaO sorbents for integrated CO₂ capture and conversion. Appl. Catal. B Environ. 244, 63–75. doi: 10.1016/j.apcatb.2018.11.040

CrossRef Full Text | Google Scholar

Tada, S., Ochieng, O. J., Kikuchi, R., Haneda, T., and Kameyama, H. (2014). Promotion of CO₂ methanation activity and CH₄ selectivity at low temperatures over Ru/CeO₂/Al₂O₃ catalysts. Int. J. Hyd. Energy 39, 10090–10100. doi: 10.1016/j.ijhydene.2014.04.133

CrossRef Full Text | Google Scholar

Tada, S., Shimizu, T., Kameyama, H., Haneda, T., and Kikuchi, R. (2012). Ni/CeO₂ catalysts with high CO₂ methanation activity and high CH₄ selectivity at low temperatures. Int. J. Hyd. Energy 37, 5527–5531. doi: 10.1016/j.ijhydene.2011.12.122

CrossRef Full Text | Google Scholar

Taufiq-Yap, Y. H., Sudarno, R. U., and Zainal, Z. (2013). CeO₂-SiO₂ supported nickel catalysts for dry reforming of methane toward syngas production. Appl. Catal. A Gen. 468, 359–369. doi: 10.1016/j.apcata.2013.09.020

CrossRef Full Text | Google Scholar

Toemen, S., Abu Bakar, W. A. W., and Ali, R. (2016). Effect of ceria and strontia over Ru/Mn/Al₂O₃ catalyst: catalytic methanation, physicochemical and mechanistic studies. J. CO₂ Utiliz. 13, 38–49. doi: 10.1016/j.jcou.2015.11.005

CrossRef Full Text | Google Scholar

Torrente-Murciano, L., Chapman, R. S. L., Narvaez-Dinamarca, A., Mattia, D., and Jones, M. D. (2016). Effect of nanostructured ceria as support for the iron catalysed hydrogenation of CO₂ into hydrocarbons. Phys. Chem. Chem. Phys. 18, 15496–15500. doi: 10.1039/C5CP07788E

PubMed Abstract | CrossRef Full Text | Google Scholar

Trovarelli, A. (1996). Catalytic properties of ceria and CeO₂-containing materials. Catal. Rev. Sci. Eng. 38, 439–520. doi: 10.1080/01614949608006464

CrossRef Full Text | Google Scholar

Trovarelli, A., de Leitenburg, C., and Dolcetti, G. (1991). CO and CO₂ hydrogenation under transient conditions over Rh-CeO₂ - novel positive effects of metal support interaction on catalytic activity and selectivity. J. Chem. Soc. Chem. Commun. 7, 472–473. doi: 10.1039/C39910000472

CrossRef Full Text | Google Scholar

Trovarelli, A., and Fornasiero, P. (2013). Catalysis by Ceria and Related Materials, 2nd Edn. London: Imperial College Press, 1–908.

Google Scholar

Trovarelli, A., and Llorca, J. (2017). Catalysts at nanoscale: how do crystal shapes shape catalysis. ACS Catal. 7, 4716–4735. doi: 10.1021/acscatal.7b01246

CrossRef Full Text | Google Scholar

Tsubaki, N., and Fujimoto, K. (2003). Promotional SMSI effect on supported palladium catalysts for methanol synthesis. Top. Catal. 22, 325–335. doi: 10.1023/A:1023548608733

CrossRef Full Text | Google Scholar

Upham, D. C., Derk, A. R., Sharma, S., Metiu, H., and McFarland, E. W. (2015). CO₂ methanation by Ru-doped ceria: the role of the oxidation state of the surface. Catal. Sci. Technol. 5, 1783–1791. doi: 10.1039/C4CY01106F

CrossRef Full Text | Google Scholar

US EPA (U.S. Environmental Protection Agency). (2016). Inventory of U.S. Greenhouse Gas Emissions and Sinks: 1990–2014. EPA 430-R-16-002. Available online at: www.epa.gov/climatechange/ghgemissions/usinventoryreport.html

Usman, M., Wan Daus, W. M. A., and Abbas, H. F. (2015). Dry reforming of methane: influence of processes parameters-a review. Renew. Sustn. Energy. Rev. 45, 710–744. doi: 10.1016/j.rser.2015.02.026

CrossRef Full Text | Google Scholar

Vasiliades, M. A., Djinović, P., Davlyatova, L. F., Pintar, A., and Efstathiou, A. M. (2018). Origin and reactivity of active and inactive carbon formed during DRM over Ni/Ce_0.38Zr_0.62O_2−δ studied by transient isotopic techniques. Catal. Today 299, 201–211. doi: 10.1016/j.cattod.2017.03.057

CrossRef Full Text | Google Scholar

Vasiliades, M. A., Makri, M. M., Djinović, P., Erjavec, B., Pintar, A., and Efstathiou, A. M. (2016). Dry reforming of methane over 5 wt% Ni/Ce_1−xPr_xO_2−δ catalysts: performance and characterisation of active and inactive carbon by transient isotopic techniques. Appl. Catal. B Env. 197, 168–183. doi: 10.1016/j.apcatb.2016.03.012

CrossRef Full Text | Google Scholar

Vourros, A., Garagounis, I., Kyriakou, V., Carabineiro, S. A. C., Maldonado-Hodard, F. J., Mamellos, G. E., et al. (2017). Carbon dioxide hydrogenation over supported au nanoparticles: effect of the support. J. CO₂ Utiliz. 19, 247–256. doi: 10.1016/j.jcou.2017.04.005

CrossRef Full Text | Google Scholar

Wang, F., He, S., Chen, H., Wang, B., Zheng, L. R., Wei, M., et al. (2016). Active site dependent reaction mechanism over Ru/CeO₂ catalyst toward CO₂ methanation. J. Am. Chem. Soc. 138, 6298–6305. doi: 10.1021/jacs.6b02762

PubMed Abstract | CrossRef Full Text | Google Scholar

Wang, F., Li, C. M., Zhang, X. Y., Wei, M., Evans, D. G., and Duan, X. (2015). Catalytic behavior of supported Ru nanoparticles on the {100}, {110}, and {111} facet of CeO₂. J. Catal. 329, 177–186. doi: 10.1016/j.jcat.2015.05.014

CrossRef Full Text | Google Scholar

Wang, F., Xu, L., Yang, J., Zhang, J., Zhang, L., Li, H., et al. (2017). Enhanced catalytic performance of Ir catalysts supported on ceria-based solid solutions for methane dry reforming reaction. Catal. Today 281, 295–303. doi: 10.1016/j.cattod.2016.03.055

CrossRef Full Text | Google Scholar

Wang, J. B., Lee, H.-K., and Huang, T.-J. (2002). Synergistic catalysis of carbon dioxide hydrogenation into methanol by yttria-doped ceria/γ-alumina-supported copper oxide catalysts: effect of support and dopant. Catal. Lett. 83, 79–86. doi: 10.1023/A:1020613700495

CrossRef Full Text | Google Scholar

Wang, L., Liu, H., Chen, Y., and Yang, S. (2017). Reverse water–gas shift reaction over co-precipitated Co–CeO₂ catalysts: effect of Co content on selectivity and carbon formation. Int. J. Hyd. Energy 42, 3682–3689. doi: 10.1016/j.ijhydene.2016.07.048

CrossRef Full Text | Google Scholar

Wang, L., Liu, H., Liu, Y., Chen, Y., and Yang, S. (2013). Effect of precipitants on Ni-CeO₂ catalysts prepared by a co-precipitation method for the reverse water-gas shift reaction. J. Rare Earths 31, 969–974. doi: 10.1016/S1002-0721(13)60014-9

CrossRef Full Text | Google Scholar

Wang, L. C., Widmann, D., and Behm, R. J. (2015). Reactive removal of surface oxygen by H₂, CO and CO/H₂ on a Au/CeO₂ catalyst and its relevance to the preferential CO oxidation (PROX) and reverse water gas shift (RWGS) reaction. Catal. Sci. Technol. 5, 925–941. doi: 10.1039/C4CY01030B

CrossRef Full Text | Google Scholar

Wang, L. H., and Liu, H. (2018). Mesoporous Co-CeO₂ catalyst prepared by colloidal solution combustion method for reverse water-gas shift reaction. Catal. Today 316, 155–161. doi: 10.1016/j.cattod.2018.04.015

CrossRef Full Text | Google Scholar

Wang, N., Qian, W., Chu, W., and Wei, F. (2016). Crystal-plane effect of nanoscale CeO₂ on the catalytic performance of Ni/CeO₂ catalysts for methane dry reforming. Catal. Sci. Technol 6, 3594–3605. doi: 10.1039/C5CY01790D

CrossRef Full Text | Google Scholar

Wang, W., Wang, S. P., Ma, X. B., and Gong, J. L. (2011). Recent advances in catalytic hydrogenation of carbon dioxide. Chem. Soc. Rev. 40, 3703–3727. doi: 10.1039/c1cs15008a

PubMed Abstract | CrossRef Full Text | Google Scholar

Wang, W., Zhang, Y., Wang, Z., Yan, J.-M., Ge, Q., and Liu, C.-J. (2016). Reverse water gas shift over In₂O₃-CeO₂ catalysts. Catal. Today 259, 402–408. doi: 10.1016/j.cattod.2015.04.032

CrossRef Full Text | Google Scholar

Wei, W., and Jinlong, G. (2011). Methanation of carbon dioxide: an overview. Front. Chem. Sci. Eng. 5, 2–10. doi: 10.1007/s11705-010-0528-3

CrossRef Full Text | Google Scholar

Westermann, A., Azambre, B., Bacariza, M. C., Graça, I., Ribeiro, M. F., Lopes, J. M., et al. (2017). The promoting effect of Ce in the CO₂ methanation performances on NiUSY zeolite: a FTIR In Situ/Operando study. Catal. Today 283, 74–81. doi: 10.1016/j.cattod.2016.02.031

CrossRef Full Text | Google Scholar

Wolfbeisser, A., Sophiphun, O., Bernardi, J., Wittayakun, J., Föttinger, K., and Rupprechter, G. (2016). Methane dry reforming over ceria-zirconia supported Ni catalysts. Catal.Today 277, 234–245. doi: 10.1016/j.cattod.2016.04.025

CrossRef Full Text | Google Scholar

Wu, K., Sun, L.-D., and Yan, C.-H. (2016). Recent progress in well-controlled synthesis of ceria-based nanocatalysts towards enhanced catalytic performance. Adv. Energy Mater. 6, 1–46. doi: 10.1002/aenm.201600501

CrossRef Full Text | Google Scholar

Xie, C., Chen, C., Yu, Y., Su, J., Li, Y., Somorjai, G. A., et al. (2017). Tandem catalysis for CO₂ hydrogenation to C₂-C₄ hydrocarbons. Nano. Lett. 17, 3798–3802. doi: 10.1021/acs.nanolett.7b01139

PubMed Abstract | CrossRef Full Text | Google Scholar

Xie, S., Wang, Z., Cheng, F., Zhang, P., Maib, W., and Tong, Y. (2017). Ceria and ceria-based nanostructured materials for photoenergy applications. Nano Energy 34, 313–337. doi: 10.1016/j.nanoen.2017.02.029

CrossRef Full Text | Google Scholar

Yang, L., Pastor-Perez, L., Gu, S., Sepulveda-Escribano, A., and Reina, T. R. (2018). Highly efficient Ni/CeO₂-Al₂O₃ catalysts for CO₂ upgrading via reverse water-gas shift: effect of selected transition metal promoters. Appl. Catal. B Environ. 232, 464–471. doi: 10.1016/j.apcatb.2018.03.091

CrossRef Full Text | Google Scholar

Zeng, S., Zhang, X., Fu, X., and Pan, H. (2013). Co/Ce_xZr_1−xO₂ solid solution catalysts with cubic fluorite structure for carbon dioxide reforming of methane. Appl. Catal. B Environ. 136–137, 308–316. doi: 10.1016/j.apcatb.2013.02.019

CrossRef Full Text | Google Scholar

Zhan, H., Li, F., Gao, P., Zhao, N., Xiao, F., Wei, W., et al. (2014). Methanol synthesis from CO₂ hydrogenation over La–M–Cu–Zn–O (M = Y, Ce, Mg, Zr) catalysts derived from perovskite-type precursors. J. Power Sources 251, 113–121. doi: 10.1016/j.jpowsour.2013.11.037

CrossRef Full Text | Google Scholar

Zhang, F., Liu, Z., Zhang, S., Akter, N., Palomino, R. M., Vovchok, D., et al. (2018). In situ elucidation of the active state of Co-CeO_x catalysts in the dry reforming of methane: the important role of the reducible oxide support and interactions with cobalt. ACS Catal 8, 3550–3560. doi: 10.1021/acscatal.7b03640

CrossRef Full Text | Google Scholar

Zhang, S., Huang, Z. Q., Ma, Y. Y., Gao, W., Li, J., Cao, F. X., et al. (2017). Solid frustrated-Lewis-pair catalysts constructed by regulations on surface defects of porous nanorods of CeO₂. Nat. Commun. 8, 1–11. doi: 10.1038/ncomms15266

PubMed Abstract | CrossRef Full Text | Google Scholar

Zhao, B., Pan, Y.-X., and Liu, C.-J. (2012). The promotion effect of CeO₂ on CO₂ adsorption and hydrogenation over Ga₂O₃. Catal. Today 194, 60–64. doi: 10.1016/j.cattod.2012.05.011

CrossRef Full Text | Google Scholar

Zhao, X., Li, H., Zhang, J., Shi, L., and Zhang, D. (2016). Design and synthesis of NiCe@m-SiO₂ yolk-shell framework catalysts with improved coke- and sintering-resistance in dry reforming of methane. Int. J. Hyd. Energy 41, 2447–2456. doi: 10.1016/j.ijhydene.2015.10.111

CrossRef Full Text | Google Scholar

Zhou, G., Liu, H., Cui, K., Jia, A., Hu, G., Jiao, Z., et al. (2016). Role of surface Ni and Ce species of Ni/CeO₂ catalyst in CO₂ methanation. Appl. Surf. Sci. 383, 248–252. doi: 10.1016/j.apsusc.2016.04.180

CrossRef Full Text | Google Scholar

Zhu, H. W., Razzaq, R., Li, C. S., Muhmmad, Y., and Zhang, S. J. (2013). Catalytic methanation of carbon dioxide by active oxygen material Ce_xZr_1−xO₂ supported NiCo bimetallic nanocatalysts. AICHE J. 59, 2567–2576. doi: 10.1002/aic.14026

CrossRef Full Text | Google Scholar