Open Access Article
Shuairen
Qian
a,
Zhengwen
Li
a,
Xiaohang
Sun
a,
Yuxin
Chen
a,
Kai
Feng
ab,
Kaiqi
Nie
a,
Binhang
Yan
*a and
Yi
Cheng
*a
aDepartment of Chemical Engineering, Tsinghua University, Beijing 100084, P. R. China. E-mail: binhangyan@tsinghua.edu.cn; yicheng@tsinghua.edu.cn
bInstitute of Functional Nano & Soft Materials (FUNSOM), Soochow University, Suzhou, Jiangsu 215123, P. R. China
First published on 24th January 2025
Ammonia is one of the most important feedstocks for both fertilizer production and energy carriers. Identifying the appropriate reaction mechanism from the multiple pathways of ammonia synthesis is critical to the rational design of efficient catalysts. However, the low adhesion of nitrogen molecules hinders the observation of the behavior of reaction intermediates and the understanding of the reaction mechanisms. Kinetic analysis is a powerful tool to recognize reaction mechanisms, but it is difficult to expand case-by-case research to target systems. Herein, we establish a framework for the investigation of reaction mechanisms based on kinetic analysis and apply it to ammonia synthesis over a Co3Mo3N bimetallic nitride catalyst. The energetics of elementary reactions calculated by density functional theory (DFT) is used for a microkinetic model to obtain information about reaction mechanisms. Theoretical calculations indicate that the reaction rate via the surface reaction mechanism is much higher than that via the MvK mechanism. Nitrogen-vacancy-generation-induced charge redispersion is the major hindrance to the subsequent hydrogenation of NHx species for the MvK mechanism. This information guides the design and analysis of kinetic experiments. A series of steady-state and transient kinetic experiments demonstrate the dominant role of the dissociation mechanism over associative and MvK mechanisms. The low coverage of surface N species derived from both DFT-based microkinetic simulations and transient kinetic experiments originates from the high energy barrier to N2 dissociation. This work reveals the reaction mechanism of ammonia synthesis over bimetallic nitrides based on both theoretical calculations and experimental results and proposes a new paradigm for elucidating reaction mechanisms in heterogeneous catalysis from a kinetic perspective.
N triple bond.10–12 Many studies have been devoted to weakening the N
N bond through electron transfer from the catalyst surface to the antibonding orbitals of N2 molecules, such as the addition of alkali metal promoters,13 the construction of electron-rich centers,14–17 and assistance from external fields.18,19 Defect engineering mediated by nitrogen (N) vacancies is another effective approach to accelerate the reaction process.20–23 Similar to oxygen vacancies, the electrons located at the nitrogen vacancies are favorable for N2 activation.20–22,24 Transition metal nitrides are considered a class of potential catalysts with abundant lattice defects and they can generate ammonia through the activation and regeneration of lattice N, i.e., the Mars–van Krevelen (MvK) mechanism.25–27 In addition, an ensemble of metal sites with their electronic structure modulated by N heteroatoms is also accessible on the catalyst surface of metal nitrides. These metal sites, depending on nitrogen affinity, can also play a vital role in N2 dissociation (Fig. 1).28,29 However, due to the weak adhesion of N2 molecules to catalyst surfaces, it is difficult to determine the behavior and transformations of the intermediate species using well-developed spectroscopic tools. As a result, the reaction mechanisms and coexistence of two pathways contributing to ammonia production on nitride surfaces have not yet been precisely and intuitively identified by spectroscopic methods. Kinetic analysis is a powerful tool to identify the behavior of reaction intermediates and to understand reaction mechanisms.30,31 In particular, transient kinetic analysis, in contrast to steady-state kinetic analysis, where rate expressions derived based on microkinetic are fitted with experimental data, allows for the mathematical manipulation of transient response signals to obtain abundant information about reaction mechanisms.32–34 Many kinetic investigations on ammonia synthesis and other processes have been reported.16,35–43 Nevertheless, these studies have been conducted on a case-by-case basis without establishing a systematized procedure. It is essential to establish a complete framework based on kinetic analysis and to apply it to target catalytic reaction systems.
Herein, we establish a framework for the investigation of reaction mechanisms based on kinetic analysis and apply it to ammonia synthesis over metal nitride catalysts. The electron energy calculated from density functional theory (DFT) is used as the initial value for solving a mean-field microkinetic model (MKM), and information on reaction mechanisms (e.g., the rate-determining step) and the coverage of surface species is used to guide the design and analysis of kinetic experiments. Combining steady-state and transient kinetics, we identify the reaction mechanisms and the contributions of different pathways, and apply the mechanisms to catalyst design and larger scale applications. In this work, a Co3Mo3N bimetallic nitride catalyst, with both metal sites favoring N2 dissociation and electron-enrichment of lattice N sites, is chosen as a model nitride catalyst.28,44–46 Ammonia production over the Co3Mo3N catalyst via different reaction pathways is identified by both microkinetic models and transient kinetics analysis. The rate-determining step (RDS) obtained from degree of rate control (DRC) analysis is applied to the derivation of rate expressions. A series of isotope experiments demonstrate that ammonia synthesis via the dissociation mechanism shows higher reactivity than that via the MvK mechanism. Defective charges promote N2 activation but inhibit hydrogenation of NHx species. Steady-state isotopic-transient kinetic analysis (SSITKA) experiments reveal the low surface coverage and turnover frequency of dissociation mechanism intermediates on the catalyst surface. Overall, this framework combining theoretical calculations and experimental measurements from a kinetic perspective serves as a powerful tool for the elucidation of reaction mechanisms.
(1.09 eV). This result confirms that it is difficult for continuous hydrogenation similar to enzymatic processes in heterogeneous catalysis for ammonia synthesis.9,47,48 Therefore, an associative pathway via NNH* intermediate species is considered to be a candidate for an associative mechanism. Direct N2 dissociation also occurs easily on the CoMo2 sites due to the Sabatier optimal of Co–Mo predicted by the volcano curve.35,49 Both the dissociation pathway and the associative pathway are surface reaction mechanisms and the hydrogenation process for surface
species is identical, and completely different from the lattice N-mediated MvK mechanism. For the MvK mechanism, N2 adsorption occurs on the N vacancy, and the surface N species hydrogenation process occurs on a defective surface rather than on a clean surface. Lattice vacancies are more capable of N2 adsorption due to the formation of covalent interactions between surface Mo atoms and N (Fig. 2b). Nevertheless, barriers to the hydrogenation of
species and
desorption on the defective surface are much higher than those on a clean surface, leading to the potentially unfavorable occurrence of ammonia synthesis via a lattice-vac pathway (Fig. 2c).
To further validate the potential reaction mechanism on the Co3Mo3N catalyst, we performed mean-field microkinetic modelling based on the above DFT-calculated potential energy surfaces, as illustrated in Fig. 3. The reaction rate heatmaps of other associative pathways were investigated, as shown in Fig. S10–S18.† The NNH* associative pathway exhibits more significant reactivity than the other associative pathway, which is consistent with the above analysis based on the energy barriers of the key elementary steps. Mixed pathways with different associative intermediates were also considered, to observe the potential reaction fluxes (Fig. S22†). Interestingly, all contributions to ammonia production in mixed pathways originate from the NNH* associative pathway. Therefore, the NNH* associative pathway is more favorable and the associative mechanism is denoted as the NNH* associative pathway in subsequent studies. The reaction rates (in terms of TOF) via the dissociation mechanism and associative mechanism show significant temperature sensitivity, as illustrated in Fig. 3d. In low-temperature regions, the associative pathway has higher reactivity for ammonia synthesis. In high-temperature regions, the dissociation pathway dominates the reaction contribution. In contrast, the MvK pathway exhibits four orders of magnitude lower intrinsic activity under conventional reaction conditions. Degree of rate control (DRC) analysis was performed to determine the rate-determining step (RDS) for different reaction pathways (Fig. S23†).
dissociation and
hydrogenation processes are the RDS for the dissociation pathway and associative pathway, respectively. The RDS of the MvK pathway is the
hydrogenation process. Thus, the low activity can be attributed to the hydrogenation-blocking behavior exhibited in Fig. 2c, which seems to contradict previous reports on lattice-N-mediated ammonia synthesis performance over a Co3Mo3N catalyst.28,50
species, rendering the hydrogenation inert. This behavior is similarly confirmed by charge analysis. The accumulated charge located in the N vacancy on the defective surface is redistributed, causing a more electron-rich Mo center and generating stronger binding capacity to the surface species (Fig. 4b–d). The charge density difference of
adsorption demonstrates a redistribution of electron density, and the adsorption strength depends on electron transfer (Fig. 4 and S25†). Similar to catalyst poisoning, stronger
adsorption blocks the active sites on the catalyst surface. This phenomenon also puts the classical linear scaling relationship into perspective.51,52
Furthermore, we investigated the critical pathways followed by surface mechanisms (Fig. 6a). According to microkinetic simulations, the RDS of the dissociation pathway and the associative pathway are
dissociation and
hydrogenation processes, respectively, and the essential difference lies in whether the surface H is directly involved in RDS or not, which would result in different kinetic behaviors. The H2–D2 isotopic reaction of ammonia synthesis was performed over the Co3Mo3N catalyst. An inverse isotope effect (kH/kD = 0.50) was observed experimentally, indicating that the hydrogenation step is not the rate-determining step (Fig. 6b). Similar experimental phenomena were previously found for ammonia synthesis via the dissociation mechanism over Fe-promoted catalysts.53 Steady-state kinetic experiments were also performed to further confirm the reaction pathways (details are given in S6 Steady-state kinetic analysis in ESI†). The kinetic models were derived using the assumptions about the rate-determining step. The modelled reaction rate of the dissociation pathway gives a better fit to the experimental reaction rate than that of the associative pathway (Fig. 6c and d). We also derived kinetic models for the associative mechanism with a potential rate-determining step of NNH* dissociation and obtained a worse fit (Fig. S28†).39 On the other hand, the
dissociation process can occur without the assistance of H2 feed (Fig. 5c), suggesting that the dissociation pathway may be the potential reaction mechanism and that
is the most abundant surface intermediate due to the slow consumption of
imposed by
dissociation as the RDS.
Additional insights into the transient kinetics and behavior of surface N species over the Co3Mo3N catalyst were probed by steady-state isotopic-transient kinetic analysis (SSITKA) with an isotopic switch of 14N2 to 15N2 (Fig. 6e and S29†). 14NH3 and 15NH3 production signals were studied to obtain kinetic information. There is a slight delay in the decay of the 14NH3 signal due to the transient release of NH3 produced through lattice N during switching of the reaction gas. The continuous increase in the 15NH3 signal shows that ammonia production is derived mainly from surface N rather than lattice N. In addition, isotope switching experiments at different temperatures were implemented to evaluate the kinetic behavior of the most abundant surface intermediate (Fig. S29†). Response curves at different temperatures show similar features, but a notable difference is the much longer residence time at high temperature. The behavior of the most abundant surface intermediate was determined by establishing the Arrhenius relationship. The intrinsic activation energy for the
dissociation elementary step is 113.7 kJ mol−1, which is higher than the apparent activation energy for steady-state ammonia synthesis (75.1 kJ mol−1) over the Co3Mo3N catalyst (Fig. 6f and S31†). The hydrogenation process of N* species can be achieved rapidly compared to the N2 dissociation process, which leads to the low abundance of surface N* species (Fig. 5d). Steady-state and transient kinetic analysis combined with theoretical calculations accurately identify the reaction mechanism of ammonia synthesis, which is expected to provide insights into a mechanistic understanding of such materials and practical applications at larger scales.
species. Microkinetic simulations provide insights into the design of kinetic experiments. Both steady-state and transient kinetic analysis show that ammonia synthesis is dominated by the surface reaction mechanism of the dissociation pathway. The high activation energy barrier for N2 dissociation results in low coverage of surface N species. The combination of theoretical calculations and experimental results provides more detailed evidence to elucidate the reaction mechanism in heterogeneous catalysis. This study provides a paradigm for the study of reaction mechanisms from a kinetic perspective.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4cy01359j |
| This journal is © The Royal Society of Chemistry 2025 |