Influence of lanthanide oxide supports on the performance of barium-promoted cobalt catalysts for ammonia synthesis

Efficient Ru/MgO–CeO2 catalyst for ammonia synthesis as a hydrogen and energy carrier

Open AccessCCS ChemistryRESEARCH ARTICLE1 May 2022Boosting Efficient Ammonia Synthesis over Atomically Dispersed Co-Based Catalyst via the Modulation of Geometric and Electronic Structures Yanliang Zhou†, Congying Wang†, Xuanbei Peng†, Tianhua Zhang, Xiuyun Wang, Yafei Jiang, Haifeng Qi, Lirong Zheng, Jianxin Lin and Lilong Jiang Yanliang Zhou† National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 , Congying Wang† National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 , Xuanbei Peng† National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 , Tianhua Zhang National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 , Xiuyun Wang *Corresponding authors: E-mail Address: [email protected] E-mail Address: [email protected] National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 , Yafei Jiang Department of Chemistry, Southern University of Science and Technology, Shenzhen 518055 , Haifeng Qi Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023 , Lirong Zheng Institute of High Energy Physics, Chinese Academy of Sciences, Beijing 100049 , Jianxin Lin National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 and Lilong Jiang *Corresponding authors: E-mail Address: [email protected] E-mail Address: [email protected] National Engineering Research Center of Chemical Fertilizer Catalyst, Fuzhou University, Fuzhou, Fujian 350002 https://doi.org/10.31635/ccschem.021.202100912 SectionsSupplemental MaterialAboutAbstractPDF ToolsAdd to favoritesDownload CitationsTrack Citations ShareFacebookTwitterLinked InEmail Ammonia (NH3) synthesis at mild conditions is of great significance, while the significant bottleneck of this process is the activation of N2 to realize the desired NH3 synthesis performance, which requires deep insight and rational design of active sites at the atomic level. Here, were synthesized atomically dispersed Co-based catalysts with different Co-N coordination numbers (CNs) to explore the coordination-sensitive NH3 synthesis reaction for the first time. Our studies showed that Co-based catalysts increased the NH3 synthesis rate gradually with a decrease in CN. The Co-N2 catalyst exhibited the highest NH3 synthesis rate of 85.3 mmol gCo−1 h−1 at 300 °C and 1 MPa, which outperformed most of the previously reported Co-based catalysts. Various characterizations and theoretical calculations demonstrated that atomically dispersed Co catalyst with low CN could generate more unoccupied Co 3d charges and tetrahedral cobalt(II) sites. The unoccupied Co 3d charge, in turn, promoted the electron donation from the Co active center to the antibonding π-orbital (π*) of N2 and expedites N2 hydrogenation. Furthermore, the Co-N2 catalyst with more tetrahedral cobalt(II) sites could effectively facilitate the desorption of N-containing intermediate species (such as *NH3 and *N2H4) to obtain a high NH3 synthesis rate. Download figure Download PowerPoint Introduction Ammonia (NH3) is not only an essential raw material for the synthesis of nitric acid, fertilizer, ammonium salt, and so on but also a promising renewable energy carrier.1,2 The state-of-the-art manufacture of NH3 comes from the Haber–Bosch (HB) process using iron-based catalysts that require harsh reaction conditions (400–500 °C, 10–30 MPa), thereby suffering from high energy consumption and environmental pollution problems.3–5 Therefore, it is urgent to develop effective routes that are both energy-saving and environment-friendly. Most recently, electric power generated from renewable energy sources is widely used for hydrogen (H2) production via water electrolysis. It becomes economically acceptable to NH3 synthesis from renewable H2 and N2 via an electrolysis-driven HB (eHB) process.6 The eHB route is attractive for realizing efficient utilization of renewable energy and a "carbon-free" society. However, the major challenge of NH3 synthesis lies in the activation of N2 (945 kJ mol−1) at mild conditions to realize desired NH3 synthesis rate,7 which would require a deep insight into the reaction mechanism; therefore, the development of advanced, efficient catalysts that can produce NH3 at mild conditions is beneficial. Currently, industrial applied Fe- or Ru-based catalysts that exist as nanoparticles usually obey the dissociative mechanism,8,9 requiring harsh conditions to dissociate the stable N≡N triple bond. In contrast to the N2 dissociative mechanism, most of the enzyme-catalyzed N2 fixation processes followed the associative mechanism, wherein the N≡N triple bond breaks stepwise after partial hydrogenation of the N2 molecule.10,11 Notably, the dissociation energy of the N–N bond (297 kJ/mol) from *N2H4 intermediates is less than a third of that from the N≡N triple bond. Consequently, the exploitation of advanced catalysts that obey the N2 hydrogenation process instead of direct N2 dissociation is promising for realizing the desired NH3 synthesis performance at mild conditions. Further, NH3 synthesis is a typical structure sensitivity reaction, where the pathway of N2 activation is closely related to the geometric and electronic structures of active sites.8,12 For instance, theoretical studies have demonstrated that N2 could preferentially undergo hydrogenation via an associative pathway other than direct dissociation on Ru(0001) surface,13 RhCo3 clusters,12 and Co3Mo3N catalysts.14 In addition, very recently, a limited number of researches have provided us with experimental evidence that the N2 hydrogenation to N2Hx species is preferred over atomically dispersed Ru and Co, as well as Li-promoted Ru catalysts.6,15,16 Among them, atomically dispersed catalysts present well, having the potential for NH3 synthesis at mild conditions, as the direct N2 dissociation is difficult while the N2 hydrogenation is feasible on single-atom sites.15 Meanwhile, atomically dispersed catalysts with definite structures offer the possibility to investigate the geometric and electronic effects on NH3 synthesis at the atomic level. Differing from nanoparticle catalysts, in which the particle size and crystal face usually play an important part in the reactivity, catalytic activity of atomically dispersed catalysts is mainly determined by the coordination environment of single-atom sites.17–19 However, up to now, the modulation of the coordination structure of single-atom active sites to optimize the catalytic activity of NH3 synthesis has not yet been researched. Moreover, the effects of geometric and electronic structures in these single-atom sites on the dynamic transformation of intermediates remain unclear. Herein, we synthesized a series of atomically dispersed Co-Nx (x = 2∼4) catalysts through the pyrolysis of nitrogen-anchored Co-based precursors. The coordination numbers (CNs) of Co-N over the as-prepared catalysts were modulated by varying the calcination temperature. The coordination-sensitive NH3 synthesis reaction in the case of Co-based catalyst is disclosed through a combination of a suite of elaborated experimental characterizations and theoretical calculations. The geometric and electronic structures of Co active sites could be simultaneously tuned via the modulation of Co-N CNs, which are closely related to the N2 activation and desorption of N-containing intermediate species (such as *N2H4 and *NH3), thus resulting in different catalytic behaviors in the NH3 synthesis. This finding is beneficial to rationally design advanced Co-based catalysts by regulating the geometric and electronic structures to realize efficient NH3 synthesis at mild conditions. Experimental Methods Catalyst preparation Synthesis of hollow N-doped porous carbon spheres support The synthetic method of hollow N-doped porous carbon spheres (HNPCSs) support was referenced in previous work.20 Briefly, NH3 solution (10 mL) and ethanol (240 mL) were dissolved in deionized water (80 mL) and stirred evenly at room temperature (RT). Then, tetraethyl orthosilicate (11.2 mL) was added to this solution and stirred further for 1 h. Subsequently, poloxamer, resorcinol, and formaldehyde (2.24 mL) were added to the above solution and continually stirred for 0.5 h. After the addition of melamine (1.26 g) and formaldehyde (1.68 mL), the mixture was treated at 100 °C for 24 h. After filtration and washing, the sample obtained was calcined under an Ar atmosphere at 700 °C for 2 h. Finally, the sample was etched by hydrofluoric acid (HF) solution to remove the SiO2 substrate. After filtration, washing, and drying, the resulting substance was herein referred to as HNPCSs support. Synthesis of Co-Nx and Co-NPs catalysts In detail, HNPCSs (120 mg) and cobalt phthalocyanine (CoPc; 80 mg) was dispersed in dimethylformamide (DMF; 120 mL), respectively, and the mixtures were stirred for 2 h. Then the CoPc and DMF mixed solution was added slowly to the HNPCSs suspension. After stirring for 24 h, the sample was dried in a vacuum dryer at 60 °C for 12 h. Finally, the samples were pyrolyzed under Ar atmosphere at different temperatures of 450, 550, and 650 °C for 2 h, denoted as Co-N4, Co-N3, and Co-N2, respectively. The synthetic procedure used for the Co-NPs catalyst was similar to that of Co-N2, except that the calcination was performed at 700 °C for 10 h. Synthesis of catalysts as reference The Cs-Co/MgO catalyst was synthesized by an impregnation method. In detail, a certain amount of cobalt nitrate hexahydrate and cesium nitrate was dissolved in deionized water. MgO support was added to this solution, and the mixture was stirred evenly. After impregnation at RT for 24 h, the mixture was dried at 80 °C for 24 h. The acquired catalyst was denoted as Cs-Co/MgO, in which the content of Co was the same as that over Co-N2, and the molar ratio of Cs to Co was ∼1.0. A Fe-based catalyst was purchased commercially from Fujian SJ. FD. Co. Ltd. (Fuzhou, Fujian, China) for comparative studies. NH3 synthesis performance test The NH3 synthesis activities over the as-synthesized catalysts were tested in a pressurized fixed bed reactor. In detail, the catalyst (0.2 g, 20–30 mesh) was loaded into the stainless steel reactor (inner diameter 10 mm). Before measurement, the catalysts were treated in a 25%N2–75%H2 feed gas at 300 °C for 2 h. Subsequently, the catalyst performance was evaluated in 300 °C at a weight hourly space velocity (WHSV) of 60,000 mL g−1 h−1 and 1 MPa. The outlet NH3 was trapped by diluted H2SO4 solution and then detected by ion chromatography (DIONEX, ICS-600; Thermo Scientific, Waltham, MA, USA). The turnover frequency (TOFCo) was calculated based on the total molar of Co metal using the following equation: TOF Co = r n M (1)where, r represents the NH3 synthesis rate (mol g−1 s−1), nM is the molar amounts of Co obtained from inductively coupled plasma (ICP) analysis. Catalyst characterization X-ray diffraction (XRD) measurement was recorded on a PANalytical X'Pert Pro diffractometer (PANalytical, Almelo, The Netherlands) using a Cu Kα radiation source. N2 adsorption/desorption isotherms were collected on an ASAP 2020 apparatus (MicroMetric, Lincolnshire, United Kingdom). Elemental analysis (EA) was conducted with a Vario EL-Cube instrument (Elementar, Jiangsu, China) to measure the N contents of the samples. The Co contents of the catalysts were measured by ICP atomic emission spectroscopy (ICP-AES) analysis equipped with an Ultima 2 spectrometer (Perkin-Elmer, Waltham, MA, USA). Catalyst morphologies were detected on scanning electron microscopy (SEM; a Hitachi Model S-4800; Hitachi, Tokyo, Japan). Transmission electron microscopy (TEM) images of the catalysts were obtained on a JEM-2010 instrument (JEOL Ltd., Tokyo, Japan). Aberration-corrected high-angle annular dark-field scanning TEM (AC-HAADF-STEM) analysis was performed on a JEOL JEM-ARM 200 F instrument (JEOL Ltd., Tokyo, Japan). Raman spectroscopy was measured on a multichannel modular triple Raman system (Renishaw Co., London, United Kingdom). Ultraviolet photoelectron spectroscopy (UPS) was measured using a helium resonance lamp offering He I (hν = 21.2 eV) photons. X-ray photoelectron spectroscopy (XPS) was performed on an ESCALAB 250Xi photoelectron spectrometer (Thermo Fisher Scientific, Shanghai, China) with a monochromatic Al Kα source (hν = 1486.6 eV) as the X-ray source. The XPS binding energy was referenced to the C 1s peak at 284.6 eV of adventitious carbon. Electron-paramagnetic resonance (EPR) test was performed on an E500 spectrometer (Bruker-BioSpin, Shanghai, China) with a 100 KHz magnetic field modulation at RT. UV–vis diffuse reflection spectrum (DRS) data were obtained from a Perkin Elmer Lambda 750s UV–vis spectrometer (Perkin-Elmer, Waltham, MA, USA). The productions of NH3 synthesis were trapped at the aqueous solution containing sulfuric acid and para-(dimethylamino) benzaldehyde for the UV–vis DRS measurement. X-ray absorption spectroscopy (XAS), containing X-ray absorption near-edge structure (XANES) and extended X-ray absorption fine structure (EXAFS) analyses were performed at the 1W1B beamline of the Beijing Synchrotron Radiation Facility (BSRF), China. Spectra were collected at the Co K-edge in transmission mode with a Si (111) double crystal monochromator. The Co foil and CoPc samples were used as references. Density functional theory (DFT) calculations First-principle calculations were performed using the generalized gradient approximation (GGA) of Perdew–Burke–Ernzerhof (PBE),21 as implemented in the Vienna ab initio Simulation Package (VASP 5.4.4).22 The valence electronic states of all atoms were expanded in a plane-wave basis set with a cutoff energy of 400 eV, and gamma points were used for Brillouin zone integration. All atoms were allowed to relax until the forces fell below 0.02 eV Å−1. The energy convergence criterion was set to 10−5 eV. Grimme D3 method with the zero-damping function was used to describe van der Waals interactions.23 The graphene supercell with a surface periodicity of 10 × 10, including 200 atoms as a basis, was employed to construct the Co-Nx (x = 4, 3, and 2) moieties. A vacuum space of 20 Å was used in the normal direction of the graphene plane to ensure negligible interaction between the mirror images. Results and Discussion Structure characterization The process for the synthesis of Co-Nx catalysts with different Co-N CNs is depicted in Figure 1a. The atomically dispersed Co-Nx catalysts were prepared by CoPc pyrolysis supported on HNPCSs precursor. The CN of Co-Nx catalysts was modulated by varying the pyrolysis temperature (as shown in the "Catalyst preparation" section). To highlight the coordination structure of atomically dispersed Co center, Co nanoparticle loaded on the same support (Co-NPs) was prepared for comparison. EXAFS analyses of the Co K-edge were conducted to demonstrate the coordination structure of Co-Nx catalysts. The Co K-edge EXAFS spectra of as-synthesized catalysts and reference Co foil and CoPc, are illustrated in Figure 1b. An apparent peak located at 1.5 Å for the as-synthesized Co-Nx samples was attributed to Co-N coordination, compared with CoPc reference.24 Meanwhile, no typical peaks for Co-Co coordination at 2.2 Å were visible, indicating the atomically dispersed Co atoms on these Co-Nx catalysts. Besides, the peak intensity of Co-N coordination decreased with increased pyrolysis temperature, suggesting a decrease in Co-N CN. Based on fitting results, the average CNs of Co-N of the three samples were 3.9, 3.0, and 2.1 (Table 1), and thus, the samples were denoted as Co-N4, Co-N3, and Co-N2, respectively. Additionally, the fitting result of Co K-edge EXAFS spectra of Co-N2 based on our hypothetical model was consistent with the experimental result (Figure 1c), demonstrating the validity of the depicted models. In the case of Co-NPs, the Co-Co coordination existed predominant beside the weak Co-N coordination, indicating that Co entities were distributed mainly in the form of nanoparticles. Figure 1 | (a) Schematic diagram of the preparation process of Co-Nx with different CNs. (b) Co K-edge EXAFS spectra of as-prepared samples. (c) EXAFS spectra and the corresponding curve-fitting results of Co-N2 catalyst. Download figure Download PowerPoint Table 1 | EXAFS Data Fitting Results of the As-Synthesized Catalysts Samples Shell CN R (Å)a σ2 × 102 (Å2)b ΔE0 (eV)c R-Factor (%) Co foil Co-Co 12.0 2.49 0.7 6.3 0.9 Co-N4 Co-N 3.9 1.92 0.4 8.1 0.07 Co-N3 Co-N 3.0 1.91 0.3 7.2 0.09 Co-N2 Co-N 2.1 1.89 0.3 −1.1 0.8 Co-NPs Co-N 2.0 2.03 0.7 −1.8 0.7 Co-Co 2.1 2.49 0.7 −1.8 0.7 Note: The accuracy of parameters: CN, ±20%; R, ±1%; σ2, ±20%; ΔE0, ±10%. The fitting range in k- and R-space is 3.0–12.3 Å−1 and 1.0–2.7 Å, respectively. aR, bonding distance. bσ2, the Debye–Waller factor. cΔE0, inner potential shift. SEM ( Supporting Information Figure S1) and TEM images (Figures 2a and 2b) simultaneously displayed uniform microspheres with the hollow structure of Co-Nx and Co-NPs catalysts. The average diameter of the microspheres was ∼150 nm of these samples. The high-resolution TEM (HR-TEM) images (Figure 2c and Supporting Information Figure S2) did not show any Co nanoparticles sights, implying a high dispersion of Co species as clusters or single atoms over Co-Nx catalysts. We further used the AC-HAADF-STEM characterization to inspect the Co species over Co-Nx catalysts. We found that plenty of highly dispersed Co single atoms were visible over Co-N2 (Figure 2d), Co-N3 (Figure 2e), and Co-N4 (Figure 2f) catalysts. In comparison with Co-Nx catalysts, distinct nanoparticles were observed over the Co-NPs catalyst ( Supporting Information Figure S3). Combined with the EXAFS results, we deduced that atomically dispersed Co-Nx catalysts with different Co-N CNs were synthesized successfully. Figure 2 | (a and b) TEM and (c) HR-TEM images of Co-N2 catalyst. AC-HAADF-STEM images of (d) Co-N2, (e) Co-N3, and (f) Co-N4 catalysts. Download figure Download PowerPoint The XRD patterns ( Supporting Information Figure S4) showed that all Co-Nx displayed a broad diffraction peak at ∼26.4°, to the crystal plane of carbon The highly was by Raman measurement. The Raman spectra ( Supporting Information Figure displayed that samples peaks at and corresponding to the and of or carbon and Furthermore, the intensity of the to of these samples were ( Supporting Information Table that the coordination structure has a on carbon Notably, the diffraction peaks on the Co-N4 sample are attributed to the CoPc suggesting an of CoPc species and the of Co-N4 which with the fitting results of XRD diffraction peaks were related to Co or CoPc species in the Co-N3 and Co-N2 samples. to the above EXAFS and our demonstrated that the pyrolysis of CoPc would form atomically dispersed Co sites over Co-Nx catalysts after the pyrolysis of the at 700 °C for 10 h, the of diffraction peaks at and in Co-NPs catalyst were to the (111) and crystal of Co respectively. The average size of Co nanoparticles over Co-NPs was to the of (111) crystal plane via which with the particle observed in the HR-TEM ( Supporting Information Figure S3). showed that the Co contents in these samples were distributed in the range of ( Supporting Information Table to the results, the N contents of the synthesized Co catalysts ( Supporting Information Table S1) decreased with increased pyrolysis temperature. N2 ( Supporting Information Table S1) results showed that the surface of Co-Nx catalysts increased from to g−1 with increased pyrolysis temperature. However, at a high pyrolysis temperature, the surface of Co-NPs catalyst decreased to of the geometric and electronic structure was performed to insight into the of different CNs on the geometric and electronic structure of Co sites. to the results (Figure the peak intensity in the range of eV was of the geometric of Co that tetrahedral or The from the tetrahedral of Co sites were to to this The intensity of this peak over Co-N2 was than that of Co-N3 or Co-N4, indicating that more Co were at the tetrahedral sites in the Co-N2 Besides, the of the absorption in the images (Figure could be used to the states of Co A of absorption from Co-N4 to Co-N2 was indicating that the valence of Co species decreased with decreased CN of the Co-Nx catalysts. Figure | Co K-edge spectra and the images in the range of (a) eV and (b) eV. Download figure Download PowerPoint Further, XPS were performed to obtain the valence of Co and N species over the as-synthesized catalysts. shown in Figure the Co spectra were fitting into the peaks with binding of and eV, to and peaks of surface Co were observed on these catalysts, except for Co-NPs, which with the results of XRD and The atomic ratio of over the Co-N4, Co-N3, and Co-N2 catalysts determined from XPS results were and (Table This finding was supported by the of Co entities over Co-N2 as shown in the (Figure results, that the decreased CN have been promoted to generate more unoccupied Co 3d over the Co-N2 results were further by The spectra ( Supporting Information Figure showed that the of and over these catalysts were attributed to an electron in the of and carbon We found that the intensity of increased with the of CN, indicating that more on the Co-N2 catalyst. The N 1s spectra (Figure three of N and N over Co-Nx the comparison of the content of different N species from the peak (Table we observed that the N content increased from to while the N content decreased from to with of CN over Co-Nx catalysts. This result that the atomically dispersed Co mainly with the these demonstrated that the geometric and electronic structures of the atomically dispersed Co catalyst were modulated through different CNs of the in turn, the catalytic activity the NH3 synthesis. Figure | (a) Co and (b) N 1s XPS spectra of the as-synthesized catalysts. Download figure Download PowerPoint Table 2 | The XPS Spectra Results of the As-Synthesized Catalysts Samples N (%) N (%) N (%) (%) (%) (%) Co-N4 24 60 Co-N3 12 Co-N2 20 Co Catalyst activity and Figure the NH3 synthesis rate over the as-synthesized catalysts with a 25%N2–75%H2 gas and a of mL The NH3 synthesis rate in the case of Co-N2 was 85.3 gCo−1 h−1 at mild conditions of 300 °C and 1 MPa, than over Co-N3 gCo−1 and Co-N4 gCo−1 An NH3 synthesis rate of gCo−1 h−1 was acquired over Co-NPs, which is more to over the atomically dispersed Co-Nx catalysts. Meanwhile, the NH3 synthesis rate over the carbon as support was mmol h−1 at 300 °C and 1 MPa, as shown in Supporting Information Table suggesting that the of support to the catalytic activity of Co-Nx could be results that NH3 synthesis is a coordination-sensitive reaction, and the Co-N2 catalyst with the CN the highest NH3 synthesis rate at mild conditions. It has been reported that the addition of a electronic to Co-based catalysts could NH3 synthesis performance, referred to as an electronic Herein, we the of to the highly active Co-N2 catalyst on NH3 synthesis It showed that the NH3 synthesis rate over was that of the (Figure The typical Cs-Co/MgO and the Fe-based catalysts were also performed and evaluated for comparison ( Supporting Information Table 300 °C and 1 MPa, the NH3 synthesis rate over Co-N2 mmol gCo−1 was than of Cs-Co/MgO mmol and Fe-based mmol catalysts, indicating the performance of NH3 synthesis activity over Co-N2 catalyst. For based on the total number of Co active sites on these catalysts, were calculated and depicted in Figure Notably, the of Co-N2 and were and respectively, which outperformed most of the previously reported Co-based catalysts in Supporting Information Table Figure | (a) NH3 synthesis rate based on Co content over as-synthesized catalysts at 1 and 300 (b) TOF was calculated on the total number of Co atoms basis over the catalysts. (c) N2 and (d) H2 reaction over Co-N2 and Co-NPs catalysts. Download figure Download PowerPoint A test of the Co-N2 catalyst was conducted at 300 °C and 1 MPa. shown in Supporting Information Figure the NH3 synthesis rate a stable of mmol gCo−1 h−1 a The used catalyst was further tested using HR-TEM and EXAFS shown in the Supporting Information Figure no or at different were observed over the used Co-N2 catalyst. Moreover, the Co K-edge EXAFS spectrum of the used Co-N2 catalyst ( Supporting Information Figure showed that existed the Co-N coordination, while no Co-Co coordination was indicating the of a highly stable Co-N2 active in the process of NH3 synthesis. the of these demonstrated the of Co-N2 catalyst in NH3 synthesis at mild conditions. studies studies were conducted to demonstrate the of N2 and H2 activation over the Co-Nx catalysts. The reaction of N2 and H2 usually as related to the and the of hydrogen For most catalysts, the reaction of N2 is to suggesting that the could be the direct dissociation of the N≡N triple bond. shown in Figure the reaction of N2 over Co-N2 was than that of over low reaction of N2 has been reported over Ru-based catalysts supported by or where the of bond than direct N≡N triple bond dissociation was Additionally, the reaction of H2 on Co-NPs was (Figure The demonstrated that the of H2 on Co to hydrogen

Activity of cobalt and iron catalysts in ammonia synthesis was determined under a pressure of 10 MPa and at the temperature range of 673–823 K, in a six-channel integral steel reactor. The catalytic ammonia decomposition was studied in a differential reactor under the atmosphere of low concentration of ammonia (<6%) in the temperature range of 673–823 K under atmospheric pressure. The determined values of the activation energy for the ammonia synthesis reaction over cobalt and iron catalysts are 268 and 180 kJ/mol, respectively, whilst for the ammonia decomposition reaction they are equal to 111 and 138 kJ/mol. The cobalt catalyst showed lower activity than a commercial iron catalyst in ammonia synthesis reaction. The cobalt catalyst turned out to be more effective in ammonia decomposition reaction than the iron one.

Carbon support surface effects in the catalytic performance of Ba-promoted Ru catalyst for ammonia synthesis

Solid Acid Electrochemical Cell for the Production of Hydrogen from Ammonia

Y-modified perovskite-type oxides BaCe1-x Y x O3-δ (x = 0-0.30) were synthesised and used as supports for cobalt catalysts. The influence of yttrium content on the properties of the support and catalyst performance in the ammonia synthesis reaction was examined using PXRD, STEM-EDX, and sorption techniques (N2 physisorption, H2-TPD, CO2-TPD). The studies revealed that the incorporation of a small amount of yttrium into barium cerate (up to 10 mol%) increased specific surface area and basicity. The catalyst testing under conditions close to the industrial ones (T = 400-470 °C, p = 6.3 MPa, H2/N2 = 3) showed that the most active catalyst was deposited on a support containing 10 mol% Y. The NH3 synthesis reaction rate was 15-20% higher than that of the undoped Co/BaCeO3 catalyst. The activity of the catalysts decreased with further increasing Y content in the support (up to 30 mol%). However, all the studied Co/BaCe1-x Y x O3-δ catalysts exhibited excellent thermal stability, over 240 h of operation. The particularly beneficial properties of the catalyst containing 10 mol% of Y were associated with the highest basicity of the support surface, favourable adsorption properties (suitable proportion of weakly and strongly hydrogen-binding sites), and preferred size of cobalt particles (60 nm). The Co/BaCe0.90Y0.10O3-δ catalyst showed better ammonia synthesis performance compared to the commercial iron catalyst (ZA-5), giving prospects for process reorganisation towards energy-efficient ammonia production.

Effects of Reaction Conditions on Performance of Ru Catalyst and Iron Catalyst for Ammonia Synthesis

Effect of manganese on the catalytic performance of an iron-manganese bimetallic catalyst for light olefin synthesis

Ammonia is one of the promising carriers for hydrogen and a critical ingredient in many industries including fertilizers and pharmaceuticals. In the KAAP process, ruthenium- (Ru-) based catalysts showed 10-20 more activity compared with iron- (Fe-) based catalysts. The modifications that are applied to Ru-based catalysts revolve around changing the material of its support and/or promoters. This study compares the performance of a Ru-based catalyst for ammonia synthesis supported by La2Ce2O7 using barium (Ba), cesium (Cs), potassium (K), and lithium (Li) as promoters. Based on structural, physicochemical, adsorption, and electronic state analysis, the Cs-promoted catalyst is expected to perform best among all the promoted catalysts, while our findings suggest that the K-promoted catalyst performed the best in the actual catalytic reaction. This result will affect the development of Ru/La2Ce2O7-based catalysts, especially in ammonia synthesis at different temperatures and pressures.

Both scientific discovery and technological development are at some point faced with thequestionof how toprogress from a trial-and-error approach to ahighly controlled design process. In heterogeneous catalysis, the search for the optimal active site of a catalyst for a given chemical reaction has been the central objective of research for almost a century. In 1925, Taylor put forward the idea that on a solid catalyst ‘there will be all extremes between the case in which all the atoms in the surface are active and that in which relatively few are so active’ [1]. Ever since the formulation of the Taylor concept of active sites, the quest for observing, identifying, modifying, and designing active sites of heterogeneous catalysts has been on. Heterogeneous catalysis involves an extremely complex set of phenomena, and in order to develop catalyst design strategies, an identification of key parameters, that are principally responsible for the catalytic rate and selectivity (lumped together as ‘activity’ in the following) is needed. A simple approach in this direction has been developed recently for transition-metal surface catalysis [2,3]. The central concept is known as energy scaling relations [4], which together with activity maps and the d-band model have made it possible to develop a quantitative understanding of trends in transition-metal catalysis and enabled prediction of new catalysts [3,5]. These scaling relations are correlations between surface bond energies of different adsorbed species including transition states. Correlations between activation energies and reaction energies, Bronsted–Evans–Polanyi relations, are known throughout chemistry [6,7] and have for long been assumed in heterogeneous catalysis [8]. With the advance of computational methods, it has been discovered that scaling relations are much more general and for a number of reactions over transition-metal surfaces they have been shown to include essentially all intermediates and transition states.The scaling relations enable amapping of the many energetic parameters determining the rate of a catalytic reaction onto a reduced phase space spanned by a few energy parameters known as descriptors [2,3]. As a result, a catalytic activity map can be constructed defining the rate and/or selectivity in the relevant descriptor space i.e. the relevant bond strength between one or more of the reactants or intermediates and the catalyst surface. The activity map exhibits at least one maximum for the optimal bond strength(s), which defines the optimum catalyst. This approach is illustrated for a simple model of the ammonia synthesis process in Fig. 1a. Following [9], the rate of ammonia synthesis at industrial conditions is calculated in a model that assumes N2 dissociation to be rate limiting and that adsorbed N atoms are the main intermediate covering the surface. In such a model, the rate can be calculated as a function of the transition-state energy for N2 dissociation, EN-N, and the N adsorption energy, EN.The two energy parameters are seen to scale verywell, and hence a single parameter, EN, is a good descriptor of the catalytic activity (see Fig. 1b). This is a very simple example of complexity reduction from two to one descriptor.The quantitative aspect of the descriptor approach provides new possibilities in catalyst design. This is also illustrated in Fig. 1b. Knowing which descriptor value defines the highest activity allows for searches for new catalysts with close to optimum properties. While the concept of scaling relations has proven extremely useful by providing an understanding of trends as well as new catalyst design criteria, it has also helped us identify some of the limitations on the performance of large classes of catalysts [2]. Fig. 1a illustrates the point. Clearly, a much better catalyst for ammonia synthesis could be devised if we could find effective ways of circumventing the scaling relations that we know for (stepped) transition-metal surfaces, or, equivalently, find catalystswith active site motifs that obey a different lower lying scaling relation than the so far identified ones. There are several other cases where scaling relations have been suggested to impose limitations on the performance of catalysts. Fig. 1c and d show two such examples: it has proven very difficult to find electrocatalysts that bring down the overpotential for O2 reduction significantly below that for Pt, making lowtemperature fuel cells less efficient than wewould like, and similarly, it has proven difficult, so far to find electrocatalysts that can reduce CO2 to form hydrocarbons and alcohols without substantial overpotentials. In both cases, this can be traced

Ru-K/Sibunit catalysts with different molar ratio of promotor and active component were studied in the low- temperature synthesis and decomposition of ammonia. It was shown that activity of the catalysts in the synthesis reaction increases with the molar ratio of potassium and ruthenium: 0.087 and 0.397 mmol NH3/gcat*h for K/Ru = 0.5 and 2.5, respectively, at a temperature of 350 C, whereas in the decomposition reaction the activity decreases and is equal to 349.2 and 73.8 mmol NH3/gcat*h, respectively, for K/Ru = 0.5 and 2.5 at 450 C.

Controlled Assembly of Hierarchical Metal Catalysts with Enhanced Performances

Steam reforming of acetic acid over cobalt catalysts: Effects of Zr, Mg and K addition

Highly active manganese nitride-europium nitride catalyst for ammonia synthesis

Development and application of wüstite-based ammonia synthesis catalysts