Chinese Journal of Catalysis ›› 2024, Vol. 60: 42-67.DOI: 10.1016/S1872-2067(24)60032-X
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Mu-Lin Lia, Yi-Meng Xiea, Jingting Songa, Ji Yanga,*(), Jin-Chao Donga, Jian-Feng Lia,b,*(
)
Received:
2024-03-13
Accepted:
2024-04-02
Online:
2024-05-18
Published:
2024-05-20
Contact:
E-mail: About author:
Ji Yang graduated with a Ph.D. from Xiamen University in 2022. He carried out postdoctoral research in Jian-Feng Li’s group at Xiamen University from 2022 to 2024. His study focuses on the structural evolution of single-atom catalysts under electrocatalytic process by employing in-situ/operando Raman/XAFS characterizations. He has published more than 26 peer-reviewed papers.Supported by:
Mu-Lin Li, Yi-Meng Xie, Jingting Song, Ji Yang, Jin-Chao Dong, Jian-Feng Li. Ammonia electrosynthesis on carbon-supported metal single-atom catalysts[J]. Chinese Journal of Catalysis, 2024, 60: 42-67.
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URL: https://www.cjcatal.com/EN/10.1016/S1872-2067(24)60032-X
Fig. 1. The central nitrogen species and corresponding circulation in the natural and artificial ecosystems. In this picture, “a” and “b” symbols correspond to the artificial and biological processes, respectively. Reprinted with permission from Ref. [24]. Copyright 2018, Springer Nature.
Fig. 2. Multiple proposed dinitrogen reduction (N2RR) pathways on heterogeneous catalysts, including dissociative pathway, associative alternating pathway, associative distal pathway, and enzymatic pathway. Reprinted with permission from Ref. [26]. Copyright 2023, Taylor&Francis Group.
Fig. 3. The reaction pathways of NO3--to-NH3, including O-end, N-side, O-side, and N-end pathways, respectively. The N2 formation from NO3RR follows the NO-dimer pathway. Reprinted with permission from Ref. [30]. Copyright 2021, Wiley-VCH Verlag GmbH & Co.
Fig. 4. The proposed five reaction pathways of NO-to-NH3. The “*” represents the catalytic site. Reprinted with permission from Ref. [33]. Copyright 2024, Elsevier.
Fig. 5. (a) The atomic configurations of transitional metal single atoms on pristine g-C3N4 and corresponding adsorption energies. Reprinted with permission from Ref. [38]. Copyright 2018, John Wiley & Sons, Ltd. (b) The atomic structures with M@C3, M@C4, M@N3, and M@N4. Reprinted with permission from Ref. [13]. Copyright 2018, American Chemical Society. (c) The predicted TM atoms and corresponding catalyst structures of p-TM[TCNE] nanosheets (TM = 3d/4d/5d transition metals). Reprinted with permission from Ref. [40]. Copyright 2022, American Chemical Society.
Fig. 6. (a) The binding energy (left) and the difference between binding and cohesive energies (right) of different TM/g-C3N4. Reprinted with permission from Ref. [41]. Copyright 2022, Elsevier. (b) The selected metal atoms and corresponding atomic structure of TM/g-CN (TM = 3d, 4d, and 5d transitional metals). (c) The AIMD time-dependent energy and temperature evolution for Ti/g-CN and Zr/g-CN, respectively. Reprinted with permission from Ref. [30]. Copyright 2021, John Wiley & Sons, Ltd. (d) The atomic models of single atom on g-C3N4 including 3d, 4d, and 5d transition metals. Reprinted with permission from Ref. [42]. Copyright 2021, American Chemical Society
Fig. 7. (a) The N2 adsorption energy (Eads) on TM@C3N with different M-C and M-N coordination structures. (b) The activated N-N bond length (dN-N) vs. Bader charge (Q) transfer from TM@C3N to N2. Reprinted with permission from Ref. [39]. Copyright 2023, Elsevier. (c) The free energies for N2 chemisorption (top section) and the N-N bond length of the adsorbed *N2 (bottom section) on various TM@C9N4. Reprinted with permission from Ref. [44]. Copyright 2021, Elsevier. (d) The ΔGPDS on different SACs. Reprinted with permission from Ref. [13]. Copyright 2018, American Chemical Society.
Fig. 8. (a) The Gibbs free energies of NO3- adsorbed on different TM/g-C3N4 (TM = 3d, 4d, and 5d transitional metals). Reprinted with permission from Ref. [41]. Copyright 2022, Elsevier. (b) The adsorption energy of NO3- on TM/g-C3N4. (c) The charge density difference of Ru/g-C3N4 and NO3- adsorbed on Ru/g-C3N4. Reprinted with permission from Ref. [42]. Copyright 2021, American Chemical Society.
Fig. 9. (a) The scaling relationship of the free energy changes for the *N2 → *N2H and *NH2 → *NH3 steps. (b) The calculated ΔG*N2 vs. ΔG*H on the 11 promising TM@C9N4 candidates. (c) The theoretical limiting potential for 9 promising TM@C9N4 candidates. Reprinted with permission from Ref. [44]. Copyright 2021, Elsevier.
Fig. 10. (a) The limiting potentials for NO3RR on different TM/g-C3N4. Reprinted with permission from Ref. [41]. Copyright 2022, Elsevier. (b) The limiting potentials on different TM/g-C3N4 for NO3RR. (c) The volcano correlation curve between limiting potential and G*NO3 of different TM/g-C3N4. Reprinted with permission from Ref. [42]. Copyright 2021, American Chemical Society.
Fig. 11. (a) The schematic illustration of the synthetic process of SA-Ag/NC. Reprinted with permission from Ref. [48]. Copyright 2020, American Chemical Society. (b) The schematic of the synthetic process of the Fe-SAs/NSDG. Reprinted with permission from Ref. [49]. Copyright 2022, Elsevier.
Fig. 12. (a) The schematic illustration of the synthetic process of Cu-N-C. Reprinted with permission from Ref. [52]. Copyright 2022, Elsevier. (b) The schematic illustration of the synthetic process of Fe-N/P-C catalyst. Reprinted with permission from Ref. [54]. Copyright 2023, John Wiley & Sons, Ltd.
Fig. 13. (a) The schematic illustration of the synthetic process of Fe1/NC-X. Reprinted with permission from Ref. [57]. Copyright 2023, Elsevier. (b) The schematic illustration of the synthetic process of FeSAs/g-C3N4. Reprinted with permission from Ref. [58]. Copyright 2022, Elsevier. (c) The schematic illustration of the synthetic process of BCN-Cu. Reprinted with permission from Ref. [60]. Copyright 2021, Elsevier.
Fig. 14. (a) The schematic illustration of the Cu-N-C synthetic procedure. Reprinted with permission from Ref. [61]. Copyright 2022, American Chemical Society. (b) The schematic illustration of Fe/Cu-HNG catalyst. Reprinted with permission from Ref. [62]. Copyright 2023, Springer Nature.
Catalyst | Electrolyte | Potential (V vs. RHE) | Production rate | FE | Ref. |
---|---|---|---|---|---|
Ru SAs/N-C | 0.05 mol L-1 H2SO4 | -0.2 | 120.9 μgNH3 h-1 mg-1cat. | 29.6% | [ |
Ru@ZrO2/NC | 0.1 mol L-1 HCl | -0.21 | 3.665 mgNH3 h-1 mg-1Ru | 21% | [ |
Ru SAs/GDY/G | 0.5 mol L-1 Na2SO4 | -0.1 | 4.7 mgNH3 h-1 mg-1Ru | 37.6% | [ |
Rh SA/GDY | 0.005 mol L-1 H2SO4 and 0.1 mol L-1 K2SO4 | -0.2 | 74.15 μg h-1 cm-2 | 20.36% | [ |
Au1/C3N4 | 5 mmol L-1 H2SO4 | -0.1 | 1350 μg h-1 mg-1Au | 11.1% | [ |
AuSAs-NDPCs | 0.1 mol L-1 HCl | -0.2 | 2.32 μg h-1 cm-2 | 12.3% | [ |
SA-Ag/NC | 0.1 mol L-1 HCl | — | 69.4 mg h-1 mg-1Ag at -0.65 V vs. RHE | 21.9% at -0.60 V vs. RHE | [ |
FeSA-N-C | 0.1 mol L-1 KOH | 0.0 | 7.48 μg h-1 mg-1 | 56.55% | [ |
FeSA-NO-C | 0.1 mol L-1 HCl | -0.4 | 31.9 μgNH3 h-1 mg-1cat. | 11.8 % | [ |
FeSA-NSC | 0.1 mol L-1 HCl | -0.4 | 30.4 μg h-1 mg-1cat. | 21.9% | [ |
FeSAs/NSDG | 0.1 mol L-1 KOH | — | 28.89 μg h-1 mg-1cat. at -0.4 V vs. RHE | 23.7% at -0.1 V vs. RHE | [ |
NC-Cu SA | 0.1 mol L-1 KOH | -0.35 | ∼53.3 μgNH3 h-1 mg-1cat. | 13.8% | [ |
0.1 mol L-1 HCl | -0.30 | ∼49.3 μgNH3 h-1 mg-1cat. | 11.7% | ||
Ni-Nx-C-700-3h | 0.1 mol L-1 KOH | — | 115 μg h-1 cm-2 at -0.8 V vs. RHE | 21% at -0.2 V vs. RHE | [ |
Mn−O3N1/PC | 0.1 mol L-1 HCl | -0.35 | 66.41 μg h-1 mg-1cat. | 8.91% | [ |
SA-Mo/NPC | 0.1 mol L-1 KOH | -0.3 | 34 μg h-1 mg-1cat. | 14.6% | [ |
Table 1 The activity comparisons for ammonia synthesis from N2RR on the recently reported SACs.
Catalyst | Electrolyte | Potential (V vs. RHE) | Production rate | FE | Ref. |
---|---|---|---|---|---|
Ru SAs/N-C | 0.05 mol L-1 H2SO4 | -0.2 | 120.9 μgNH3 h-1 mg-1cat. | 29.6% | [ |
Ru@ZrO2/NC | 0.1 mol L-1 HCl | -0.21 | 3.665 mgNH3 h-1 mg-1Ru | 21% | [ |
Ru SAs/GDY/G | 0.5 mol L-1 Na2SO4 | -0.1 | 4.7 mgNH3 h-1 mg-1Ru | 37.6% | [ |
Rh SA/GDY | 0.005 mol L-1 H2SO4 and 0.1 mol L-1 K2SO4 | -0.2 | 74.15 μg h-1 cm-2 | 20.36% | [ |
Au1/C3N4 | 5 mmol L-1 H2SO4 | -0.1 | 1350 μg h-1 mg-1Au | 11.1% | [ |
AuSAs-NDPCs | 0.1 mol L-1 HCl | -0.2 | 2.32 μg h-1 cm-2 | 12.3% | [ |
SA-Ag/NC | 0.1 mol L-1 HCl | — | 69.4 mg h-1 mg-1Ag at -0.65 V vs. RHE | 21.9% at -0.60 V vs. RHE | [ |
FeSA-N-C | 0.1 mol L-1 KOH | 0.0 | 7.48 μg h-1 mg-1 | 56.55% | [ |
FeSA-NO-C | 0.1 mol L-1 HCl | -0.4 | 31.9 μgNH3 h-1 mg-1cat. | 11.8 % | [ |
FeSA-NSC | 0.1 mol L-1 HCl | -0.4 | 30.4 μg h-1 mg-1cat. | 21.9% | [ |
FeSAs/NSDG | 0.1 mol L-1 KOH | — | 28.89 μg h-1 mg-1cat. at -0.4 V vs. RHE | 23.7% at -0.1 V vs. RHE | [ |
NC-Cu SA | 0.1 mol L-1 KOH | -0.35 | ∼53.3 μgNH3 h-1 mg-1cat. | 13.8% | [ |
0.1 mol L-1 HCl | -0.30 | ∼49.3 μgNH3 h-1 mg-1cat. | 11.7% | ||
Ni-Nx-C-700-3h | 0.1 mol L-1 KOH | — | 115 μg h-1 cm-2 at -0.8 V vs. RHE | 21% at -0.2 V vs. RHE | [ |
Mn−O3N1/PC | 0.1 mol L-1 HCl | -0.35 | 66.41 μg h-1 mg-1cat. | 8.91% | [ |
SA-Mo/NPC | 0.1 mol L-1 KOH | -0.3 | 34 μg h-1 mg-1cat. | 14.6% | [ |
Catalyst | Electrolyte | Potential (V vs. RHE) | Production rate | FE | Ref. |
---|---|---|---|---|---|
Cu-PTCDA | 0.1 mol L-1 PBS and 500 ppm NO3- | -0.4 | 436 μgNH3 h-1 cm-2 | 77% | [ |
Cu-N-C | 50 mg L-1 NO3- and 0.5 M Na2SO4 | 1.5 V vs. SCE | 9.23 mg h-1 mg-1cat. | 94% | [ |
Cu MNC-7 | 50 mL Na2SO4 and 100 mg-N mL-1 NaNO3 | -0.64 | 5466 mmol h-1 g-1Cu | 94.8% | [ |
Cu-cis-N2O2 | 1000 ppm N-KNO3/0.5 mol L-1 Na2SO4 | -1.6 | 28.73 mg h-1 cm-2 | 77% | [ |
PR-CuNC | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | -0.5 | 130.71 mg h-1 mg-1Cu | 94.61% | [ |
BCN-Cu | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | -0.6 | 1900.07 μg h-1 cm-2 | 97.37% | [ |
Fe-PPy SACs | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | — | 2.75 mg h-1 cm-2 at -0.7V | 100% at -0.3 V | [ |
Fe SAC | 0.50 mol L-1 KNO3/0.10 mol L-1 K2SO4 | -0.66 | 20000 μg h−1 mg−1cat. | 75% | [ |
FeSAs/g-C3N4 | 50 mg N/L NO3--N and 0.1 mol L-1 Na2SO4 | -0.65 | — | 77.3% | [ |
Fe1/N-C-900 | 0.1 mol L-1 K2SO4 and 0.5 mol L-1 KNO3 | — | 18.8 mgNH3 h-1 mg-1cat. at -0.9 V | 86% at -0.7 V | [ |
Fe-N/P-C SAC | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | — | 17980 μg h-1 mg-1cat. at -0.8 V | 90.3% at -0.4 V | [ |
Table 2 The activity comparisons for ammonia synthesis from NO3RR on the recently reported SACs.
Catalyst | Electrolyte | Potential (V vs. RHE) | Production rate | FE | Ref. |
---|---|---|---|---|---|
Cu-PTCDA | 0.1 mol L-1 PBS and 500 ppm NO3- | -0.4 | 436 μgNH3 h-1 cm-2 | 77% | [ |
Cu-N-C | 50 mg L-1 NO3- and 0.5 M Na2SO4 | 1.5 V vs. SCE | 9.23 mg h-1 mg-1cat. | 94% | [ |
Cu MNC-7 | 50 mL Na2SO4 and 100 mg-N mL-1 NaNO3 | -0.64 | 5466 mmol h-1 g-1Cu | 94.8% | [ |
Cu-cis-N2O2 | 1000 ppm N-KNO3/0.5 mol L-1 Na2SO4 | -1.6 | 28.73 mg h-1 cm-2 | 77% | [ |
PR-CuNC | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | -0.5 | 130.71 mg h-1 mg-1Cu | 94.61% | [ |
BCN-Cu | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | -0.6 | 1900.07 μg h-1 cm-2 | 97.37% | [ |
Fe-PPy SACs | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | — | 2.75 mg h-1 cm-2 at -0.7V | 100% at -0.3 V | [ |
Fe SAC | 0.50 mol L-1 KNO3/0.10 mol L-1 K2SO4 | -0.66 | 20000 μg h−1 mg−1cat. | 75% | [ |
FeSAs/g-C3N4 | 50 mg N/L NO3--N and 0.1 mol L-1 Na2SO4 | -0.65 | — | 77.3% | [ |
Fe1/N-C-900 | 0.1 mol L-1 K2SO4 and 0.5 mol L-1 KNO3 | — | 18.8 mgNH3 h-1 mg-1cat. at -0.9 V | 86% at -0.7 V | [ |
Fe-N/P-C SAC | 0.1 mol L-1 KOH and 0.1 mol L-1 KNO3 | — | 17980 μg h-1 mg-1cat. at -0.8 V | 90.3% at -0.4 V | [ |
Catalyst | Electrolyte | Potential (V vs. RHE) | Production rate | FE | Ref. |
---|---|---|---|---|---|
Ru SA-NC | 1 mol L‒1 KOH and 0.5 mol L‒1 NO2- | -0.6 V | 0.69 mmol h−1 cm−2 | 97.8% | [ |
Nb-SA/BNC | 0.1 mol L‒1 HCl | -0.6 V | 8.2 × 10-8 mol cm-2 s-1 | 77% | [ |
Ce-SA/NHCS | 0.05 mol L‒1 HCl | -0.7V | 1023 μg h-1 mg-1cat. | 91% | [ |
SA-Ni/graphene | 0.5 mol L‒1 K2SO4 and H2SO4 (pH = 1) | — | 1.6 mmol mg-1 h-1 at -0.68 V | 81.2% at -0.51 V | [ |
Table 3 The activity comparisons for ammonia synthesis from NO2RR and NORR on the recently reported SACs.
Catalyst | Electrolyte | Potential (V vs. RHE) | Production rate | FE | Ref. |
---|---|---|---|---|---|
Ru SA-NC | 1 mol L‒1 KOH and 0.5 mol L‒1 NO2- | -0.6 V | 0.69 mmol h−1 cm−2 | 97.8% | [ |
Nb-SA/BNC | 0.1 mol L‒1 HCl | -0.6 V | 8.2 × 10-8 mol cm-2 s-1 | 77% | [ |
Ce-SA/NHCS | 0.05 mol L‒1 HCl | -0.7V | 1023 μg h-1 mg-1cat. | 91% | [ |
SA-Ni/graphene | 0.5 mol L‒1 K2SO4 and H2SO4 (pH = 1) | — | 1.6 mmol mg-1 h-1 at -0.68 V | 81.2% at -0.51 V | [ |
Fig. 15. (a) The HAADF-STEM image of Ru SAs/N-C. (b) The FT-EXAFS fitting curve for Ru SAs/N-C. The FE (c) and yield rate (d) of NH3 production at different working potentials on Ru SAs/N-C and Ru NPs/N-C. Reprinted with permission from Ref. [70]. Copyright 2018, John Wiley & Sons, Ltd. FE (e) and yield rate (f) of NH3 over Ru@ZrO2/NC and the other controlled samples. (g) ΔGPDS for NRR on various active structures. Reprinted with permission from Ref. [55]. Copyright 2019, Cell Press. (h) The NH3 yield and FE of Ru SAs/GDY/G at different applied potentials. (i) The NH3 yield rate normalized by the mass of Ru for Ru SAs/GDY/G at different potentials. Reprinted with permission from Ref. [63]. Copyright 2023, American Chemical Society.
Fig. 16. (a) The FT-EXAFS spectra of Au1/C3N4 and the other standard samples. The FE (b) and yield rate (c) of NH3 for Au1/C3N4 at different potentials. (d) The free energy profile of NRR on Au1/C3N4 and Au (211). Reprinted with permission from Ref. [75]. Copyright 2018, Elsevier. (e) The HADDF-STEM image of SA-Ag/NC. (f) The FE-EXAFS fitting curve of SA-Ag/NC. (g) The FE and yield rate of NH3 over SA-Ag/NC. The cycling tests (h) and chronoamperometry result (i) of SA-Ag/NC. Reprinted with permission from Ref. [48]. Copyright 2020, American Chemical Society.
Fig. 17. (a) The HAADF-STEM image of FeSA-N-C, scale bar, 2 nm. (b) The FE-EXAFS spectra of FeSA-N-C and Fe foil. (c) The comparison of linear sweep voltammograms between FeSA-N-C and N-C. (d) The NH3 FE and yield rate at different potentials. (e) The mean force (PMF) potential for N2 adsorption on FeSA-N-C in 0.1 mol L-1 KOH electrolyte. (f) The energy barriers of the adsorption of hydrogen and nitrogen. Reprinted with permission from Ref. [68]. Copyright 2019, Springer Nature.
Fig. 18. (a) The FT-EXAFS fitting curve and atomic structure of FeSA-NSC-900. (b) The comparison of the FE values and NH3 yields for FeSA-NSC-900 with other reported state-of-the-art Fe SACs and Fe-based compounds. (c) The free energy profiles of FeN3S1 and FeN4 models at -0.4 V are presented by gray and red lines, respectively. Reprinted with permission from Ref. [59]. Copyright 2022, John Wiley & Sons, Ltd.
Fig. 19. (a) The HAADF-STEM image of NC-Cu SA. (b) The FT-EXAFS fitting curve for the NC-Cu SA. NH3 yield rate and FE at different potentials for NC-Cu SA in 0.1 mol L-1 KOH (c) and 0.1 mol L-1 HCl (d). Reprinted with permission from Ref. [78]. Copyright 2019, American Chemical Society. (e) NH3 yield rate (red) and FE (blue) at different potentials for SA-Mo/NPC. (f) The chronoamperometric curve and FE stability for SA-Mo/NPC. Reprinted with permission from Ref. [69]. Copyright 2019, John Wiley & Sons, Ltd.
Fig. 20. (a) The FE of NH3 (blue) and NO2- (mauve) of various elements incorporated in PTCDA at the potential of -0.4 V vs. RHE. (b) The NH3 yield rate at different potentials at the second hour. (c) NH3 FE at different potentials at the second hour. H (d) and NO3- (e) adsorption energies. Reprinted with permission from Ref. [84]. Copyright 2020, Springer Nature.
Fig. 21. (a) The FT-EXAFS fitting curve and atomic model of Cu MNC-7. (b) The charge density difference of NC, Cu(I)-N3C1, and Cu(II)-N4. (c) The activation energy for NO3RR using Cu(I)-N3C1 and Cu(II)-N4 as models. (d) The NO3- conversion and nitrogen product selectivity of different catalysts. Reprinted with permission from Ref. [67]. Copyright 2022, American Chemical Society.
Fig. 22. The HAADF-STEM image (a) and corresponding local EELS (b) of Fe-PPy SACs. (c) The LSVs of the Fe-PPy SACs, Fe NPs, and PPy with and without adding NO3- in the electrolytes. (d) The yield rate of the three catalysts at high overpotentials. (e) The NH3 FE over three catalysts. Reprinted with permission from Ref. [88]. Copyright 2021, Royal society of chemistry. (f) The FT-EXAFS fitting curve and atomic configuration of Fe SAC. (g) The NH3 FE of Fe SAC at different potentials. (h) The NH3 yield rate and partial current density of Fe SAC, Fe NP/NC, and NC. (i) The NH3 yield rate of Fe SAC, Co SAC, and Ni SAC. Reprinted with permission from Ref. [66]. Copyright 2021, Springer Nature.
Fig. 23. (a) Selection of 3d/4d/5d/f metals synthesized via the sacrificial support method. (b) The Schematic of the nitrogen-coordinated metal active site (M-N4) on a prototype carbon matrix illustrates in-plane and out-of-plane configurations. (c) Electrochemical NO2RR for M-N-C catalysts in 0.05 mol L?1 PBS?+?0.01 mol L?1 KNO2 for 0.5?h. The bottom section shows the corresponding NH3 yield rate. Reprinted with permission from Ref. [91]. Copyright 2023, Springer Nature.
Fig. 24. (a) The HAADF-STEM image of Nb-SA/BNC. (b) The FT-EXAFS fitting curve and corresponding atomic structure of Nb-SA/BNC. (c) The NH3 yield rate of NORR for NB-SA/BNC and the other controlled samples. Reprinted with permission from Ref. [93]. Copyright 2020, Elsevier. (d) The NH3 FE and yield rate of NORR over Ce-SA/NHCS. Reprinted with permission from Ref. [94]. Copyright 2023, Elsevier.
Fig. 25. (a) The first-order derivatives of the XANES spectra were recorded at different cathodic potentials in nitrate electrolysis. (b) Corresponding Cu K edge FT-EXAFS spectra at different potentials from fresh, 0.00 to -1.00 V vs. RHE. (c) The XAS comparisons of electrolysis of Cu-N-C at -1.00 V vs. RHE with and without nitrate. (d) Corresponding FT-EXAFS spectra and HAADF-STEM image (inset) after durability measurements. (e) Identical-location electron microscopic characterizations. Reprinted with permission from Ref. [61]. Copyright 2022, American Chemical Society.
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