from 01.01.2023 until now
Russian Federation
In this study, Ni-Fe oxide catalysts supported on γ-Al₂O₃ were synthesized using the sol-gel method, with the Ni/Fe molar ratio varied (1:1, 20:1, 15:5, 5:15, 1:20). The synthesis process involved preparing a film-forming solution based on butanol, nitric acid, tetraethoxysilane, and metal nitrates, followed by deposition onto γ-Al₂O₃, drying at 100°C, and annealing at 400°C. To investigate the structural, morphological, and textural properties of the resulting materials, X-ray diffraction (XRD), scanning electron microscopy (SEM) with micro-X-ray spectral analysis, and low-temperature nitrogen adsorption were employed. It was found that an equimolar Ni/Fe ratio of 1:1 ensures the formation of a homogeneous mixed oxide phase, uniform distribution of active components across the support surface, and high particle dispersion. Analysis of SEM images reveals a continuous coating free of agglomerates, indicating good adhesion of the catalyst to the support. XRF data confirm the presence of NiO and α-Fe₂O₃ phases, which interact strongly with γ-Al₂O₃, ensuring the stability of the catalytic system. The specific surface area of the catalyst with a Ni/Fe ratio of 1:1, determined by the BET method, is 134.8 m²/g, which is only 3.4% lower than that of the initial γ-Al₂O₃ (139.5 m²/g). This indicates that the support retains high porosity after the deposition of active components. At the same time, an excess of nickel (20:1, 15:5) or iron (5:15, 1:20) leads to phase segregation, the formation of large NiO or Fe₂O₃ agglomerates, a decrease in specific surface area to 95-112 m²/g, and impaired adhesion to the substrate. Thus, the optimal Ni/Fe ratio of 1:1 shows promise for the development of thermally stable catalysts with a well-developed mesoporous structure, suitable for high-temperature hydrogenation and hydrocarbon conversion processes. The results obtained can be used for the further optimization of catalytic systems based on Ni-Fe oxides.
SOL-GEL METHOD, NICKEL-IRON CATALYSTS, COMPOSITION, STRUCTURE, γ-AL2O3
1. J.K. Prabhakar, P.A. Apte, G. Deo. Chemical Engineering Journal. 471, 144252, (2023).
2. S. Wang, Z. Shen, A. Osatiashtiani, A. Nabavi. Chem. Eng. J., 486, 150170, (2024).
3. R. Ye, X. Wang, Z.-H. Lu, R. Zhanf, G. Feng. Chem. Commun., 60, 11466–11482, (2024).
4. L.V. Furda, E.A. Tarasenko, S.N. Dudina, O.E. Lebedeva. Butlerov Commun., 64, 102–107, (2020).
5. N. Laosiripojana, W. Sutthisripok, S. Charojrochkul, S. Assabumrungrat. Fuel Process. Technol., 127, 26–32, (2014).
6. L. Wu, Z. Yan, J. Xie, Q. Xu, Z. Li. Bioresour. Technol., 402, 130844, (2024).
7. I.A. Pronin, I.A. Averin, D.Ts. Dimitrov, A.A. Karmanov. Nano-Microsyst. Technol., 8, 3–7, (2014).
8. E.V. Karlova, E.S. Podyelnikova, V.P. Lunichkina, T.V. Kon'kova. Adv. Chem. Chem. Eng., 3, 72–74, (2016).
9. M. Sarkari, F. Fazlollahi, H. Atashi, V. Hosseinpour. Fuel Process. Technol., 97, 130–139, (2012).
10. A.S. Al-Fatesh, W.U. Khan, A.A. Ibrahim, A.E. Abasaeed, A.H. Fakeeha. J. Saudi Chem. Soc., 20, 343–352, (2016).
11. M. Chaaban, H. El-Rassy. ACS Omega, 5, 27401–27412, (2020).
12. L. Zhou, L. Li, N. Wei, J. Li, K. Takanabe, J.-M. Basset. Appl. Catal. B Environ., 174, 272–280, (2015).
13. V. Claude, J.G. Mahy, S. Douven, T. Lohay, F. Micheli, S.D. Lambert. J. Environ. Chem. Eng., 8, 104528, (2020).
14. J. Feng, W. Chen, L. Zhang, X. Li. Appl. Surf. Sci., 389, 860–868, (2016).
15. A.A.S. Goncalves, M.J.F. Costa, L. Zhang, F. Ciesielczyk, M. Jaroniec. Chem. Mater., 30, 436–446, (2018).
16. B. Hu, Z. Li, J. Wang, Y. Zhang. Ceram. Int., 43, 1215–1222, (2017).



