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Fe Nanoparticle Size Control of the Fe-MOF-Derived Catalyst Using a Solvothermal Method: Effect on FTS Activity and Olefin Production

[Image: see text] The design of a highly active Fe-supported catalyst with the optimum particle and pore size, dispersion, loading, and stability is essential for obtaining the desired product selectivity. This study employed a solvothermal method to prepare two Fe-MIL-88B metal–organic framework (M...

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Detalles Bibliográficos
Autores principales: Rashed, Ahmed E., Nasser, Alhassan, Elkady, Marwa F., Matsushita, Yoshihisa, El-Moneim, Ahmed Abd
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2022
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8928532/
https://www.ncbi.nlm.nih.gov/pubmed/35309432
http://dx.doi.org/10.1021/acsomega.1c05927
Descripción
Sumario:[Image: see text] The design of a highly active Fe-supported catalyst with the optimum particle and pore size, dispersion, loading, and stability is essential for obtaining the desired product selectivity. This study employed a solvothermal method to prepare two Fe-MIL-88B metal–organic framework (MOF)-derived catalysts using triethylamine (TEA) or NaOH as deprotonation catalysts. The catalysts were analyzed using X-ray diffraction, N(2)-physisorption, Fourier transform infrared spectroscopy, scanning electron microscopy, transmission electron microscopy, H(2) temperature-programed reduction, and thermogravimetric analysis and were evaluated for the Fischer–Tropsch synthesis performance. It was evident that the catalyst preparation in the presence of TEA produces a higher MOF yield and smaller crystal size than those produced using NaOH. The pyrolysis of MOFs yielded catalysts with different Fe particle sizes of 6 and 35 nm for the preparation in the presence of TEA and NaOH, respectively. Also, both types of catalysts exhibited a high Fe loading (50%) and good stability after 100 h reaction time. The smaller particle size TEA catalyst showed higher activity and higher olefin yield, with 94% CO conversion and a higher olefin yield of 24% at a lower reaction temperature of 280 °C and 20 bar at H(2)/CO = 1. Moreover, the smaller particle size TEA catalyst exhibited higher Fe time yield and CH(4) selectivity but with lower chain growth probability (α) and C(5+) selectivity.