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Ultrasonic-assisted preparation of highly active Co(3)O(4)/MCM-41 adsorbent and its desulfurization performance for low H(2)S concentration gas

Co(3)O(4)/MCM-41 adsorbents were successfully prepared by ultrasonic assisted impregnation (UAI) and traditional mechanical stirring impregnation (TMI) technologies and characterized by X-ray diffraction (XRD), N(2) adsorption desorption, Fourier transform infrared spectra (FT-IR), transmission elec...

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Detalles Bibliográficos
Autores principales: Jiang, Bolong, Zhang, Jiaojing, Chen, Yanguang, Song, Hua, Hao, Tianzhen, Kuang, Junhu
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9056334/
https://www.ncbi.nlm.nih.gov/pubmed/35518214
http://dx.doi.org/10.1039/d0ra05606e
Descripción
Sumario:Co(3)O(4)/MCM-41 adsorbents were successfully prepared by ultrasonic assisted impregnation (UAI) and traditional mechanical stirring impregnation (TMI) technologies and characterized by X-ray diffraction (XRD), N(2) adsorption desorption, Fourier transform infrared spectra (FT-IR), transmission electron microscopy (TEM), scanning electron microscopy (SEM) and thermogravimetry-differential thermal analysis (TG-DTA). The H(2)S removal performances for a simulated low H(2)S concentration gas were investigated in a fixed-bed. The effect of preparation and adsorption conditions on the H(2)S removal over Co(3)O(4)/MCM-41 were systematically examined. The results showed that UAI promotes more and well defined highly dispersed active Co(3)O(4) phase on MCM-41. As compared to the Co(3)O(4)/MCM-41-T prepared via TMI, the saturated H(2)S capacity of Co(3)O(4)/MCM-41-U prepared via UAI improved by 33.2%. The desulfurization performance of adsorbents decreased in the order of Co(3)O(4)/MCM-41-U > Co(3)O(4)/MCM-41-T > MCM-41. The Co(3)O(4)/MCM-41-U prepared using Co(NO(3))(2) concentration of 10%, ultrasonic time of 2 h, calcination temperature of 550 °C and calcination time of 3 h exhibited the best H(2)S removal efficiency. At adsorption temperature of 25 °C with model gas flowrate of 20 mL min(−1), the breakthrough time of Co(3)O(4)/MCM-41-U was 10 min, and the saturated H(2)S capacity and H(2)S removal rate was 52.6 mg g(−1) and 47.8%, respectively.