Abstract
Ni-Bi oxides supported on novel fibrous silica nanospheres were evaluated as catalysts for the oxidative dehydrogenation (ODH) of n-butane to 1,3-butadiene (BD) in a continuous-flow fixed-bed reactor under varying reaction conditions, including the temperature and oxygen-to-n-butane ratios. The fibrous silica nanospheres were synthesized using a straightforward hydrothermal template-assisted method, followed by the impregnation of Ni (10-20 wt %) and Bi (10-30 wt %) onto the silica support. Characterization confirmed the presence of NiO and Bi2SiO5 phases in the Ni-Bi-Ox/FS catalyst system. An optimized combination of acidic and basic sites was found to enhance the catalytic activity and selectivity. Notably, the 20Ni-10Bi/FS catalyst demonstrated 40.1% n-butane conversion and 20% butadiene yield, with a dehydrogenation selectivity of 71.6% (50.0% BD and 21.6% butenes) at 500 °C and an oxygen-to-butane ratio of 1. The catalyst maintained stable catalytic performance and selectivity over 32 h of continuous operation. Thermogravimetric analysis (TGA) of the spent catalyst confirmed its high stability. This study provides further insights into the development of high-performance ODH catalysts.
| Original language | English |
|---|---|
| Pages (from-to) | 10686-10698 |
| Number of pages | 13 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 64 |
| Issue number | 22 |
| DOIs | |
| State | Published - 4 Jun 2025 |
Bibliographical note
Publisher Copyright:© 2025 American Chemical Society.
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering