Journal
FUEL
Volume 276, Issue -, Pages -Publisher
ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2020.118044
Keywords
Fischer-Tropsch synthesis; Fe-Co bimetallic catalyst; Catalyst promotion; Diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS)
Categories
Funding
- Petrotech Society, India
- Department of science and technology (DST), India [DST/INT/SA/P08/2014]
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Effect of noble metal promotion over the Fischer Tropsch activity of 10Fe/20Co/SiO2 (weight %) bimetallic catalyst was investigated via a detailed experimental study. The addition of noble metal can promote the structural as well as electronic properties of the catalyst, thus affect the activity and product selectivity of the catalyst. The catalyst 10Fe/20Co/SiO2 was impregnated with varying Rh and Ru loading (0.05 to 1 wt%), and their activity was tested under identical reaction conditions. Different catalyst characterization techniques viz. Brunauer-Emmett-Teller surface area, transmission electron microscope, X-ray diffraction, temperature-programmed reduction, O-2 titration and H-2 pules chemisorption, were used to study the promotional effect on the catalyst structure. The increased metal loading (Ru and Rh) increases the metal dispersion and the reducibility, resulting in higher H-2 chemisorption uptake. Diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) was used to investigate the adsorption properties of CO on Rh and Ru promoted catalyst with CO and H-2 as probe molecules. The correlation was observed between DRIFTS results and experimental results obtained from the laboratory reactor. A clear distinction between the adsorption trend of CO over Ru and Rh promoted catalyst was observed. Also, the increased intensity of bridge bonded CO was observed, resulting in higher wax formation in the Ru promoted catalyst. The promoted catalysts (0.5Ru/10Fe/20Co/SiO2 and 0.5Rh/10Fe/20Co/SiO2) were compared with unpromoted bimetallic catalyst at varying temperatures (220-280 degrees C). The findings also suggest that Rh promotion enhances the water-gas shift reaction, which significantly changes the H-2/CO ratio and the overall catalyst performance.
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